Differences between Version 3.2 and 3.2.1 Build 2 of package Modelica

Version: 3.2	Version: 3.2.1 Build 2
Version date: 2010-10-25	Version date: 2013-08-14

model Blocks.Examples.PID_Controller

Component	Version 3.2	Version 3.2.1
PI	initType=Modelica_3_2.Blocks.Types.Init.SteadyState	initType=Modelica.Blocks.Types.InitPID.SteadyState
inertia1	a(fixed=true)	a(fixed=true, start=0)

---

model Blocks.Examples.RealNetwork1

Component	Version 3.2	Version 3.2.1
product	nu=3	nu=2
linearDependency1		Present
minMax		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(add.y, showValue.numberPort);
connect(add.y, product.u[1]);	connect(integerStep.y, product.u[1]);
connect(integerStep.y, product.u[2]);	connect(integerConstant.y, product.u[2]);
connect(integerConstant.y, product.u[3]);
connect(product.y, showValue1.numberPort);
	connect(add.y, linearDependency1.u1); connect(product.y, linearDependency1.u2); connect(add.y, minMax.u[1]); connect(product.y, minMax.u[2]);

---

model Blocks.Examples.BooleanNetwork1

Component	Version 3.2	Version 3.2.1
rSFlipFlop		Present
sampleTriggerSet		Present
sampleTriggerReset		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(onDelay.y, showValue6.activePort);
	connect(sampleTriggerSet.y, rSFlipFlop.S); connect(sampleTriggerReset.y, rSFlipFlop.R);

---

block Blocks.Continuous.LimIntegrator

Component	Version 3.2	Version 3.2.1
strict		Present

Equations in Version 3.2	Equations in Version 3.2.1
... der(y) = k*u;
assert(y >= outMin - 0.01*abs(outMin) and y <= outMax + 0.01*abs(outMax), "LimIntegrator: During initialization the limits have been ignored.\n"+ "However, the result is that the output y is not within the required limits:\n"+ " y = " + String(y) + ", outMin = " + String(outMin) + ", outMax = " + String(outMax));	assert(y >= outMin - 0.001*abs(outMax-outMin) and y <= outMax + 0.001*abs(outMax-outMin), "LimIntegrator: During initialization the limits have been ignored.\n" + "However, the result is that the output y is not within the required limits:\n" + " y = " + String(y) + ", outMin = " + String(outMin) + ", outMax = " + String(outMax));
	elseif strict then der(y) = noEvent(if y < outMin and k*u < 0 or y > outMax and k*u > 0 then 0 else k*u);
else
der(y) = if y < outMin and u < 0 or y > outMax and u > 0 then 0 else k*u;	der(y) = if y < outMin and k*u < 0 or y > outMax and k*u > 0 then 0 else k*u;
end if;

---

block Blocks.Continuous.PID

Component	Version 3.2	Version 3.2.1
I	k=1/Ti	k=unitTime/Ti
	initType=if initType == InitPID.SteadyState then InitPID.SteadyState else if initType == InitPID.InitialState or initType == InitPID.DoNotUse_InitialIntegratorState then InitPID.InitialState else InitPID.NoInit	initType=if initType == InitPID.SteadyState then Init.SteadyState else if initType == InitPID.InitialState or initType == InitPID.DoNotUse_InitialIntegratorState then Init.InitialState else Init.NoInit
D	k=Td	k=Td/unitTime
	initType=if initType == InitPID.SteadyState or initType == InitPID.InitialOutput then InitPID.SteadyState else if initType == InitPID.InitialState then InitPID.InitialState else InitPID.NoInit	initType=if initType == InitPID.SteadyState or initType == InitPID.InitialOutput then Init.SteadyState else if initType == InitPID.InitialState then Init.InitialState else Init.NoInit
unitTime		Present

---

block Blocks.Continuous.LimPID

Component	Version 3.2	Version 3.2.1
controllerType	=Modelica_3_2.Blocks.Types.SimpleController.PID	=.Modelica.Blocks.Types.SimpleController.PID
Ti	start=0.5
		=0.5
Td	start=0.1
		=0.1
initType	=Modelica_3_2.Blocks.Types.InitPID.DoNotUse_InitialIntegratorState	=.Modelica.Blocks.Types.InitPID.DoNotUse_InitialIntegratorState
I	k=1/Ti	k=unitTime/Ti
	initType=if initType == InitPID.SteadyState then InitPID.SteadyState else if initType == InitPID.InitialState or initType == InitPID.DoNotUse_InitialIntegratorState then InitPID.InitialState else InitPID.NoInit	initType=if initType == InitPID.SteadyState then Init.SteadyState else if initType == InitPID.InitialState or initType == InitPID.DoNotUse_InitialIntegratorState then Init.InitialState else Init.NoInit
D	k=Td	k=Td/unitTime
	initType=if initType == InitPID.SteadyState or initType == InitPID.InitialOutput then InitPID.SteadyState else if initType == InitPID.InitialState then InitPID.InitialState else InitPID.NoInit	initType=if initType == InitPID.SteadyState or initType == InitPID.InitialOutput then Init.SteadyState else if initType == InitPID.InitialState then Init.InitialState else Init.NoInit
limiter		strict=strict
strict		Present
unitTime		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if initType==InitPID.InitialOutput then
y = y_start;	gainPID.y = y_start;
end if; ...

---

block Blocks.Continuous.StateSpace

Component	Version 3.2	Version 3.2.1
A		=[1, 0; 0, 1]
B		=[1; 1]
C		=[1, 1]

---

function Blocks.Continuous.Internal.Filter.base.Bessel

Component	Version 3.2	Version 3.2.1
n_den2	Present

Equations in Version 3.2	Equations in Version 3.2.1
... alpha2 = alpha*alpha;
for i in 1:n_den2 loop	for i in 1:size(c0, 1) loop
den2[i, 1] = den2[i, 1]*alpha2; ...

---

function Blocks.Continuous.Internal.Filter.base.Butterworth

Component	Version 3.2	Version 3.2.1
n_den2	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
for i in 1:n_den2 loop	for i in 1:size(c0, 1) loop
den2[i, 1] = 1.0; ...

---

function Blocks.Continuous.Internal.Filter.base.ChebyshevI

Component	Version 3.2	Version 3.2.1
n_den2	Present

Equations in Version 3.2	Equations in Version 3.2.1
... fac = asinh(1/epsilon)/order;
	den1 = fill(1/sinh(fac),size(den1,1));
if size(cr,1) == 0 then
for i in 1:n_den2 loop	for i in 1:size(c0, 1) loop
den2[i,1] = 1/(cosh(fac)^2 - cos((2*i - 1)*pi/(2*order))^2); ... else
den1[1] = 1/sinh(fac);	for i in 1:size(c0, 1) loop
for i in 1:n_den2 loop
den2[i,1] = 1/(cosh(fac)^2 - cos(i*pi/order)^2); ... alpha2 = alpha*alpha;
for i in 1:n_den2 loop	for i in 1:size(c0, 1) loop
den2[i, 1] = den2[i, 1]*alpha2; ... end for;
if size(cr,1) == 1 then	den1 = den1*alpha;
den1[1] = den1[1]*alpha;
end if;
end if;
(cr,c0,c1) =      &nbspModelica_3_2.Blocks.Continuous.Internal.Filter.Utilities.toHighestPowerOne(      &nbspden1, den2); ...

---

function Blocks.Continuous.Internal.Filter.coefficients.bandPass

Component	Version 3.2	Version 3.2.1
w_band	SIunits.AngularVelocity	Real

---

function Blocks.Continuous.Internal.Filter.coefficients.bandStop

Component	Version 3.2	Version 3.2.1
w_band	SIunits.AngularVelocity	Real

---

block Blocks.Discrete.FirstOrderHold

Component	Version 3.2	Version 3.2.1
ySample	Present
uSample		Present
pre_uSample		Present

Equations in Version 3.2	Equations in Version 3.2.1
when sampleTrigger then	initial equation
ySample = u;	pre(tSample) = time;
tSample = time;	pre(uSample) = u;
c = if firstTrigger then 0 else (ySample - pre(ySample))/samplePeriod;	pre(pre_uSample) = u;
end when;	pre(c) = 0.0;
y = pre(ySample) + pre(c)*(time - tSample);
	equation  &nbspwhen sampleTrigger then tSample = time; uSample = u; pre_uSample = pre(uSample); c = if firstTrigger then 0 else (uSample - pre_uSample)/samplePeriod; end when; y = pre_uSample + pre(c)*(time - tSample);

---

block Blocks.Discrete.TransferFunction

Component	Version 3.2	Version 3.2.1
a		={1}

---

block Blocks.Discrete.StateSpace

Component	Version 3.2	Version 3.2.1
A		=[1, 0; 0, 1]
B		=[1; 1]
C		=[1, 1]

---

block Blocks.Interfaces.SI2BooleanSO

Component	Version 3.2	Version 3.2.1
u1	Blocks.Interfaces.RealInput	Blocks.Interfaces.BooleanInput
	input
u2	Blocks.Interfaces.RealInput	Blocks.Interfaces.BooleanInput
	input
y	output

---

block Blocks.Logical.TriggeredTrapezoid

Equations in Version 3.2	Equations in Version 3.2.1
initial equation	y = if time < T then endValue - (T - time)*rate else endValue;
pre(y) = 0; equation    &nbspy = if time < T then endValue - (T - time)*rate else endValue;
when {initial(),u,not u} then ...

---

block Blocks.Math.MultiSwitch

Component	Version 3.2	Version 3.2.1
y	start=y_default
	fixed=true

---

block Blocks.Math.Feedback

Component	Version 3.2	Version 3.2.1
u1	input
u2	input
y	output

---

block Blocks.Math.Add3

Component	Version 3.2	Version 3.2.1
u1	input
u2	input
u3	input
y	output

---

block Blocks.Math.Abs

Component	Version 3.2	Version 3.2.1
generateEvent		Present

Equations in Version 3.2	Equations in Version 3.2.1
y = abs(u);	y=if generateEvent then (if u>=0 then u else -u) else (if noEvent(u>=0) then u else -u);

---

block Blocks.Math.Sign

Component	Version 3.2	Version 3.2.1
generateEvent		Present

Equations in Version 3.2	Equations in Version 3.2.1
y = sign(u);	y=if generateEvent then (if u>0 then 1 elseif u<0 then -1 else 0) else (if noEvent(u>0) then 1 elseif noEvent(u<0) then -1 else 0);

---

block Blocks.Math.Mean

Component	Version 3.2	Version 3.2.1
t0	discrete	parameter
		fixed=false
x	start=0
x0		Present
yGreaterOrEqualZero		Present

Equations in Version 3.2	Equations in Version 3.2.1
when initial() then	initial equation
t0 = time;
end when;	x = x0;
der(x) = u;	y = 0;
	equation  &nbspder(x) = u;
when sample(t0+1/f, 1/f) then
y=f*x;	y = if not yGreaterOrEqualZero then f*pre(x) else max(0.0, f*pre(x));
reinit(x, 0); ...

---

block Blocks.Math.RootMeanSquare

Component	Version 3.2	Version 3.2.1
product	Blocks.Math.Product	Blocks.Math.MultiProduct
mean		final yGreaterOrEqualZero=true

Equations in Version 3.2	Equations in Version 3.2.1
connect(u, product.u1); connect(u, product.u2);
connect(product.y, mean.u); ... connect(sqrt1.y, y);
	connect(u, product.u[1]); connect(u, product.u[2]);

---

block Blocks.Math.Harmonic

Component	Version 3.2	Version 3.2.1
product1	Blocks.Math.Product	Blocks.Math.MultiProduct
product2	Blocks.Math.Product	Blocks.Math.MultiProduct

Equations in Version 3.2	Equations in Version 3.2.1
connect(sin2.y, product2.u2); connect(sin1.y, product1.u1); connect(u, product1.u2); connect(u, product2.u1);
connect(product2.y, mean2.u); ... connect(rectangularToPolar.y_arg, y_arg);
	connect(sin1.y, product1.u[1]); connect(u, product1.u[2]); connect(u, product2.u[1]); connect(sin2.y, product2.u[2]);

---

block Blocks.MathBoolean.MultiSwitch

Component	Version 3.2	Version 3.2.1
y	start=y_default
	fixed=true

Equations in Version 3.2	Equations in Version 3.2.1
firstActiveIndex = Modelica_3_2.Math.BooleanVectors.firstTrueIndex(u);	initial equation
y = if firstActiveIndex == 0 then (if use_pre_as_default then pre(y) else y_default) else expr[firstActiveIndex];	pre(y) = y_default;
	equation    &nbspfirstActiveIndex =      &nbspModelica.Math.BooleanVectors.firstTrueIndex(                                   &nbspu); y = if firstActiveIndex == 0 then (if use_pre_as_default then pre(y) else y_default) else                                     &nbspexpr[firstActiveIndex];

---

block Blocks.MathBoolean.OnDelay

Equations in Version 3.2	Equations in Version 3.2.1
... algorithm
when u then	when initial() then
	delaySignal = u; t_next = time - 1; elsewhen u then
delaySignal = true; ...

---

block Blocks.Nonlinear.Limiter

Component	Version 3.2	Version 3.2.1
strict		Present

Equations in Version 3.2	Equations in Version 3.2.1
... assert(u >= uMin - 0.01*abs(uMin) and              &nbspu <= uMax + 0.01*abs(uMax),              "Limiter: During initialization the limits have been ignored.\n"+              "However, the result is that the input u is not within the required limits:\n"+              " u = " + String(u) + ", uMin = " + String(uMin) + ", uMax = " + String(uMax));
	elseif strict then y = smooth(0, noEvent(if u > uMax then uMax else if u < uMin then uMin else u));
else ...

---

block Blocks.Nonlinear.VariableLimiter

Component	Version 3.2	Version 3.2.1
strict		Present

Equations in Version 3.2	Equations in Version 3.2.1
	if strict then uMax = noEvent(max(limit1, limit2)); uMin = noEvent(min(limit1, limit2)); else
uMax = max(limit1, limit2);
uMin = min(limit1, limit2);
	end if;
if initial() and not limitsAtInit then ... assert(u >= uMin - 0.01*abs(uMin) and              &nbspu <= uMax + 0.01*abs(uMax),              "VariableLimiter: During initialization the limits have been ignored.\n"+              "However, the result is that the input u is not within the required limits:\n"+              " u = " + String(u) + ", uMin = " + String(uMin) + ", uMax = " + String(uMax));
	elseif strict then y = smooth(0, noEvent(if u > uMax then uMax else if u < uMin then uMin else u));
else ...

---

block Blocks.Sources.Ramp

Component	Version 3.2	Version 3.2.1
duration	min=Modelica_3_2.Constants.small	min=0.0

---

block Blocks.Sources.KinematicPTP

Component	Version 3.2	Version 3.2.1
deltaq		={1}
qd_max		={1}
qdd_max		={1}

---

block Blocks.Sources.KinematicPTP2

Component	Version 3.2	Version 3.2.1
q_end		={1}
qd_max		={1}
qdd_max		={1}
r_s	Present
r_sd	Present
r_sdd	Present

Equations in Version 3.2	Equations in Version 3.2.1
... s3 = 0;
r_sdd = 0;	s = 0;
r_sd = 0; r_s = 0;
else ... if time < startTime then
r_sdd = 0;	s = 0;
r_sd = 0; r_s = 0;
elseif noWphase then
if time < Ta1s then
r_sdd = sdd_max;	s = (sdd_max/2)*(time - startTime)*(time - startTime);
r_sd = sdd_max*(time - startTime); r_s = (sdd_max/2)*(time - startTime)*(time - startTime);
elseif time < Tes then
r_sdd = -sdd_max;	s = s1 + sd_max2*(time - Ta1s) - (sdd_max/2)*(time - Ta1s)*(time - Ta1s);
r_sd = sd_max2 - sdd_max*(time - Ta1s); r_s = s1 + sd_max2*(time - Ta1s) - (sdd_max/2)*(time - Ta1s)*(time                 &nbsp- Ta1s);
else
r_sdd = 0;	s = s2;
r_sd = 0; r_s = s2;
end if;
elseif time < Ta2s then
r_sdd = sdd_max;	s = (sdd_max/2)*(time - startTime)*(time - startTime);
r_sd = sdd_max*(time - startTime); r_s = (sdd_max/2)*(time - startTime)*(time - startTime);
elseif time < Tvs then
r_sdd = 0;	s = s1 + sd_max*(time - Ta2s);
r_sd = sd_max; r_s = s1 + sd_max*(time - Ta2s);
elseif time < Tes then
r_sdd = -sdd_max;	s = s2 + sd_max*(time - Tvs) - (sdd_max/2)*(time - Tvs)*(time - Tvs);
r_sd = sd_max - sdd_max*(time - Tvs); r_s = s2 + sd_max*(time - Tvs) - (sdd_max/2)*(time - Tvs)*(time - Tvs);
else
r_sdd = 0;	s = s3;
r_sd = 0; r_s = s3;
end if;
end if;
	sd = der(s); sdd = der(sd);
qdd = p_deltaq*sdd; ... endTime = Tes;
s = position({r_s, r_sd, r_sdd}, time); sd = der(s); sdd = der(sd);
motion_ref = time <= endTime; ...

---

block Blocks.Sources.TimeTable

Component	Version 3.2	Version 3.2.1
table		=fill(0.0, 0, 2)
nextEvent		discrete

---

block Blocks.Sources.BooleanTable

Component	Version 3.2	Version 3.2.1
table		={0,1}

---

block Blocks.Sources.RadioButtonSource

Component	Version 3.2	Version 3.2.1
buttonTimeTable		={0,1}

---

block ComplexBlocks.Sources.ComplexExpression

Component	Version 3.2	Version 3.2.1
y	output

---

model StateGraph.Examples.Utilities.valve

Component	Version 3.2	Version 3.2.1
inflow1	StateGraph.Examples.Utilities.inflow2	StateGraph.Examples.Utilities.Inflow2
outflow1	StateGraph.Examples.Utilities.outflow2	StateGraph.Examples.Utilities.Outflow2

---

model StateGraph.Examples.Utilities.Tank

Component	Version 3.2	Version 3.2.1
inflow1	StateGraph.Examples.Utilities.inflow1	StateGraph.Examples.Utilities.Inflow1
outflow1	StateGraph.Examples.Utilities.outflow1	StateGraph.Examples.Utilities.Outflow1
level		start=0
		fixed=true

---

model StateGraph.Examples.Utilities.Source

Component	Version 3.2	Version 3.2.1
outflow1	StateGraph.Examples.Utilities.outflow1	StateGraph.Examples.Utilities.Outflow1

---

block StateGraph.Interfaces.PartialTransition

Equations in Version 3.2	Equations in Version 3.2.1
initial equation
	if enableTimer then pre(t_start) = time; end if;
pre(enableFire) = false; ...

---

model StateGraph.PartialCompositeStep

Equations in Version 3.2	Equations in Version 3.2.1
initial equation
pre(newActive) = pre(active);	pre(newActive) = false;
...

---

block StateGraph.Temporary.RadioButton

Equations in Version 3.2	Equations in Version 3.2.1
	initial equation pre(reset) = fill(false, size(reset,1));
algorithm ...

---

model Electrical.Analog.Examples.CauerLowPassAnalog

Component	Version 3.2	Version 3.2.1
C1		v(start=0, fixed=true)
C3		v(start=0, fixed=true)
C5		v(start=0, fixed=true)
L1		i(start=0, fixed=true)
L2		i(start=0, fixed=true)
R1		R=1
R2		R=1
V		V=1

---

model Electrical.Analog.Examples.CauerLowPassOPV

Component	Version 3.2	Version 3.2.1
C1		v(start=0, fixed=true)
C2		v(start=0, fixed=true)
C3		v(start=0, fixed=true)
C4		v(start=0, fixed=true)
R1		R=1
R2		R=1
R3		R=1
R6		R=1
R7		R=1
R10		R=1
C7		v(start=0, fixed=true)
R11		R=1
V		V=1

---

model Electrical.Analog.Examples.CauerLowPassSC

Component	Version 3.2	Version 3.2.1
C1		v(start=0, fixed=true)
C2		v(start=0, fixed=true)
C3		v(start=0, fixed=true)
C4		v(start=0, fixed=true)
C7		v(start=0, fixed=true)
V		V=1
R4		Capacitor1(v(start=0, fixed=true))
R5		Capacitor1(v(start=0, fixed=true))
R8		Capacitor1(v(start=0, fixed=true))
R9		Capacitor1(v(start=0, fixed=true))
R1		Capacitor1(v(start=0, fixed=true))
R2		Capacitor1(v(start=0, fixed=true))
R3		Capacitor1(v(start=0, fixed=true))
Rp1		Capacitor1(v(start=0, fixed=true))
R7		Capacitor1(v(start=0, fixed=true))
R10		Capacitor1(v(start=0, fixed=true))
R11		Capacitor1(v(start=0, fixed=true))

---

model Electrical.Analog.Examples.CharacteristicIdealDiodes

Component	Version 3.2	Version 3.2.1
Ideal		Vknee=0
With_Ron_Goff		Vknee=0
SineVoltage1		freqHz=1
SineVoltage2		freqHz=1
SineVoltage3		freqHz=1

---

model Electrical.Analog.Examples.CharacteristicThyristors

Component	Version 3.2	Version 3.2.1
IdealThyristor1	Vknee=5	Vknee=1
		off(start=true, fixed=true)
SineVoltage1		freqHz=1
IdealGTOThyristor1	Vknee=0	Vknee=1
		off(fixed=true, start=true)
BooleanStep1	Present
booleanStep1		Present
IdealThyristor2		Present
R2		Present
IdealGTOThyristor2		Present
R4		Present
booleanPulse		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(IdealThyristor1.n, R3.p);	initial equation
	equation  &nbspconnect(IdealThyristor1.n, R3.p);
connect(Ground1.p, SineVoltage1.n);
connect(SineVoltage1.p, IdealThyristor1.p);
connect(BooleanStep1.y, IdealThyristor1.fire);
connect(IdealGTOThyristor1.n, R1.p);
connect(R3.n, R1.n);
connect(R1.n, Ground1.p);
connect(IdealGTOThyristor1.p, IdealThyristor1.p);
connect(IdealGTOThyristor1.fire, IdealThyristor1.fire);
	connect(IdealThyristor1.fire, booleanStep1.y); connect(IdealThyristor2.n,R2. p); connect(IdealGTOThyristor2.n,R4. p); connect(R2.n,R4. n); connect(IdealGTOThyristor2.p,IdealThyristor2. p); connect(IdealGTOThyristor2.fire,IdealThyristor2. fire); connect(R4.n, Ground1.p); connect(R2.n, R1.n); connect(SineVoltage1.p, IdealThyristor2.p); connect(booleanPulse.y, IdealThyristor2.fire);

---

model Electrical.Analog.Examples.ChuaCircuit

Component	Version 3.2	Version 3.2.1
L		i(start=0, fixed=true)
C1	v(start=4)	v(start=4, fixed=true)
C2		v(start=0, fixed=true)

---

model Electrical.Analog.Examples.DifferenceAmplifier

Component	Version 3.2	Version 3.2.1
C1		v(start=0, fixed=true)
C4		v(start=0, fixed=true)
C5		v(start=0, fixed=true)
C2		v(start=0, fixed=true)
C3		v(start=0, fixed=true)
Transistor1		ct(v(start=0, fixed=true))
Transistor2		ct(v(start=0, fixed=true))

---

model Electrical.Analog.Examples.HeatingMOSInverter

Component	Version 3.2	Version 3.2.1
Capacitor1		v(start=0, fixed=true)

Equations in Version 3.2	Equations in Version 3.2.1
connect(Sin.n, G.p);	initial equation
	HeatCapacitor1.T= 293.15; equation  &nbspconnect(Sin.n, G.p);
connect(Capacitor1.n, G.p); ...

---

model Electrical.Analog.Examples.HeatingNPN_OrGate

Component	Version 3.2	Version 3.2.1
CapVal	constant	parameter
tauVal	constant	parameter
T1		ibe(start=0)
		vbc(start=0)
T2		ibe(start=0)
		vbc(start=0)

Equations in Version 3.2	Equations in Version 3.2.1
connect(Gnd1.p, V1.n);	initial equation
	HeatCapacitor1.T= 293.15; equation  &nbspconnect(Gnd1.p, V1.n);
connect(V1.p, R1.p); ...

---

model Electrical.Analog.Examples.HeatingResistor

Component	Version 3.2	Version 3.2.1
heatingResistor		i(start=0)

---

model Electrical.Analog.Examples.HeatingRectifier

Component	Version 3.2	Version 3.2.1
Capacitor1		v(start=0, fixed=true)

Equations in Version 3.2	Equations in Version 3.2.1
connect(SineVoltage1.p, HeatingDiode1.p);	initial equation
	HeatCapacitor1.T = 293.15; equation  &nbspconnect(SineVoltage1.p, HeatingDiode1.p);
connect(SineVoltage1.n, G.p); ...

---

model Electrical.Analog.Examples.NandGate

Component	Version 3.2	Version 3.2.1
VIN1		nperiod=-1
VIN2		nperiod=-1
Nand		C4(v(start=0, fixed=true))
		C7(v(start=0, fixed=true))

---

model Electrical.Analog.Examples.OvervoltageProtection

Component	Version 3.2	Version 3.2.1
CL		v(start=0, fixed=true)
zDiode1		v(start=0)

---

model Electrical.Analog.Examples.Rectifier

Component	Version 3.2	Version 3.2.1
Inductor2		i(start=0, fixed=true)
Inductor3		i(start=0, fixed=true)

---

model Electrical.Analog.Examples.ShowSaturatingInductor

Component	Version 3.2	Version 3.2.1
SaturatingInductance1		i(start=0)
Inductance1		i(start=0, fixed=true)

---

model Electrical.Analog.Examples.ShowVariableResistor

Component	Version 3.2	Version 3.2.1
R1		R=1
R2		R=1
R3		R=1
R4		R=1
R5		R=1
SineVoltage1		V=1
		freqHz=1
Ramp1		duration=2

---

model Electrical.Analog.Examples.SwitchWithArc

Component	Version 3.2	Version 3.2.1
booleanPulse		period=1
inductor1		i(start=0, fixed=true)
resistor1		R=1
inductor2		i(start=0, fixed=true)
resistor2		R=1
switch2		dVdt=10000
		V0=30
		Vmax=60

---

model Electrical.Analog.Examples.ThyristorBehaviourTest

Component	Version 3.2	Version 3.2.1
thyristor_v4_1		vControl(fixed=true)
		vAK(start=0)
		vGK(start=0)
inductor		i(start=0, fixed=true)

---

model Electrical.Analog.Examples.AmplifierWithOpAmpDetailed

Equations in Version 3.2	Equations in Version 3.2.1
connect(resistor.n, opAmp.m);	initial equation
	resistor2.i = 0; opAmp.q_fp1 = 0; opAmp.q_fr1 = 0; opAmp.q_fr2 = 0; opAmp.q_fr3 = 0; equation  &nbspconnect(resistor.n, opAmp.m);
connect(resistor1.n, resistor2.p); ...

---

model Electrical.Analog.Examples.CompareTransformers

Component	Version 3.2	Version 3.2.1
inductor22		i(start=0, fixed=true)

Equations in Version 3.2	Equations in Version 3.2.1
connect(sineVoltage1.n, ground11.p);	initial equation
	basicTransformer.i1=0; basicTransformer.i2=0; equation  &nbspconnect(sineVoltage1.n, ground11.p);
connect(sineVoltage1.p, resistor11.p); ...

---

model Electrical.Analog.Examples.ControlledSwitchWithArc

Component	Version 3.2	Version 3.2.1
resistor1		R=1
resistor2		R=1
switch2		V0=30
		dVdt=10000
		Vmax=60

Equations in Version 3.2	Equations in Version 3.2.1
connect(inductor1.n,resistor1. p);	initial equation
	inductor1.i = 0; inductor2.i = 0; equation  &nbspconnect(inductor1.n,resistor1. p);
connect(resistor1.n,ground1. p); ...

---

model Electrical.Analog.Examples.SimpleTriacCircuit

Component	Version 3.2	Version 3.2.1
L		i(start=0, fixed=true)
		p(v(start=0))
simpleTriac		thyristor1(vGK(start=0))

Equations in Version 3.2	Equations in Version 3.2.1
connect(L.n, R.p);	initial equation
	simpleTriac.thyristor.vControl=0; simpleTriac.thyristor1.vControl=0; equation  &nbspconnect(L.n, R.p);
connect(R.n, V.p); ...

---

model Electrical.Analog.Examples.IdealTriacCircuit

Component	Version 3.2	Version 3.2.1
idealTriac		capacitor(v(start=0, fixed=true))
		idealThyristor(off(start=true, fixed=true))
		idealThyristor1(off(start=true, fixed=true))

---

model Electrical.Analog.Examples.AD_DA_conversion

Component	Version 3.2	Version 3.2.1
aD_Converter		Rin=1000000
		VRefLow=0
		VRefHigh=10
dA_Converter		Vref=10

---

model Electrical.Analog.Examples.Utilities.Transistor

Component	Version 3.2	Version 3.2.1
Tr		UIC=true

---

model Electrical.Analog.Basic.SaturatingInductor

Component	Version 3.2	Version 3.2.1
Psi		start=0
		fixed=true

---

model Electrical.Analog.Basic.Transformer

Component	Version 3.2	Version 3.2.1
dv		Present

Equations in Version 3.2	Equations in Version 3.2.1
v1 = L1*der(i1) + M*der(i2);
v2 = M*der(i1) + L2*der(i2);	dv = (L1 - M)*der(i1) + (M - L2)*der(i2);
	v2 = v1 - dv;

---

model Electrical.Analog.Basic.M_Transformer

Component	Version 3.2	Version 3.2.1
p	extent=[-80, -40; -62, 40]
n	extent=[62, -40; 80, 40]
i		each start=0
		fixed=true
Lm		parameter
		each final fixed=false

Equations in Version 3.2	Equations in Version 3.2.1
algorithm	initial equation
for s in 1:N loop ...

---

model Electrical.Analog.Basic.OpAmp

Component	Version 3.2	Version 3.2.1
Slope	start=1	start=10000

Equations in Version 3.2	Equations in Version 3.2.1
... f = 2/(VMax.v - VMin.v);
absSlope = smooth(0,(if (Slope < 0) then -Slope else Slope));	absSlope = if (Slope < 0) then -Slope else Slope;
out.v = (VMax.v + VMin.v)/2 + absSlope*vin/(1 + absSlope*smooth(0,(if (f*vin      < 0) then -f*vin else f*vin)));

---

model Electrical.Analog.Basic.VariableResistor

Component	Version 3.2	Version 3.2.1
R		unit="Ohm"

---

model Electrical.Analog.Basic.VariableConductor

Component	Version 3.2	Version 3.2.1
G		unit="S"

---

model Electrical.Analog.Basic.VariableCapacitor

Component	Version 3.2	Version 3.2.1
C		unit="F"
IC		Present
UIC		Present

Equations in Version 3.2	Equations in Version 3.2.1
assert(C>=0,"Capacitance C (= " + String(C) + ") has to be >= 0!");	initial equation
Q = noEvent(max(C,Cmin))*v;	if UIC then
i = der(Q);	v = IC;
	end if; equation  &nbspassert(C>=0,"Capacitance C (= " +         &nbspString(C) + ") has to be >= 0!"); Q = noEvent(max(C,Cmin))*v; i = der(Q);

---

model Electrical.Analog.Basic.VariableInductor

Component	Version 3.2	Version 3.2.1
L		unit="H"
IC		Present
UIC		Present

Equations in Version 3.2	Equations in Version 3.2.1
assert(L>=0,"Inductance L_ (= " + String(L) + ") has to be >= 0!");	initial equation
Psi = noEvent(max(L,Lmin))*i;	if UIC then
v = der(Psi);	i = IC;
	end if; equation  &nbspassert(L>=0,"Inductance L_ (= " +         &nbspString(L) + ") has to be >= 0!"); Psi = noEvent(max(L,Lmin))*i; v = der(Psi);

---

model Electrical.Analog.Ideal.IdealDiode

Component	Version 3.2	Version 3.2.1
s		start=0

---

model Electrical.Analog.Ideal.OpenerWithArc

Component	Version 3.2	Version 3.2.1
quenched		fixed=true

---

model Electrical.Analog.Ideal.CloserWithArc

Component	Version 3.2	Version 3.2.1
off	=not on
		start=false
		fixed=true
quenched		fixed=true

Equations in Version 3.2	Equations in Version 3.2.1
	off = not on;
when edge(off) then ...

---

model Electrical.Analog.Ideal.ControlledCloserWithArc

Component	Version 3.2	Version 3.2.1
off	=(control.v < level)
		start=false
		fixed=true
quenched		fixed=true

Equations in Version 3.2	Equations in Version 3.2.1
	off =(control.v < level);
control.i = 0; ...

---

model Electrical.Analog.Ideal.AD_Converter

Equations in Version 3.2	Equations in Version 3.2.1
... algorithm
when (trig==4 or trig==8) then	when (trig==L.'1' or trig==L.'H') then
z= if u>VRefLow then integer((u-VRefLow)/(VRefHigh-VRefLow)*(2^N - 1) + 0.5) else 0; ...

---

model Electrical.Analog.Ideal.DA_Converter

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
when trig==4 or trig==8 then	when trig==L.'1' or trig==L.'H' then
y= 0;
for i in 1:N loop
y = if ( x[i] == 4 or x[i] == 8) then y + 2^(i-1) else y;	y = if ( x[i] == L.'1' or x[i] == L.'H') then y + 2^(i-1) else y;
end for; ...

---

model Electrical.Analog.Lines.OLine

Component	Version 3.2	Version 3.2.1
R		T_ref=fill(T_ref, N + 1)
		alpha=fill(alpha_R, N + 1)
		useHeatPort=fill(useHeatPort, N + 1)
		T=fill(T, N + 1)
G		T_ref=fill(T_ref, N)
		alpha=fill(alpha_G, N)
		useHeatPort=fill(useHeatPort, N)
		T=fill(T, N)
alpha_R		Present
alpha_G		Present
useHeatPort		Present
T		Present
T_ref		Present
heatPort		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(L[N + 1].n, p2);
	if useHeatPort then for i in 1:N + 1 loop connect(heatPort, R[i].heatPort); end for; for i in 1:N loop connect(heatPort, G[i].heatPort); end for; end if;

---

model Electrical.Analog.Lines.M_OLine

Component	Version 3.2	Version 3.2.1
N	final min=1	final min=2
r	final min=Modelica_3_2.Constants.small
	unit="Ohm/m"
		each final min=Modelica.Constants.small
		each unit="Ohm/m"
l	final min=Modelica_3_2.Constants.small
	unit="H/m"
		each final min=Modelica.Constants.small
		each unit="H/m"
g	final min=Modelica_3_2.Constants.small
	unit="S/m"
		each final min=Modelica.Constants.small
		each unit="S/m"
c	final min=Modelica_3_2.Constants.small
	unit="F/m"
		each final min=Modelica.Constants.small
		each unit="F/m"
s		alpha_R=fill(alpha_R, N - 1)
		alpha_G=fill(alpha_G, N - 1)
		T_ref=fill(T_ref, N - 1)
		useHeatPort=fill(useHeatPort, N - 1)
		T=fill(T, N - 1)
s_first		alpha_R=alpha_R
		alpha_G=alpha_G
		T_ref=T_ref
		useHeatPort=useHeatPort
		T=T
s_last		alpha_R=alpha_R
		T_ref=T_ref
		useHeatPort=useHeatPort
		T=T
alpha_R		Present
alpha_G		Present
useHeatPort		Present
T		Present
T_ref		Present
heatPort		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(s_last.n,n);
	if useHeatPort then connect(heatPort, s_first.heatPort); for i in 1:N - 1 loop connect(heatPort, s[i].heatPort); end for; connect(heatPort, s_last.heatPort); end if;

---

model Electrical.Analog.Lines.ULine

Component	Version 3.2	Version 3.2.1
R		T_ref=fill(T_ref, N + 1)
		alpha=fill(alpha, N + 1)
		useHeatPort=fill(useHeatPort, N + 1)
		T=fill(T, N + 1)
alpha		Present
useHeatPort		Present
T		Present
T_ref		Present
heatPort		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(R[N + 1].n, p2);
	if useHeatPort then for i in 1:N + 1 loop connect(heatPort, R[i].heatPort); end for; end if;

---

model Electrical.Analog.Lines.TLine2

Component	Version 3.2	Version 3.2.1
TD		parameter
		=NL/F

Equations in Version 3.2	Equations in Version 3.2.1
... assert(F > 0, "F has to be positive");
TD = NL/F;
i1 = (v1 - es)/Z0; ...

---

model Electrical.Analog.Lines.TLine3

Component	Version 3.2	Version 3.2.1
TD		parameter
		=1/F/4

Equations in Version 3.2	Equations in Version 3.2.1
... assert(F > 0, "F has to be positive");
TD = 1/F/4;
i1 = (v1 - es)/Z0; ...

---

model Electrical.Analog.Semiconductors.NPN

Component	Version 3.2	Version 3.2.1
IC		Present
UIC		Present

Equations in Version 3.2	Equations in Version 3.2.1
ExMin = exp(EMin);	initial equation
	if UIC then C.v = IC; end if; equation  &nbspExMin = exp(EMin);
ExMax = exp(EMax); ...

---

model Electrical.Analog.Semiconductors.Thyristor

Equations in Version 3.2	Equations in Version 3.2.1
... vConmain = (if Anode.i>IH or vAK>VDRM then Von else 0);
	LossPower = Anode.i*Anode.v + Cathode.i*Cathode.v + Gate.i*Gate.v;

---

model Electrical.Analog.Semiconductors.SimpleTriac

Component	Version 3.2	Version 3.2.1
thyristor		useHeatPort=useHeatPort
		T=T
thyristor1		useHeatPort=useHeatPort
		T=T
useHeatPort		Present
T		Present
heatPort		Present

Equations in Version 3.2	Equations in Version 3.2.1
	if useHeatPort then connect(heatPort, thyristor.heatPort); connect(heatPort, thyristor1.heatPort); end if;
connect(thyristor.Anode, n); ...

---

model Electrical.Analog.Sensors.PotentialSensor

Component	Version 3.2	Version 3.2.1
phi		unit="V"

---

model Electrical.Analog.Sensors.VoltageSensor

Component	Version 3.2	Version 3.2.1
v		unit="V"

---

model Electrical.Analog.Sensors.CurrentSensor

Component	Version 3.2	Version 3.2.1
i		unit="A"

---

model Electrical.Analog.Sensors.PowerSensor

Component	Version 3.2	Version 3.2.1
power		unit="W"

---

model Electrical.Analog.Sources.SignalVoltage

Component	Version 3.2	Version 3.2.1
v		unit="V"

---

model Electrical.Analog.Sources.SignalCurrent

Component	Version 3.2	Version 3.2.1
i		unit="A"

---

model Electrical.Digital.Examples.Multiplexer

Component	Version 3.2	Version 3.2.1
CLK		startTime=0
		width=50
D0	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
D1	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
D2	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
D3	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
Enable		x=Modelica.Electrical.Digital.Interfaces.Logic.'1'

---

model Electrical.Digital.Examples.FlipFlop

Component	Version 3.2	Version 3.2.1
CLK		startTime=0
		width=50
J	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
K	y0=3	y0=L.'0'
	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}

---

model Electrical.Digital.Examples.HalfAdder

Component	Version 3.2	Version 3.2.1
a	x={4,3,4,3}	x={L.'1',L.'0',L.'1',L.'0'}
	y0=3	y0=L.'0'
b	x={4,3}	x={L.'1',L.'0'}
	y0=3	y0=L.'0'
Adder		AND(G2(y(start=L.'U', fixed=true)))
		XOR(G2(y(start=L.'U', fixed=true)))
s		n=1
		value_U=0.5
		value_X=0.5
		value_0=0
		value_1=1
		value_Z=0.5
		value_W=0.5
		value_L=0
		value_H=1
		value_m=0.5
c		n=1
		value_U=0.5
		value_X=0.5
		value_0=0
		value_1=1
		value_Z=0.5
		value_W=0.5
		value_L=0
		value_H=1
		value_m=0.5

---

model Electrical.Digital.Examples.FullAdder

Component	Version 3.2	Version 3.2.1
s		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1
c_out		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1
CLK		period=1
		startTime=0
		width=50

---

model Electrical.Digital.Examples.Adder4

Component	Version 3.2	Version 3.2.1
b4	y0=3	y0=L.'0'
	x={4,3}	x={L.'1',L.'0'}
b1	x={4,3,4}	x={L.'1',L.'0',L.'1'}
	y0=3	y0=L.'0'
b2	y0=3	y0=L.'0'
	x={4}	x={L.'1'}
b3	y0=3	y0=L.'0'
	x={4}	x={L.'1'}
a1	y0=3	y0=L.'0'
	x={4,3,4}	x={L.'1',L.'0',L.'1'}
a2	y0=3	y0=L.'0'
	x={4}	x={L.'1'}
a3	y0=3	y0=L.'0'
	x={4,3}	x={L.'1',L.'0'}
a4	y0=3	y0=L.'0'
	x={3}	x={L.'0'}
Set	x=3	x=L.'0'
Adder1		Adder1(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
		Adder2(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
Adder2		Adder1(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
		Adder2(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
Adder3		Adder1(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
		Adder2(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
Adder4		Adder1(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))
		Adder2(AND(G2(y(start=L.'U', fixed=true))), XOR(G2(y(start=L.'U', fixed=true))))

---

model Electrical.Digital.Examples.Counter3

Component	Version 3.2	Version 3.2.1
Enable		after=D.Interfaces.Logic.'1'
		before=D.Interfaces.Logic.'0'
		stepTime=1
Clock		period=1
		startTime=0
		width=50

---

model Electrical.Digital.Examples.Counter

Component	Version 3.2	Version 3.2.1
Enable		after=D.Interfaces.Logic.'1'
		before=D.Interfaces.Logic.'0'
		stepTime=1
Clock		period=1
		startTime=0
		width=50
Q0		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1
Q1		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1
Q2		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1
Q3		value_0=0
		value_1=1
		value_H=1
		value_L=0
		value_m=0.5
		value_U=0.5
		value_W=0.5
		value_X=0.5
		value_Z=0.5
		n=1

---

model Electrical.Digital.Examples.VectorDelay

Component	Version 3.2	Version 3.2.1
delay		inertialDelaySensitive(each y(start=L.'U', fixed=true))
table	x={3,4,3,4,3}	x={L.'0',L.'1',L.'0',L.'1',L.'0'}
table1	x={3,4}	x={L.'0',L.'1'}
table2	x={3,4,3}	x={L.'0',L.'1',L.'0'}

---

model Electrical.Digital.Examples.DFFREG

Component	Version 3.2	Version 3.2.1
clock	x={3,4,3,4,3,4,3}	x={L.'0',L.'1',L.'0',L.'1',L.'0',L.'1',L.'0'}
data_0	x={4,3}	x={L.'1',L.'0'}
reset	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_1	x={8,2}	x={L.'H',L.'X'}
dFFREG		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))
		dFFR(clock(start=L.'U', fixed=true), reset(start=L.'U', fixed=true))

---

model Electrical.Digital.Examples.DFFREGL

Component	Version 3.2	Version 3.2.1
clock	x={3,4,3,4,3,4,3}	x={L.'0',L.'1',L.'0',L.'1',L.'0',L.'1',L.'0'}
data_0	x={4,3}	x={L.'1',L.'0'}
reset	x={4,3,4}	x={L.'1',L.'0',L.'1'}
data_1	x={8,2}	x={L.'H',L.'X'}
dFFREGL		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))
		dFFR(clock(start=L.'U', fixed=true), reset(start=L.'U', fixed=true))

---

model Electrical.Digital.Examples.DFFREGSRH

Component	Version 3.2	Version 3.2.1
clock	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6}	x={L.'W'}
reset	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_1	x={3}	x={L.'0'}
set	x={3,4,3}	x={L.'0',L.'1',L.'0'}

---

model Electrical.Digital.Examples.DFFREGSRL

Component	Version 3.2	Version 3.2.1
clock	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6}	x={L.'W'}
reset	x={4,3,4}	x={L.'1',L.'0',L.'1'}
data_1	x={3}	x={L.'0'}
set	x={4,3,4}	x={L.'1',L.'0',L.'1'}

---

model Electrical.Digital.Examples.DLATREG

Component	Version 3.2	Version 3.2.1
enable	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6,4}	x={L.'W',L.'1'}
reset	x={3,4,3,4,3}	x={L.'0',L.'1',L.'0',L.'1',L.'0'}
data_1	x={3,4}	x={L.'0',L.'1'}
dLATREG		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))

---

model Electrical.Digital.Examples.DLATREGL

Component	Version 3.2	Version 3.2.1
enable	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6,4}	x={L.'W',L.'1'}
reset	x={4,3,4,3,4}	x={L.'1',L.'0',L.'1',L.'0',L.'1'}
data_1	x={3,4}	x={L.'0',L.'1'}
dLATREGL		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))

---

model Electrical.Digital.Examples.DLATREGSRH

Component	Version 3.2	Version 3.2.1
enable	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6,4}	x={L.'W',L.'1'}
reset	x={3,4,3,4,3}	x={L.'0',L.'1',L.'0',L.'1',L.'0'}
data_1	x={3,4}	x={L.'0',L.'1'}
set	x={3,4,3}	x={L.'0',L.'1',L.'0'}
dLATREGSRH		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))

---

model Electrical.Digital.Examples.DLATREGSRL

Component	Version 3.2	Version 3.2.1
enable	x={3,4,3}	x={L.'0',L.'1',L.'0'}
data_0	x={6,4}	x={L.'W',L.'1'}
reset	x={4,3,4,3,4}	x={L.'1',L.'0',L.'1',L.'0',L.'1'}
data_1	x={3,4}	x={L.'0',L.'1'}
set	x={4,3,4}	x={L.'1',L.'0',L.'1'}
dLATREGSRL		delay(inertialDelaySensitive(each y(start=L.'U', fixed=true)))

---

model Electrical.Digital.Examples.NXFER

Component	Version 3.2	Version 3.2.1
e_table	x={3,4,5}	x={L.'0',L.'1',L.'Z'}
x_table	x={4,3}	x={L.'1',L.'0'}

---

model Electrical.Digital.Examples.NRXFER

Component	Version 3.2	Version 3.2.1
e_table	x={3,4,5}	x={L.'0',L.'1',L.'Z'}
x_table	x={4,3}	x={L.'1',L.'0'}

---

model Electrical.Digital.Examples.BUF3S

Component	Version 3.2	Version 3.2.1
e_table	x={3,4,5}	x={L.'0',L.'1',L.'Z'}
x_table	x={4,3}	x={L.'1',L.'0'}

---

model Electrical.Digital.Examples.INV3S

Component	Version 3.2	Version 3.2.1
e_table	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={3,4,5}	x={L.'0',L.'1',L.'Z'}
x_table	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={4,3}	x={L.'1',L.'0'}

---

model Electrical.Digital.Examples.WiredX

Component	Version 3.2	Version 3.2.1
e_table2	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={3,4,3}	x={L.'0',L.'1',L.'0'}
x_table2	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={4,3}	x={L.'1',L.'0'}
e_table1	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={3,4,3}	x={L.'0',L.'1',L.'0'}
x_table1	y0=Modelica_3_2.Electrical.Digital.Interfaces.Logic.'U'	y0=L.'U'
	x={3,4,3}	x={L.'0',L.'1',L.'0'}

---

model Electrical.Digital.Examples.Utilities.DFF

Equations in Version 3.2	Equations in Version 3.2.1
... connect(Not1.y, RSFF1.r);
connect(clk, RSFF1.clk);
connect(d, Not1.x);
connect(d, RSFF1.s);
	connect(clk, RSFF1.clk);

---

model Electrical.Digital.Examples.Utilities.HalfAdder

Component	Version 3.2	Version 3.2.1
AND		G2(y(start=L.'U', fixed=true))
XOR		G2(y(start=L.'U', fixed=true))

---

package Electrical.Digital.Tables

Component	Version 3.2	Version 3.2.1
MUX2x1Table		Present

---

model Electrical.Digital.Delay.TransportDelay

Component	Version 3.2	Version 3.2.1
LogicValues		Present

Equations in Version 3.2	Equations in Version 3.2.1
x_delayed = integer(delay(x, delayTime));	x_delayed = LogicValues[integer(delay(Integer(pre(x)), delayTime))];
y = if delayTime > 0 then           (if time >= delayTime then x_delayed else y0) else            &nbsppre(x);

---

model Electrical.Digital.Delay.InertialDelaySensitive

Component	Version 3.2	Version 3.2.1
delayTable		constant

Equations in Version 3.2	Equations in Version 3.2.1
... when {initial(),(tLH > 0 or tHL > 0) and change(x) and not initial()} then
y_old = if initial() or pre(y) == 0 then y0 else pre(y);	y_old = if initial() or pre(y) == L.'U' then y0 else pre(y);
lh = delayTable[y_old, x]; ...

---

model Electrical.Digital.Basic.And

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(auxiliary[n]);	auxiliary_n = auxiliary[n];
	y = pre(auxiliary_n);

---

model Electrical.Digital.Basic.Nand

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(Modelica_3_2.Electrical.Digital.Tables.NotTable[auxiliary[n]]);	auxiliary_n = Modelica.Electrical.Digital.Tables.NotTable[auxiliary[n]];
	y = pre(auxiliary_n);

---

model Electrical.Digital.Basic.Or

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(auxiliary[n]);	auxiliary_n = auxiliary[n];
	y = pre(auxiliary_n);

---

model Electrical.Digital.Basic.Nor

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(Modelica_3_2.Electrical.Digital.Tables.NotTable[auxiliary[n]]);	auxiliary_n = Modelica.Electrical.Digital.Tables.NotTable[auxiliary[n]];
	y = pre(auxiliary_n);

---

model Electrical.Digital.Basic.Xor

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(auxiliary[n]);	auxiliary_n = auxiliary[n];
	y = pre(auxiliary_n);

---

model Electrical.Digital.Basic.Xnor

Component	Version 3.2	Version 3.2.1
auxiliary	each fixed=true
auxiliary_n		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end for;
y = pre(Modelica_3_2.Electrical.Digital.Tables.NotTable[auxiliary[n]]);	auxiliary_n = Modelica.Electrical.Digital.Tables.NotTable[auxiliary[n]];
	y = pre(auxiliary_n);

---

block Electrical.Digital.Sources.Step

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
when initial() then y = before; end when;
if time >= stepTime then ...

---

block Electrical.Digital.Sources.Table

Component	Version 3.2	Version 3.2.1
x	={1}	={L.'1'}

---

model Electrical.Digital.Sources.Clock

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
when sample(startTime, period) then ... y = if (not time>=startTime) or time >= t_i + t_width then L.'0' else L.'1';

---

block Electrical.Digital.Converters.LogicToBoolean

Equations in Version 3.2	Equations in Version 3.2.1
for i in 1:n loop
y[i] = if x[i] == 4 or x[i] == 8 then true else false;	y[i] = if x[i] == L.'1' or x[i] == L.'H' then true else false;
end for;

---

model Electrical.Digital.Registers.DFFREG

Equations in Version 3.2	Equations in Version 3.2.1
connect(dataOut, dataOut);
connect(delay.y, dataOut); ...

---

model Electrical.Digital.Registers.DFFREGSRH

Component	Version 3.2	Version 3.2.1
delay		inertialDelaySensitive(each y(start=L.'U', fixed=true))
dFFSR		clock(start=L.'U', fixed=true)
		reset(start=L.'U', fixed=true)
		set(start=L.'U', fixed=true)

---

model Electrical.Digital.Registers.DLATREG

Equations in Version 3.2	Equations in Version 3.2.1
connect(dataOut, dataOut);
connect(delay.y, dataOut); ...

---

model Electrical.Digital.Registers.DLATREGSRH

Equations in Version 3.2	Equations in Version 3.2.1
connect(dataOut, dataOut);
connect(delay.y, dataOut); ...

---

model Electrical.Digital.Tristates.NXFERGATE

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL
		y(start=L.'U', fixed=true)

---

model Electrical.Digital.Tristates.NRXFERGATE

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL
		y(start=L.'U', fixed=true)

---

model Electrical.Digital.Tristates.PXFERGATE

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL

---

model Electrical.Digital.Tristates.PRXFERGATE

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL

---

model Electrical.Digital.Tristates.BUF3S

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL
		y(start=L.'U', fixed=true)

---

model Electrical.Digital.Tristates.BUF3SL

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL

---

model Electrical.Digital.Tristates.INV3S

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL
		y(start=L.'U', fixed=true)

---

model Electrical.Digital.Tristates.INV3SL

Component	Version 3.2	Version 3.2.1
inertialDelaySensitive	each tLH=tLH
	each tHL=tHL
		tLH=tLH
		tHL=tHL

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_DOL

Component	Version 3.2	Version 3.2.1
aimc		p=aimcData.p
		fsNominal=aimcData.fsNominal
		Rs=aimcData.Rs
		TsRef=aimcData.TsRef
		alpha20s(displayUnit="1/K") = aimcData.alpha20s
		Lszero=aimcData.Lszero
		Lssigma=aimcData.Lssigma
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		Lm=aimcData.Lm
		Lrsigma=aimcData.Lrsigma
		Rr=aimcData.Rr
		TrRef=aimcData.TrRef
		TsOperational=293.15
		alpha20r=aimcData.alpha20r
		TrOperational=293.15
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
aimcData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimc.is=zeros(3); aimc.ir=zeros(2); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ...

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_YD

Component	Version 3.2	Version 3.2.1
aimc		p=aimcData.p
		fsNominal=aimcData.fsNominal
		Rs=aimcData.Rs
		TsRef=aimcData.TsRef
		alpha20s(displayUnit="1/K") = aimcData.alpha20s
		Lszero=aimcData.Lszero
		Lssigma=aimcData.Lssigma
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		Lm=aimcData.Lm
		Lrsigma=aimcData.Lrsigma
		Rr=aimcData.Rr
		TrRef=aimcData.TrRef
		TsOperational=293.15
		alpha20r=aimcData.alpha20r
		TrOperational=293.15
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
switchYD		m=m
aimcData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimc.is=zeros(3); aimc.ir=zeros(2); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ...

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_Transformer

Component	Version 3.2	Version 3.2.1
aimc		p=aimcData.p
		fsNominal=aimcData.fsNominal
		Rs=aimcData.Rs
		TsRef=aimcData.TsRef
		alpha20s(displayUnit="1/K") = aimcData.alpha20s
		Lszero=aimcData.Lszero
		Lssigma=aimcData.Lssigma
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		Lm=aimcData.Lm
		Lrsigma=aimcData.Lrsigma
		Rr=aimcData.Rr
		TrRef=aimcData.TrRef
		TsOperational=293.15
		alpha20r=aimcData.alpha20r
		TrOperational=293.15
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
transformer		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15
transformerData		parameter
idealCommutingSwitch	Goff=fill(5E-4, m)	Goff=fill(50E-5, m)
		Ron=fill(1e-5, m)
aimcData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimc.is=zeros(3); aimc.ir=zeros(2); transformer.i1[1:2]=zeros(2); equation  &nbspconnect(star.pin_n, ground.p);
connect(terminalBox.plug_sn, aimc.plug_sn); ...

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMS_Start

Component	Version 3.2	Version 3.2.1
Rstart	=0.16	=0.16/aimsData.turnsRatio^2
aims		p=aimsData.p
		Jr=aimsData.Jr
		Js=aimsData.Js
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		useTurnsRatio=aimsData.useTurnsRatio
		turnsRatio=aimsData.turnsRatio
		VsNominal=aimsData.VsNominal
		VrLockedRotor=aimsData.VrLockedRotor
		Rs=aimsData.Rs
		TsRef=aimsData.TsRef
		Lszero=aimsData.Lszero
		Lssigma=aimsData.Lssigma
		Lm=aimsData.Lm
		Lrsigma=aimsData.Lrsigma
		Lrzero=aimsData.Lrzero
		Rr=aimsData.Rr
		TrRef=aimsData.TrRef
		frictionParameters=aimsData.frictionParameters
		statorCoreParameters=aimsData.statorCoreParameters
		strayLoadParameters=aimsData.strayLoadParameters
		rotorCoreParameters=aimsData.rotorCoreParameters
		fsNominal=aimsData.fsNominal
		TsOperational=293.15
		alpha20s=aimsData.alpha20s
		alpha20r=aimsData.alpha20r
		TrOperational=293.15
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
switchedRheostat		m=m
aimsData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aims.is=zeros(3); aims.ir=zeros(3); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ...

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_Inverter

Component	Version 3.2	Version 3.2.1
aimc		p=aimcData.p
		fsNominal=aimcData.fsNominal
		Rs=aimcData.Rs
		TsRef=aimcData.TsRef
		alpha20s(displayUnit="1/K") = aimcData.alpha20s
		Lszero=aimcData.Lszero
		Lssigma=aimcData.Lssigma
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		Lm=aimcData.Lm
		Lrsigma=aimcData.Lrsigma
		Rr=aimcData.Rr
		TrRef=aimcData.TrRef
		TsOperational=293.15
		alpha20r=aimcData.alpha20r
		TrOperational=293.15
loadTorqueStep		offsetTorque=0
aimcData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(signalVoltage.plug_n, star.plug_p);	initial equation
	aimc.is[1:2]=zeros(2); aimc.ir=zeros(2); equation  &nbspconnect(signalVoltage.plug_n, star.plug_p);
connect(star.pin_n, ground.p); ...

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_Steinmetz

Component	Version 3.2	Version 3.2.1
aimc	useSupport=true
		p=aimcData.p
		fsNominal=aimcData.fsNominal
		Rs=aimcData.Rs
		TsRef=aimcData.TsRef
		alpha20s(displayUnit="1/K") = aimcData.alpha20s
		Lszero=aimcData.Lszero
		Lssigma=aimcData.Lssigma
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		Lm=aimcData.Lm
		Lrsigma=aimcData.Lrsigma
		Rr=aimcData.Rr
		TrRef=aimcData.TrRef
		TsOperational=293.15
		alpha20r=aimcData.alpha20r
		TrOperational=293.15
quadraticLoadTorque		useSupport=false
relSpeedSensor	Mechanics.Rotational.Sensors.RelSpeedSensor	Mechanics.Rotational.Sensors.SpeedSensor
fixed	Present
aimcData		Present
currentQuasiRMSSensor		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(ground.p, sineVoltage.n);	initial equation
	aimc.is=zeros(3); aimc.ir=zeros(2); cStart.v=0; cRun.v = 0; equation  &nbspconnect(ground.p, sineVoltage.n);
connect(sineVoltage.p, idealCloser.p); ... connect(TerminalBox1.plug_sp, aimc.plug_sp);
connect(TerminalBox1.plugSupply, plugToPin_p2.plug_p);	connect(aimc.flange, loadInertia.flange_a);
connect(TerminalBox1.plugSupply, plugToPin_p3.plug_p);	connect(relSpeedSensor.flange, aimc.flange);
connect(TerminalBox1.plugSupply, plugToPin_p1.plug_p);	connect(relSpeedSensor.w, greaterThreshold.u);
connect(quadraticLoadTorque.support, fixed.flange);	connect(plugToPin_p3.plug_p, currentQuasiRMSSensor.plug_p);
connect(relSpeedSensor.flange_a, fixed.flange);	connect(plugToPin_p2.plug_p, currentQuasiRMSSensor.plug_p);
connect(relSpeedSensor.w_rel, greaterThreshold.u);	connect(plugToPin_p1.plug_p, currentQuasiRMSSensor.plug_p);
connect(aimc.support, fixed.flange);	connect(currentQuasiRMSSensor.plug_n, TerminalBox1.plugSupply);
connect(aimc.flange, relSpeedSensor.flange_b); connect(aimc.flange, loadInertia.flange_a);

---

model Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_withLosses

Component	Version 3.2	Version 3.2.1
m	protected
aimc	Jr=J	Jr=aimcData.Jr
	p=2	p=aimcData.p
	fsNominal=fNominal	fsNominal=aimcData.fsNominal
	Rs=0.56	Rs=aimcData.Rs
	alpha20s(displayUnit="1/K") = Modelica_3_2.Electrical.Machines.Thermal.Constants.alpha20Copper	alpha20s(displayUnit="1/K") = aimcData.alpha20s
	Lssigma=1.52/(2*pi*fNominal)	Lssigma=aimcData.Lssigma
	Lm=66.4/(2*pi*fNominal)	Lm=aimcData.Lm
	Lrsigma=2.31/(2*pi*fNominal)	Lrsigma=aimcData.Lrsigma
	Rr=0.42	Rr=aimcData.Rr
	TsRef=293.15	TsRef=aimcData.TsRef
	TrRef=293.15	TrRef=aimcData.TrRef
	statorCoreParameters(PRef=PcoreRef, VRef=VcoreNominal, wRef=2*pi*fNominal)
	strayLoadParameters(PRef=0.005*sqrt(3)*VNominal*INominal*pfNominal, IRef=INominal/sqrt(3), wRef=wNominal)
	alpha20r(displayUnit="1/K") = Modelica_3_2.Electrical.Machines.Thermal.Constants.alpha20Aluminium
	wMechanical(start=wNominal, fixed=true)
	frictionParameters(PRef=PfrictionRef, wRef=wNominal)
		Lszero=aimcData.Lszero
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		wMechanical(fixed=true, start=2*pi*aimcData.fsNominal/aimcData.p)
		alpha20r=aimcData.alpha20r
loadInertia	J=J	J=aimcData.Jr
PI		initType=Modelica.Blocks.Types.Init.InitialState
pi	Present
J	Present
PcoreRef	Present
VcoreNominal	Present
PfrictionRef	Present
aimcData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimc.i_0_s=0; der(aimc.idq_sr)=zeros(2); der(aimc.idq_rr)=zeros(2); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ...

---

model Electrical.Machines.Examples.SynchronousInductionMachines.SMR_Inverter

Component	Version 3.2	Version 3.2.1
smr		p=smrData.p
		fsNominal=smrData.fsNominal
		Rs=smrData.Rs
		TsRef=smrData.TsRef
		Lszero=smrData.Lszero
		Lssigma=smrData.Lssigma
		Jr=smrData.Jr
		Js=smrData.Js
		frictionParameters=smrData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=smrData.statorCoreParameters
		strayLoadParameters=smrData.strayLoadParameters
		Lmd=smrData.Lmd
		Lmq=smrData.Lmq
		useDamperCage=smrData.useDamperCage
		Lrsigmad=smrData.Lrsigmad
		Lrsigmaq=smrData.Lrsigmaq
		Rrd=smrData.Rrd
		Rrq=smrData.Rrq
		TrRef=smrData.TrRef
		TsOperational=293.15
		alpha20s=smrData.alpha20s
		ir(fixed=true)
		TrOperational=293.15
		alpha20r=smrData.alpha20r
loadTorqueStep		offsetTorque=0
smrData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(signalVoltage.plug_n, star.plug_p);	initial equation
	smr.is[1:2]=zeros(2); equation  &nbspconnect(signalVoltage.plug_n, star.plug_p);
connect(star.pin_n, ground.p); ...

---

model Electrical.Machines.Examples.SynchronousInductionMachines.SMPM_Inverter

Component	Version 3.2	Version 3.2.1
smpm		p=smpmData.p
		fsNominal=smpmData.fsNominal
		Rs=smpmData.Rs
		TsRef=smpmData.TsRef
		Lszero=smpmData.Lszero
		Lssigma=smpmData.Lssigma
		Jr=smpmData.Jr
		Js=smpmData.Js
		frictionParameters=smpmData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=smpmData.statorCoreParameters
		strayLoadParameters=smpmData.strayLoadParameters
		VsOpenCircuit=smpmData.VsOpenCircuit
		Lmd=smpmData.Lmd
		Lmq=smpmData.Lmq
		useDamperCage=smpmData.useDamperCage
		Lrsigmad=smpmData.Lrsigmad
		Lrsigmaq=smpmData.Lrsigmaq
		Rrd=smpmData.Rrd
		Rrq=smpmData.Rrq
		TrRef=smpmData.TrRef
		permanentMagnetLossParameters=smpmData.permanentMagnetLossParameters
		TsOperational=293.15
		alpha20s=smpmData.alpha20s
		ir(fixed=true)
		TrOperational=293.15
		alpha20r=smpmData.alpha20r
loadTorqueStep		offsetTorque=0
smpmData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(signalVoltage.plug_n, star.plug_p);	initial equation
	smpm.is[1:2]=zeros(2); equation  &nbspconnect(signalVoltage.plug_n, star.plug_p);
connect(star.pin_n, ground.p); ...

---

model Electrical.Machines.Examples.SynchronousInductionMachines.SMPM_CurrentSource

Component	Version 3.2	Version 3.2.1
smpm	useDamperCage=false	useDamperCage=smpmData.useDamperCage
		p=smpmData.p
		fsNominal=smpmData.fsNominal
		TsOperational=293.15
		Rs=smpmData.Rs
		TsRef=smpmData.TsRef
		alpha20s=smpmData.alpha20s
		Lszero=smpmData.Lszero
		Lssigma=smpmData.Lssigma
		Jr=smpmData.Jr
		Js=smpmData.Js
		frictionParameters=smpmData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=smpmData.statorCoreParameters
		strayLoadParameters=smpmData.strayLoadParameters
		TrOperational=293.15
		VsOpenCircuit=smpmData.VsOpenCircuit
		Lmd=smpmData.Lmd
		Lmq=smpmData.Lmq
		Lrsigmad=smpmData.Lrsigmad
		Lrsigmaq=smpmData.Lrsigmaq
		Rrd=smpmData.Rrd
		Rrq=smpmData.Rrq
		TrRef=smpmData.TrRef
		alpha20r=smpmData.alpha20r
		permanentMagnetLossParameters=smpmData.permanentMagnetLossParameters
smpmData		Present
currentQuasiRMSSensor		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(angleSensor.phi, currentController.phi);
connect(signalCurrent.plug_n, terminalBox.plugSupply);
connect(id.y, currentController.id_rms); ... connect(torqueSensor.flange_b, inertiaLoad.flange_a);
	connect(signalCurrent.plug_n, currentQuasiRMSSensor.plug_p); connect(currentQuasiRMSSensor.plug_n, voltageQuasiRMSSensor.plug_p);

---

model Electrical.Machines.Examples.SynchronousInductionMachines.SMEE_Generator

Component	Version 3.2	Version 3.2.1
smee	useSupport=true
		p=2
		Jr=0.29
		Js=0.29
		useDamperCage=true
		statorCoreParameters(VRef=100)
		strayLoadParameters(IRef=100)
		brushParameters(ILinear=0.01)
		TsOperational=293.15
		ir(fixed=true)
		TrOperational=293.15
		TeOperational=293.15
rotorDisplacementAngle	useSupport=true
mechanicalPowerSensor	useSupport=true
smeeData		SNominal=30e3
		VsNominal=100
		fsNominal=50
		IeOpenCircuit=10
		x0=0.1
		xd=1.6
		xq=1.6
		xdTransient=0.1375
		xdSubtransient=0.121428571
		xqSubtransient=0.148387097
		Ta=0.014171268
		Td0Transient=0.261177343
		Td0Subtransient=0.006963029
		Tq0Subtransient=0.123345081
		alpha20s(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		alpha20r(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		alpha20e(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		TsSpecification=293.15
		TsRef=293.15
		TrSpecification=293.15
		TrRef=293.15
		TeSpecification=293.15
		TeRef=293.15
fixed	Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(rotorDisplacementAngle.plug_n, smee.plug_sn);	initial equation
	smee.is[1:2]=zeros(2); equation  &nbspconnect(rotorDisplacementAngle.plug_n, smee.plug_sn);
connect(rotorDisplacementAngle.plug_p, smee.plug_sp); ... connect(terminalBox.plug_sp, smee.plug_sp);
connect(constantSpeed.support, fixed.flange);	connect(smee.flange, rotorDisplacementAngle.flange);
connect(mechanicalPowerSensor.support, fixed.flange);	connect(smee.flange, mechanicalPowerSensor.flange_a);
connect(smee.support, fixed.flange); connect(rotorDisplacementAngle.support, smee.support); connect(smee.flange, rotorDisplacementAngle.flange); connect(smee.flange, mechanicalPowerSensor.flange_a);

---

model Electrical.Machines.Examples.SynchronousInductionMachines.SMEE_LoadDump

Component	Version 3.2	Version 3.2.1
smee		p=2
		Jr=0.29
		Js=0.29
		statorCoreParameters(VRef=100)
		strayLoadParameters(IRef=100)
		brushParameters(ILinear=0.01)
		TsOperational=293.15
		ir(fixed=true)
		TrOperational=293.15
		TeOperational=293.15
smeeData		SNominal=30e3
		VsNominal=100
		fsNominal=50
		IeOpenCircuit=10
		x0=0.1
		xd=1.6
		xq=1.6
		xdTransient=0.1375
		xdSubtransient=0.121428571
		xqSubtransient=0.148387097
		Ta=0.014171268
		Td0Transient=0.261177343
		Td0Subtransient=0.006963029
		Tq0Subtransient=0.123345081
		TsSpecification=293.15
		TsRef=293.15
		alpha20s(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		TrSpecification=293.15
		TrRef=293.15
		alpha20r(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		TeSpecification=293.15
		TeRef=293.15
		alpha20e(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
setPointGain	k=smeeData.VsNominal/wNominal	k=(smeeData.VsNominal/wNominal)/unitMagneticFlux
voltageController		initType=Modelica.Blocks.Types.InitPID.InitialState
		Td=0.001
switch		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
		V0=fill(30, m)
		dVdt=fill(10e3, m)
		Vmax=fill(60, m)
unitMagneticFlux		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(terminalBox.plug_sn, smee.plug_sn);	initial equation
	smee.idq_sr=zeros(2); smee.ie=0; equation  &nbspconnect(terminalBox.plug_sn, smee.plug_sn);
connect(terminalBox.plug_sp, smee.plug_sp); ...

---

model Electrical.Machines.Examples.DCMachines.DCPM_Start

Component	Version 3.2	Version 3.2.1
dcpm		VaNominal=dcpmData.VaNominal
		IaNominal=dcpmData.IaNominal
		wNominal=dcpmData.wNominal
		TaNominal=dcpmData.TaNominal
		Ra=dcpmData.Ra
		TaRef=dcpmData.TaRef
		La=dcpmData.La
		Jr=dcpmData.Jr
		useSupport=false
		Js=dcpmData.Js
		frictionParameters=dcpmData.frictionParameters
		coreParameters=dcpmData.coreParameters
		strayLoadParameters=dcpmData.strayLoadParameters
		brushParameters=dcpmData.brushParameters
		TaOperational=293.15
		alpha20a=dcpmData.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
loadTorqueStep		offsetTorque=0
dcpmData		Present

---

model Electrical.Machines.Examples.DCMachines.DCEE_Start

Component	Version 3.2	Version 3.2.1
dcee		VaNominal=dceeData.VaNominal
		IaNominal=dceeData.IaNominal
		wNominal=dceeData.wNominal
		TaNominal=dceeData.TaNominal
		Ra=dceeData.Ra
		TaRef=dceeData.TaRef
		La=dceeData.La
		Jr=dceeData.Jr
		useSupport=false
		Js=dceeData.Js
		frictionParameters=dceeData.frictionParameters
		coreParameters=dceeData.coreParameters
		strayLoadParameters=dceeData.strayLoadParameters
		brushParameters=dceeData.brushParameters
		IeNominal=dceeData.IeNominal
		Re=dceeData.Re
		TeRef=dceeData.TeRef
		Le=dceeData.Le
		sigmae=dceeData.sigmae
		TaOperational=293.15
		alpha20a=dceeData.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
		alpha20e=dceeData.alpha20e
		TeOperational=293.15
		ie(fixed=true)
loadTorqueStep		offsetTorque=0
dceeData		Present

---

model Electrical.Machines.Examples.DCMachines.DCSE_Start

Component	Version 3.2	Version 3.2.1
dcse		VaNominal=dcseData.VaNominal
		IaNominal=dcseData.IaNominal
		wNominal=dcseData.wNominal
		TaNominal=dcseData.TaNominal
		TeNominal=dcseData.TeNominal
		Ra=dcseData.Ra
		TaRef=dcseData.TaRef
		La=dcseData.La
		Jr=dcseData.Jr
		useSupport=false
		Js=dcseData.Js
		frictionParameters=dcseData.frictionParameters
		coreParameters=dcseData.coreParameters
		strayLoadParameters=dcseData.strayLoadParameters
		brushParameters=dcseData.brushParameters
		Re=dcseData.Re
		TeRef=dcseData.TeRef
		Le=dcseData.Le
		sigmae=dcseData.sigmae
		TaOperational=293.15
		alpha20a=dcseData.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
		alpha20e=dcseData.alpha20e
		TeOperational=293.15
dcseData		Present

---

model Electrical.Machines.Examples.DCMachines.DCSE_SinglePhase

Component	Version 3.2	Version 3.2.1
dcse		VaNominal=dcseData.VaNominal
		IaNominal=dcseData.IaNominal
		wNominal=dcseData.wNominal
		TaNominal=dcseData.TaNominal
		TeNominal=dcseData.TeNominal
		Ra=dcseData.Ra
		TaRef=dcseData.TaRef
		La=dcseData.La
		Jr=dcseData.Jr
		useSupport=false
		Js=dcseData.Js
		frictionParameters=dcseData.frictionParameters
		coreParameters=dcseData.coreParameters
		strayLoadParameters=dcseData.strayLoadParameters
		brushParameters=dcseData.brushParameters
		Re=dcseData.Re
		TeRef=dcseData.TeRef
		Le=dcseData.Le
		sigmae=dcseData.sigmae
		TaOperational=293.15
		alpha20a=dcseData.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
		alpha20e=dcseData.alpha20e
		TeOperational=293.15
dcseData		Present

---

model Electrical.Machines.Examples.DCMachines.DCPM_Temperature

Component	Version 3.2	Version 3.2.1
dcpm	TaNominal=353.15	TaNominal=dcpmData.TaNominal
	TaRef=353.15	TaRef=dcpmData.TaRef
	alpha20a(displayUnit="1/K") = Machines.Thermal.Constants.alpha20Copper
		VaNominal=dcpmData.VaNominal
		IaNominal=dcpmData.IaNominal
		wNominal=dcpmData.wNominal
		Ra=dcpmData.Ra
		La=dcpmData.La
		Jr=dcpmData.Jr
		useSupport=false
		Js=dcpmData.Js
		frictionParameters=dcpmData.frictionParameters
		coreParameters=dcpmData.coreParameters
		strayLoadParameters=dcpmData.strayLoadParameters
		brushParameters=dcpmData.brushParameters
		phiMechanical(fixed=true)
		ia(fixed=true)
		TaOperational=293.15
		alpha20a=dcpmData.alpha20a
thermalAmbientDCPM		Ta=293.15
		Tpm=293.15
dcpmData		Present

---

model Electrical.Machines.Examples.DCMachines.DCPM_Cooling

Component	Version 3.2	Version 3.2.1
dcpm	TaNominal=353.15	TaNominal=dcpmData.TaNominal
	TaRef=353.15	TaRef=dcpmData.TaRef
	alpha20a(displayUnit="1/K") = Machines.Thermal.Constants.alpha20Copper
		VaNominal=dcpmData.VaNominal
		IaNominal=dcpmData.IaNominal
		wNominal=dcpmData.wNominal
		Ra=dcpmData.Ra
		La=dcpmData.La
		Jr=dcpmData.Jr
		useSupport=false
		Js=dcpmData.Js
		frictionParameters=dcpmData.frictionParameters
		coreParameters=dcpmData.coreParameters
		strayLoadParameters=dcpmData.strayLoadParameters
		brushParameters=dcpmData.brushParameters
		phiMechanical(fixed=true)
		ia(fixed=true)
		TaOperational=293.15
		alpha20a=dcpmData.alpha20a
inlet		constantAmbientPressure=0
volumeFlow		m=0
cooling		m=0
		h_g=0
		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		T0fixed=false
outlet		constantAmbientPressure=0
dcpmData		Present

---

model Electrical.Machines.Examples.DCMachines.DCPM_QuasiStationary

Component	Version 3.2	Version 3.2.1
dcpm1	wMechanical(start=w0, fixed=true)
	alpha20a(displayUnit="1/K")
		VaNominal=dcpmData.VaNominal
		IaNominal=dcpmData.IaNominal
		wNominal=dcpmData.wNominal
		TaNominal=dcpmData.TaNominal
		Ra=dcpmData.Ra
		TaRef=dcpmData.TaRef
		La=dcpmData.La
		Jr=dcpmData.Jr
		useSupport=false
		Js=dcpmData.Js
		frictionParameters=dcpmData.frictionParameters
		coreParameters=dcpmData.coreParameters
		strayLoadParameters=dcpmData.strayLoadParameters
		brushParameters=dcpmData.brushParameters
		phiMechanical(fixed=true)
		ia(fixed=true)
		TaOperational=293.15
		alpha20a=dcpmData.alpha20a
		wMechanical(fixed=true, start=w0)
dcpm2	wMechanical(start=w0, fixed=true)
	alpha20a(displayUnit="1/K")
		VaNominal=dcpmData.VaNominal
		IaNominal=dcpmData.IaNominal
		wNominal=dcpmData.wNominal
		TaNominal=dcpmData.TaNominal
		Ra=dcpmData.Ra
		TaRef=dcpmData.TaRef
		La=dcpmData.La
		Jr=dcpmData.Jr
		useSupport=false
		Js=dcpmData.Js
		frictionParameters=dcpmData.frictionParameters
		coreParameters=dcpmData.coreParameters
		strayLoadParameters=dcpmData.strayLoadParameters
		brushParameters=dcpmData.brushParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true, start=w0)
		TaOperational=293.15
		alpha20a=dcpmData.alpha20a
dcpmData		Present

---

model Electrical.Machines.Examples.DCMachines.DCPM_withLosses

Component	Version 3.2	Version 3.2.1
dcpm1		VaNominal=dcpmData1.VaNominal
		IaNominal=dcpmData1.IaNominal
		wNominal=dcpmData1.wNominal
		TaNominal=dcpmData1.TaNominal
		Ra=dcpmData1.Ra
		TaRef=dcpmData1.TaRef
		La=dcpmData1.La
		Jr=dcpmData1.Jr
		useSupport=false
		Js=dcpmData1.Js
		frictionParameters=dcpmData1.frictionParameters
		coreParameters=dcpmData1.coreParameters
		strayLoadParameters=dcpmData1.strayLoadParameters
		brushParameters=dcpmData1.brushParameters
		TaOperational=293.15
		alpha20a=dcpmData1.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
dcpm2	wNominal=148.44025288212	wNominal=dcpmData2.wNominal
	TaNominal=368.15	TaNominal=dcpmData2.TaNominal
	Ra=0.03864	Ra=dcpmData2.Ra
	TaRef=293.15	TaRef=dcpmData2.TaRef
	frictionParameters(PRef=100)
	alpha20a(displayUnit="1/K") = Modelica_3_2.Electrical.Machines.Thermal.Constants.alpha20Copper
	coreParameters(PRef=200)
	strayLoadParameters(PRef=50)
	brushParameters(V=0.5)
		VaNominal=dcpmData2.VaNominal
		IaNominal=dcpmData2.IaNominal
		La=dcpmData2.La
		Jr=dcpmData2.Jr
		useSupport=false
		Js=dcpmData2.Js
		frictionParameters=dcpmData2.frictionParameters
		coreParameters=dcpmData2.coreParameters
		strayLoadParameters=dcpmData2.strayLoadParameters
		brushParameters=dcpmData2.brushParameters
		alpha20a=dcpmData2.alpha20a
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		ia(fixed=true)
		core(v(start=0))
dcpmData1		Present
dcpmData2		Present

---

model Electrical.Machines.Examples.Transformers.TransformerTestbench

Component	Version 3.2	Version 3.2.1
transformerData		parameter
		f=50
		V1=100
		V2=100
		SNominal=30E3
		v_sc=0.05
		P_sc=300
transformer		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15

Equations in Version 3.2	Equations in Version 3.2.1
connect(starS.pin_n, groundS.p);	initial equation
	transformer.i2[1:2]=zeros(2); equation  &nbspconnect(starS.pin_n, groundS.p);
connect(source.plug_n, starS.plug_p); ...

---

model Electrical.Machines.Examples.Transformers.AsymmetricalLoad

Component	Version 3.2	Version 3.2.1
transformerData		parameter
		f=50
		V1=100
		V2=100
		SNominal=30E3
		v_sc=0.05
		P_sc=300
transformer		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15

Equations in Version 3.2	Equations in Version 3.2.1
connect(starS.pin_n, groundS.p);	initial equation
	transformer.i2[1]=0; equation  &nbspconnect(starS.pin_n, groundS.p);
connect(source.plug_n, starS.plug_p); ...

---

model Electrical.Machines.Examples.Transformers.Rectifier6pulse

Component	Version 3.2	Version 3.2.1
diode1		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
		Vknee=fill(0, m)
diode2		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
		Vknee=fill(0, m)
transformerData1		parameter
		f=50
		V1=100
		V2=100
		SNominal=30E3
		v_sc=0.05
		P_sc=300
transformer1		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15

Equations in Version 3.2	Equations in Version 3.2.1
connect(cDC1.n, cDC2.p);	initial equation
	cDC1.v=VC0/2; cDC2.v=VC0/2; transformer1.i2[1:2]=zeros(2); equation  &nbspconnect(cDC1.n, cDC2.p);
connect(cDC1.n, groundDC.p); ...

---

model Electrical.Machines.Examples.Transformers.Rectifier12pulse

Component	Version 3.2	Version 3.2.1
diode3		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
		Vknee=fill(0, m)
diode4		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
		Vknee=fill(0, m)
transformer2		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15
transformerData2		parameter
		f=50
		V1=100
		V2=100
		SNominal=30E3
		v_sc=0.05
		P_sc=300

Equations in Version 3.2	Equations in Version 3.2.1
connect(diode3.plug_n, star3.plug_p);	initial equation
	transformer2.core.plug_p1.pin[1:3].i=zeros(3); equation  &nbspconnect(diode3.plug_n, star3.plug_p);
connect(diode4.plug_p, star4.plug_p); ...

---

model Electrical.Machines.BasicMachines.AsynchronousInductionMachines.AIM_SquirrelCage

Component	Version 3.2	Version 3.2.1
ir		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(airGapS.spacePhasor_r, squirrelCageR.spacePhasor_r);
connect(airGapS.support, internalSupport);
connect(airGapS.flange, inertiaRotor.flange_a); ... connect(squirrelCageR.heatPort, internalThermalPort.heatPortRotorWinding);
	connect(airGapS.support, internalSupport);

---

model Electrical.Machines.BasicMachines.AsynchronousInductionMachines.AIM_SlipRing

Component	Version 3.2	Version 3.2.1
lrsigma	final L=fill(Lrsigma, 2)	final L=fill(internalTurnsRatio^2*Lrsigma, 2)
lrzero	final L=Lrzero	final L=internalTurnsRatio^2*Lrzero
rotorCore		final useHeatPort=true
		final turnsRatio=internalTurnsRatio

Equations in Version 3.2	Equations in Version 3.2.1
connect(airGapS.support, internalSupport); connect(airGapS.flange, inertiaRotor.flange_a); connect(plug_rn, plug_rn);
connect(lssigma.spacePhasor_b, airGapS.spacePhasor_s); ... connect(plug_rp, rr.plug_p);
	connect(airGapS.flange, inertiaRotor.flange_a); connect(fixed.flange, internalSupport); connect(internalSupport, airGapS.support);

---

model Electrical.Machines.BasicMachines.SynchronousInductionMachines.SM_PermanentMagnet

Component	Version 3.2	Version 3.2.1
idq_dr	SIunits.Current	Blocks.Interfaces.RealOutput
	output
permanentMagnet	Electrical.Machines.BasicMachines.Components.PermanentMagnet	Electrical.Machines.BasicMachines.Components.PermanentMagnetWithLosses
heatFlowSensorDamperCage	Present
ir		Present
permanentMagnetLossParameters		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
	connect(ir, damperCage.i); connect(idq_dr, damperCage.i); connect(damperCageLossPower, damperCage.lossPower); if not useDamperCage then damperCageLossPower=0; end if;
connect(airGapR.spacePhasor_r, damperCage.spacePhasor_r); ... connect(airGapR.support, internalSupport);
	connect(lssigma.spacePhasor_b, airGapR.spacePhasor_s);
connect(airGapR.flange, inertiaRotor.flange_a);
connect(lssigma.spacePhasor_b, airGapR.spacePhasor_s);	connect(permanentMagnet.heatPort, internalThermalPort.heatPortPermanentMagnet);
connect(damperCage.heatPort, heatFlowSensorDamperCage.port_a);	connect(permanentMagnet.flange, inertiaRotor.flange_b);
connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);	connect(damperCage.heatPort, internalThermalPort.heatPortRotorWinding);
	connect(internalSupport, permanentMagnet.support);

---

model Electrical.Machines.BasicMachines.SynchronousInductionMachines.SM_ElectricalExcited

Component	Version 3.2	Version 3.2.1
idq_dr	SIunits.Current	Blocks.Interfaces.RealOutput
	output
brush		final useHeatPort=true
heatFlowSensorDamperCage	Present
ir		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
	connect(ir, damperCage.i); connect(idq_dr, damperCage.i); connect(damperCageLossPower, damperCage.lossPower); if not useDamperCage then damperCageLossPower=0; end if;
connect(airGapR.spacePhasor_r, damperCage.spacePhasor_r);
connect(airGapR.spacePhasor_r, electricalExcitation.spacePhasor_r);
connect(airGapR.support, internalSupport); connect(airGapR.flange, inertiaRotor.flange_a);
connect(electricalExcitation.pin_en, pin_en); ... connect(re.heatPort, internalThermalPort.heatPortExcitation);
connect(damperCage.heatPort, heatFlowSensorDamperCage.port_a);	connect(airGapR.flange, inertiaRotor.flange_a);
connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);	connect(airGapR.support, internalSupport);
	connect(damperCage.heatPort, internalThermalPort.heatPortRotorWinding);

---

model Electrical.Machines.BasicMachines.SynchronousInductionMachines.SM_ReluctanceRotor

Component	Version 3.2	Version 3.2.1
heatFlowSensorDamperCage	Present
ir		Present
idq_dr		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
	connect(ir, damperCage.i); connect(idq_dr, damperCage.i); connect(damperCageLossPower, damperCage.lossPower); if not useDamperCage then damperCageLossPower=0; end if;
connect(airGapR.spacePhasor_r, damperCage.spacePhasor_r);
connect(airGapR.support, internalSupport);
	connect(lssigma.spacePhasor_b, airGapR.spacePhasor_s);
connect(airGapR.flange, inertiaRotor.flange_a);
connect(lssigma.spacePhasor_b, airGapR.spacePhasor_s);	connect(damperCage.heatPort, internalThermalPort.heatPortRotorWinding);
connect(damperCage.heatPort, heatFlowSensorDamperCage.port_a); connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);

---

model Electrical.Machines.BasicMachines.DCMachines.DC_ElectricalExcited

Component	Version 3.2	Version 3.2.1
ie		start=0

---

model Electrical.Machines.BasicMachines.Components.DamperCage

Component	Version 3.2	Version 3.2.1
i		Present
lossPower		Present

---

model Electrical.Machines.Sensors.VoltageQuasiRMSSensor

Component	Version 3.2	Version 3.2.1
V		final quantity="ElectricPotential"
		final unit="V"

---

model Electrical.Machines.Sensors.CurrentQuasiRMSSensor

Component	Version 3.2	Version 3.2.1
I		final quantity="ElectricCurrent"
		final unit="A"

---

model Electrical.Machines.Sensors.ElectricalPowerSensor

Component	Version 3.2	Version 3.2.1
P		final quantity="Power"
		final unit="W"
Q		final quantity="Power"
		final unit="var"

---

model Electrical.Machines.Sensors.MechanicalPowerSensor

Component	Version 3.2	Version 3.2.1
P		final quantity="Power"
		final unit="W"

Equations in Version 3.2	Equations in Version 3.2.1
... connect(torqueSensor.flange_b, flange_b);
connect(product.y, P); connect(torqueSensor.tau, product.u2);
connect(flange_a, relSpeedSensor.flange_b);
connect(relSpeedSensor.w_rel, product.u1);
connect(relSpeedSensor.flange_a, fixed.flange);
connect(relSpeedSensor.flange_a, support);
	connect(relSpeedSensor.w_rel, product.u1); connect(torqueSensor.tau, product.u2); connect(product.y, P);

---

model Electrical.Machines.Sensors.RotorDisplacementAngle

Component	Version 3.2	Version 3.2.1
rotorDisplacementAngle		final quantity="Angle"
		final unit="rad"

Equations in Version 3.2	Equations in Version 3.2.1
connect(constant_.y, add.u2); connect(add.y, rotatorVS2R.angle); connect(ToSpacePhasorVS.y, rotatorVS2R.u); connect(rotatorVS2R.y, ToPolarVSR.u); connect(ToPolarVSR.y, deMultiplex2.u);
connect(plug_p, VoltageSensor1.plug_p);
connect(plug_n, VoltageSensor1.plug_n);
connect(VoltageSensor1.v, ToSpacePhasorVS.u); connect(deMultiplex2.y2[1], rotorDisplacementAngle); connect(relativeAngleSensor.phi_rel, add.u1);
connect(relativeAngleSensor.flange_b, flange); ... connect(relativeAngleSensor.flange_a, fixed.flange);
	connect(relativeAngleSensor.phi_rel, add.u1); connect(constant_.y, add.u2); connect(VoltageSensor1.v, ToSpacePhasorVS.u); connect(ToSpacePhasorVS.y, rotatorVS2R.u); connect(rotatorVS2R.y, ToPolarVSR.u); connect(add.y, rotatorVS2R.angle); connect(ToPolarVSR.y, deMultiplex2.u); connect(deMultiplex2.y2[1], rotorDisplacementAngle);

---

function Electrical.Machines.SpacePhasors.Functions.ToSpacePhasor

Component	Version 3.2	Version 3.2.1
m		protected
pi	Real	SIunits.Angle
		protected

---

function Electrical.Machines.SpacePhasors.Functions.FromSpacePhasor

Component	Version 3.2	Version 3.2.1
m		protected
pi	Real	SIunits.Angle
		protected

---

function Electrical.Machines.SpacePhasors.Functions.ToPolar

Component	Version 3.2	Version 3.2.1
small		protected

---

function Electrical.Machines.SpacePhasors.Functions.FromPolar

Component	Version 3.2	Version 3.2.1
pi	Real	SIunits.Angle
		protected
small		protected

---

function Electrical.Machines.SpacePhasors.Functions.quasiRMS

Component	Version 3.2	Version 3.2.1
m		protected
pi	Real	SIunits.Angle
		protected

---

function Electrical.Machines.SpacePhasors.Functions.activePower

Component	Version 3.2	Version 3.2.1
m		protected
pi		Present

---

record Electrical.Machines.Losses.FrictionParameters

Component	Version 3.2	Version 3.2.1
PRef	start=0
		=0

---

record Electrical.Machines.Losses.BrushParameters

Component	Version 3.2	Version 3.2.1
V	start=0
		=0

---

record Electrical.Machines.Losses.StrayLoadParameters

Component	Version 3.2	Version 3.2.1
PRef	start=0
		=0

---

record Electrical.Machines.Losses.CoreParameters

Component	Version 3.2	Version 3.2.1
PRef	start=0
		=0

---

model Electrical.Machines.Losses.Friction

Component	Version 3.2	Version 3.2.1
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = tau*w;	lossPower = -tau*w;

---

model Electrical.Machines.Losses.InductionMachines.Brush

Component	Version 3.2	Version 3.2.1
brush		each final useHeatPort=true
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... for j in 1:m loop
connect(brush[j].heatPort, heatPort);	connect(brush[j].heatPort, internalHeatPort);
end for;

---

model Electrical.Machines.Losses.InductionMachines.StrayLoad

Component	Version 3.2	Version 3.2.1
iRMS	=Machines.SpacePhasors.Functions.quasiRMS(i)	=quasiRMS(i)
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = tau*w;	lossPower = -tau*w;

---

model Electrical.Machines.Losses.InductionMachines.Core

Component	Version 3.2	Version 3.2.1
coreParameters	final m=3	final m=m
heatPort	Present
m		Present
turnsRatio		Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = -3/2*(+spacePhasor.v_[1]*spacePhasor.i_[1]+spacePhasor.v_[2]*spacePhasor.i_[2]);	lossPower = 3/2*(+spacePhasor.v_[1]*spacePhasor.i_[1]+spacePhasor.v_[2]*spacePhasor.i_[2]);

---

model Electrical.Machines.Losses.DCMachines.Brush

Component	Version 3.2	Version 3.2.1
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = -v*i;	lossPower = v*i;

---

model Electrical.Machines.Losses.DCMachines.StrayLoad

Component	Version 3.2	Version 3.2.1
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = tau*w;	lossPower = -tau*w;

---

model Electrical.Machines.Losses.DCMachines.Core

Component	Version 3.2	Version 3.2.1
heatPort	Present

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
heatPort.Q_flow = -v*i;	lossPower = v*i;

---

model Electrical.Machines.Thermal.AsynchronousInductionMachines.ThermalAmbientAIMS

Component	Version 3.2	Version 3.2.1
thermalCollectorRotor	m=thermalPort.m
		final m=mr
mr		Present

---

model Electrical.Machines.Interfaces.PartialBasicMachine

Component	Version 3.2	Version 3.2.1
phiMechanical		start=0
wMechanical		start=0

---

model Electrical.Machines.Interfaces.PartialBasicInductionMachine

Component	Version 3.2	Version 3.2.1
strayLoadParameters	wRef(start=2*pi*fsNominal/p)
		wRef=2*pi*fsNominal/p
powerBalance	final lossPowerStatorWinding=-sum(rs.heatPort.Q_flow)	final lossPowerStatorWinding=sum(rs.resistor.LossPower)
	final lossPowerStatorCore=-statorCore.heatPort.Q_flow	final lossPowerStatorCore=statorCore.lossPower
	final lossPowerStrayLoad=-strayLoad.heatPort.Q_flow	final lossPowerStrayLoad=strayLoad.lossPower
	final lossPowerFriction=-friction.heatPort.Q_flow	final lossPowerFriction=friction.lossPower
statorCore		final useHeatPort=true
		final turnsRatio=1
strayLoad		final useHeatPort=true
		final m=m

Equations in Version 3.2	Equations in Version 3.2.1
... connect(strayLoad.plug_p, plug_sp);
connect(strayLoad.flange, inertiaRotor.flange_b);
connect(strayLoad.support, internalSupport); ... connect(friction.heatPort, internalThermalPort.heatPortFriction);
	connect(strayLoad.flange, inertiaRotor.flange_b);

---

connector Electrical.Machines.Interfaces.InductionMachines.PartialThermalPortInductionMachines

Component	Version 3.2	Version 3.2.1
connector	partial

---

model Electrical.Machines.Interfaces.InductionMachines.PartialThermalAmbientInductionMachines

Component	Version 3.2	Version 3.2.1
model	partial

---

record Electrical.Machines.Interfaces.InductionMachines.PartialPowerBalanceInductionMachines

Component	Version 3.2	Version 3.2.1
record	partial
powerStator		=0
powerMechanical		=0
powerInertiaStator		=0
powerInertiaRotor		=0
lossPowerTotal		=0
lossPowerStatorWinding		=0
lossPowerStatorCore		=0
lossPowerRotorCore		=0
lossPowerStrayLoad		=0
lossPowerFriction		=0

---

connector Electrical.Machines.Interfaces.InductionMachines.ThermalPortAIMS

Component	Version 3.2	Version 3.2.1
mr		Present

---

model Electrical.Machines.Interfaces.PartialBasicDCMachine

Component	Version 3.2	Version 3.2.1
powerBalance	final lossPowerArmature=-ra.heatPort.Q_flow	final lossPowerArmature=ra.LossPower
	final lossPowerCore=-core.heatPort.Q_flow	final lossPowerCore=core.lossPower
	final lossPowerStrayLoad=-strayLoad.heatPort.Q_flow	final lossPowerStrayLoad=strayLoad.lossPower
	final lossPowerFriction=-friction.heatPort.Q_flow	final lossPowerFriction=friction.lossPower
	final lossPowerBrush=-brush.heatPort.Q_flow	final lossPowerBrush=brush.lossPower
ia		start=0
brush		final useHeatPort=true
core		final useHeatPort=true
strayLoad		final useHeatPort=true

Equations in Version 3.2	Equations in Version 3.2.1
... connect(strayLoad.n, ra.p);
connect(strayLoad.flange, inertiaRotor.flange_b);
connect(strayLoad.support, internalSupport); ... connect(ra.heatPort, internalThermalPort.heatPortArmature);
	connect(inertiaRotor.flange_b, strayLoad.flange);

---

connector Electrical.Machines.Interfaces.DCMachines.PartialThermalPortDCMachines

Component	Version 3.2	Version 3.2.1
connector	partial

---

model Electrical.Machines.Interfaces.DCMachines.PartialThermalAmbientDCMachines

Component	Version 3.2	Version 3.2.1
model	partial

---

record Electrical.Machines.Interfaces.DCMachines.PartialPowerBalanceDCMachines

Component	Version 3.2	Version 3.2.1
record	partial
powerArmature		=0
powerMechanical		=0
powerInertiaStator		=0
powerInertiaRotor		=0
lossPowerTotal		=0
lossPowerArmature		=0
lossPowerCore		=0
lossPowerStrayLoad		=0
lossPowerFriction		=0
lossPowerBrush		=0

---

model Electrical.Machines.Interfaces.PartialBasicTransformer

Component	Version 3.2	Version 3.2.1
powerBalance	final lossPower1=-sum(r1.heatPort.Q_flow)	final lossPower1=sum(r1.resistor.LossPower)
	final lossPower2=-sum(r2.heatPort.Q_flow)	final lossPower2=sum(r2.resistor.LossPower)

---

block Electrical.Machines.Utilities.VfController

Component	Version 3.2	Version 3.2.1
orientation		Present

Equations in Version 3.2	Equations in Version 3.2.1
... der(x) = 2*pi*u;
y = {amplitude*sin(x + BasePhase - (k - 1)*2/m*pi) for k in 1:m};	y = amplitude*sin(fill(x + BasePhase, m) + orientation);

---

model Electrical.Machines.Utilities.SwitchYD

Component	Version 3.2	Version 3.2.1
idealCommutingSwitch		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)

---

model Electrical.Machines.Utilities.SwitchedRheostat

Component	Version 3.2	Version 3.2.1
idealCommutingSwitch		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)

---

model Electrical.MultiPhase.Examples.TransformerYY

Component	Version 3.2	Version 3.2.1
idealTransformer		Lm1=fill(Lm, m)
		n=fill(nT, m)
Lm		Present
nT		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(starS.pin_n, groundS.p);	initial equation
	transformerL.i[1:m-1]=zeros(m-1) "Y-connection"; equation  &nbspconnect(starS.pin_n, groundS.p);
connect(starT1.pin_n,groundT1. p); ...

---

model Electrical.MultiPhase.Examples.TransformerYD

Component	Version 3.2	Version 3.2.1
idealTransformer		Lm1=fill(Lm, m)
Lm		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(groundS.p, starS.pin_n);	initial equation
	transformerL.i[1:m]=zeros(m) "D-connection"; equation  &nbspconnect(groundS.p, starS.pin_n);
connect(groundT.p, starT.pin_n); ...

---

model Electrical.MultiPhase.Examples.Rectifier

Component	Version 3.2	Version 3.2.1
idealDiode1		Ron=fill(Ron, m)
		Goff=fill(Goff, m)
		Vknee=fill(Vknee, m)
idealDiode2		Ron=fill(Ron, m)
		Goff=fill(Goff, m)
		Vknee=fill(Vknee, m)
Ron		Present
Goff		Present
Vknee		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(cDC1.n, cDC2.p);	initial equation
	cDC1.v=0; cDC2.v=0; supplyL.i[1:m-1]=zeros(m-1) "Y-connection"; equation  &nbspconnect(cDC1.n, cDC2.p);
connect(cDC1.n, groundDC.p); ...

---

model Electrical.MultiPhase.Basic.VariableResistor

Component	Version 3.2	Version 3.2.1
R		each unit="Ohm"

---

model Electrical.MultiPhase.Basic.VariableConductor

Component	Version 3.2	Version 3.2.1
G		each unit="S"

---

model Electrical.MultiPhase.Basic.VariableCapacitor

Component	Version 3.2	Version 3.2.1
C		each unit="F"

---

model Electrical.MultiPhase.Basic.VariableInductor

Component	Version 3.2	Version 3.2.1
L		each unit="H"

---

model Electrical.MultiPhase.Sensors.PowerSensor

Equations in Version 3.2	Equations in Version 3.2.1
... connect(voltageSensor.plug_n, nv);
	connect(voltageSensor.v, product.u1);
connect(currentSensor.i, product.u2);
connect(product.u1, voltageSensor.v);
connect(product.y, sum.u); ...

---

model Electrical.MultiPhase.Sources.SignalVoltage

Component	Version 3.2	Version 3.2.1
v		each unit="V"

---

model Electrical.MultiPhase.Sources.SineVoltage

Component	Version 3.2	Version 3.2.1
phase	=-{(j - 1)/m*2*Modelica_3_2.Constants.pi for j in 1:m}	=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

---

model Electrical.MultiPhase.Sources.SignalCurrent

Component	Version 3.2	Version 3.2.1
i		each unit="A"

---

model Electrical.MultiPhase.Sources.SineCurrent

Component	Version 3.2	Version 3.2.1
phase	=-{(j - 1)/m*2*Modelica_3_2.Constants.pi for j in 1:m}	=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

---

model Electrical.QuasiStationary.SinglePhase.Examples.SeriesResonance

Equations in Version 3.2	Equations in Version 3.2.1
connect(f.y, voltageSource.f);	initial equation
	voltageSource.pin_p.reference.gamma=0; equation  &nbspconnect(f.y, voltageSource.f);
connect(polarToComplex.y, voltageSource.V); ...

---

model Electrical.QuasiStationary.SinglePhase.Examples.ParallelResonance

Component	Version 3.2	Version 3.2.1
I		k=1

Equations in Version 3.2	Equations in Version 3.2.1
connect(currentSource.pin_n, resistor.pin_p);	initial equation
	currentSource.pin_p.reference.gamma=0; equation  &nbspconnect(currentSource.pin_n, resistor.pin_p);
connect(currentSource.pin_n, inductor.pin_p); ...

---

model Electrical.QuasiStationary.SinglePhase.Examples.Rectifier

Component	Version 3.2	Version 3.2.1
voltageQS		phi=0
		i(re(start=0), im(start=0))

Equations in Version 3.2	Equations in Version 3.2.1
connect(voltageQS.pin_p, resistorQS.pin_p);	initial equation
	voltageQS.pin_p.reference.gamma=0; equation  &nbspconnect(voltageQS.pin_p, resistorQS.pin_p);
connect(voltageQS.pin_n, rectifierQS.pin_nQS); ...

---

model Electrical.QuasiStationary.SinglePhase.Basic.VariableResistor

Component	Version 3.2	Version 3.2.1
R_ref		unit="Ohm"

---

model Electrical.QuasiStationary.SinglePhase.Basic.VariableConductor

Component	Version 3.2	Version 3.2.1
G_ref		unit="S"

---

model Electrical.QuasiStationary.SinglePhase.Basic.VariableCapacitor

Component	Version 3.2	Version 3.2.1
C		unit="F"

---

model Electrical.QuasiStationary.SinglePhase.Basic.VariableInductor

Component	Version 3.2	Version 3.2.1
L		unit="H"

---

model Electrical.QuasiStationary.SinglePhase.Interfaces.TwoPin

Component	Version 3.2	Version 3.2.1
omega	=der(pin_p.reference.gamma)

Equations in Version 3.2	Equations in Version 3.2.1
... pin_p.reference.gamma = pin_n.reference.gamma;
	omega = der(pin_p.reference.gamma); v = pin_p.v - pin_n.v;
i = pin_p.i;
v = pin_p.v - pin_n.v;

---

model Electrical.QuasiStationary.SinglePhase.Interfaces.AbsoluteSensor

Component	Version 3.2	Version 3.2.1
omega	=der(pin.reference.gamma)

Equations in Version 3.2	Equations in Version 3.2.1
	omega = der(pin.reference.gamma);
pin.i = Complex(0);

---

model Electrical.QuasiStationary.SinglePhase.Utilities.GraetzRectifier

Component	Version 3.2	Version 3.2.1
idealDiode1		Vknee=0
idealDiode2		Vknee=0
idealDiode3		Vknee=0
idealDiode4		Vknee=0

---

model Electrical.QuasiStationary.Machines.Examples.TransformerTestbench

Component	Version 3.2	Version 3.2.1
RL	sizes= 3	sizes= -1
	=fill(1/3, 3)	=fill(1/3, m)
source		m=m
starS		m=m
electricalPowerSensorS		m=m
currentSensorS		m=m
polarIS	sizes= 3	sizes= -1
voltageSensorS		m=m
polarVS	sizes= 3	sizes= -1
deltaS		m=m
voltageSensorL		m=m
polarVL	sizes= 3	sizes= -1
deltaL		m=m
currentSensorL		m=m
polarIL	sizes= 3	sizes= -1
electricalPowerSensorL		m=m
load		m=m
starL		m=m
transformerData		f=50
		V1=100
		V2=100
		SNominal=30E3
		v_sc=0.05
		P_sc=300
transformer		T1Ref=293.15
		alpha20_1(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T2Ref=293.15
		alpha20_2(displayUnit="1/K") = Modelica.Electrical.Machines.Thermal.Constants.alpha20Zero
		T1Operational=293.15
		T2Operational=293.15
m		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(starS.pin_n, groundS.pin);	initial equation
	source.voltageSource.pin_p.reference.gamma=zeros(m); equation  &nbspconnect(starS.pin_n, groundS.pin);
connect(source.plug_n, starS.plug_p); ...

---

model Electrical.QuasiStationary.Machines.BasicMachines.Components.PartialCore

Component	Version 3.2	Version 3.2.1
v1	=plug_p1.pin.v - plug_n1.pin.v
i1	=plug_p1.pin.i
v2	=plug_p2.pin.v - plug_n2.pin.v
i2	=plug_p2.pin.i
v3	=plug_p3.pin.v - plug_n3.pin.v
i3	=plug_p3.pin.i
im	=i1 + i2/n12 + i3/n13

Equations in Version 3.2	Equations in Version 3.2.1
	v1 = plug_p1.pin.v - plug_n1.pin.v; i1 = plug_p1.pin.i; v2 = plug_p2.pin.v - plug_n2.pin.v; i2 = plug_p2.pin.i; v3 = plug_p3.pin.v - plug_n3.pin.v; i3 = plug_p3.pin.i; im = i1 + i2/n12 + i3/n13;
Connections.branch(plug_p1.reference, plug_n1.reference); ...

---

model Electrical.QuasiStationary.Machines.Interfaces.PartialBasicTransformer

Component	Version 3.2	Version 3.2.1
powerBalance	final lossPower1=-sum(r1.heatPort.Q_flow)	final lossPower1=-sum(r1.resistor.LossPower)
	final lossPower2=-sum(r2.heatPort.Q_flow)	final lossPower2=-sum(r2.resistor.LossPower)

---

model Electrical.QuasiStationary.MultiPhase.Examples.BalancingStar

Component	Version 3.2	Version 3.2.1
voltageSource	phi={-(j - 1)*2*Modelica_3_2.Constants.pi/m for j in 1:m}	phi=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

Equations in Version 3.2	Equations in Version 3.2.1
connect(ground.pin, star.pin_n);	initial equation
	voltageSource.voltageSource.pin_p.reference.gamma=zeros(m); equation  &nbspconnect(ground.pin, star.pin_n);
connect(star.plug_p, voltageSource.plug_n); ...

---

model Electrical.QuasiStationary.MultiPhase.Examples.BalancingDelta

Component	Version 3.2	Version 3.2.1
voltageSource	phi={-(j - 1)*2*Modelica_3_2.Constants.pi/m for j in 1:m}	phi=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

Equations in Version 3.2	Equations in Version 3.2.1
connect(ground.pin, star.pin_n);	initial equation
	voltageSource.voltageSource.pin_p.reference.gamma=zeros(m); equation  &nbspconnect(ground.pin, star.pin_n);
connect(star.plug_p, voltageSource.plug_n); ...

---

model Electrical.QuasiStationary.MultiPhase.Basic.Star

Component	Version 3.2	Version 3.2.1
plugToPins_p		final m=m

---

model Electrical.QuasiStationary.MultiPhase.Basic.Delta

Component	Version 3.2	Version 3.2.1
plugToPins_p		final m=m
plugToPins_n		final m=m

---

model Electrical.QuasiStationary.MultiPhase.Basic.VariableResistor

Component	Version 3.2	Version 3.2.1
R_ref		each unit="Ohm"

---

model Electrical.QuasiStationary.MultiPhase.Basic.VariableConductor

Component	Version 3.2	Version 3.2.1
G_ref		each unit="S"

---

model Electrical.QuasiStationary.MultiPhase.Basic.VariableCapacitor

Component	Version 3.2	Version 3.2.1
C		each unit="F"

---

model Electrical.QuasiStationary.MultiPhase.Basic.VariableInductor

Component	Version 3.2	Version 3.2.1
L		each unit="H"

---

model Electrical.QuasiStationary.MultiPhase.Sensors.FrequencySensor

Component	Version 3.2	Version 3.2.1
potentialSensor	Present
plugToPins_p	Present
frequencySensor		Present
plugToPin_p		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(plug_p, plugToPins_p.plug_p);	connect(plug_p, plugToPin_p.plug_p);
connect(plugToPins_p.pin_p, potentialSensor.pin);	connect(plugToPin_p.pin_p, frequencySensor.pin);
connect(potentialSensor.y, y);	connect(frequencySensor.y, y);

---

model Electrical.QuasiStationary.MultiPhase.Sensors.PowerSensor

Equations in Version 3.2	Equations in Version 3.2.1
... connect(sum.y, y);
connect(currentP, currentP);

---

model Electrical.QuasiStationary.MultiPhase.Sources.VoltageSource

Component	Version 3.2	Version 3.2.1
phi	={0 - (j - 1)*2*pi/m for j in 1:m}	=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

---

model Electrical.QuasiStationary.MultiPhase.Sources.CurrentSource

Component	Version 3.2	Version 3.2.1
phi	={0 - (j - 1)*2*pi/m for j in 1:m}	=-Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

---

model Electrical.QuasiStationary.MultiPhase.Interfaces.TwoPlug

Component	Version 3.2	Version 3.2.1
omega	=der(plug_p.reference.gamma)

Equations in Version 3.2	Equations in Version 3.2.1
	omega = der(plug_p.reference.gamma);
v = plug_p.pin.v - plug_n.pin.v; ...

---

model Electrical.QuasiStationary.MultiPhase.Interfaces.OnePort

Component	Version 3.2	Version 3.2.1
omega	=der(plug_p.reference.gamma)

Equations in Version 3.2	Equations in Version 3.2.1
... plug_p.reference.gamma = plug_n.reference.gamma;
	omega = der(plug_p.reference.gamma);
v = plug_p.pin.v - plug_n.pin.v; ...

---

model Electrical.QuasiStationary.MultiPhase.Interfaces.AbsoluteSensor

Component	Version 3.2	Version 3.2.1
omega	=der(plug_p.reference.gamma)

Equations in Version 3.2	Equations in Version 3.2.1
	omega = der(plug_p.reference.gamma);

---

model Electrical.Spice3.Examples.Inverter

Component	Version 3.2	Version 3.2.1
mp		Sinternal(start=0)
		IC=-1e40
mn		IC=-1e40

---

model Electrical.Spice3.Examples.InvertersApartRecord

Component	Version 3.2	Version 3.2.1
MPmos		CBD=0
		CBS=0
MNmos		CBD=0
		CBS=0
mp1		IC=-1e40
mn1		IC=-1e40
mp2		IC=-1e40
mn2		IC=-1e40
c1		IC=0
		UIC=true
c2		IC=0
		UIC=true

---

model Electrical.Spice3.Examples.InvertersExtendedModel

Component	Version 3.2	Version 3.2.1
mp1		IC=-1e40
mn1		IC=-1e40
mp2		IC=-1e40
mn2		IC=-1e40
c1		IC=0
		UIC=true
c2		IC=0
		UIC=true

---

model Electrical.Spice3.Examples.FourInverters

Component	Version 3.2	Version 3.2.1
modp		CBD=0
		CBS=0
modn		CBD=0
		CBS=0
mp1		IC=-1e40
mn1		IC=-1e40
mp2		IC=-1e40
mn2		IC=-1e40
mp3		IC=-1e40
mp4		IC=-1e40
mn3		IC=-1e40
mn4		IC=-1e40
c1		IC=0
		UIC=true
c2		IC=0
		UIC=true
c3		IC=0
		UIC=true
c4		IC=0
		UIC=true

---

model Electrical.Spice3.Examples.Nand

Component	Version 3.2	Version 3.2.1
mp1	modelcard(PHI=0.7)	modelcard(PHI=0.7, CBD=0, CBS=0)
		Sinternal(start=0)
		IC=-1e40
mp2	modelcard(PHI=0.7)	modelcard(PHI=0.7, CBD=0, CBS=0)
		IC=-1e40
mn2		Dinternal(start=0)
		modelcard(CBD=0, CBS=0)
		IC=-1e40
mn1		modelcard(CBD=0, CBS=0)
		IC=-1e40

---

model Electrical.Spice3.Examples.Nor

Component	Version 3.2	Version 3.2.1
mp1		Dinternal(start=0, fixed=true)
		Sinternal(start=0, fixed=true)
		IC=-1e40
mp2		Dinternal(start=0, fixed=true)
		Sinternal(start=0, fixed=true)
		IC=-1e40
mn1		Dinternal(start=0, fixed=true)
		Sinternal(start=0, fixed=true)
		IC=-1e40
mn2		Dinternal(start=0, fixed=true)
		Sinternal(start=0, fixed=true)
		IC=-1e40

---

model Electrical.Spice3.Examples.Graetz

Component	Version 3.2	Version 3.2.1
D1		IC=-1e40
		SENS_AREA=false
		pin(start=0, fixed=true)
D3		IC=-1e40
		SENS_AREA=false
		n(v(start=0, fixed=true))
D4		IC=-1e40
		SENS_AREA=false
D2		IC=-1e40
		SENS_AREA=false

---

model Electrical.Spice3.Examples.Oscillator

Component	Version 3.2	Version 3.2.1
T1		vbe(start=0, fixed=true)
T2		vbe(start=0, fixed=true)

---

model Electrical.Spice3.Basic.C_Capacitor

Component	Version 3.2	Version 3.2.1
vinternal	start=IC
	fixed=UIC

Equations in Version 3.2	Equations in Version 3.2.1
vinternal = p.v - n.v;	initial equation
i = C*der(vinternal);	vinternal=IC;
	equation    &nbspvinternal = p.v - n.v; i = C*der(vinternal);

---

model Electrical.Spice3.Basic.L_Inductor

Component	Version 3.2	Version 3.2.1
iinternal	start=IC
	fixed=UIC
ICP		Present

Equations in Version 3.2	Equations in Version 3.2.1
iinternal = p.i;	initial equation
L*der(iinternal) = v;	if UIC then
	iinternal = IC; else der(iinternal) = 0; end if; equation  &nbspiinternal = p.i; L*der(iinternal) = v + ICP.v; ICP.L=L; ICP.di = der(iinternal);

---

model Electrical.Spice3.Sources.V_pulse

Component	Version 3.2	Version 3.2.1
counter		fixed=true
counter2		fixed=true

---

model Electrical.Spice3.Sources.V_pwl

Component	Version 3.2	Version 3.2.1
tab		protected
	table=table	table=tablenew
x		Present
tlast		Present
valuelast		Present
lastvaluematrix		Present
tablenew		Present

---

model Electrical.Spice3.Sources.I_pwl

Component	Version 3.2	Version 3.2.1
tab		protected
	table=table	table=tablenew
x		Present
tlast		Present
valuelast		Present
lastvaluematrix		Present
tablenew		Present

---

model Electrical.Spice3.Internal.MOS

Component	Version 3.2	Version 3.2.1
C		constant
Dinternal	Real	SIunits.Voltage
Sinternal	Real	SIunits.Voltage
ird	Real	SIunits.Current
irs	Real	SIunits.Current
ibdgmin	Real	SIunits.Current
ibsgmin	Real	SIunits.Current
icBD	Real	SIunits.Current
icBS	Real	SIunits.Current
icGB	Real	SIunits.Current
icGS	Real	SIunits.Current
icGD	Real	SIunits.Current

---

record Electrical.Spice3.Internal.ModelcardMOS

Component	Version 3.2	Version 3.2.1
TNOM	=-1e40	=27

---

model Electrical.Spice3.Internal.MOS2

Component	Version 3.2	Version 3.2.1
TEMP	Real	SIunits.Temp_C
p	=Mos2.mos2RenameParameters(modelcard, C)	=Spice3.Internal.Mos2.mos2RenameParametersRevised(modelcard)
m	=Mos2.mos2RenameParametersDev(modelcard, mtype, W, L, AD, AS, PD, PS, NRD, NRS, OFF, IC, TEMP)	=Spice3.Internal.Mosfet.mosfetRenameParametersDev(W, L, AD, AS, PD, PS, NRD, NRS, OFF, IC_VDS, IC_VGS, IC_VBS, UIC, TEMP)
vp	=Mos2.mos2ModelLineParamsInitEquations(p, C, m_type)	=Spice3.Internal.Mos2.mos2ModelLineParamsInitEquations(p, C, m_type)
c1	=Mos.mos2CalcInitEquations(p, C, vp, m)	=Spice3.Internal.Mos.mos2CalcInitEquations(p, C, vp, m)
c2	=Mos.mos2CalcCalcTempDependencies(p, C, vp, m, c1, m_type)	=Spice3.Internal.Mos.mos2CalcCalcTempDependencies(p, C, vp, m, c1, m_type)
Dinternal	Real	SIunits.Voltage
Sinternal	Real	SIunits.Voltage
ird	Real	SIunits.Current
irs	Real	SIunits.Current
ibdgmin	Real	SIunits.Current
ibsgmin	Real	SIunits.Current
icBD	Real	SIunits.Current
icBS	Real	SIunits.Current
icGB	Real	SIunits.Current
icGS	Real	SIunits.Current
icGD	Real	SIunits.Current
IC_VDS		Present
IC_VGS		Present
IC_VBS		Present
UIC		Present
m1		Present
p1		Present
c11		Present
c22		Present
vBD		Present
vBS		Present
vGB		Present
vGD		Present
cc_obsolete		Present
p_obsolete		Present

Equations in Version 3.2	Equations in Version 3.2.1
... assert( NRS <> 0, "NRS, length of source in squares, must not be zero");
	cc = Spice3.Internal.Mos.mos2CalcNoBypassCodeRevised(        &nbspm1,        &nbspm_type,        &nbspc22,        &nbspp1,        &nbspm_bInit,         {G.v,B.v,Dinternal,Sinternal}); vBD = B.v - Dinternal; vBS = B.v - Sinternal; vGB = G.v - B.v; vGD = G.v - Dinternal; vGS = G.v - Sinternal; ird * c11.m_drainResistance = (D.v - Dinternal); irs * c11.m_sourceResistance = (S.v - Sinternal); icBD = cc.cBD * der(vBD); icBS = cc.cBS * der(vBS); icGB = cc.cGB * der(vGB); icGD = cc.cGD * der(vGD); icGS = cc.cGS * der(vGS); ibsgmin = Spice3.Internal.SpiceConstants.CKTgmin*(B.v -      &nbspSinternal); ibdgmin = Spice3.Internal.SpiceConstants.CKTgmin*(B.v -      &nbspDinternal); G.i = icGB + icGD + icGS; B.i = cc.iBD + cc.iBS+ ibdgmin + ibsgmin -icGB + icBD + icBS; D.i = ird; S.i = irs; 0 = -ird + cc.idrain - cc.iBD - ibdgmin - icGD - icBD; 0 = -irs - cc.idrain - cc.iBS - ibsgmin - icGS - icBS;
vDS = D.v - S.v;
vGS = G.v - S.v;	(cc_obsolete,qm) = Spice3.Internal.Mos.mos2CalcNoBypassCode( m, m_type, c2, p, C, vp, m_bInit, {G.v,B.v,Dinternal,Sinternal});
(cc,qm) = Mos.mos2CalcNoBypassCode( m, m_type, c2, p, C, vp, m_bInit, {G.v,B.v,Dinternal,Sinternal});	icqmGB = 0;
ird * c1.m_drainResistance = (D.v - Dinternal);	icqmGS = 0;
irs * p.m_sourceResistance = (S.v - Sinternal);	icqmGD = 0;
icBD = cc.cBD * (der(B.v) - der(Dinternal)); icBS = cc.cBS * (der(B.v) - der(Sinternal)); icGB = cc.cGB * (der(G.v) - der(B.v)); icGD = cc.cGD * (der(G.v) - der(Dinternal)); icGS = cc.cGS * (der(G.v) - der(Sinternal)); icqmGB = qm.qm_capgb*(der(G.v) - der(B.v)); icqmGS = qm.qm_capgs*(der(G.v) - der(Sinternal)); icqmGD = qm.qm_capgd*(der(G.v) - der(Dinternal)); ibsgmin = SpiceConstants.CKTgmin*(B.v - Sinternal); ibdgmin = SpiceConstants.CKTgmin*(B.v - Dinternal); G.i = icGB + icGD + icGS + icqmGB + icqmGD + icqmGS; B.i = cc.iBD + cc.iBS+ ibdgmin + ibsgmin -icGB + icBD + icBS - icqmGB; D.i = ird; S.i = irs; 0 = -ird + cc.idrain - cc.iBD - ibdgmin - icGD - icBD - icqmGD; 0 = -irs - cc.idrain - cc.iBS - ibsgmin - icGS - icBS - icqmGS;

---

record Electrical.Spice3.Internal.ModelcardMOS2

Component	Version 3.2	Version 3.2.1
NFS	Real	SIunits.Conversions.NonSIunits.PerArea_cm
XJ	Real	SIunits.Length
UCRIT	Real	Electrical.Spice3.Types.ElectricFieldStrength_cm
VMAX	Real	SIunits.Velocity

---

model Electrical.Spice3.Internal.BJT

Component	Version 3.2	Version 3.2.1
p	=Bjt3.bjtRenameParameters(modelcard, Con)	=Spice3.Internal.Bjt3.bjtRenameParameters(modelcard, Con, TBJT)
p1	=Bjt3.bjtRenameParametersDev(AREA, OFF, IC_VBE, IC_VCE, SENS_AREA)	=Spice3.Internal.Bjt3.bjtRenameParametersDev(AREA, OFF, IC_VBE, IC_VCE, SENS_AREA)
m	=Bjt3.bjtRenameParametersDevTemp(TEMP)	=Spice3.Internal.Bjt3.bjtRenameParametersDevTemp(TEMP)
vl	=Bjt3.bjtModelLineInitEquations(p)	=Spice3.Internal.Bjt3.bjtModelLineInitEquations(p)
c	=Bjt3.bjt3CalcTempDependencies(p1, p, m, vl)	=Spice3.Internal.Bjt3.bjt3CalcTempDependencies(p1, p, m, vl)
v	=Bjt3.bjtInitEquations(p1, p, vl)	=Spice3.Internal.Bjt3.bjtInitEquations(p1, p, vl)
p2	Present

Equations in Version 3.2	Equations in Version 3.2.1
... vBC = B.v - C.v;
(cc,capbe,capbc,capbx) = Bjt3.bjtNoBypassCode( m, p1, p, c, v, vl, {C.v,B.v,E.v,Cinternal,Binternal,Einternal}, m_bInit);	(cc,capbe,capbc,capbx) = Spice3.Internal.Bjt3.bjtNoBypassCode( m, p1, p, c, v, vl, {C.v,B.v,E.v,Cinternal,Binternal,Einternal}, m_bInit);
icapbe = if (m_bInit) then 0.0 else capbe*(der(Binternal) - der(Einternal)); ... irb * p.m_baseResist = (B.v - Binternal);
ibcgmin = SpiceConstants.CKTgmin * (Binternal - Cinternal);	ibcgmin = Spice3.Internal.SpiceConstants.CKTgmin*( Binternal - Cinternal);
ibegmin = SpiceConstants.CKTgmin * (Binternal - Einternal);	ibegmin = Spice3.Internal.SpiceConstants.CKTgmin*( Binternal - Einternal);
C.i = irc; ...

---

model Electrical.Spice3.Internal.DIODE

Component	Version 3.2	Version 3.2.1
C		constant

---

model Electrical.Spice3.Internal.R_SEMI

Component	Version 3.2	Version 3.2.1
C		constant

---

record Electrical.Spice3.Internal.SpiceConstants

Component	Version 3.2	Version 3.2.1
CONSTboltz		Present

---

function Electrical.Spice3.Internal.Functions.energyGapDepTemp

Component	Version 3.2	Version 3.2.1
gap0	Present
coeff1	Present
coeff2	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
ret := gap0 - (coeff1 * temp * temp) / (temp + coeff2);	ret := Spice3.Internal.MaterialParameters.EnergyGapSi - ( Spice3.Internal.MaterialParameters.FirstBandCorrFactorSi *temp*temp)/(temp + Spice3.Internal.MaterialParameters.SecondBandCorrFactorSi);

---

function Electrical.Spice3.Internal.Functions.junctionPotDepTemp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
phibtemp := energyGapDepTemp( temp);	phibtemp := Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(temp);
phibtnom = energyGapDepTemp( tnom);	phibtnom = Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(tnom);
vt = SpiceConstants.CONSTKoverQ * temp;	vt = Spice3.Internal.SpiceConstants.CONSTKoverQ* temp;
ret = (phi0 - phibtnom)*temp/tnom + phibtemp + vt*3*    &nbspModelica_3_2.Math.log(tnom/temp); ...

---

function Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET

Component	Version 3.2	Version 3.2.1
ret	SIunits.Current	Real

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
vt := SpiceConstants.CONSTKoverQ * temp;	vt := Spice3.Internal.SpiceConstants.CONSTKoverQ* temp;
vtnom = SpiceConstants.CONSTKoverQ * tnom;	vtnom = Spice3.Internal.SpiceConstants.CONSTKoverQ* tnom;
energygaptnom = energyGapDepTemp( tnom);	energygaptnom = Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(tnom);
energygaptemp = energyGapDepTemp( temp);	energygaptemp = Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(temp);
ret = satcur0 * exp( energygaptnom / vtnom - energygaptemp / vt); ...

---

function Electrical.Spice3.Internal.Functions.junctionVCrit

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
vte := SpiceConstants.CONSTKoverQ * temp * ncoeff;	vte := Spice3.Internal.SpiceConstants.CONSTKoverQ* temp*ncoeff;
ret = vte*Modelica_3_2.Math.log(vte/(sqrt(2)*satcur)); ...

---

function Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3

Component	Version 3.2	Version 3.2.1
phi0	Real	SIunits.Voltage
junctionpot	Real	SIunits.Voltage
phibtemp	Real	SIunits.Voltage
phibtnom	Real	SIunits.Voltage
vt	Real	SIunits.Voltage
vtnom	Real	SIunits.Voltage

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
phibtemp := energyGapDepTemp( temp);	phibtemp := Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(temp);
phibtnom = energyGapDepTemp( tnom);	phibtnom = Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp(tnom);
vt = SpiceConstants.CONSTKoverQ * temp;	vt = Spice3.Internal.SpiceConstants.CONSTKoverQ * temp;
vtnom = SpiceConstants.CONSTKoverQ * tnom;	vtnom = Spice3.Internal.SpiceConstants.CONSTKoverQ * tnom;
arg = -phibtemp/(2*Modelica_3_2.Constants.k*temp) + 1.1150877/( Modelica_3_2.Constants.k*(2*SpiceConstants.REFTEMP));	arg = -phibtemp/(2*Modelica.Constants.k*temp) + 1.1150877/(Modelica.Constants.k*(2*Spice3.Internal.SpiceConstants.REFTEMP));
fact2 = temp/SpiceConstants.REFTEMP;	fact2 = temp/Spice3.Internal.SpiceConstants.REFTEMP;
pbfact = -2*vt*(1.5*Modelica_3_2.Math.log(fact2) + SpiceConstants.CHARGE *arg);	pbfact = -2*vt*(1.5*Modelica.Math.log(fact2)+Spice3.Internal.SpiceConstants.CHARGE*arg);
arg1 = -phibtnom/(Modelica_3_2.Constants.k*2*tnom) + 1.1150877/(2* Modelica_3_2.Constants.k*SpiceConstants.REFTEMP);	arg1 = -phibtnom/(Modelica.Constants.k*2*tnom) + 1.1150877/(2*Modelica.Constants.k*Spice3.Internal.SpiceConstants.REFTEMP);
fact1 = tnom/SpiceConstants.REFTEMP;	fact1 = tnom/Spice3.Internal.SpiceConstants.REFTEMP;
pbfact1 = -2*vtnom*(1.5*Modelica_3_2.Math.log(fact1) + SpiceConstants.CHARGE*arg1);	pbfact1 = -2 * vtnom*(1.5*Modelica.Math.log(fact1)+Spice3.Internal.SpiceConstants.CHARGE*arg1);
pbo = (phi0-pbfact1)/fact1; ... gmanew = (junctionpot-pbo)/pbo;
jucntioncap = cap0 / (1+mcoeff* (400e-6*(tnom-SpiceConstants.REFTEMP)-gmaold)) * (1+mcoeff* (400e-6*(temp-SpiceConstants.REFTEMP)-gmanew));	jucntioncap = cap0 / (1+mcoeff* (400e-6*(tnom-Spice3.Internal.SpiceConstants.REFTEMP)-gmaold)) * (1+mcoeff* (400e-6*(temp-Spice3.Internal.SpiceConstants.REFTEMP)-gmanew));

---

function Electrical.Spice3.Internal.Functions.junctionCapCoeffs

Component	Version 3.2	Version 3.2.1
phij	Real	SIunits.Voltage
f1	Real	SIunits.Voltage

---

function Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFET

Equations in Version 3.2	Equations in Version 3.2.1
... if (satcur > 1e-101) then
vte = SpiceConstants.CONSTKoverQ * temp * ncoeff;	vte = Spice3.Internal.SpiceConstants.CONSTKoverQ* temp*ncoeff;
max_exponent = Modelica_3_2.Math.log(max_current/satcur); ... out_current = out_cond * voltage;
out_cond = out_cond + SpiceConstants.CKTgmin;	out_cond = out_cond + Spice3.Internal.SpiceConstants.CKTgmin;
elseif (voltage >= max_exponent * vte) then ... evbd = exp( voltage / vte);
out_cond = satcur*evbd/vte + SpiceConstants.CKTgmin;	out_cond = satcur*evbd/vte + Spice3.Internal.SpiceConstants.CKTgmin;
out_current = satcur *(evbd-1); ...

---

function Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
vt := SpiceConstants.CONSTKoverQ*temp;	vt := Spice3.Internal.SpiceConstants.CONSTKoverQ* temp;
vte = emissioncoeff * vt; ...

---

function Electrical.Spice3.Internal.Functions.junctionVoltage23SPICE3

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
vt := SpiceConstants.CONSTKoverQ*temp;	vt := Spice3.Internal.SpiceConstants.CONSTKoverQ* temp;
v23 = vb; ... else
tol = SpiceConstants.CKTreltol*cbv;	tol = Spice3.Internal.SpiceConstants.CKTreltol* cbv;
v23 = vb - vt*Modelica_3_2.Math.log(1 + cbv/satcur); ...

---

function Electrical.Spice3.Internal.Functions.junction3

Equations in Version 3.2	Equations in Version 3.2.1
... if (satcur > 1.0e-101) then
vte = SpiceConstants.CONSTKoverQ*temp*ncoeff;	vte = Spice3.Internal.SpiceConstants.CONSTKoverQ* temp*ncoeff;
max_exponent = Modelica_3_2.Math.log(max_current/satcur); ... evd = exp( voltage / vte);
current = satcur*(evd - 1) + SpiceConstants.CKTgmin*voltage;	current = satcur*(evd - 1) + Spice3.Internal.SpiceConstants.CKTgmin *voltage;
cond = satcur*evd/vte + SpiceConstants.CKTgmin;	cond = satcur*evd/vte + Spice3.Internal.SpiceConstants.CKTgmin;
elseif (voltage >= -v23) then
arg = 3*vte/(voltage*SpiceConstants.CONSTe);	arg = 3*vte/(voltage*Spice3.Internal.SpiceConstants.CONSTe);
arg = arg * arg * arg;
current = -1.*satcur*(1 + arg) + SpiceConstants.CKTgmin*voltage;	current = -1.*satcur*(1 + arg) + Spice3.Internal.SpiceConstants.CKTgmin *voltage;
cond = satcur*3*arg/voltage + SpiceConstants.CKTgmin;	cond = satcur*3*arg/voltage + Spice3.Internal.SpiceConstants.CKTgmin;
else ... evrev = exp( vr / vte);
current = -1.*satcur*evrev + SpiceConstants.CKTgmin*voltage;	current = -1.*satcur*evrev + Spice3.Internal.SpiceConstants.CKTgmin *voltage;
cond = satcur*evrev/vte + SpiceConstants.CKTgmin;	cond = satcur*evrev/vte + Spice3.Internal.SpiceConstants.CKTgmin;
end if; ...

---

function Electrical.Spice3.Internal.Functions.junction2

Equations in Version 3.2	Equations in Version 3.2.1
... if (satcur > 1.0e-101) then
vte = SpiceConstants.CONSTKoverQ*temp*ncoeff;	vte = Spice3.Internal.SpiceConstants.CONSTKoverQ* temp*ncoeff;
max_exponent = Modelica_3_2.Math.log(max_current/satcur); ... evd = exp( voltage / vte);
current = satcur*(evd - 1) + SpiceConstants.CKTgmin*voltage;	current = satcur*(evd - 1) + Spice3.Internal.SpiceConstants.CKTgmin *voltage;
cond = satcur*evd/vte + SpiceConstants.CKTgmin;	cond = satcur*evd/vte + Spice3.Internal.SpiceConstants.CKTgmin;
else
arg = 3*vte/(voltage*SpiceConstants.CONSTe);	arg = 3*vte/(voltage*Spice3.Internal.SpiceConstants.CONSTe);
arg = arg * arg * arg;
current = -1*satcur*(1 + arg) + SpiceConstants.CKTgmin*voltage;	current = -1*satcur*(1 + arg) + Spice3.Internal.SpiceConstants.CKTgmin *voltage;
cond = satcur*3*arg/voltage + SpiceConstants.CKTgmin;	cond = satcur*3*arg/voltage + Spice3.Internal.SpiceConstants.CKTgmin;
end if; ...

---

record Electrical.Spice3.Internal.Mosfet.Mosfet

Component	Version 3.2	Version 3.2.1
m_drainArea	start=SpiceConstants.CKTdefaultMosAD	start=Spice3.Internal.SpiceConstants.CKTdefaultMosAD
m_sourceArea	start=SpiceConstants.CKTdefaultMosAS	start=Spice3.Internal.SpiceConstants.CKTdefaultMosAS
m_drainPerimeter		Present
m_sourcePerimeter		Present
m_uic		Present

---

record Electrical.Spice3.Internal.Mosfet.MosfetModelLineParams

Component	Version 3.2	Version 3.2.1
m_bulkJctBotGradingCoeff	Real	SIunits.LinearTemperatureCoefficient
m_bulkJctSideGradingCoeff	Real	SIunits.LinearTemperatureCoefficient
m_mjswIsGiven		Present
m_cgsoIsGiven		Present
m_cgdoIsGiven		Present
m_cgboIsGiven		Present
m_pbIsGiven		Present

---

record Electrical.Spice3.Internal.Mosfet.MosfetCalc

Component	Version 3.2	Version 3.2.1
m_lEff	Real	SIunits.Length

---

record Electrical.Spice3.Internal.Mos.MosModelLineParams

Component	Version 3.2	Version 3.2.1
m_surfaceStateDensityIsGiven		start=0
m_tnom	start=SpiceConstants.CKTnomTemp	start=Spice3.Internal.SpiceConstants.CKTnomTemp

---

record Electrical.Spice3.Internal.Mos.MosCalc

Component	Version 3.2	Version 3.2.1
m_tSurfMob	Real	SIunits.Conversions.NonSIunits.Area_cmPerVoltageSecond
m_tSatCurDens	Real	SIunits.CurrentDensity
m_tCj	Real	SIunits.CapacitancePerArea
m_tCjsw	Real	SIunits.Permittivity
m_tDepCap	Real	SIunits.Voltage
m_f1b	Real	SIunits.Voltage
m_f1s	Real	SIunits.Voltage
m_dVt	Real	SIunits.Voltage

---

function Electrical.Spice3.Internal.Mos.mosCalcInitEquations

Equations in Version 3.2	Equations in Version 3.2.1
... out_c.m_capOx = in_vp.m_oxideCapFactor * out_c.m_lEff * in_m.m_width;
	out_c.m_tTransconductance = 0;
	out_c.m_tSurfMob = 0; out_c.m_tPhi = 0.7; out_c.m_tVto = 1.; out_c.m_tSatCurDens = 0; out_c.m_tDrainSatCur = 0; out_c.m_tSourceSatCur = 0; out_c.m_tCBDb = 0; out_c.m_tCBDs = 0; out_c.m_tCBSb = 0; out_c.m_tCBSs = 0; out_c.m_tCj = 0; out_c.m_tCjsw = 0; out_c.m_tBulkPot = 0.7; out_c.m_tDepCap = 0.35; out_c.m_tVbi = 1.; out_c.m_VBScrit = 0.7; out_c.m_VBDcrit = 0.7; out_c.m_f1b = 0; out_c.m_f2b = 0; out_c.m_f3b = 0; out_c.m_f1s = 0; out_c.m_f2s = 0; out_c.m_f3s = 0; out_c.m_dVt = 0; out_c.m_capgd = 0; out_c.m_capgs = 0; out_c.m_capgb = 0; out_c.m_qgs = 0; out_c.m_qgd = 0; out_c.m_qgb = 0; out_c.m_vds = 0; out_c.m_vgs = 0; out_c.m_vbs = 0; out_c.m_cbs = 0; out_c.m_gbs = 0; out_c.m_cbd = 0; out_c.m_gbd = 0; out_c.m_cdrain = 0; out_c.m_gds = 0; out_c.m_gm = 0; out_c.m_gmbs = 0; out_c.m_capbsb = 0; out_c.m_chargebsb = 0; out_c.m_capbss = 0; out_c.m_chargebss = 0; out_c.m_capbdb = 0; out_c.m_chargebdb = 0; out_c.m_capbds = 0; out_c.m_chargebds = 0; out_c.m_Beta = 0; out_c.m_von = 0; out_c.m_vdsat = 0; out_c.m_mode = 1;

---

function Electrical.Spice3.Internal.Mos.mosCalcCalcTempDependencies

Equations in Version 3.2	Equations in Version 3.2.1
... out_c.m_tSurfMob = in_p.m_surfaceMobility / ratio4;
out_c.m_tPhi = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionPotDepTemp( in_vp.m_phi, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tPhi = Spice3.Internal.Functions.junctionPotDepTemp( in_vp.m_phi, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tVbi = in_vp.m_vt0 - in_m_type*(in_vp.m_gamma*sqrt(in_vp.m_phi)) + 0.5*( Modelica_3_2.Electrical.Spice3.Internal.Functions.energyGapDepTemp( in_p.m_tnom) - Modelica_3_2.Electrical.Spice3.Internal.Functions.energyGapDepTemp( in_m.m_dTemp)) + in_m_type*0.5*(out_c.m_tPhi - in_vp.m_phi);	out_c.m_tVbi = in_vp.m_vt0 - in_m_type*(in_vp.m_gamma*sqrt(in_vp.m_phi)) + 0.5*(Spice3.Internal.Functions.energyGapDepTemp_old( in_p.m_tnom) - Spice3.Internal.Functions.energyGapDepTemp_old( in_m.m_dTemp)) + in_m_type*0.5*(out_c.m_tPhi - in_vp.m_phi);
out_c.m_tVto = out_c.m_tVbi + in_m_type * in_vp.m_gamma * sqrt(out_c.m_tPhi);
out_c.m_tBulkPot = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionPotDepTemp( in_p.m_bulkJctPotential, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tBulkPot = Spice3.Internal.Functions.junctionPotDepTemp( in_p.m_bulkJctPotential, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tDepCap = in_p.m_fwdCapDepCoeff * out_c.m_tBulkPot;
if (in_p.m_jctSatCurDensity == 0.0 or in_m.m_sourceArea == 0.0 or in_m.m_drainArea == 0.0) then
out_c.m_tDrainSatCur = Modelica_3_2.Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCur, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tDrainSatCur = Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCur, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tSourceSatCur = out_c.m_tDrainSatCur;
out_c.m_VBScrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);	out_c.m_VBScrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);
out_c.m_VBDcrit = out_c.m_VBScrit;
else
out_c.m_tSatCurDens = Modelica_3_2.Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCurDensity, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tSatCurDens = Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCurDensity, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tDrainSatCur = out_c.m_tSatCurDens * in_m.m_drainArea;
out_c.m_tSourceSatCur = out_c.m_tSatCurDens * in_m.m_sourceArea;
out_c.m_VBScrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);	out_c.m_VBScrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);
out_c.m_VBDcrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tDrainSatCur);	out_c.m_VBDcrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tDrainSatCur);
end if;
if ( not (in_p.m_capBDIsGiven > 0.5) or not (in_p.m_capBSIsGiven > 0.5)) then
(res,out_c.m_tCj) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_bulkCapFactor, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(res,out_c.m_tCj) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_bulkCapFactor, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
(res,out_c.m_tCjsw) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_sideWallCapFactor, in_p.m_bulkJctSideGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(res,out_c.m_tCjsw) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_sideWallCapFactor, in_p.m_bulkJctSideGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
(out_c.m_f1s,out_c.m_f2s,out_c.m_f3s) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctSideGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);	(out_c.m_f1s,out_c.m_f2s,out_c.m_f3s) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctSideGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);
end if;
if (in_p.m_capBDIsGiven > 0.5) then
(res,out_c.m_tCBDb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBD, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(res,out_c.m_tCBDb) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBD, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tCBDs = 0.0; ... out_c.m_tCBDb = out_c.m_tCj * in_m.m_drainArea;
out_c.m_tCBDs = out_c.m_tCjsw * in_m.m_drainPerimiter;	out_c.m_tCBDs = out_c.m_tCjsw * in_m.m_drainPerimeter;
end if;
if (in_p.m_capBSIsGiven > 0.5) then
(res,out_c.m_tCBSb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBS, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(res,out_c.m_tCBSb) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBS, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tCBSs = 0.0; ... out_c.m_tCBSb = out_c.m_tCj * in_m.m_sourceArea;
out_c.m_tCBSs = out_c.m_tCjsw * in_m.m_sourcePerimiter;	out_c.m_tCBSs = out_c.m_tCjsw * in_m.m_sourcePerimeter;
end if;
(out_c.m_f1b,out_c.m_f2b,out_c.m_f3b) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctBotGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);	(out_c.m_f1b,out_c.m_f2b,out_c.m_f3b) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctBotGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);
out_c.m_dVt = in_m.m_dTemp * SpiceConstants.CONSTKoverQ;	out_c.m_dVt = in_m.m_dTemp*Spice3.Internal.SpiceConstants.CONSTKoverQ;

---

function Electrical.Spice3.Internal.Mos.mosCalcNoBypassCode

Equations in Version 3.2	Equations in Version 3.2.1
... int_c := in_c;
	out_cc.m_capgd = 0;
int_c.m_vgs = in_m_type * (in_m_pVoltageValues[1] - in_m_pVoltageValues[4]); ... int_c.m_vds = in_m_type * (in_m_pVoltageValues[3] - in_m_pVoltageValues[4]);
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVBSIsGiven >0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVBSIsGiven > 0.5) then
int_c.m_vbs = in_m_type * in_m.m_dICVBS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
int_c.m_vbs = if (in_m.m_off >0.5) then 0. else int_c.m_VBScrit;
end if;
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVDSIsGiven > 0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVDSIsGiven > 0.5) then
int_c.m_vds = in_m_type * in_m.m_dICVDS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
int_c.m_vds = if (in_m.m_off > 0.5) then 0. else (int_c.m_VBDcrit - int_c.m_VBScrit);
end if;
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVGSIsGiven > 0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVGSIsGiven > 0.5) then
int_c.m_vgs = in_m_type * in_m.m_dICVGS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
if ( in_m.m_off > 0.5) then ... vgb = int_c.m_vgs - int_c.m_vbs;
(int_c.m_cbd,int_c.m_gbd) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbd, int_c.m_gbd, vbd, in_m.m_dTemp, 1.0, int_c.m_tDrainSatCur);	(int_c.m_cbd,int_c.m_gbd) = Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbd, int_c.m_gbd, vbd, in_m.m_dTemp, 1.0, int_c.m_tDrainSatCur);
out_cc.iBD = in_m_type * int_c.m_cbd;
(int_c.m_cbs,int_c.m_gbs) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbs, int_c.m_gbs, int_c.m_vbs, in_m.m_dTemp, 1.0, int_c.m_tSourceSatCur);	(int_c.m_cbs,int_c.m_gbs) = Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbs, int_c.m_gbs, int_c.m_vbs, in_m.m_dTemp, 1.0, int_c.m_tSourceSatCur);
out_cc.iBS = in_m_type * int_c.m_cbs; ... if (int_c.m_mode == 1) then
int_c = Mos1.drainCur( int_c.m_vbs, int_c.m_vgs, int_c.m_vds, int_c, in_p, in_C, in_vp, in_m_type);	int_c = Spice3.Internal.Mos1.drainCur( int_c.m_vbs, int_c.m_vgs, int_c.m_vds, int_c, in_p, in_C, in_vp, in_m_type);
else
int_c = Mos1.drainCur( vbd, vgd, -int_c.m_vds, int_c, in_p, in_C, in_vp, in_m_type);	int_c = Spice3.Internal.Mos1.drainCur( vbd, vgd, -int_c.m_vds, int_c, in_p, in_C, in_vp, in_m_type);
end if; ... int_c.m_chargebds = 0.0;
(int_c.m_capbsb,int_c.m_chargebsb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBSb, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);	(int_c.m_capbsb,int_c.m_chargebsb) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBSb, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);
(int_c.m_capbdb,int_c.m_chargebdb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBDb, vbd, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);	(int_c.m_capbdb,int_c.m_chargebdb) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBDb, vbd, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);
if ( not (in_p.m_capBSIsGiven > 0.5)) then
(int_c.m_capbss,int_c.m_chargebss) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBSs, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);	(int_c.m_capbss,int_c.m_chargebss) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBSs, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);
end if;
if (not (in_p.m_capBDIsGiven > 0.5)) then
(int_c.m_capbds,int_c.m_chargebds) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBDs, vbd, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);	(int_c.m_capbds,int_c.m_chargebds) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBDs, vbd, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);
end if; ...

---

function Electrical.Spice3.Internal.Mos.mosCalcDEVqmeyer

Component	Version 3.2	Version 3.2.1
vddif	Real	SIunits.Voltage
vddif1	Real	SIunits.Voltage
vddif2	Real	Electrical.Spice3.Types.VoltageSquare

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
	out_qm.qm_qgs = 0.0;
	out_qm.qm_qgb = 0.0; out_qm.qm_qgd = 0.0; out_qm.qm_vgs = 0.0; out_qm.qm_vgb = 0.0; out_qm.qm_vgd = 0.0;

---

function Electrical.Spice3.Internal.Mos.mos2CalcCalcTempDependencies

Equations in Version 3.2	Equations in Version 3.2.1
... out_c.m_tSurfMob = in_p.m_surfaceMobility / ratio4;
out_c.m_tPhi = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionPotDepTemp( in_vp.m_phi, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tPhi = Spice3.Internal.Functions.junctionPotDepTemp( in_vp.m_phi, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tVbi = in_vp.m_vt0 - in_m_type*(in_vp.m_gamma*sqrt(in_vp.m_phi)) + 0.5*( Modelica_3_2.Electrical.Spice3.Internal.Functions.energyGapDepTemp( in_p.m_tnom) - Modelica_3_2.Electrical.Spice3.Internal.Functions.energyGapDepTemp( in_m.m_dTemp)) + in_m_type*0.5*(out_c.m_tPhi - in_vp.m_phi);	out_c.m_tVbi = in_vp.m_vt0 - in_m_type*(in_vp.m_gamma*sqrt(in_vp.m_phi)) + 0.5*(Spice3.Internal.Functions.energyGapDepTemp( in_p.m_tnom) - Spice3.Internal.Functions.energyGapDepTemp(in_m.m_dTemp)) + in_m_type*0.5*(out_c.m_tPhi - in_vp.m_phi);
out_c.m_tVto = out_c.m_tVbi + in_m_type * in_vp.m_gamma * sqrt(out_c.m_tPhi);
out_c.m_tBulkPot = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionPotDepTemp( in_p.m_bulkJctPotential, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tBulkPot = Spice3.Internal.Functions.junctionPotDepTemp( in_p.m_bulkJctPotential, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tDepCap = in_p.m_fwdCapDepCoeff * out_c.m_tBulkPot;
if (in_p.m_jctSatCurDensity == 0.0 or in_m.m_sourceArea == 0.0 or in_m.m_drainArea == 0.0) then
out_c.m_tDrainSatCur = Modelica_3_2.Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCur, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tDrainSatCur = Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCur, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tSourceSatCur = out_c.m_tDrainSatCur;
out_c.m_VBScrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);	out_c.m_VBScrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);
out_c.m_VBDcrit = out_c.m_VBScrit;
else
out_c.m_tSatCurDens = Modelica_3_2.Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCurDensity, in_m.m_dTemp, in_p.m_tnom);	out_c.m_tSatCurDens = Spice3.Internal.Functions.saturationCurDepTempSPICE3MOSFET( in_p.m_jctSatCurDensity, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tDrainSatCur = out_c.m_tSatCurDens * in_m.m_drainArea;
out_c.m_tSourceSatCur = out_c.m_tSatCurDens * in_m.m_sourceArea;
out_c.m_VBScrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);	out_c.m_VBScrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tSourceSatCur);
out_c.m_VBDcrit = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tDrainSatCur);	out_c.m_VBDcrit = Spice3.Internal.Functions.junctionVCrit( in_m.m_dTemp, 1.0, out_c.m_tDrainSatCur);
end if;
if ( not (in_p.m_capBDIsGiven > 0.5) or not (in_p.m_capBSIsGiven > 0.5)) then
(out_c.m_tCj) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_bulkCapFactor, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(out_c.m_tCj) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_bulkCapFactor, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
(out_c.m_tCjsw) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_sideWallCapFactor, in_p.m_bulkJctSideGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(out_c.m_tCjsw) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_sideWallCapFactor, in_p.m_bulkJctSideGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
(out_c.m_f1s,out_c.m_f2s,out_c.m_f3s) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctSideGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);	(out_c.m_f1s,out_c.m_f2s,out_c.m_f3s) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctSideGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);
end if;
if (in_p.m_capBDIsGiven > 0.5) then
(out_c.m_tCBDb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBD, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(out_c.m_tCBDb) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBD, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tCBDs = 0.0; ... out_c.m_tCBDb = out_c.m_tCj * in_m.m_drainArea;
out_c.m_tCBDs = out_c.m_tCjsw * in_m.m_drainPerimiter;	out_c.m_tCBDs = out_c.m_tCjsw * in_m.m_drainPerimeter;
end if;
if (in_p.m_capBSIsGiven > 0.5) then
(out_c.m_tCBSb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBS, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);	(out_c.m_tCBSb) = Spice3.Internal.Functions.junctionParamDepTempSPICE3( in_p.m_bulkJctPotential, in_p.m_capBS, in_p.m_bulkJctBotGradingCoeff, in_m.m_dTemp, in_p.m_tnom);
out_c.m_tCBSs = 0.0; ... out_c.m_tCBSb = out_c.m_tCj * in_m.m_sourceArea;
out_c.m_tCBSs = out_c.m_tCjsw * in_m.m_sourcePerimiter;	out_c.m_tCBSs = out_c.m_tCjsw * in_m.m_sourcePerimeter;
end if;
(out_c.m_f1b,out_c.m_f2b,out_c.m_f3b) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctBotGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);	(out_c.m_f1b,out_c.m_f2b,out_c.m_f3b) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_bulkJctBotGradingCoeff, in_p.m_fwdCapDepCoeff, out_c.m_tBulkPot);
out_c.m_dVt = in_m.m_dTemp * SpiceConstants.CONSTKoverQ;	out_c.m_dVt = in_m.m_dTemp*Spice3.Internal.SpiceConstants.CONSTKoverQ;

---

function Electrical.Spice3.Internal.Mos.mos2CalcNoBypassCode

Equations in Version 3.2	Equations in Version 3.2.1
... int_c.m_vds = in_m_type * (in_m_pVoltageValues[3] - in_m_pVoltageValues[4]);
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVBSIsGiven >0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVBSIsGiven > 0.5) then
int_c.m_vbs = in_m_type * in_m.m_dICVBS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
int_c.m_vbs = if (in_m.m_off >0.5) then 0. else int_c.m_VBScrit;
end if;
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVDSIsGiven > 0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVDSIsGiven > 0.5) then
int_c.m_vds = in_m_type * in_m.m_dICVDS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
int_c.m_vds = if (in_m.m_off > 0.5) then 0. else (int_c.m_VBDcrit - int_c.m_VBScrit);
end if;
if ( SpiceRoot.useInitialConditions()) and (in_m.m_dICVGSIsGiven > 0.5) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_dICVGSIsGiven > 0.5) then
int_c.m_vgs = in_m_type * in_m.m_dICVGS;
elseif ( SpiceRoot.initJunctionVoltages()) then	elseif ( Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
if ( in_m.m_off > 0.5) then ... end if;
if (int_c.m_vds<>0 and int_c.m_vgs<>0 and int_c.m_vbs<>0 and not (SpiceRoot.useInitialConditions()) and (in_m.m_off<>0)) then	if (int_c.m_vds <> 0 and int_c.m_vgs <> 0 and int_c.m_vbs <> 0 and not ( Spice3.Internal.SpiceRoot.useInitialConditions()) and (in_m.m_off <> 0)) then
int_c.m_vbs = -1; ... if ( int_c.m_vds >= 0) then
int_c.m_vbs = SpiceRoot.limitJunctionVoltage(int_c.m_vbs);	int_c.m_vbs = Spice3.Internal.SpiceRoot.limitJunctionVoltage( int_c.m_vbs);
vbd = int_c.m_vbs - int_c.m_vds;
else
vbd = SpiceRoot.limitJunctionVoltage(vbd);	vbd = Spice3.Internal.SpiceRoot.limitJunctionVoltage( vbd);
int_c.m_vbs = vbd + int_c.m_vds; ... vgb = int_c.m_vgs - int_c.m_vbs;
(int_c.m_cbd,int_c.m_gbd) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbd, int_c.m_gbd, vbd, in_m.m_dTemp, 1.0, int_c.m_tDrainSatCur);	(int_c.m_cbd,int_c.m_gbd) = Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbd, int_c.m_gbd, vbd, in_m.m_dTemp, 1.0, int_c.m_tDrainSatCur);
out_cc.iBD = in_m_type * int_c.m_cbd;
(int_c.m_cbs,int_c.m_gbs) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbs, int_c.m_gbs, int_c.m_vbs, in_m.m_dTemp, 1.0, int_c.m_tSourceSatCur);	(int_c.m_cbs,int_c.m_gbs) = Spice3.Internal.Functions.junction2SPICE3MOSFET( int_c.m_cbs, int_c.m_gbs, int_c.m_vbs, in_m.m_dTemp, 1.0, int_c.m_tSourceSatCur);
out_cc.iBS = in_m_type * int_c.m_cbs; ... if (int_c.m_mode == 1) then
int_c = Mos2.drainCur( int_c.m_vbs, int_c.m_vgs, int_c.m_vds,int_m, int_c, in_p, in_C, in_vp, in_m_type);	int_c = Spice3.Internal.Mos2.drainCur( int_c.m_vbs, int_c.m_vgs, int_c.m_vds,int_m, int_c, in_p, in_C, in_vp, in_m_type);
else
int_c = Mos2.drainCur( vbd, vgd, -int_c.m_vds,int_m, int_c, in_p, in_C, in_vp, in_m_type);	int_c = Spice3.Internal.Mos2.drainCur( vbd, vgd, -int_c.m_vds,int_m, int_c, in_p, in_C, in_vp, in_m_type);
end if; ... int_c.m_chargebds = 0.0;
(int_c.m_capbsb,int_c.m_chargebsb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBSb, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);	(int_c.m_capbsb,int_c.m_chargebsb) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBSb, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);
(int_c.m_capbdb,int_c.m_chargebdb) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBDb, vbd, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);	(int_c.m_capbdb,int_c.m_chargebdb) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBDb, vbd, int_c.m_tDepCap, in_p.m_bulkJctBotGradingCoeff, int_c.m_tBulkPot, int_c.m_f1b, int_c.m_f2b, int_c.m_f3b);
if ( not (in_p.m_capBSIsGiven > 0.5)) then
(int_c.m_capbss,int_c.m_chargebss) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBSs, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);	(int_c.m_capbss,int_c.m_chargebss) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBSs, int_c.m_vbs, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);
end if;
if (not (in_p.m_capBDIsGiven > 0.5)) then
(int_c.m_capbds,int_c.m_chargebds) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( int_c.m_tCBDs, vbd, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);	(int_c.m_capbds,int_c.m_chargebds) = Spice3.Internal.Functions.junctionCap( int_c.m_tCBDs, vbd, int_c.m_tDepCap, in_p.m_bulkJctSideGradingCoeff, int_c.m_tBulkPot, int_c.m_f1s, int_c.m_f2s, int_c.m_f3s);
end if; ...

---

function Electrical.Spice3.Internal.Mos1.mos1RenameParameters

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
intern.m_oxideCapFactor := 0;	intern.m_cgboIsGiven := 0;
	intern.m_cgdoIsGiven = 0; intern.m_cgsoIsGiven = 0; intern.m_mjswIsGiven = 0; intern.m_pbIsGiven = 0; intern.m_surfaceStateDensityIsGiven = 0; intern.m_oxideCapFactor = 0;
intern.m_vtOIsGiven = if (ex.VTO > -1e40) then 1 else 0; ... intern.m_latDiff = ex.LD "In m lateral diffusion (default 0)";
intern.m_jctSatCur = ex.IS "A bulk junction saturation current (default 1e-14)";	intern.m_jctSatCur = ex.IS "A bulk junction saturation current (default 1e-14)";
intern.m_drainResistanceIsGiven = if                                          (ex.RD > -1e40) then 1 else 0; ...

---

function Electrical.Spice3.Internal.Mos1.mos1RenameParametersDev

Equations in Version 3.2	Equations in Version 3.2.1
... dev.m_sourceSquares = NRS "NRS, length of source in squares";
dev.m_drainPerimiter = PD "PD, Drain perimeter";	dev.m_drainPerimeter = PD "PD, Drain perimeter";
dev.m_sourcePerimiter = PS "PS, Source perimeter";	dev.m_sourcePerimeter = PS "PS, Source perimeter";
dev.m_dICVDSIsGiven = if (IC > -1e40) then 1 else 0   "ICVDS IsGivenValue"; ... dev.m_off = OFF "Non-zero to indicate device is off for dc analysis";
dev.m_bPMOS = mtype "P type MOSfet model";	dev.m_bPMOS = mtype "P type MOSFET model";
dev.m_nLevel = ex.LEVEL "Level"; ... dev.m_dTemp = TEMP + SpiceConstants.CONSTCtoK "Device temperature";
	dev.m_drainPerimiter = 0;
	dev.m_sourcePerimiter = 0; dev.m_uic = false;

---

record Electrical.Spice3.Internal.Mos2.Mos2ModelLineParams

Component	Version 3.2	Version 3.2.1
m_critField	Real	Electrical.Spice3.Types.ElectricFieldStrength_cm
m_maxDriftVel	Real	SIunits.Velocity
m_junctionDepth	Real	SIunits.Length
m_fastSurfaceStateDensity	Real	SIunits.Conversions.NonSIunits.PerArea_cm
m_xd		Present

---

function Electrical.Spice3.Internal.Mos2.mos2RenameParameters

Equations in Version 3.2	Equations in Version 3.2.1
... intern.m_transconductance = if (ex.KP > -1e40) then ex.KP else 2e-5;
intern.m_tnom = if (ex.TNOM > -1e40) then ex.TNOM + SpiceConstants.CONSTCtoK else 300.15;	intern.m_tnom = if (ex.TNOM > -1e40) then ex.TNOM + Spice3.Internal.SpiceConstants.CONSTCtoK else 300.15;
intern.m_jctSatCurDensity = ex.JS; ...

---

function Electrical.Spice3.Internal.Mos2.mos2RenameParametersDev

Equations in Version 3.2	Equations in Version 3.2.1
... assert(ex.LEVEL== 1, "only MOS Level1 implemented");
dev.m_dTemp = TEMP + SpiceConstants.CONSTCtoK;	dev.m_dTemp = TEMP + Spice3.Internal.SpiceConstants.CONSTCtoK;

---

record Electrical.Spice3.Internal.Diode.DiodeModelLineParams

Component	Version 3.2	Version 3.2.1
m_gradingCoeff	Real	SIunits.LinearTemperatureCoefficient
m_nomTemp	SIunits.Temp_C	SIunits.Temp_K

---

function Electrical.Spice3.Internal.Diode.diodeNoBypassCode

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
	m_dCurrent = out_cc.m_dCurrent;
(m_dCap,m_dCharge) =    &nbspModelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapTransTime(              &nbspin_c.m_tJctCap,              &nbspm_dPNVoltage,              &nbspin_c.m_tJctPot*in_p.m_depletionCapCoeff,              &nbspin_p.m_gradingCoeff,              &nbspin_p.m_junctionPot,              &nbspin_c.m_tF1,              &nbspin_c.m_f2,              &nbspin_c.m_f3,              &nbspin_p.m_transitTime,              &nbspm_dCond,              &nbspm_dCurrent); ...

---

function Electrical.Spice3.Internal.Rsemiconductor.resistorInitEquations

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
out.m_dWidth := in_p.m_dWidth;	out.m_dLength := 0;
	out.m_dConduct = 0; out.m_dCond_dTemp = 0; out.m_dWidth = in_p.m_dWidth;
if ( in_p.m_dResIsGiven < 0.5) then ...

---

record Electrical.Spice3.Internal.Bjt3.BjtModelLineParams

Component	Version 3.2	Version 3.2.1
m_tnom	start=SpiceConstants.CKTnomTemp	start=Spice3.Internal.SpiceConstants.CKTnomTemp
m_invRollOffF	Real	Electrical.Spice3.Types.InverseElectricCurrent
m_invRollOffR	Real	Electrical.Spice3.Types.InverseElectricCurrent

---

record Electrical.Spice3.Internal.Bjt3.Bjt3

Component	Version 3.2	Version 3.2.1
m_invRollOffF	Real	Electrical.Spice3.Types.InverseElectricCurrent
m_invRollOffR	Real	Electrical.Spice3.Types.InverseElectricCurrent

---

function Electrical.Spice3.Internal.Bjt3.bjt3CalcTempDependencies

Component	Version 3.2	Version 3.2.1
arg	Real	Electrical.Spice3.Types.GapEnergyPerEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
fact1 := in_p.m_tnom/SpiceConstants.REFTEMP;	fact1 := in_p.m_tnom/Spice3.Internal.SpiceConstants.REFTEMP;
vt = m.m_dTemp*SpiceConstants.CONSTKoverQ;	vt = m.m_dTemp*Spice3.Internal.SpiceConstants.CONSTKoverQ;
fact2 = m.m_dTemp/SpiceConstants.REFTEMP;	fact2 = m.m_dTemp/Spice3.Internal.SpiceConstants.REFTEMP;
egfet = 1.16 - (7.02e-4 * m.m_dTemp * m.m_dTemp) / (m.m_dTemp + 1108);
arg = -egfet/(2*Modelica_3_2.Constants.k*m.m_dTemp) + 1.1150877/( Modelica_3_2.Constants.k*(SpiceConstants.REFTEMP + SpiceConstants.REFTEMP));	arg = -egfet/(2*Modelica.Constants.k*m.m_dTemp) + 1.1150877/(Modelica.Constants.k *(Spice3.Internal.SpiceConstants.REFTEMP + Spice3.Internal.SpiceConstants.REFTEMP));
pbfact = -2*vt*(1.5*Modelica_3_2.Math.log(fact2) + SpiceConstants.CHARGE *arg);	pbfact = -2*vt*(1.5*Modelica.Math.log(fact2) + Spice3.Internal.SpiceConstants.CHARGE *arg);
ratlog = Modelica_3_2.Math.log(m.m_dTemp/in_p.m_tnom); ... out_c.m_tBCleakCur = in_vl.m_leakBCcurrent * exp(factlog / in_p.m_leakBCemissionCoeff) / bfactor                         * in_p3.m_area;
out_c.m_tBEcap = in_p.m_depletionCapBE/(1 + in_p.m_junctionExpBE*(4e-4 *(in_p.m_tnom - SpiceConstants.REFTEMP) - gmaold));	out_c.m_tBEcap = in_p.m_depletionCapBE/(1 + in_p.m_junctionExpBE*(4e-4*( in_p.m_tnom - Spice3.Internal.SpiceConstants.REFTEMP) - gmaold));
out_c.m_tBEpot = fact2 * pbo + pbfact;
gmanew = (out_c.m_tBEpot - pbo) / pbo;
out_c.m_tBEcap = out_c.m_tBEcap*(1 + in_p.m_junctionExpBE*(4e-4*(m.m_dTemp - SpiceConstants.REFTEMP) - gmanew));	out_c.m_tBEcap = out_c.m_tBEcap*(1 + in_p.m_junctionExpBE*(4e-4*(m.m_dTemp - Spice3.Internal.SpiceConstants.REFTEMP) - gmanew));
pbo = (in_p.m_potentialBC - pbfact) / fact1;
gmaold = (in_p.m_potentialBC - pbo) / pbo;
out_c.m_tBCcap = in_p.m_depletionCapBC/(1 + in_p.m_junctionExpBC*(4e-4 *(in_p.m_tnom - SpiceConstants.REFTEMP) - gmaold));	out_c.m_tBCcap = in_p.m_depletionCapBC/(1 + in_p.m_junctionExpBC*(4e-4*( in_p.m_tnom - Spice3.Internal.SpiceConstants.REFTEMP) - gmaold));
out_c.m_tBCpot = fact2 * pbo + pbfact;
gmanew = (out_c.m_tBCpot - pbo) / pbo;
out_c.m_tBCcap = out_c.m_tBCcap*(1 + in_p.m_junctionExpBC*(4e-4*(m.m_dTemp - SpiceConstants.REFTEMP) - gmanew));	out_c.m_tBCcap = out_c.m_tBCcap*(1 + in_p.m_junctionExpBC*(4e-4*(m.m_dTemp - Spice3.Internal.SpiceConstants.REFTEMP) - gmanew));
out_c.m_tDepCapBE = in_p.m_depletionCapCoeff * out_c.m_tBEpot; ... xfc = Modelica_3_2.Math.log(1 - in_p.m_depletionCapCoeff);
out_c.m_tVcrit = vt*Modelica_3_2.Math.log(vt/(SpiceConstants.CONSTroot2 *in_p.m_satCur));	out_c.m_tVcrit = vt*Modelica.Math.log(vt/(Spice3.Internal.SpiceConstants.CONSTroot2 *in_p.m_satCur));
out_c.m_dVt = vt; ... out_c.m_tBCcap = out_c.m_tBCcap * in_p3.m_area;
(out_c.m_tF1c,out_c.m_f2c,out_c.m_f3c) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_junctionExpBC, in_p.m_depletionCapCoeff, out_c.m_tBCpot);	(out_c.m_tF1c,out_c.m_f2c,out_c.m_f3c) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_junctionExpBC, in_p.m_depletionCapCoeff, out_c.m_tBCpot);
(out_c.m_tF1e,out_c.m_f2e,out_c.m_f3e) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_junctionExpBE, in_p.m_depletionCapCoeff, out_c.m_tBEpot);	(out_c.m_tF1e,out_c.m_f2e,out_c.m_f3e) = Spice3.Internal.Functions.junctionCapCoeffs( in_p.m_junctionExpBE, in_p.m_depletionCapCoeff, out_c.m_tBEpot);

---

function Electrical.Spice3.Internal.Bjt3.bjt3NoBypassCode

Component	Version 3.2	Version 3.2.1
temp	SIunits.Temp_K	Real

Equations in Version 3.2	Equations in Version 3.2.1
... vbx = in_p.m_type * (in_m_pVoltageValues[2] - in_m_pVoltageValues[4]);
if (SpiceRoot.useInitialConditions()) then	if (Spice3.Internal.SpiceRoot.useInitialConditions()) then
if (in_p3.m_bICvbeIsGiven > 0.5) then ... vbx = vbe - vce;
elseif (SpiceRoot.initJunctionVoltages()) then	elseif (Spice3.Internal.SpiceRoot.initJunctionVoltages()) then
if (in_p3.m_bOff) then ... vbc = vbe - vce;
(cbe,gbe) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2( vbe, in_m.m_dTemp, in_p.m_emissionCoeffF, in_c.m_tSatCur);	(cbe,gbe) = Spice3.Internal.Functions.junction2( vbe, in_m.m_dTemp, in_p.m_emissionCoeffF, in_c.m_tSatCur);
out_cc.iBE = in_p.m_type * cbe / in_c.m_tBetaF;
(cben,gben) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2( vbe, in_m.m_dTemp, in_p.m_leakBEemissionCoeff, in_c.m_tBEleakCur);	(cben,gben) = Spice3.Internal.Functions.junction2( vbe, in_m.m_dTemp, in_p.m_leakBEemissionCoeff, in_c.m_tBEleakCur);
out_cc.iBEN = in_p.m_type * cben;
(cbc,gbc) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2( vbc, in_m.m_dTemp, in_p.m_emissionCoeffR, in_c.m_tSatCur);	(cbc,gbc) = Spice3.Internal.Functions.junction2( vbc, in_m.m_dTemp, in_p.m_emissionCoeffR, in_c.m_tSatCur);
out_cc.iBC = in_p.m_type * cbc / in_c.m_tBetaR;
(cbcn,gbcn) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junction2( vbc, in_m.m_dTemp, in_p.m_leakBCemissionCoeff, in_c.m_tBCleakCur);	(cbcn,gbcn) = Spice3.Internal.Functions.junction2( vbc, in_m.m_dTemp, in_p.m_leakBCemissionCoeff, in_c.m_tBCleakCur);
out_cc.iBCN = in_p.m_type * cbcn; ... end if;
(capbe,chargebe) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapTransTime( in_c.m_tBEcap, vbe, in_c.m_tDepCapBE, in_p.m_junctionExpBE, in_c.m_tBEpot, in_c.m_tF1e, in_c.m_f2e, in_c.m_f3e, in_p.m_transitTimeF, gbe, cbe);	(capbe,chargebe) = Spice3.Internal.Functions.junctionCapTransTime( in_c.m_tBEcap, vbe, in_c.m_tDepCapBE, in_p.m_junctionExpBE, in_c.m_tBEpot, in_c.m_tF1e, in_c.m_f2e, in_c.m_f3e, in_p.m_transitTimeF, gbe, cbe);
out_cc.iXX = 0;
aux1 = in_c.m_tBCcap*in_p.m_baseFractionBCcap;
(capbc,chargebc) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCapTransTime( aux1, vbc, in_c.m_tDepCapBC, in_p.m_junctionExpBC, in_c.m_tBCpot, in_c.m_tF1c, in_c.m_f2c, in_c.m_f3c, in_p.m_transitTimeR, gbc, cbc);	(capbc,chargebc) = Spice3.Internal.Functions.junctionCapTransTime( aux1, vbc, in_c.m_tDepCapBC, in_p.m_junctionExpBC, in_c.m_tBCpot, in_c.m_tF1c, in_c.m_f2c, in_c.m_f3c, in_p.m_transitTimeR, gbc, cbc);
aux2= in_c.m_tBCcap*(1. - in_p.m_baseFractionBCcap);
(capbx,chargebx) = Modelica_3_2.Electrical.Spice3.Internal.Functions.junctionCap( aux2, vbx, in_c.m_tDepCapBC, in_p.m_junctionExpBC, in_c.m_tBCpot, in_c.m_tF1c, in_c.m_f2c, in_c.m_f3c);	(capbx,chargebx) = Spice3.Internal.Functions.junctionCap( aux2, vbx, in_c.m_tDepCapBC, in_p.m_junctionExpBC, in_c.m_tBCpot, in_c.m_tF1c, in_c.m_f2c, in_c.m_f3c);

---

function Electrical.Spice3.Internal.Bjt3.bjtRenameParameters

Component	Version 3.2	Version 3.2.1
TBJT		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
intern.m_satCur := ex.IS;	intern.m_type := TBJT;
	intern.m_satCur = ex.IS;
intern.m_betaF = ex.BF; ... intern.m_depletionCapCoeff = ex.FC;
intern.m_tnom = if (ex.TNOM > -1e40) then ex.TNOM + SpiceConstants.CONSTCtoK else 300.15;	intern.m_tnom = if (ex.TNOM > -1e40) then ex.TNOM + Spice3.Internal.SpiceConstants.CONSTCtoK else 300.15;

---

function Electrical.Spice3.Internal.Bjt3.bjtRenameParametersDevTemp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
m.m_dTemp :=TEMP + SpiceConstants.CONSTCtoK;	m.m_dTemp := TEMP + Spice3.Internal.SpiceConstants.CONSTCtoK;

---

model Magnetic.FluxTubes.Examples.SaturatedInductor

Component	Version 3.2	Version 3.2.1
r_mFe		B(start=0)

---

model Magnetic.FluxTubes.Examples.SolenoidActuator.ComparisonQuasiStationary

Component	Version 3.2	Version 3.2.1
advancedFeed_x	exact=true	exact=false

---

model Magnetic.FluxTubes.Examples.SolenoidActuator.Components.AdvancedSolenoid

Component	Version 3.2	Version 3.2.1
g_mFePole		r_i=0

---

model Magnetic.FluxTubes.Basic.ElectroMagneticConverter

Component	Version 3.2	Version 3.2.1
N	start=1
		=1

---

model Magnetic.FluxTubes.Basic.ConstantReluctance

Component	Version 3.2	Version 3.2.1
R_m	start=1
		=1

---

model Magnetic.FluxTubes.Basic.LeakageWithCoefficient

Component	Version 3.2	Version 3.2.1
c_usefulFlux	start=0.7
		=0.7

---

model Magnetic.FluxTubes.Basic.EddyCurrent

Component	Version 3.2	Version 3.2.1
rho	start=0.098e-6
		=0.098e-6
l	start=1
		=1
A	start=1
		=1

---

model Magnetic.FluxTubes.Shapes.FixedShape.HollowCylinderAxialFlux

Component	Version 3.2	Version 3.2.1
l	start=0.01
		=0.01
r_i	start=0
		=0
r_o	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.FixedShape.HollowCylinderRadialFlux

Component	Version 3.2	Version 3.2.1
l	start=0.01
		=0.01
r_i	start=0.01
		=0.01
r_o	start=0.02
		=0.02

---

model Magnetic.FluxTubes.Shapes.Force.HollowCylinderAxialFlux

Component	Version 3.2	Version 3.2.1
r_i	start=0
		=0
r_o	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.Force.HollowCylinderRadialFlux

Component	Version 3.2	Version 3.2.1
r_i	start=0.01
		=0.01
r_o	start=0.015
		=0.015

---

model Magnetic.FluxTubes.Shapes.Force.CuboidParallelFlux

Component	Version 3.2	Version 3.2.1
a	start=0.01
		=0.01
b	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.Force.CuboidOrthogonalFlux

Component	Version 3.2	Version 3.2.1
a	start=0.01
		=0.01
b	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.Force.LeakageAroundPoles

Component	Version 3.2	Version 3.2.1
w	start=0.1
		=0.1
r	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.Leakage.QuarterCylinder

Component	Version 3.2	Version 3.2.1
l	start=0.1
		=0.1

---

model Magnetic.FluxTubes.Shapes.Leakage.QuarterHollowCylinder

Component	Version 3.2	Version 3.2.1
l	start=0.1
		=0.1

---

model Magnetic.FluxTubes.Shapes.Leakage.HalfCylinder

Component	Version 3.2	Version 3.2.1
l	start=0.1
		=0.1

---

model Magnetic.FluxTubes.Shapes.Leakage.HalfHollowCylinder

Component	Version 3.2	Version 3.2.1
l	start=0.1
		=0.1

---

model Magnetic.FluxTubes.Shapes.Leakage.QuarterSphere

Component	Version 3.2	Version 3.2.1
r	start=0.005
		=0.005

---

model Magnetic.FluxTubes.Shapes.Leakage.EighthOfSphere

Component	Version 3.2	Version 3.2.1
r	start=0.01
		=0.01

---

model Magnetic.FluxTubes.Shapes.Leakage.CoaxCylindersEndFaces

Component	Version 3.2	Version 3.2.1
r_0	start=10e-3
		=10e-3
r_1	start=17e-3
		=17e-3
r_2	start=20e-3
		=20e-3

---

connector Magnetic.FluxTubes.Interfaces.MagneticPort

Component	Version 3.2	Version 3.2.1
V_m	SIunits.MagneticPotentialDifference	SIunits.MagneticPotential

---

model Magnetic.FluxTubes.Interfaces.PartialTwoPorts

Component	Version 3.2	Version 3.2.1
Phi		start=0

---

model Magnetic.FluxTubes.Sources.SignalMagneticPotentialDifference

Component	Version 3.2	Version 3.2.1
V_m		unit="A"

---

model Magnetic.FluxTubes.Sources.SignalMagneticFlux

Component	Version 3.2	Version 3.2.1
Phi		unit="Wb"

---

model Magnetic.FluxTubes.Sensors.MagneticPotentialDifferenceSensor

Component	Version 3.2	Version 3.2.1
V_m		final quantity="MagneticPotential"
		final unit="A"

---

model Magnetic.FluxTubes.Sensors.MagneticFluxSensor

Component	Version 3.2	Version 3.2.1
Phi		final quantity="MagneticFlux"
		final unit="Wb"

---

model Magnetic.FundamentalWave.Examples.Components.EddyCurrentLosses

Component	Version 3.2	Version 3.2.1
star_e		m=m
star_m		m=m
sineVoltage_e		m=m
		V=fill(1, m)
		freqHz=fill(1, m)
sineVoltage_m		m=m
		V=fill(1, m)
		freqHz=fill(1, m)
converter_e	orientation=Modelica_3_2.Magnetic.FundamentalWave.BasicMachines.Functions.symmetricOrientation(3)	orientation=Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)
	m=3	m=m
	effectiveTurns=fill(N, 3)	effectiveTurns=fill(N, m)
converter_m	orientation=Modelica_3_2.Magnetic.FundamentalWave.BasicMachines.Functions.symmetricOrientation(3)	orientation=Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)
	effectiveTurns=fill(N, 3)	effectiveTurns=fill(N, m)
	m=3	m=m
loss_e	G=fill(Gc, 3)	G=fill(Gc, m)
		m=m
loss_m	G=3*N^2*Gc/2	G=m*N^2*Gc/2
powerb_e		m=m
powerb_m		m=m
RLeader	Present
leader_e	Present
leader_m	Present
m		Present
R		Present
resistor_e		Present
resistor_m		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(sineVoltage_e.plug_n, converter_e.plug_n);	initial equation
	reluctance_e.Phi = Complex(0, 0); reluctance_m.Phi = Complex(0, 0); equation  &nbspconnect(sineVoltage_e.plug_n, converter_e.plug_n);
connect(sineVoltage_e.plug_n, star_e.plug_p); ... connect(converter_m.port_n, mground_m.port_p);
connect(leader_e.plug_p, sineVoltage_e.plug_p);	connect(resistor_e.plug_p, sineVoltage_e.plug_p);
connect(sineVoltage_m.plug_p, leader_m.plug_p);	connect(sineVoltage_m.plug_p, resistor_m.plug_p);
connect(leader_e.plug_n, powerb_e.pc);	connect(resistor_e.plug_n, powerb_e.pc);
connect(powerb_e.pv, powerb_e.pc); ... connect(powerb_e.nv, sineVoltage_e.plug_n);
connect(leader_m.plug_n, powerb_m.pc);	connect(resistor_m.plug_n, powerb_m.pc);
connect(powerb_m.pc, powerb_m.pv); ...

---

model Magnetic.FundamentalWave.Examples.BasicMachines.AIMC_DOL

Component	Version 3.2	Version 3.2.1
sineVoltage	freqHz=fill(fsNominal, m)	freqHz=fill(fNominal, m)
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
aimcM	p=p	p=aimcData.p
	Rs=Rs	Rs=aimcData.Rs
	Lssigma=Lssigma	Lssigma=aimcData.Lssigma
	Lm=Lm	Lm=aimcData.Lm
	Lrsigma=Lrsigma	Lrsigma=aimcData.Lrsigma
	Rr=Rr	Rr=aimcData.Rr
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = aimcData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = aimcData.alpha20r
		Jr=aimcData.Jr
		Js=aimcData.Js
		fsNominal=aimcData.fsNominal
		TsRef=aimcData.TsRef
		Lszero=aimcData.Lszero
		frictionParameters=aimcData.frictionParameters
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		TrRef=aimcData.TrRef
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		TsOperational=293.15
		TrOperational=293.15
aimcE	p=p	p=aimcData.p
	Rs=Rs	Rs=aimcData.Rs
	Lssigma=Lssigma	Lssigma=aimcData.Lssigma
	Lm=Lm	Lm=aimcData.Lm
	Lrsigma=Lrsigma	Lrsigma=aimcData.Lrsigma
	Rr=Rr	Rr=aimcData.Rr
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = aimcData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = aimcData.alpha20r
		fsNominal=aimcData.fsNominal
		TsRef=aimcData.TsRef
		Lszero=aimcData.Lszero
		Jr=aimcData.Jr
		Js=aimcData.Js
		frictionParameters=aimcData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimcData.statorCoreParameters
		strayLoadParameters=aimcData.strayLoadParameters
		TsOperational=293.15
		TrRef=aimcData.TrRef
		TrOperational=293.15
fsNominal	Present
Rs	Present
Lssigma	Present
Lm	Present
Lrsigma	Present
Rr	Present
fNominal		Present
aimcData		Present
currentQuasiRMSSensor		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimcE.is = zeros(m); aimcE.ir = zeros(2); aimcM.is = zeros(m); aimcM.ir[1:2] = zeros(2); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ... connect(terminalBoxM.plug_sp, aimcM.plug_sp);
connect(terminalBoxM.plugSupply, currentRMSsensorM.plug_n);
connect(aimcE.flange, loadInertiaE.flange_a); ... connect(currentRMSsensorE.plug_p, idealCloser.plug_n);
	connect(currentRMSsensorM.plug_n, currentQuasiRMSSensor.plug_p); connect(terminalBoxM.plugSupply, currentQuasiRMSSensor.plug_n);

---

model Magnetic.FundamentalWave.Examples.BasicMachines.AIMS_Start

Component	Version 3.2	Version 3.2.1
RStart	=0.16	=0.16/aimsData.turnsRatio^2
sineVoltage	freqHz=fill(fsNominal, m)	freqHz=fill(fNominal, m)
idealCloser		Ron=fill(1e-5, m)
		Goff=fill(1e-5, m)
currentRMSsensorM	Electrical.Machines.Sensors.CurrentQuasiRMSSensor	Electrical.MultiPhase.Sensors.CurrentQuasiRMSSensor
aimsM	Rs=Rs	Rs=aimsData.Rs
	Lssigma=Lssigma	Lssigma=aimsData.Lssigma
	Lm=Lm	Lm=aimsData.Lm
	Lrsigma=Lrsigma	Lrsigma=aimsData.Lrsigma
	Rr=Rr	Rr=aimsData.Rr
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = aimsData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = aimsData.alpha20r
	p=p	p=aimsData.p
		Jr=aimsData.Jr
		Js=aimsData.Js
		fsNominal=aimsData.fsNominal
		TsRef=aimsData.TsRef
		Lszero=aimsData.Lszero
		frictionParameters=aimsData.frictionParameters
		statorCoreParameters=aimsData.statorCoreParameters
		strayLoadParameters=aimsData.strayLoadParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		Lrzero=aimsData.Lrzero
		TrRef=aimsData.TrRef
		useTurnsRatio=aimsData.useTurnsRatio
		VsNominal=aimsData.VsNominal
		VrLockedRotor=aimsData.VrLockedRotor
		rotorCoreParameters=aimsData.rotorCoreParameters
		TurnsRatio=aimsData.turnsRatio
		TsOperational=293.15
		TrOperational=293.15
aimsE	p=p	p=aimsData.p
	Rs=Rs	Rs=aimsData.Rs
	Lssigma=Lssigma	Lssigma=aimsData.Lssigma
	Lm=Lm	Lm=aimsData.Lm
	Lrsigma=Lrsigma	Lrsigma=aimsData.Lrsigma
	Rr=Rr	Rr=aimsData.Rr
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = aimsData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = aimsData.alpha20r
		fsNominal=aimsData.fsNominal
		TsRef=aimsData.TsRef
		Lszero=aimsData.Lszero
		Jr=aimsData.Jr
		Js=aimsData.Js
		frictionParameters=aimsData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=aimsData.statorCoreParameters
		strayLoadParameters=aimsData.strayLoadParameters
		Lrzero=aimsData.Lrzero
		TrRef=aimsData.TrRef
		useTurnsRatio=aimsData.useTurnsRatio
		VsNominal=aimsData.VsNominal
		VrLockedRotor=aimsData.VrLockedRotor
		rotorCoreParameters=aimsData.rotorCoreParameters
		TsOperational=566.3
		turnsRatio=aimsData.turnsRatio
		TrOperational=566.3
rheostatM		m=m
rheostatE		m=m
fsNominal	Present
p	Present
Rs	Present
Lssigma	Present
Lm	Present
Lrsigma	Present
Rr	Present
fNominal		Present
aimsData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(star.pin_n, ground.p);	initial equation
	aimsE.is = zeros(3); aimsE.ir = zeros(3); aimsM.is = zeros(3); aimsM.ir = zeros(3); equation  &nbspconnect(star.pin_n, ground.p);
connect(sineVoltage.plug_n, star.plug_p); ...

---

model Magnetic.FundamentalWave.Examples.BasicMachines.SMPM_Inverter

Component	Version 3.2	Version 3.2.1
currentRMSsensorM	Electrical.Machines.Sensors.CurrentQuasiRMSSensor	Electrical.MultiPhase.Sensors.CurrentQuasiRMSSensor
smpmM	Rs=Rs	Rs=smpmData.Rs
	Lssigma=Lssigma	Lssigma=smpmData.Lssigma
	Lmd=Lmd	Lmd=smpmData.Lmd
	Lmq=Lmq	Lmq=smpmData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smpmData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smpmData.Lrsigmaq
	Rrd=Rrd	Rrd=smpmData.Rrd
	Rrq=Rrq	Rrq=smpmData.Rrq
	p=p	p=smpmData.p
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smpmData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smpmData.alpha20r
		Jr=smpmData.Jr
		Js=smpmData.Js
		fsNominal=smpmData.fsNominal
		TsRef=smpmData.TsRef
		Lszero=smpmData.Lszero
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		useDamperCage=smpmData.useDamperCage
		TrRef=smpmData.TrRef
		VsOpenCircuit=smpmData.VsOpenCircuit
		frictionParameters=smpmData.frictionParameters
		statorCoreParameters=smpmData.statorCoreParameters
		strayLoadParameters=smpmData.strayLoadParameters
		permanentMagnetLossParameters=smpmData.permanentMagnetLossParameters
		TsOperational=293.15
		TrOperational=293.15
		ir(fixed=true)
smpmE	Rs=Rs	Rs=smpmData.Rs
	Lssigma=Lssigma	Lssigma=smpmData.Lssigma
	Lmd=Lmd	Lmd=smpmData.Lmd
	Lmq=Lmq	Lmq=smpmData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smpmData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smpmData.Lrsigmaq
	Rrd=Rrd	Rrd=smpmData.Rrd
	Rrq=Rrq	Rrq=smpmData.Rrq
	p=p	p=smpmData.p
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smpmData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smpmData.alpha20r
		fsNominal=smpmData.fsNominal
		TsRef=smpmData.TsRef
		Lszero=smpmData.Lszero
		Jr=smpmData.Jr
		Js=smpmData.Js
		frictionParameters=smpmData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=smpmData.statorCoreParameters
		strayLoadParameters=smpmData.strayLoadParameters
		VsOpenCircuit=smpmData.VsOpenCircuit
		useDamperCage=smpmData.useDamperCage
		TrRef=smpmData.TrRef
		permanentMagnetLossParameters=smpmData.permanentMagnetLossParameters
		TsOperational=293.15
		ir(fixed=true)
		TrOperational=293.15
rotorAngleM	p=p	p=smpmM.p
rotorAngleE	p=p	p=smpmE.p
torqueStepM		offsetTorque=0
torqueStepE		offsetTorque=0
p	Present
Rs	Present
Lssigma	Present
Lmd	Present
Lmq	Present
Lrsigmad	Present
Lrsigmaq	Present
Rrd	Present
Rrq	Present
smpmData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(signalVoltage.plug_n, star.plug_p);	initial equation
	smpmE.is[1:2] = zeros(2); smpmM.is[1:2] = zeros(2); equation  &nbspconnect(signalVoltage.plug_n, star.plug_p);
connect(star.pin_n, ground.p); ...

---

model Magnetic.FundamentalWave.Examples.BasicMachines.SMEE_Generator

Component	Version 3.2	Version 3.2.1
smeeM	Rs=Rs	Rs=smeeData.Rs
	Lssigma=Lssigma	Lssigma=smeeData.Lssigma
	Lmd=Lmd	Lmd=smeeData.Lmd
	Lmq=Lmq	Lmq=smeeData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smeeData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smeeData.Lrsigmaq
	Rrd=Rrd	Rrd=smeeData.Rrd
	Rrq=Rrq	Rrq=smeeData.Rrq
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smeeData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smeeData.alpha20r
	alpha20e(displayUnit="1/K")	alpha20e(displayUnit="1/K") = smeeData.alpha20e
		Jr=0.29
		Js=0.29
		p=2
		fsNominal=smeeData.fsNominal
		TsRef=smeeData.TsRef
		useDamperCage=true
		TrRef=smeeData.TrRef
		VsNominal=smeeData.VsNominal
		IeOpenCircuit=smeeData.IeOpenCircuit
		Re=smeeData.Re
		TeRef=smeeData.TeRef
		sigmae=smeeData.sigmae
		statorCoreParameters(VRef=100)
		strayLoadParameters(IRef=100)
		brushParameters(ILinear=0.01)
		TsOperational=293.15
		TrOperational=293.15
		TeOperational=293.15
		ir(fixed=true)
smeeE	Rs=Rs	Rs=smeeData.Rs
	Lssigma=Lssigma	Lssigma=smeeData.Lssigma
	Lmd=Lmd	Lmd=smeeData.Lmd
	Lmq=Lmq	Lmq=smeeData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smeeData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smeeData.Lrsigmaq
	Rrd=Rrd	Rrd=smeeData.Rrd
	Rrq=Rrq	Rrq=smeeData.Rrq
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smeeData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smeeData.alpha20r
	alpha20e(displayUnit="1/K")	alpha20e(displayUnit="1/K") = smeeData.alpha20e
		p=2
		fsNominal=smeeData.fsNominal
		TsRef=smeeData.TsRef
		Jr=0.29
		Js=0.29
		frictionParameters(PRef=0)
		statorCoreParameters(PRef=0, VRef=100)
		strayLoadParameters(PRef=0, IRef=100)
		useDamperCage=true
		VsNominal=smeeData.VsNominal
		IeOpenCircuit=smeeData.IeOpenCircuit
		Re=smeeData.Re
		TeRef=smeeData.TeRef
		sigmae=smeeData.sigmae
		brushParameters(V=0, ILinear=0.01)
		TrRef=smeeData.TrRef
		TsOperational=293.15
		ir(fixed=true)
		TrOperational=293.15
		TeOperational=293.15
smeeData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(rotorAngleE.plug_n,smeeE. plug_sn);	initial equation
	smeeE.is[1:2] = zeros(2); smeeM.is[1:2] = zeros(2); equation  &nbspconnect(rotorAngleE.plug_n, smeeE.plug_sn);
connect(rotorAngleE.plug_p,smeeE. plug_sp); ...

---

model Magnetic.FundamentalWave.Examples.BasicMachines.SMR_Inverter

Component	Version 3.2	Version 3.2.1
currentRMSsensorM	Electrical.Machines.Sensors.CurrentQuasiRMSSensor	Electrical.MultiPhase.Sensors.CurrentQuasiRMSSensor
smrM	p=p	p=smrData.p
	Rs=Rs	Rs=smrData.Rs
	Lssigma=Lssigma	Lssigma=smrData.Lssigma
	Lmd=Lmd	Lmd=smrData.Lmd
	Lmq=Lmq	Lmq=smrData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smrData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smrData.Lrsigmaq
	Rrd=Rrd	Rrd=smrData.Rrd
	Rrq=Rrq	Rrq=smrData.Rrq
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smrData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smrData.alpha20r
		Jr=smrData.Jr
		Js=smrData.Js
		fsNominal=smrData.fsNominal
		TsRef=smrData.TsRef
		Lszero=smrData.Lszero
		frictionParameters=smrData.frictionParameters
		statorCoreParameters=smrData.statorCoreParameters
		strayLoadParameters=smrData.strayLoadParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		useDamperCage=smrData.useDamperCage
		TrRef=smrData.TrRef
		TsOperational=293.15
		TrOperational=293.15
		ir(fixed=true)
smrE	p=p	p=smrData.p
	Rs=Rs	Rs=smrData.Rs
	Lssigma=Lssigma	Lssigma=smrData.Lssigma
	Lmd=Lmd	Lmd=smrData.Lmd
	Lmq=Lmq	Lmq=smrData.Lmq
	Lrsigmad=Lrsigmad	Lrsigmad=smrData.Lrsigmad
	Lrsigmaq=Lrsigmaq	Lrsigmaq=smrData.Lrsigmaq
	Rrd=Rrd	Rrd=smrData.Rrd
	Rrq=Rrq	Rrq=smrData.Rrq
	alpha20s(displayUnit="1/K")	alpha20s(displayUnit="1/K") = smrData.alpha20s
	alpha20r(displayUnit="1/K")	alpha20r(displayUnit="1/K") = smrData.alpha20r
		fsNominal=smrData.fsNominal
		TsRef=smrData.TsRef
		Lszero=smrData.Lszero
		Jr=smrData.Jr
		Js=smrData.Js
		frictionParameters=smrData.frictionParameters
		phiMechanical(fixed=true)
		wMechanical(fixed=true)
		statorCoreParameters=smrData.statorCoreParameters
		strayLoadParameters=smrData.strayLoadParameters
		useDamperCage=smrData.useDamperCage
		TrRef=smrData.TrRef
		TsOperational=293.15
		ir(fixed=true)
		TrOperational=293.15
rotorAngleM	p=p	p=smrM.p
rotorAngleE	p=p	p=smrE.p
torqueStepM		offsetTorque=0
torqueStepE		offsetTorque=0
p	Present
Rs	Present
Lssigma	Present
Lmd	Present
Lmq	Present
Lrsigmad	Present
Lrsigmaq	Present
Rrd	Present
Rrq	Present
smrData		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(signalVoltage.plug_n, star.plug_p);	initial equation
	smrE.is[1:2] = zeros(2); smrM.is[1:2] = zeros(2); equation  &nbspconnect(signalVoltage.plug_n, star.plug_p);
connect(star.pin_n, ground.p); ...

---

model Magnetic.FundamentalWave.Components.MultiPhaseElectroMagneticConverter

Component	Version 3.2	Version 3.2.1
v		Present
i		Present
V_m		Present
Phi		Present

---

model Magnetic.FundamentalWave.BasicMachines.AsynchronousInductionMachines.AIM_SquirrelCage

Component	Version 3.2	Version 3.2.1
ir		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(airGap.port_rn, rotorCage.port_n); connect(airGap.port_rp, rotorCage.port_p);
connect(rotorCage.heatPortWinding, internalThermalPort.heatPortRotorWinding);
	connect(airGap.port_rn, rotorCage.port_p); connect(airGap.port_rp, rotorCage.port_n);

---

model Magnetic.FundamentalWave.BasicMachines.AsynchronousInductionMachines.AIM_SlipRing

Component	Version 3.2	Version 3.2.1
plug_rn	final m=m	final m=mr
plug_rp	final m=m	final m=mr
rotor	final m=m	final m=mr
mr		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(rotor.plug_n, plug_rn);
connect(airGap.port_rn, rotor.port_n); connect(airGap.port_rp, rotor.port_p);
connect(rotor.heatPortCore, internalThermalPort.heatPortRotorCore); ... connect(plug_rp, rotor.plug_p);
	connect(airGap.port_rn, rotor.port_p); connect(airGap.port_rp, rotor.port_n);

---

model Magnetic.FundamentalWave.BasicMachines.SynchronousInductionMachines.SM_PermanentMagnet

Component	Version 3.2	Version 3.2.1
permanentMagnet	Magnetic.FundamentalWave.Sources.ConstantMagneticPotentialDifference	Magnetic.FundamentalWave.BasicMachines.Components.PermanentMagnet
heatFlowSensorDamperCage	Present
TpmOperational		Present
permanentMagnetLossParameters		Present
ir		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
	connect(ir, rotorCage.i); connect(damperCageLossPower, rotorCage.lossPower); if not useDamperCage then damperCageLossPower=0; end if;
connect(permanentMagnet.port_p, airGap.port_rn);
connect(permanentMagnet.port_n, short.port_n);	connect(permanentMagnet.support, airGap.support);
connect(permanentMagnet.port_n, rotorCage.port_n);	connect(permanentMagnet.heatPort, internalThermalPort.heatPortPermanentMagnet);
connect(short.port_p, airGap.port_rp);	connect(permanentMagnet.flange, inertiaRotor.flange_b);
connect(rotorCage.port_p, airGap.port_rp);	connect(airGap.port_rp, rotorCage.port_n);
connect(rotorCage.heatPortWinding, heatFlowSensorDamperCage.port_a);	connect(short.port_n, airGap.port_rp);
connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);	connect(short.port_p, permanentMagnet.port_n);
	connect(rotorCage.port_p, permanentMagnet.port_n); connect(rotorCage.heatPortWinding, internalThermalPort.heatPortRotorWinding);

---

model Magnetic.FundamentalWave.BasicMachines.SynchronousInductionMachines.SM_ElectricalExcited

Component	Version 3.2	Version 3.2.1
brush		final useHeatPort=true
heatFlowSensorDamperCage	Present
ir		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(short.port_n, rotorCage.port_n);	connect(ir, rotorCage.i);
connect(excitation.port_n, short.port_n);	connect(damperCageLossPower, rotorCage.lossPower);
connect(excitation.port_n, rotorCage.port_n);	if not useDamperCage then
	damperCageLossPower=0; end if;
connect(pin_en, excitation.pin_n);
connect(airGap.port_rn, excitation.port_p);
connect(airGap.port_rp, short.port_p); connect(airGap.port_rp, rotorCage.port_p);
connect(pin_ep, brush.p); ... connect(excitation.heatPortWinding, internalThermalPort.heatPortExcitation);
connect(rotorCage.heatPortWinding, heatFlowSensorDamperCage.port_a);	connect(airGap.port_rp, rotorCage.port_n);
connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);	connect(short.port_n, airGap.port_rp);
	connect(rotorCage.port_p, excitation.port_n); connect(short.port_p, excitation.port_n); connect(rotorCage.heatPortWinding, internalThermalPort.heatPortRotorWinding);

---

model Magnetic.FundamentalWave.BasicMachines.SynchronousInductionMachines.SM_ReluctanceRotor

Component	Version 3.2	Version 3.2.1
heatFlowSensorDamperCage	Present
ir		Present
damperCageLossPower		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(airGap.port_rn, short.port_n);	connect(ir, rotorCage.i);
connect(airGap.port_rn, rotorCage.port_n);	connect(damperCageLossPower, rotorCage.lossPower);
connect(airGap.port_rp, short.port_p);	if not useDamperCage then
connect(airGap.port_rp, rotorCage.port_p);	damperCageLossPower=0;
connect(rotorCage.heatPortWinding, heatFlowSensorDamperCage.port_a);	end if;
connect(heatFlowSensorDamperCage.port_b, internalThermalPort.heatPortRotorWinding);	connect(rotorCage.port_n, airGap.port_rp);
	connect(short.port_n, airGap.port_rp); connect(rotorCage.port_p, airGap.port_rn); connect(short.port_p, airGap.port_rn); connect(rotorCage.heatPortWinding, internalThermalPort.heatPortRotorWinding);

---

model Magnetic.FundamentalWave.BasicMachines.Components.SymmetricMultiPhaseWinding

Component	Version 3.2	Version 3.2.1
electroMagneticConverter	final orientation=Functions.symmetricOrientation(m)	final orientation=Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)
core	final G=(m/2)*GcRef/effectiveTurns^2	final G=(m/2)*GcRef*effectiveTurns^2
strayReluctance	final R_m(d=3*effectiveTurns^2/2/Lsigma, q=3*effectiveTurns^2/2/Lsigma)	final R_m(d=m*effectiveTurns^2/2/Lsigma, q=m*effectiveTurns^2/2/Lsigma)

---

model Magnetic.FundamentalWave.BasicMachines.Components.SymmetricMultiPhaseCageWinding

Component	Version 3.2	Version 3.2.1
i	each start=0
winding	final orientation={2*pi*(k - 1)/m for k in 1:m}	final orientation=Modelica.Electrical.MultiPhase.Functions.symmetricOrientation(m)

---

model Magnetic.FundamentalWave.BasicMachines.Components.SaliencyCageWinding

Component	Version 3.2	Version 3.2.1
i	Magnetic.FundamentalWave.Types.SalientCurrent	Blocks.Interfaces.RealOutput
		sizes= 2
lossPower		Present

---

model Magnetic.FundamentalWave.Interfaces.PartialBasicInductionMachine

Component	Version 3.2	Version 3.2.1
m	constant	parameter
		min=3
frictionParameters	wRef(start=2*pi*fsNominal/p)
		wRef=2*pi*fsNominal/p
statorCoreParameters	wRef(start=2*pi*fsNominal/p)
		wRef=2*pi*fsNominal/p
strayLoadParameters	wRef(start=2*pi*fsNominal/p)
		wRef=2*pi*fsNominal/p
phiMechanical		start=0
wMechanical		start=0
powerBalance	final powerStator=Modelica_3_2.Electrical.Machines.SpacePhasors.Functions.activePower(vs, is)	final powerStator=Modelica.Electrical.MultiPhase.Functions.activePower(vs, is)
	final lossPowerStatorWinding=-sum(stator.heatPortWinding.Q_flow)	final lossPowerStatorWinding=sum(stator.resistor.resistor.LossPower)
	final lossPowerStatorCore=-stator.heatPortCore.Q_flow	final lossPowerStatorCore=stator.core.lossPower
	final lossPowerStrayLoad=-strayLoad.heatPort.Q_flow	final lossPowerStrayLoad=strayLoad.lossPower
	final lossPowerFriction=-friction.heatPort.Q_flow	final lossPowerFriction=friction.lossPower
thermalAmbient		final m=m
thermalPort		final m=m
strayLoad		final useHeatPort=true
		final m=m
friction		final useHeatPort=true
internalThermalPort		final m=m

Equations in Version 3.2	Equations in Version 3.2.1
connect(stator.plug_n, plug_sn);	initial algorithm
	assert(not Modelica.Math.isPowerOf2(m), String(m) +     " phases are currently not supported in this version of FundametalWave"); equation  &nbspconnect(stator.plug_n, plug_sn);
connect(thermalPort,internalThermalPort); ...

---

record Magnetic.FundamentalWave.Types.Salient

Component	Version 3.2	Version 3.2.1
d		replaceable
q		replaceable

---

model Mechanics.MultiBody.World

Component	Version 3.2	Version 3.2.1
ndim_pointGravity	=if enableAnimation and animateGravity and gravityType == 2 then 1 else 0	=if enableAnimation and animateGravity and gravityType == GravityTypes.UniformGravity then 1 else 0

Equations in Version 3.2	Equations in Version 3.2.1
Connections.root(frame_b.R);
assert(Modelica_3_2.Math.Vectors.length(n) > 1.e-10, "Parameter n of World object is wrong (length(n) > 0 required)");	assert(Modelica.Math.Vectors.length( n) > 1.e-10, "Parameter n of World object is wrong (length(n) > 0 required)");
frame_b.r_0 = zeros(3); ...

---

model Mechanics.MultiBody.Examples.Elementary.FreeBody

Component	Version 3.2	Version 3.2.1
body	r_0(start={0.2,-0.5,0.1}, fixed=true)	r_0(start={0.2,-0.5,0.1}, each fixed=true)
	v_0(fixed=true)
		v_0(each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.InitSpringConstant

Component	Version 3.2	Version 3.2.1
spring	c(fixed=false) = 100	c(fixed=false, start=100)

---

model Mechanics.MultiBody.Examples.Elementary.PointGravity

Component	Version 3.2	Version 3.2.1
body1	r_0(start={0,0.6,0}, fixed=true)	r_0(start={0,0.6,0}, each fixed=true)
	v_0(start={1,0,0}, fixed=true)	v_0(start={1,0,0}, each fixed=true)
body2	r_0(start={0.6,0.6,0}, fixed=true)	r_0(start={0.6,0.6,0}, each fixed=true)
	v_0(start={0.6,0,0}, fixed=true)	v_0(start={0.6,0,0}, each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.PointGravityWithPointMasses

Component	Version 3.2	Version 3.2.1
body1	r_0(start={0,0.6,0}, fixed=true)	r_0(start={0,0.6,0}, each fixed=true)
	v_0(start={1,0,0}, fixed=true)	v_0(start={1,0,0}, each fixed=true)
body2	r_0(start={0.6,0.6,0}, fixed=true)	r_0(start={0.6,0.6,0}, each fixed=true)
	v_0(start={0.6,0,0}, fixed=true)	v_0(start={0.6,0,0}, each fixed=true)
body3	r_0(start={0,0.8,0}, fixed=true)	r_0(start={0,0.8,0}, each fixed=true)
	v_0(start={0.6,0,0}, fixed=true)	v_0(start={0.6,0,0}, each fixed=true)
body4	r_0(start={0.3,0.8,0}, fixed=true)	r_0(start={0.3,0.8,0}, each fixed=true)
	v_0(start={0.6,0,0}, fixed=true)	v_0(start={0.6,0,0}, each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.PointGravityWithPointMasses2

Component	Version 3.2	Version 3.2.1
pointMass1	r_0(start={3,0,0}, fixed=true)	r_0(start={3,0,0}, each fixed=true)
	v_0(start={0,0,-1}, fixed=true)	v_0(start={0,0,-1}, each fixed=true)
pointMass3	r_0(start={2,1,0}, fixed=true)	r_0(start={2,1,0}, each fixed=true)
	v_0(start={0,0,-1}, fixed=true)	v_0(start={0,0,-1}, each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.SpringDamperSystem

Component	Version 3.2	Version 3.2.1
body1	r_0(start={0.3,-0.2,0}, fixed=true)	r_0(start={0.3,-0.2,0}, each fixed=true)
	v_0(fixed=true)
	w_0_start(displayUnit="deg/s") = {0,0,0.03490658503988659}
		v_0(each fixed=true)
		w_0_start(each displayUnit="deg/s") = {0,0,0.03490658503988659}

---

model Mechanics.MultiBody.Examples.Elementary.SpringWithMass

Component	Version 3.2	Version 3.2.1
body	r_0(start={0,-0.3,0}, fixed=true)	r_0(start={0,-0.3,0}, each fixed=true)
	v_0(fixed=true)
		v_0(each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.ThreeSprings

Component	Version 3.2	Version 3.2.1
body1	r_0(start={0.5,-0.3,0}, fixed=true)	r_0(start={0.5,-0.3,0}, each fixed=true)
	v_0(fixed=true)
		v_0(each fixed=true)

---

model Mechanics.MultiBody.Examples.Elementary.HeatLosses

Component	Version 3.2	Version 3.2.1
body1	r_0(start={0.3,-0.2,0}, fixed=true)	r_0(start={0.3,-0.2,0}, each fixed=true)
	v_0(fixed=true)
	w_0_start(displayUnit="deg/s") = {0,0,0.034906585039887}
		v_0(each fixed=true)
		w_0_start(each displayUnit="deg/s") = {0,0,0.034906585039887}
body2	r_0(start={0.6,-0.2,0}, fixed=true)	r_0(start={0.6,-0.2,0}, each fixed=true)
	v_0(fixed=true)
	w_0_start(displayUnit="deg/s") = {0,0,0.034906585039887}
		v_0(each fixed=true)
		w_0_start(each displayUnit="deg/s") = {0,0,0.034906585039887}
body3	r_0(start={0.9,-0.2,0}, fixed=true)	r_0(start={0.9,-0.2,0}, each fixed=true)
	v_0(fixed=true)
	w_0_start(displayUnit="deg/s") = {0,0,0.034906585039887}
		v_0(each fixed=true)
		w_0_start(each displayUnit="deg/s") = {0,0,0.034906585039887}

---

model Mechanics.MultiBody.Examples.Elementary.UserDefinedGravityField

Component	Version 3.2	Version 3.2.1
world	redeclare function gravityAcceleration = Modelica.Mechanics.MultiBody.Examples.Elementary.Utilities.theoreticalNormalGravityWGS84 (mue=1, phi=geodeticLatitude)	redeclare function gravityAcceleration = Modelica.Mechanics.MultiBody.Examples.Elementary.Utilities.theoreticalNormalGravityWGS84 (mue=1, phi=geodeticLatitude)

---

model Mechanics.MultiBody.Examples.Elementary.Surfaces

Component	Version 3.2	Version 3.2.1
surface	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Examples.Elementary.Utilities.sineSurface (x_min=x_min, x_max=x_max, y_min=y_min, y_max=y_max, z_min=z_min, z_max=z_max, wz=wz)	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Examples.Elementary.Utilities.sineSurface (x_min=x_min, x_max=x_max, y_min=y_min, y_max=y_max, z_min=z_min, z_max=z_max, wz=wz)

---

model Mechanics.MultiBody.Examples.Loops.EngineV6_analytic

Component	Version 3.2	Version 3.2.1
engine	redeclare model Cylinder = Modelica.Mechanics.MultiBody.Examples.Loops.Utilities.Cylinder_analytic_CAD	redeclare model Cylinder = Modelica.Mechanics.MultiBody.Examples.Loops.Utilities.Cylinder_analytic_CAD

---

model Mechanics.MultiBody.Examples.Loops.Utilities.GasForce2

Equations in Version 3.2	Equations in Version 3.2.1
... press*V = k*T;
assert(s_rel >= -1.e-12, "flange_b.s - flange_a.s (= " + String(s_rel) + ") >= 0 required for GasForce component.\n" + "Most likely, the component has to be flipped.");	assert(s_rel >= -1.e-12, "flange_b.s - flange_a.s (= " + String(s_rel, significantDigits=14) + ") >= 0 required for GasForce component.\n" + "Most likely, the component has to be flipped.");
assert(s_rel <= L + 1.e-12, " flange_b.s - flange_a.s (= " + String(s_rel) + " <= L (" + String(L) + ") required for GasForce component.\n" + "Most likely, parameter L is not correct.");	assert(s_rel <= L + 1.e-12, " flange_b.s - flange_a.s (= " + String(s_rel, significantDigits=14) + ") <= L (= " + String(L, significantDigits=14) + ") required for GasForce component.\n" + "Most likely, parameter L is not correct.");

---

model Mechanics.MultiBody.Examples.Loops.Utilities.CylinderBase

Component	Version 3.2	Version 3.2.1
Rod	shapeType="2"	shapeType="modelica://Modelica/Resources/Data/Shapes/Engine/rod.dxf"
Piston	shapeType="3"	shapeType="modelica://Modelica/Resources/Data/Shapes/Engine/piston.dxf"

---

model Mechanics.MultiBody.Examples.Loops.Utilities.Cylinder_analytic_CAD

Component	Version 3.2	Version 3.2.1
CrankShape	shapeType="modelica://Modelica/Resources/Data/CAD/EngineV6/1.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/Engine/crank.dxf"

---

model Mechanics.MultiBody.Examples.Loops.Utilities.EngineV6_analytic

Component	Version 3.2	Version 3.2.1
crank		r={0,0,0}

---

model Mechanics.MultiBody.Examples.Rotational3DEffects.MovingActuatedDrive

Component	Version 3.2	Version 3.2.1
position1		w(fixed=true)
position2		w(fixed=true)

---

model Mechanics.MultiBody.Examples.Rotational3DEffects.GearConstraint

Component	Version 3.2	Version 3.2.1
gearConstraint		phi_b(fixed=true)
		w_b(fixed=true)
inertia1	phi(fixed=true)	phi(fixed=true, start=0)
	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.MultiBody.Examples.Systems.RobotR3.Components.PathPlanning6

Component	Version 3.2	Version 3.2.1
angleBegDeg	unit="deg"
		each unit="deg"
angleEndDeg	unit="deg"
		each unit="deg"

---

model Mechanics.MultiBody.Examples.Systems.RobotR3.Components.Motor

Component	Version 3.2	Version 3.2.1
convert1	k=1
		k(unit="V/A") = 1
convert2	k=1
		k(unit="V/A") = 1

---

model Mechanics.MultiBody.Examples.Systems.RobotR3.Components.MechanicalStructure

Component	Version 3.2	Version 3.2.1
b0	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/0.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b0.dxf"
b1	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/1.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b1.dxf"
b2	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/2.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b2.dxf"
b3	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/3.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b3.dxf"
b4	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/4.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b4.dxf"
b5	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/5.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b5.dxf"
b6	shapeType="modelica://Modelica/Resources/Data/CAD/RobotR3/6.dxf"	shapeType="modelica://Modelica/Resources/Data/Shapes/RobotR3/b6.dxf"
load	lengthDirection=rLoad	lengthDirection=to_unit1(rLoad)
		r={0,0,0}

Equations in Version 3.2	Equations in Version 3.2.1
... qdd = der(qd);
tau = {r1.axis.tau,r2.axis.tau,r3.axis.tau,r4.axis.tau,r5.axis.tau,r6. axis.tau};	tau = {r1.tau, r2.tau, r3.tau, r4.tau, r5.tau, r6.tau};
connect(load.frame_a, b6.frame_b); ...

---

model Mechanics.MultiBody.Forces.Force

Component	Version 3.2	Version 3.2.1
connectionLine	lengthDirection=basicForce.r_0	lengthDirection=to_unit1(basicForce.r_0)

---

model Mechanics.MultiBody.Forces.Torque

Component	Version 3.2	Version 3.2.1
connectionLine	lengthDirection=basicTorque.r_0	lengthDirection=to_unit1(basicTorque.r_0)

---

model Mechanics.MultiBody.Forces.ForceAndTorque

Component	Version 3.2	Version 3.2.1
connectionLine	lengthDirection=basicForce.r_0	lengthDirection=to_unit1(basicForce.r_0)

---

model Mechanics.MultiBody.Forces.LineForceWithMass

Component	Version 3.2	Version 3.2.1
r_CM_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid
v_CM_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid

Equations in Version 3.2	Equations in Version 3.2.1
r_rel_0 = frame_b.r_0 - frame_a.r_0; ...

---

model Mechanics.MultiBody.Forces.LineForceWithTwoMasses

Component	Version 3.2	Version 3.2.1
r_CM1_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid
r_CM2_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid
v_CM1_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid
v_CM2_0	stateSelect=StateSelect.avoid
		each stateSelect=StateSelect.avoid

Equations in Version 3.2	Equations in Version 3.2.1
r_rel_0 = frame_b.r_0 - frame_a.r_0; ...

---

function Mechanics.MultiBody.Frames.Internal.maxWithoutEvent

Component	Version 3.2	Version 3.2.1
dummy	Present

Equations in Version 3.2	Equations in Version 3.2.1
... y := if u1 > u2 then u1 else u2;
dummy = 0;

---

function Mechanics.MultiBody.Frames.Internal.maxWithoutEvent_d

Component	Version 3.2	Version 3.2.1
dummy	Present

Equations in Version 3.2	Equations in Version 3.2.1
... y_d := if u1 > u2 then u1_d else u2_d;
dummy = 0;

---

model Mechanics.MultiBody.Joints.Prismatic

Component	Version 3.2	Version 3.2.1
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)

---

model Mechanics.MultiBody.Joints.Revolute

Component	Version 3.2	Version 3.2.1
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)

---

model Mechanics.MultiBody.Joints.RevolutePlanarLoopConstraint

Component	Version 3.2	Version 3.2.1
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)
ey_a	=Modelica_3_2.Math.Vectors.normalize(cross(e, nnx_a), 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(cross(e, nnx_a))

---

model Mechanics.MultiBody.Joints.FreeMotionScalarInit

Component	Version 3.2	Version 3.2.1
r_rel_a_1	SIunits.Position	Blocks.Interfaces.RealOutput
r_rel_a_2	SIunits.Position	Blocks.Interfaces.RealOutput
r_rel_a_3	SIunits.Position	Blocks.Interfaces.RealOutput
v_rel_a_1	SIunits.Velocity	Blocks.Interfaces.RealOutput
v_rel_a_2	SIunits.Velocity	Blocks.Interfaces.RealOutput
v_rel_a_3	SIunits.Velocity	Blocks.Interfaces.RealOutput
a_rel_a_1	SIunits.Acceleration	Blocks.Interfaces.RealOutput
a_rel_a_2	SIunits.Acceleration	Blocks.Interfaces.RealOutput
a_rel_a_3	SIunits.Acceleration	Blocks.Interfaces.RealOutput
angle_1	SIunits.Angle	Blocks.Interfaces.RealOutput
angle_2	SIunits.Angle	Blocks.Interfaces.RealOutput
angle_3	SIunits.Angle	Blocks.Interfaces.RealOutput
angle_d_1	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
angle_d_2	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
angle_d_3	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
angle_dd_1	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
angle_dd_2	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
angle_dd_3	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
w_rel_b_1	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
w_rel_b_2	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
w_rel_b_3	SIunits.AngularVelocity	Blocks.Interfaces.RealOutput
z_rel_b_1	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
z_rel_b_2	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
z_rel_b_3	SIunits.AngularAcceleration	Blocks.Interfaces.RealOutput
arrow	Mechanics.MultiBody.Visualizers.Advanced.Arrow	Mechanics.MultiBody.Visualizers.SignalArrow
		graphical
model_r	Present
model_w	Present
R_rel	Present
R_rel_inv	Present
initPosition		Present
initAngle		Present
initAngularVelocity		Present
derv		Present
dera		Present
derd		Present
derdd		Present
derz		Present
zeroForceAndTorque1		Present
zeroForceAndTorque2		Present

Equations in Version 3.2	Equations in Version 3.2.1
if use_angle then	connect(initPosition.r_rel_a[1], r_rel_a_1);
Connections.branch(frame_a.R, frame_b.R);	connect(initPosition.r_rel_a[2], r_rel_a_2);
R_rel = Frames.axesRotations(sequence_start, {angle_1, angle_2, angle_3}, {der(angle_1), der(angle_2), der(angle_3)});	connect(initPosition.r_rel_a[3], r_rel_a_3);
if rooted(frame_a.R) then	connect(derv[1].y, v_rel_a_1);
R_rel_inv = Frames.nullRotation();	connect(derv[2].y, v_rel_a_2);
frame_b.R = Frames.absoluteRotation(frame_a.R, R_rel);	connect(derv[3].y, v_rel_a_3);
else	connect(dera[1].y, a_rel_a_1);
R_rel_inv = Frames.inverseRotation(R_rel);	connect(dera[2].y, a_rel_a_2);
frame_a.R = Frames.absoluteRotation(frame_b.R, R_rel_inv);	connect(dera[3].y, a_rel_a_3);
end if;	connect(initAngle.angle[1], angle_1);
else	connect(initAngle.angle[2], angle_2);
R_rel = Frames.nullRotation();	connect(initAngle.angle[3], angle_3);
R_rel_inv = Frames.nullRotation();	connect(derd[1].y, angle_d_1);
angle_1 = 0;	connect(derd[2].y, angle_d_2);
angle_2 = 0;	connect(derd[3].y, angle_d_3);
angle_3 = 0;	connect(derdd[1].y, angle_dd_1);
end if;	connect(derdd[2].y, angle_dd_2);
frame_a.f = zeros(3);	connect(derdd[3].y, angle_dd_3);
frame_a.t = zeros(3);	connect(initAngularVelocity.w_rel_b[1], w_rel_b_1);
frame_b.f = zeros(3);	connect(initAngularVelocity.w_rel_b[2], w_rel_b_2);
frame_b.t = zeros(3);	connect(initAngularVelocity.w_rel_b[3], w_rel_b_3);
	connect(derz[1].y, z_rel_b_1); connect(derz[2].y, z_rel_b_2); connect(derz[3].y, z_rel_b_3); connect(initPosition.r_rel_a, derv.u); connect(derv.y, dera.u); connect(initAngle.frame_a, frame_a); connect(initAngle.frame_b, frame_b); connect(initAngle.angle, derd.u); connect(derd.y, derdd.u); connect(zeroForceAndTorque1.frame_a, frame_a); connect(zeroForceAndTorque2.frame_a, frame_b); connect(initAngularVelocity.w_rel_b, derz.u); connect(frame_a, arrow.frame_a); connect(initPosition.r_rel_a, arrow.r_head);

---

model Mechanics.MultiBody.Joints.UniversalSpherical

Component	Version 3.2	Version 3.2.1
rodLength	fixed=not computeRodLength	fixed=false
	=Modelica_3_2.Math.Vectors.length(rRod_ia)
		start=Modelica.Math.Vectors.length(rRod_ia)
eRod_ia	=Modelica_3_2.Math.Vectors.normalize(rRod_ia, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(rRod_ia)
length2_n2_a	unit="m2"	unit="1"
length_n2_a	SIunits.Length	Real

Equations in Version 3.2	Equations in Version 3.2.1
Connections.branch(frame_a.R, frame_ia.R);	initial equation
	if not computeRodLength then rodLength = Modelica.Math.Vectors.length(rRod_ia); end if; equation  &nbspConnections.branch(frame_a.R, frame_ia.R);
if kinematicConstraint then ... length2_n2_a = n2_a*n2_a;
length_n2_a = sqrt(length2_n2_a); ...

---

model Mechanics.MultiBody.Joints.GearConstraint

Component	Version 3.2	Version 3.2.1
stateSelect		Present
phi_b		Present
w_b		Present
a_b		Present

Equations in Version 3.2	Equations in Version 3.2.1
assert(cardinality(bearing) > 0,     "Connector bearing of component is not connected");
	phi_b = actuatedRevolute_b.phi; w_b = der(phi_b); a_b = der(w_b);
connect(actuatedRevolute_a.axis, idealGear.flange_a); ...

---

model Mechanics.MultiBody.Joints.Assemblies.JointUPS

Component	Version 3.2	Version 3.2.1
eAxis_ia	=Modelica_3_2.Math.Vectors.normalize(nAxis_ia, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(nAxis_ia)
e2_ia	=Modelica_3_2.Math.Vectors.normalize(cross(n1_a, eAxis_ia), 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(cross(n1_a, eAxis_ia))
length2_n2_a	unit="m2"	unit="1"
length_n2_a	SIunits.Length	Real

Equations in Version 3.2	Equations in Version 3.2.1
... length2_n2_a = n2_a*n2_a;
length_n2_a = sqrt(length2_n2_a); ...

---

model Mechanics.MultiBody.Joints.Assemblies.JointRRR

Component	Version 3.2	Version 3.2.1
n_b	fixed=false
	={0,0,1}
		each fixed=false
		start={0,0,1}
e_a	=Modelica_3_2.Math.Vectors.normalize(n_a, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n_a)
shape_rod1	lengthDirection=rRod1_ia	lengthDirection=to_unit1(rRod1_ia)
shape_rod2	lengthDirection=rRod2_ib	lengthDirection=to_unit1(rRod2_ib)

---

model Mechanics.MultiBody.Joints.Assemblies.JointRRP

Component	Version 3.2	Version 3.2.1
e_a	=Modelica_3_2.Math.Vectors.normalize(n_a, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n_a)
shape_rod1	lengthDirection=rRod1_ia	lengthDirection=to_unit1(rRod1_ia)
shape_rod2	lengthDirection=rRod2_ib	lengthDirection=to_unit1(rRod2_ib)

---

model Mechanics.MultiBody.Joints.Internal.RevoluteWithLengthConstraint

Component	Version 3.2	Version 3.2.1
position_a	each final quantity="Position"	each final quantity="Length"
position_b	each final quantity="Position"	each final quantity="Length"
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)

Equations in Version 3.2	Equations in Version 3.2.1
... k1a = k1 - C*C;
k1b = Frames.Internal.maxWithoutEvent(k1a, 1.0e-12); ...

---

model Mechanics.MultiBody.Joints.Internal.PrismaticWithLengthConstraint

Component	Version 3.2	Version 3.2.1
position_a		each final quantity="Length"
		each final unit="m"
position_b		each final quantity="Length"
		each final unit="m"
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)

Equations in Version 3.2	Equations in Version 3.2.1
... k1a = k1*k1 - C;
k1b = Frames.Internal.maxWithoutEvent(k1a, 1.0e-12); ...

---

model Mechanics.MultiBody.Parts.Fixed

Component	Version 3.2	Version 3.2.1
lengthDirection	SIunits.Position	Mechanics.MultiBody.Types.Axis
	sizes= 3
widthDirection	SIunits.Position	Mechanics.MultiBody.Types.Axis
	sizes= 3

---

model Mechanics.MultiBody.Parts.FixedTranslation

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)

---

model Mechanics.MultiBody.Parts.FixedRotation

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)
R_rel	=if rotationType == 1 then Frames.planarRotation(Modelica_3_2.Math.Vectors.normalize(n, 0.0), Cv.from_deg(angle), 0) else if rotationType == 2 then Frames.from_nxy(n_x, n_y) else Frames.axesRotations(sequence, Cv.from_deg(angles), zeros(3))	=if rotationType == Types.RotationTypes.RotationAxis then Frames.planarRotation(Modelica.Math.Vectors.normalizeWithAssert(n), Cv.from_deg(angle), 0) else if rotationType == Types.RotationTypes.TwoAxesVectors then Frames.from_nxy(n_x, n_y) else Frames.axesRotations(sequence, Cv.from_deg(angles), zeros(3))

---

model Mechanics.MultiBody.Parts.Body

Component	Version 3.2	Version 3.2.1
cylinder	lengthDirection=r_CM	lengthDirection=to_unit1(r_CM)

---

model Mechanics.MultiBody.Parts.BodyShape

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)

---

model Mechanics.MultiBody.Parts.BodyBox

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)
r_CM	=r_shape + Modelica_3_2.Math.Vectors.normalize(lengthDirection)*length/2	=r_shape + normalizeWithAssert(lengthDirection)*length/2

Equations in Version 3.2	Equations in Version 3.2.1
... a_0 = der(v_0);
assert(innerWidth <= width, "parameter innerWidth is greater as parameter width");	assert(innerWidth <= width, "parameter innerWidth is greater than parameter width");
assert(innerHeight <= height, "parameter innerHeight is greater as paraemter height");	assert(innerHeight <= height, "parameter innerHeight is greater than parameter height");
connect(frameTranslation.frame_a, frame_a); ...

---

model Mechanics.MultiBody.Parts.BodyCylinder

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)
r_CM	=r_shape + Modelica_3_2.Math.Vectors.normalize(lengthDirection)*length/2	=r_shape + normalizeWithAssert(lengthDirection)*length/2

Equations in Version 3.2	Equations in Version 3.2.1
... a_0 = der(v_0);
assert(innerDiameter < diameter, "parameter innerDiameter is greater as parameter diameter.");	assert(innerDiameter < diameter, "parameter innerDiameter is greater than parameter diameter");
connect(frameTranslation.frame_a, frame_a); ...

---

model Mechanics.MultiBody.Parts.PointMass

Equations in Version 3.2	Equations in Version 3.2.1
... if Connections.isRoot(frame_a.R) then
assert(cardinality(frame_a)==0, " A Modelica.Mechanics.MultiBody.Parts.PointMass model is connected in a way, so that no equations are present to compute frame_a.R (the orientation object in the connector). Setting frame_a.R to an arbitrary value in the PointMass model, might lead to a wrong overall model, depending on how the PointMass model is used. You can avoid this message, by providing equations that compute the orientation object, e.g., by using the Modelica.Mechanics.MultiBody.Joints.FreeMotion joint. If a PointMass model is not connected at all, the orientation object is set to a unit rotation. But this is the only case where this is done. ");	assert(cardinality(frame_a) == 0, " A Modelica.Mechanics.MultiBody.Parts.PointMass model is connected in a way, so that no equations are present to compute frame_a.R (the orientation object in the connector). Setting frame_a.R to an arbitrary value in the PointMass model, might lead to a wrong overall model, depending on how the PointMass model is used. You can avoid this message, by providing equations that compute the orientation object, e.g., by using the Modelica.Mechanics.MultiBody.Joints.FreeMotion joint. If a PointMass model is not connected at all, the orientation object is set to a unit rotation. But this is the only case where this is done. ");
frame_a.R = Frames.nullRotation(); ...

---

model Mechanics.MultiBody.Parts.Rotor1D

Component	Version 3.2	Version 3.2.1
e	=Modelica_3_2.Math.Vectors.normalize(n, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n)
inertia		stateSelect=StateSelect.never
rotorWith3DEffects		stateSelect=StateSelect.never

---

model Mechanics.MultiBody.Parts.BevelGear1D

Component	Version 3.2	Version 3.2.1
e_a	=Modelica_3_2.Math.Vectors.normalize(n_a, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n_a)
e_b	=Modelica_3_2.Math.Vectors.normalize(n_b, 0.0)	=Modelica.Math.Vectors.normalizeWithAssert(n_b)

---

model Mechanics.MultiBody.Parts.RollingWheel

Component	Version 3.2	Version 3.2.1
angles	fixed=true
		each fixed=true
der_angles	fixed=true
		each fixed=true

---

model Mechanics.MultiBody.Sensors.AbsoluteSensor

Component	Version 3.2	Version 3.2.1
r	each final quantity="Position"	each final quantity="Length"
angles	each final quantity="Angles"	each final quantity="Angle"
transformVector_a	Mechanics.MultiBody.Sensors.TansformAbsoluteVector	Mechanics.MultiBody.Sensors.TransformAbsoluteVector
transformVector_z	Mechanics.MultiBody.Sensors.TansformAbsoluteVector	Mechanics.MultiBody.Sensors.TransformAbsoluteVector

---

model Mechanics.MultiBody.Sensors.RelativeSensor

Component	Version 3.2	Version 3.2.1
r_rel	each final quantity="Position"	each final quantity="Length"
angles	each final quantity="Angles"	each final quantity="Angle"
transformVector_v_rel	Mechanics.MultiBody.Sensors.TansformRelativeVector	Mechanics.MultiBody.Sensors.TransformRelativeVector
transformVector_a_rel	Mechanics.MultiBody.Sensors.TansformRelativeVector	Mechanics.MultiBody.Sensors.TransformRelativeVector
transformVector_z_rel	Mechanics.MultiBody.Sensors.TansformRelativeVector	Mechanics.MultiBody.Sensors.TransformRelativeVector

---

model Mechanics.MultiBody.Sensors.AbsolutePosition

Component	Version 3.2	Version 3.2.1
r	each final quantity="Position"	each final quantity="Length"

---

model Mechanics.MultiBody.Sensors.AbsoluteVelocity

Component	Version 3.2	Version 3.2.1
tansformAbsoluteVector	Mechanics.MultiBody.Sensors.TansformAbsoluteVector	Mechanics.MultiBody.Sensors.TransformAbsoluteVector

---

model Mechanics.MultiBody.Sensors.AbsoluteAngles

Component	Version 3.2	Version 3.2.1
angles	each final quantity="Angles"	each final quantity="Angle"

---

model Mechanics.MultiBody.Sensors.AbsoluteAngularVelocity

Component	Version 3.2	Version 3.2.1
w	each final unit="1/s"	each final unit="rad/s"

---

model Mechanics.MultiBody.Sensors.RelativeVelocity

Component	Version 3.2	Version 3.2.1
tansformRelativeVector	Mechanics.MultiBody.Sensors.TansformRelativeVector	Mechanics.MultiBody.Sensors.TransformRelativeVector

---

model Mechanics.MultiBody.Sensors.RelativeAngles

Component	Version 3.2	Version 3.2.1
angles	each final quantity="Angles"	each final quantity="Angle"
	displayUnit="deg"
		each displayUnit="deg"

---

model Mechanics.MultiBody.Sensors.RelativeAngularVelocity

Component	Version 3.2	Version 3.2.1
w_rel	each final unit="1/s"	each final unit="rad/s"

---

model Mechanics.MultiBody.Sensors.CutForce

Component	Version 3.2	Version 3.2.1
force	final quantity="Force"
	final unit="N"
		each final quantity="Force"
		each final unit="N"

---

model Mechanics.MultiBody.Sensors.CutForceAndTorque

Component	Version 3.2	Version 3.2.1
force	final quantity="Force"
	final unit="N"
		each final quantity="Force"
		each final unit="N"

---

model Mechanics.MultiBody.Sensors.TansformAbsoluteVector

Component	Version 3.2	Version 3.2.1
frame_a	Present
frame_resolve	Present
r_in	Present
r_out	Present
frame_r_in	Present
frame_r_out	Present
basicTransformVector	Present
zeroPosition	Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(basicTransformVector.frame_a, frame_a); connect(basicTransformVector.frame_resolve, frame_resolve); connect(zeroPosition.frame_resolve, basicTransformVector.frame_resolve); connect(basicTransformVector.r_out, r_out); connect(basicTransformVector.r_in, r_in);

---

model Mechanics.MultiBody.Sensors.TansformRelativeVector

Component	Version 3.2	Version 3.2.1
frame_resolve	Present
r_in	Present
r_out	Present
frame_r_in	Present
frame_r_out	Present
basicTransformVector	Present
zeroPosition	Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(basicTransformVector.frame_a, frame_a); connect(basicTransformVector.frame_b, frame_b); connect(basicTransformVector.frame_resolve, frame_resolve); connect(zeroPosition.frame_resolve, basicTransformVector.frame_resolve); connect(basicTransformVector.r_out, r_out); connect(basicTransformVector.r_in, r_in);

---

model Mechanics.MultiBody.Sensors.Internal.BasicAbsolutePosition

Component	Version 3.2	Version 3.2.1
r	each final quantity="Position"	each final quantity="Length"

---

model Mechanics.MultiBody.Sensors.Internal.BasicAbsoluteAngularVelocity

Component	Version 3.2	Version 3.2.1
w	final quantity="AngularVelocity"
	final unit="rad/s"
		each final quantity="AngularVelocity"
		each final unit="rad/s"

---

model Mechanics.MultiBody.Sensors.Internal.BasicRelativePosition

Component	Version 3.2	Version 3.2.1
r_rel	each final quantity="Position"	each final quantity="Length"

---

model Mechanics.MultiBody.Sensors.Internal.BasicRelativeAngularVelocity

Component	Version 3.2	Version 3.2.1
w_rel	final quantity="AngularVelocity"
	final unit="rad/s"
		each final quantity="AngularVelocity"
		each final unit="rad/s"

---

model Mechanics.MultiBody.Sensors.Internal.BasicCutForce

Component	Version 3.2	Version 3.2.1
force	final quantity="Force"
	final unit="N"
		each final quantity="Force"
		each final unit="N"

---

model Mechanics.MultiBody.Sensors.Internal.BasicCutTorque

Component	Version 3.2	Version 3.2.1
torque	final quantity="Torque"
	final unit="N.m"
		each final quantity="Torque"
		each final unit="N.m"

---

model Mechanics.MultiBody.Visualizers.FixedShape2

Component	Version 3.2	Version 3.2.1
lengthDirection	=r - r_shape	=to_unit1(r - r_shape)

---

model Mechanics.MultiBody.Visualizers.SignalArrow

Component	Version 3.2	Version 3.2.1
r_head	each final quantity="Position"	each final quantity="Length"

---

model Mechanics.MultiBody.Visualizers.Torus

Component	Version 3.2	Version 3.2.1
surface	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.torus (ri=ri, ro=ro, opening=opening, startAngle=startAngle, stopAngle=stopAngle)	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.torus (ri=ri, ro=ro, opening=opening, startAngle=startAngle, stopAngle=stopAngle)

---

model Mechanics.MultiBody.Visualizers.VoluminousWheel

Component	Version 3.2	Version 3.2.1
torus	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.torus (ri=ri, ro=rCurvature2, opening=Modelica_3_2.Constants.pi - Modelica_3_2.Math.asin(rw/rCurvature2))	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.torus (ri=ri, ro=rCurvature2, opening=Modelica.Constants.pi - Modelica.Math.asin(rw/rCurvature2))

---

model Mechanics.MultiBody.Visualizers.PipeWithScalarField

Component	Version 3.2	Version 3.2.1
xsi	min=0
	max=1
		each min=0
		each max=1

---

function Mechanics.MultiBody.Visualizers.Colors.ColorMaps.jet

Component	Version 3.2	Version 3.2.1
v1	=if d >= 0.5 then {1} else if d >= 0.25 then 1 - d:d:1 else 0.5 + d:d:1	={1 - (b - i)*d for i in 1:b}
v4	=1 - d:-d:0.5	={0.5 + (c - i)*d for i in 1:c}
b		Present
c		Present

---

function Mechanics.MultiBody.Visualizers.Colors.scalarToColor

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
color :=colorMap[integer((size(colorMap, 1) - 1)/(T_max - T_min)* min((max(T,T_min) - T_min), T_max) + 1), :];	color := colorMap[1 + integer((size(colorMap,1)-1)*(max(T_min,min(T,T_max))-T_min) / (T_max-T_min)), :];

---

model Mechanics.MultiBody.Visualizers.Advanced.Arrow

Component	Version 3.2	Version 3.2.1
arrowLine	length=noEvent(max(0, length - diameter*Types.Defaults.ArrowHeadLengthFraction))	length=arrowLength
	lengthDirection=r_head	lengthDirection=to_unit1(r_head)
arrowHead	lengthDirection=r_head	lengthDirection=to_unit1(r_head)
	r=rvisobj + rxvisobj*arrowLine.length	r=rvisobj + rxvisobj*arrowLength
arrowLength		Present

---

model Mechanics.MultiBody.Visualizers.Advanced.DoubleArrow

Component	Version 3.2	Version 3.2.1
arrowLine	length=noEvent(max(0, length - 1.5*diameter*MultiBody.Types.Defaults.ArrowHeadLengthFraction))	length=arrowLength
	lengthDirection=r_head	lengthDirection=to_unit1(r_head)
arrowHead1	lengthDirection=r_head	lengthDirection=to_unit1(r_head)
	r=rvisobj + rxvisobj*arrowLine.length	r=rvisobj + rxvisobj*arrowLength
arrowHead2	lengthDirection=r_head	lengthDirection=to_unit1(r_head)
	r=rvisobj + rxvisobj*(arrowLine.length + 0.5*arrowHead1.length)	r=rvisobj + rxvisobj*(arrowLength + 0.5*headLength)
arrowLength		Present

---

model Mechanics.MultiBody.Visualizers.Advanced.PipeWithScalarField

Component	Version 3.2	Version 3.2.1
xsi	min=0
	max=1
		each min=0
		each max=1
surface	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.pipeWithScalarField (rOuter=rOuter, length=length, xsi=xsi, T=T, T_min=T_min, T_max=T_max, colorMap=colorMapData)	redeclare function surfaceCharacteristic = Modelica.Mechanics.MultiBody.Visualizers.Advanced.SurfaceCharacteristics.pipeWithScalarField (rOuter=rOuter, length=length, xsi=xsi, T=T, T_min=T_min, T_max=T_max, colorMap=colorMapData)

---

model Mechanics.Rotational.Examples.First

Component	Version 3.2	Version 3.2.1
inertia2	w(fixed=true)	w(fixed=true, start=0)
inertia3	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.FirstGrounded

Component	Version 3.2	Version 3.2.1
inertia2	w(fixed=true)	w(fixed=true, start=0)
inertia3	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.CoupledClutches

Component	Version 3.2	Version 3.2.1
J2	w(fixed=true)	w(fixed=true, start=0)
J3	w(fixed=true)	w(fixed=true, start=0)
J4	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.LossyGearDemo1

Component	Version 3.2	Version 3.2.1
Inertia2	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.LossyGearDemo2

Component	Version 3.2	Version 3.2.1
Inertia2	w(fixed=true)	w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.ElasticBearing

Component	Version 3.2	Version 3.2.1
shaft	w(fixed=true)	w(fixed=true, start=0)
load	w(fixed=true)	w(fixed=true, start=0)
multiSensor		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(idealGear.support, housing.flange_b);
connect(housing.flange_a, springDamper.flange_b);
connect(ramp.y, torque.tau);
connect(fixed.flange, torque.support);
	connect(housing.flange_a, multiSensor.flange_b); connect(multiSensor.flange_a, springDamper.flange_b);

---

model Mechanics.Rotational.Examples.RollingWheel

Component	Version 3.2	Version 3.2.1
inertia		phi(fixed=true, start=0)
		w(fixed=true, start=0)

---

model Mechanics.Rotational.Examples.SimpleGearShift

Component	Version 3.2	Version 3.2.1
load		phi(fixed=true, start=0)
		w(fixed=true, start=0)
clutch		phi_rel(fixed=true)
		w_rel(fixed=true)

---

model Mechanics.Rotational.Components.Clutch

Component	Version 3.2	Version 3.2.1
a_rel	Present

---

model Mechanics.Rotational.Components.InitializeFlange

Component	Version 3.2	Version 3.2.1
phi_start		unit="rad"
w_start		unit="rad/s"
a_start		unit="rad/s2"

---

model Mechanics.Rotational.Components.RelativeStates

Component	Version 3.2	Version 3.2.1
phi_rel		nominal=if phi_nominal >= Modelica.Constants.eps then phi_nominal else 1
phi_nominal		Present

---

model Mechanics.Rotational.Sensors.AngleSensor

Component	Version 3.2	Version 3.2.1
phi		unit="rad"
		displayUnit="deg"

---

model Mechanics.Rotational.Sensors.SpeedSensor

Component	Version 3.2	Version 3.2.1
w		unit="rad/s"

---

model Mechanics.Rotational.Sensors.AccSensor

Component	Version 3.2	Version 3.2.1
a		unit="rad/s2"

---

model Mechanics.Rotational.Sensors.RelAngleSensor

Component	Version 3.2	Version 3.2.1
phi_rel		unit="rad"
		displayUnit="deg"

---

model Mechanics.Rotational.Sensors.RelSpeedSensor

Component	Version 3.2	Version 3.2.1
w_rel		unit="rad/s"

---

model Mechanics.Rotational.Sensors.RelAccSensor

Component	Version 3.2	Version 3.2.1
a_rel		unit="rad/s2"

---

model Mechanics.Rotational.Sensors.TorqueSensor

Component	Version 3.2	Version 3.2.1
tau		unit="N.m"

---

model Mechanics.Rotational.Sensors.PowerSensor

Component	Version 3.2	Version 3.2.1
power		unit="W"

---

model Mechanics.Rotational.Sources.Speed

Component	Version 3.2	Version 3.2.1
w_ref		unit="rad/s"

---

model Mechanics.Rotational.Sources.Accelerate

Component	Version 3.2	Version 3.2.1
a_ref		unit="rad/s2"

---

model Mechanics.Rotational.Sources.Torque

Component	Version 3.2	Version 3.2.1
tau		unit="N.m"

---

model Mechanics.Rotational.Sources.Torque2

Component	Version 3.2	Version 3.2.1
tau		unit="N.m"

---

model Mechanics.Rotational.Interfaces.PartialCompliantWithRelativeStates

Component	Version 3.2	Version 3.2.1
phi_rel	nominal=phi_nominal	nominal=if phi_nominal >= Modelica.Constants.eps then phi_nominal else 1
phi_nominal		min=0.0

---

model Mechanics.Translational.Examples.Sensors

Component	Version 3.2	Version 3.2.1
multiSensor		Present

Equations in Version 3.2	Equations in Version 3.2.1
connect(forceSensor.flange_b, mass.flange_a);
connect(sineForce.y, force.f); ... connect(mass.flange_b, positionSensor2.flange);
	connect(forceSensor.flange_b, multiSensor.flange_a); connect(multiSensor.flange_b, mass.flange_a);

---

model Mechanics.Translational.Examples.HeatLosses

Component	Version 3.2	Version 3.2.1
mass3	v(fixed=false)	v(fixed=true)
springDamper1		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(sine2.y, brake.f_normalized);
connect(brake.flange_b, massWithStopAndFriction.flange_a);
connect(elastoGap.flange_b, mass1.flange_a); ... connect(massWithStopAndFriction.heatPort, convection.solid);
	connect(brake.flange_b, springDamper1.flange_a); connect(springDamper1.flange_b, massWithStopAndFriction.flange_a); connect(springDamper1.heatPort, convection.solid);

---

model Mechanics.Translational.Components.ElastoGap

Component	Version 3.2	Version 3.2.1
c	Real	SIunits.TranslationalSpringConstant
d	Real	SIunits.TranslationalDampingConstant

---

model Mechanics.Translational.Components.SupportFriction

Equations in Version 3.2	Equations in Version 3.2.1
... free = false;
s = s_a - s_support;	s = flange_a.s - s_support;
s_a = s_b;	flange_a.s = flange_b.s;
v = der(s); ...

---

model Mechanics.Translational.Components.InitializeFlange

Component	Version 3.2	Version 3.2.1
s_start		unit="m"
v_start		unit="m/s"
a_start		unit="m/s2"

---

model Mechanics.Translational.Components.MassWithStopAndFriction

Component	Version 3.2	Version 3.2.1
stopped	=if s <= smin + L/2 then -1 else if s >= smax - L/2 then +1 else 0

Equations in Version 3.2	Equations in Version 3.2.1
... lossPower = f*v_relfric;
algorithm
when (initial()) then ... end when;
	stopped = if s <= smin + L/2 then -1 else if s >= smax - L/2 then +1 else 0;
when stopped <> 0 then
reinit(s, if stopped < 0 then smin + L/2 else smax - L/2);
if (not initial() or stopped*v>0) then
reinit(v, 0);
end if;
end when;

---

model Mechanics.Translational.Sensors.PositionSensor

Component	Version 3.2	Version 3.2.1
s		unit="m"

---

model Mechanics.Translational.Sensors.SpeedSensor

Component	Version 3.2	Version 3.2.1
v		unit="m/s"

---

model Mechanics.Translational.Sensors.AccSensor

Component	Version 3.2	Version 3.2.1
a		unit="m/s2"

---

model Mechanics.Translational.Sensors.RelPositionSensor

Component	Version 3.2	Version 3.2.1
s_rel		unit="m"

---

model Mechanics.Translational.Sensors.RelSpeedSensor

Component	Version 3.2	Version 3.2.1
v_rel		unit="m/s"

---

model Mechanics.Translational.Sensors.RelAccSensor

Component	Version 3.2	Version 3.2.1
a_rel		unit="m/s2"

---

model Mechanics.Translational.Sensors.ForceSensor

Component	Version 3.2	Version 3.2.1
f		unit="N"

---

model Mechanics.Translational.Sensors.PowerSensor

Component	Version 3.2	Version 3.2.1
power		unit="W"

---

model Mechanics.Translational.Sources.Position

Component	Version 3.2	Version 3.2.1
s_ref		unit="m"

---

model Mechanics.Translational.Sources.Speed

Component	Version 3.2	Version 3.2.1
v_ref		unit="m/s"

---

model Mechanics.Translational.Sources.Accelerate

Component	Version 3.2	Version 3.2.1
a_ref		unit="m/s2"

---

model Mechanics.Translational.Sources.Force

Component	Version 3.2	Version 3.2.1
f		unit="N"

---

model Mechanics.Translational.Sources.Force2

Component	Version 3.2	Version 3.2.1
f		unit="N"

---

model Mechanics.Translational.Interfaces.PartialCompliant

Component	Version 3.2	Version 3.2.1
s_rel	SIunits.Distance	SIunits.Position

---

model Mechanics.Translational.Interfaces.PartialCompliantWithRelativeStates

Component	Version 3.2	Version 3.2.1
s_rel	SIunits.Distance	SIunits.Position

---

model Mechanics.Translational.Interfaces.PartialElementaryOneFlangeAndSupport

Component	Version 3.2	Version 3.2.1
s	=flange.s - internalSupport.s

Equations in Version 3.2	Equations in Version 3.2.1
	s = flange.s - internalSupport.s;
connect(internalSupport.flange, support); ...

---

model Mechanics.Translational.Interfaces.PartialElementaryOneFlangeAndSupport2

Component	Version 3.2	Version 3.2.1
s	=flange.s - s_support

Equations in Version 3.2	Equations in Version 3.2.1
	s = flange.s - s_support;
if not useSupport then ...

---

model Mechanics.Translational.Interfaces.PartialElementaryTwoFlangesAndSupport

Component	Version 3.2	Version 3.2.1
s_a	=flange_a.s - internalSupport.s
s_b	=flange_b.s - internalSupport.s

Equations in Version 3.2	Equations in Version 3.2.1
	s_a = flange_a.s - internalSupport.s; s_b = flange_b.s - internalSupport.s;
connect(internalSupport.flange, support); ...

---

model Mechanics.Translational.Interfaces.PartialElementaryTwoFlangesAndSupport2

Component	Version 3.2	Version 3.2.1
s_a	=flange_a.s - s_support
s_b	=flange_b.s - s_support

Equations in Version 3.2	Equations in Version 3.2.1
	s_a = flange_a.s - s_support; s_b = flange_b.s - s_support;
if not useSupport then ...

---

model Mechanics.Translational.Interfaces.PartialForce

Component	Version 3.2	Version 3.2.1
f	=flange.f

Equations in Version 3.2	Equations in Version 3.2.1
	f = flange.f;

---

model Fluid.Examples.PumpingSystem

Component	Version 3.2	Version 3.2.1
source	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
pipe	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
pumps	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.25,0.5}, head_nominal={100,60,0})	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.25,0.5}, head_nominal={100,60,0})
	energyDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	massDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	massDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	V=50/1000
	T_start=Modelica_3_2.SIunits.Conversions.from_degC(20)
		V(displayUnit="l") = 0.05
reservoir	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
	massDynamics=Modelica_3_2.Fluid.Types.Dynamics.FixedInitial
userValve	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
sink	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
reservoirPressure	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Medium
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial

---

model Fluid.Examples.HeatingSystem

Component	Version 3.2	Version 3.2.1
tank	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=10)	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=10)
	s(each start=1)
		T_start=Modelica.SIunits.Conversions.from_degC(20)
valve		dp_start=18000
heater	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer
	modelStructure=Modelica_3_2.Fluid.Types.ModelStructure.a_vb	modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow
		p_a_start=130000
radiator	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer
	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow
	modelStructure=Modelica_3_2.Fluid.Types.ModelStructure.av_b	modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
		p_a_start=110000
pipe	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.IdealFlowHeatTransfer
	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow
		p_a_start=130000

---

model Fluid.Examples.DrumBoiler.DrumBoiler

Component	Version 3.2	Version 3.2.1
evaporator	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
sink	p=from_bar(0.5)	p=Cv.from_bar(0.5)
	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
massFlowRate	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
temperature	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
pressure	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
controller		initType=Modelica.Blocks.Types.Init.InitialState
pump	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
SteamValve	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
use_inputs		Present
q_F		Present
Y_Valve		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(controller.u,feedback.y);
connect(feedback.u2, evaporator.V); connect(levelSetPoint.y,feedback.u1);
connect(massFlowRate.m_flow, qm_S); ... connect(Y_Valve_Tab.y, SteamValve.opening);
	connect(q_F, MW2W.u); connect(Y_Valve, SteamValve.opening); connect(evaporator.V, feedback.u2); connect(levelSetPoint.y, feedback.u1);

---

model Fluid.Examples.DrumBoiler.BaseClasses.EquilibriumDrumBoiler

Component	Version 3.2	Version 3.2.1
cp_D	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
p_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
sat		Media.Interfaces.Types.SaturationProperties
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_v	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h_l	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
rho_v	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho_l	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T_D	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_W	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h_S	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

model Fluid.Examples.Tanks.TanksWithOverflow

Component	Version 3.2	Version 3.2.1
upperTank	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
massFlowRate	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
pressure	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
pipe	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
lowerTank	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
overflow	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater

---

model Fluid.Examples.Tanks.EmptyTanks

Component	Version 3.2	Version 3.2.1
tank1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
	level_start=0	level_start=1.0e-10
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial

---

model Fluid.Examples.ControlledTankSystem.ControlledTanks

Component	Version 3.2	Version 3.2.1
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial

---

model Fluid.Examples.ControlledTankSystem.Utilities.TankController

Component	Version 3.2	Version 3.2.1
stateGraphRoot		Present

---

block Fluid.Examples.ControlledTankSystem.Utilities.RadioButton

Equations in Version 3.2	Equations in Version 3.2.1
	initial equation pre(reset) = fill(false, size(reset, 1));
algorithm ...

---

model Fluid.Examples.AST_BatchPlant.BatchPlant_StandardWater

Component	Version 3.2	Version 3.2.1
B5	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)
P1	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.001,0.0015}, head_nominal={100,50,0})	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.1e-3,0.15e-3}, head_nominal={10,5,0})
	energyDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	massDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	massDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	show_NPSHa=true
	checkValve=true
		redeclare model Monitoring = Modelica.Fluid.Machines.BaseClasses.PumpMonitoring.PumpMonitoringNPSH
P2	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.001,0.0015}, head_nominal={100,50,0})	redeclare function flowCharacteristic = Modelica.Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow (V_flow_nominal={0,0.1e-3,0.15e-3}, head_nominal={10,5,0})
	energyDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	massDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	massDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
	show_NPSHa=true
	checkValve=true
		redeclare model Monitoring = Modelica.Fluid.Machines.BaseClasses.PumpMonitoring.PumpMonitoringNPSH
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
P1_on	amplitude=100	amplitude=200
P2_on	amplitude=50	amplitude=200
B7	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)
pipeB1B3	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow
pipeB2B3	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow
B6	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)	redeclare model HeatTransfer = Modelica.Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer (k=4.9)

---

model Fluid.Examples.AST_BatchPlant.BaseClasses.TankWith3InletOutletArraysWithEvaporatorCondensor

Component	Version 3.2	Version 3.2.1
T_start	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
p_ambient	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_ambient	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
h_v	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h_l	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
rho_v	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho_l	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

model Fluid.Examples.AST_BatchPlant.BaseClasses.InnerTank

Component	Version 3.2	Version 3.2.1
m_flow_negative		fixed=true
Xi	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

model Fluid.Examples.AST_BatchPlant.BaseClasses.Controller

Component	Version 3.2	Version 3.2.1
stateGraphRoot		Present

---

model Fluid.Examples.AST_BatchPlant.BaseClasses.TankWithTopPorts

Component	Version 3.2	Version 3.2.1
p_ambient	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_ambient	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
H_flow_top	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate
port_b_H_flow_bottom	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate

---

model Fluid.Examples.AST_BatchPlant.Test.OneTank

Component	Version 3.2	Version 3.2.1
tank	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
flowSource	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
ambient_fixed	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.AST_BatchPlant.Test.TwoTanks

Component	Version 3.2	Version 3.2.1
tank1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe1

Component	Version 3.2	Version 3.2.1
flowSource	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
ambient_fixed	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
valveDiscrete	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.AST_BatchPlant.Test.TankWithEmptyingPipe2

Component	Version 3.2	Version 3.2.1
ambient_fixed	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
ambient_fixed1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe1

Component	Version 3.2	Version 3.2.1
ambient_fixed1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe1	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
ambient_fixed2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
tank2	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
pipe3	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.AST_BatchPlant.Test.TanksWithEmptyingPipe2

Component	Version 3.2	Version 3.2.1
ambient_fixed	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater
valveDiscrete	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater	redeclare package Medium = Modelica.Media.Water.ConstantPropertyLiquidWater

---

model Fluid.Examples.IncompressibleFluidNetwork

Component	Version 3.2	Version 3.2.1
pipe1	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe2	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe3	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe4	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe6	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
valve1	CvData=Modelica_3_2.Fluid.Types.CvTypes.OpPoint	CvData=Modelica.Fluid.Types.CvTypes.Av
		Av=2.5e-2^2/4*Modelica.Constants.pi
valve2	CvData=Modelica_3_2.Fluid.Types.CvTypes.OpPoint	CvData=Modelica.Fluid.Types.CvTypes.Av
		Av=2.5e-2^2/4*Modelica.Constants.pi
pipe7	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
valve3	CvData=Modelica_3_2.Fluid.Types.CvTypes.OpPoint	CvData=Modelica.Fluid.Types.CvTypes.Av
		Av=2.5e-2^2/4*Modelica.Constants.pi
system		massDynamics=systemMassDynamics
		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
		use_eps_Re=true
valveOpening1	height=-0.2	height=-1
	startTime=1	startTime=50
valveOpening2	height=-0.2	height=-0.5
	startTime=2	startTime=100
valveOpening3	height=-0.2	height=-0.5
	startTime=3	startTime=150
pipe8	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe9	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe10	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipe5	Fluid.Examples.IncompressibleFluidNetwork.Pipe	Fluid.Pipes.DynamicPipe
pipeModelStructure		Present
systemMassDynamics		Present
filteredValveOpening		Present
heat8		Present
pipe11		Present

Equations in Version 3.2	Equations in Version 3.2.1
... connect(valve1.port_b, pipe7.port_a);
connect(pipe6.port_b, valve3.port_a);
connect(valve3.port_b, sink.ports[1]); ... connect(pipe7.port_b, pipe8.port_a);
connect(pipe9.port_b, valve3.port_a);
connect(pipe8.port_b, pipe10.port_a);
connect(pipe10.port_b, valve3.port_a);
connect(pipe4.port_b, pipe6.port_a); ... connect(pipe5.port_a, pipe4.port_b);
connect(pipe5.port_b, valve3.port_a);	connect(heat8.port, pipe8.heatPorts);
	connect(pipe5.port_b, pipe6.port_b); connect(pipe6.port_b, pipe10.port_b); connect(pipe11.port_b, valve3.port_a); connect(pipe9.port_b, pipe11.port_a); connect(pipe10.port_b, pipe11.port_a);

---

model Fluid.Examples.BranchingDynamicPipes

Component	Version 3.2	Version 3.2.1
system	momentumDynamics=Modelica_3_2.Fluid.Types.Dynamics.DynamicFreeInitial	momentumDynamics=Modelica.Fluid.Types.Dynamics.SteadyStateInitial
		energyDynamics=Modelica.Fluid.Types.Dynamics.SteadyStateInitial
pipe1		modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
pipe2	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.LocalPipeFlowHeatTransfer	redeclare model HeatTransfer = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.LocalPipeFlowHeatTransfer
		modelStructure=Modelica.Fluid.Types.ModelStructure.av_vb
pipe3		modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
pipe4	modelStructure=Modelica_3_2.Fluid.Types.ModelStructure.av_b	modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
heat2		alpha=-1e-2*ones(pipe2.n)

---

model Fluid.Examples.HeatExchanger.HeatExchangerSimulation

Component	Version 3.2	Version 3.2.1
HEX	redeclare model HeatTransfer_1 = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.ConstantFlowHeatTransfer (alpha0=1000)	redeclare model HeatTransfer_1 = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.LocalPipeFlowHeatTransfer (alpha0=1000)
	redeclare model HeatTransfer_2 = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.ConstantFlowHeatTransfer (alpha0=200)	redeclare model HeatTransfer_2 = Modelica.Fluid.Pipes.BaseClasses.HeatTransfer.ConstantFlowHeatTransfer (alpha0=200)
	energyDynamics=Modelica_3_2.Fluid.Types.Dynamics.FixedInitial
	massDynamics=Modelica_3_2.Fluid.Types.Dynamics.SteadyStateInitial
		modelStructure_1=Modelica.Fluid.Types.ModelStructure.av_b
		modelStructure_2=Modelica.Fluid.Types.ModelStructure.a_vb
system		energyDynamics=Modelica.Fluid.Types.Dynamics.SteadyStateInitial
		use_eps_Re=true

---

model Fluid.Examples.HeatExchanger.BaseClasses.BasicHX

Component	Version 3.2	Version 3.2.1
use_HeatTransfer	=false	=true
p_a_start1	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start1	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_start_1	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start_1	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start_1	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
p_a_start2	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start2	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_start_2	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start_2	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start_2	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
pipe_1		final modelStructure=modelStructure_1
pipe_2		final modelStructure=modelStructure_2
modelStructure_1		Present
modelStructure_2		Present

---

model Fluid.Examples.HeatExchanger.BaseClasses.WallConstProps

Component	Version 3.2	Version 3.2.1
T	stateSelect=StateSelect.prefer
		each stateSelect=StateSelect.prefer

Equations in Version 3.2	Equations in Version 3.2.1
initial equation
if energyDynamics == Types.Dynamics.SteadyState then	if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(T) = zeros(n);
elseif energyDynamics == Types.Dynamics.FixedInitial then	elseif energyDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
T = ones(n)*T_start; ... assert(m[i]>0, "Wall has negative dimensions");
if energyDynamics == Types.Dynamics.SteadyState then	if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
0 = heatPort_a[i].Q_flow + heatPort_b[i].Q_flow; ...

---

model Fluid.Examples.TraceSubstances.RoomCO2

Component	Version 3.2	Version 3.2.1
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
pipe	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)

Equations in Version 3.2	Equations in Version 3.2.1
... connect(traceVolume.port, pipe.port_a);
connect(boundary1.ports[1], volume.ports[1]);	connect(boundary1.ports[2], volume.ports[1]);
connect(boundary1.ports[2], traceSource.port);	connect(boundary1.ports[1], traceSource.port);

---

model Fluid.Examples.TraceSubstances.RoomCO2WithControls

Component	Version 3.2	Version 3.2.1
system		energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial
		use_eps_Re=true
		m_flow_nominal=0.1
		eps_m_flow=1e-2
ductOut	length=1	length=5
	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)
		modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b
ductIn	length=1	length=5
	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow (show_Res=true)
		modelStructure=Modelica.Fluid.Types.ModelStructure.a_v_b

---

model Fluid.Examples.InverseParameterization

Component	Version 3.2	Version 3.2.1
pipe1	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.NominalTurbulentPipeFlow (m_flow_nominal=1, show_Res=true, dp_nominal=100000)	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.NominalTurbulentPipeFlow (show_Res=true, m_flow_nominal=1, m_flow_turbulent=eps_m_flow_turbulent*1, dp_nominal=100000)
pipe2	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.NominalLaminarFlow (show_Res=true, dp_nominal=100000, m_flow_nominal=1)	redeclare model FlowModel = Modelica.Fluid.Pipes.BaseClasses.FlowModels.NominalLaminarFlow (show_Res=true, dp_nominal=100000, m_flow_nominal=1)
eps_m_flow_turbulent		Present

---

model Fluid.Examples.Explanatory.MeasuringTemperature

Component	Version 3.2	Version 3.2.1
T_onePort	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
T_twoPort	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankCold2	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankCold1	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankHot1	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankHot2	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
mFlow1	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
mFlow2	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
T_junction	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankCold3	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
openTankHot3	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
mFlow3	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater
junctionIdeal	redeclare package Medium = Modelica.Media.Water.StandardWater	redeclare package Medium = Modelica.Media.Water.StandardWater

---

model Fluid.Examples.Explanatory.MomentumBalanceFittings

Component	Version 3.2	Version 3.2.1
leftBoundary1	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
rightBoundary1	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
suddenExpansion1	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
leftBoundary2	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
rightBoundary2	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
suddenExpansion2	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
leftAdaptor	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase
rightAdaptor	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase	redeclare package Medium = Modelica.Media.Water.StandardWaterOnePhase

---

model Fluid.System

Component	Version 3.2	Version 3.2.1
m_flow_small	=0.01	=1e-2
use_eps_Re		Present
m_flow_nominal		Present
eps_m_flow		Present

Equations in Version 3.2	Equations in Version 3.2.1
	initial equation

---

model Fluid.Vessels.OpenTank

Component	Version 3.2	Version 3.2.1
level	start=max(level_start, Modelica_3_2.Constants.eps)	start=level_start_eps
p_ambient	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_ambient	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
level_start_eps		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if massDynamics == Types.Dynamics.FixedInitial then
level = level_start;	level = level_start_eps;
elseif massDynamics == Types.Dynamics.SteadyStateInitial then ...

---

model Fluid.Vessels.BaseClasses.PartialLumpedVessel

Component	Version 3.2	Version 3.2.1
m_flow_small	=system.m_flow_small	=if system.use_eps_Re then system.eps_m_flow*m_flow_nominal else system.m_flow_small
ports_H_flow	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate
ports_mC_flow	Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Media.Interfaces.Types.ExtraPropertyFlowRate
sum_ports_mC_flow	Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Media.Interfaces.Types.ExtraPropertyFlowRate
vessel_ps_static	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
portDensities	Present
m_flow_nominal		Present
use_Re		Present
portInDensities		Present
Re_turbulent		Present
m_flow_turbulent		Present
regularFlow		Present
inFlow		Present

Equations in Version 3.2	Equations in Version 3.2.1
... for i in 1:nPorts loop
	portInDensities[i] = Medium.density(Medium.setState_phX(vessel_ps_static[i], inStream(ports[i].h_outflow), inStream(ports[i].Xi_outflow)));
if use_portsData then
portDensities[i] = noEvent(Medium.density(Medium.setState_phX(vessel_ps_static[i], actualStream(ports[i].h_outflow), actualStream(ports[i].Xi_outflow))));	portVelocities[i] = smooth(0, ports[i].m_flow/portAreas[i]/Medium.density(Medium.setState_phX(vessel_ps_static[i], actualStream(ports[i].h_outflow), actualStream(ports[i].Xi_outflow))));
portVelocities[i] = smooth(0, ports[i].m_flow/portAreas[i]/portDensities[i]);
ports_penetration[i] = Utilities.regStep(fluidLevel - portsData_height[i] - 0.1*portsData_diameter[i], 1, 1e-3, 0.1*portsData_diameter[i]);
	m_flow_turbulent[i]=if not use_Re then m_flow_small else            &nbspmax(m_flow_small, (Modelica.Constants.pi/8)*portsData_diameter[i]                                *(Medium.dynamicViscosity(Medium.setState_phX(vessel_ps_static[i], inStream(ports[i].h_outflow), inStream(ports[i].Xi_outflow)))                                  + Medium.dynamicViscosity(medium.state))*Re_turbulent);
else
portDensities[i] = medium.d;
portVelocities[i] = 0;
ports_penetration[i] = 1;
	m_flow_turbulent[i] = Modelica.Constants.inf;
end if;
if fluidLevel >= portsData_height[i] then	regularFlow[i] = fluidLevel >= portsData_height[i];
	inFlow[i] = not regularFlow[i] and (s[i] > 0 or portsData_height[i] >= fluidLevel_max); if regularFlow[i] then
if use_portsData then
ports[i].p = vessel_ps_static[i] + (0.5/portAreas[i]^2*Utilities.regSquare2(ports[i].m_flow, m_flow_small, (portsData_zeta_in[i] - 1 + portAreas[i]^2/vesselArea^2)/portDensities[i]*ports_penetration[i], (portsData_zeta_out[i] + 1 - portAreas[i]^2/vesselArea^2)/medium.d/ports_penetration[i]));	ports[i].p = homotopy(vessel_ps_static[i] + (0.5/portAreas[i]^2*Utilities.regSquare2(ports[i].m_flow, m_flow_turbulent[i], (portsData_zeta_in[i] - 1 + portAreas[i]^2/vesselArea^2)/portInDensities[i]*ports_penetration[i], (portsData_zeta_out[i] + 1 - portAreas[i]^2/vesselArea^2)/medium.d/ports_penetration[i])), vessel_ps_static[i]);
else ... s[i] = fluidLevel - portsData_height[i];
elseif s[i] > 0 or portsData_height[i] >= fluidLevel_max then	elseif inFlow[i] then
ports[i].p = vessel_ps_static[i]; ...

---

model Fluid.Pipes.StaticPipe

Component	Version 3.2	Version 3.2.1
p_a_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Fluid.Pipes.DynamicPipe

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(true, "Unknown model structure");	assert(false, "Unknown model structure");
end if; ...

---

model Fluid.Pipes.BaseClasses.PartialTwoPortFlow

Component	Version 3.2	Version 3.2.1
H_flows	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(true, "Unknown model structure");	assert(false, "Unknown model structure");
end if; ... port_b.p = mediums[n].p;
	vsFM[1] = vs[1:iLumped-1]*lengths[1:iLumped-1]/sum(lengths[1:iLumped-1]); vsFM[2] = vs[iLumped:n]*lengths[iLumped:n]/sum(lengths[iLumped:n]);
elseif modelStructure == ModelStructure.av_b then ... m_flows[n+1] = flowModel.m_flows[1];
	vsFM[1] = vs*lengths/sum(lengths); vsFM[2] = m_flows[n+1]/Medium.density(state_b)/crossAreas[n]/nParallel;
elseif modelStructure == ModelStructure.a_vb then ... port_b.p = mediums[n].p;
	vsFM[1] = m_flows[1]/Medium.density(state_a)/crossAreas[1]/nParallel; vsFM[2] = vs*lengths/sum(lengths);
elseif modelStructure == ModelStructure.a_v_b then ... m_flows[n+1] = flowModel.m_flows[2];
	vsFM[1] = m_flows[1]/Medium.density(state_a)/crossAreas[1]/nParallel; vsFM[2] = vs*lengths/sum(lengths); vsFM[3] = m_flows[n+1]/Medium.density(state_b)/crossAreas[n]/nParallel;
else
assert(true, "Unknown model structure");	assert(false, "Unknown model structure");
end if;
if modelStructure <> ModelStructure.a_v_b then vsFM[1] = vs[1:iLumped-1]*lengths[1:iLumped-1]/sum(lengths[1:iLumped-1]); vsFM[2] = vs[iLumped:n]*lengths[iLumped:n]/sum(lengths[iLumped:n]);
else
vsFM[1] = vs[1:iLumped-1]*lengths[1:iLumped-1]/sum(lengths[1:iLumped-1]); vsFM[2] = vs[2:n-1]*lengths[2:n-1]/sum(lengths[2:n-1]); vsFM[3] = vs[iLumped:n]*lengths[iLumped:n]/sum(lengths[iLumped:n]); end if; else
if modelStructure == ModelStructure.av_vb then ... else
assert(true, "Unknown model structure");	assert(false, "Unknown model structure");
end if; ...

---

model Fluid.Pipes.BaseClasses.FlowModels.PartialStaggeredFlowModel

Component	Version 3.2	Version 3.2.1
p_a_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
rhos	SIunits.Density	Media.Interfaces.Types.Density
rhos_act	SIunits.Density	Media.Interfaces.Types.Density
mus	SIunits.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
mus_act	SIunits.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

Equations in Version 3.2	Equations in Version 3.2.1
... if use_Ib_flows then
Ib_flows = {rhos[i]*vs[i]*vs[i]*crossAreas[i] - rhos[i+1]*vs[i+1]*vs[i+1]*crossAreas[i+1] for i in 1:n-1};	Ib_flows = nParallel*{rhos[i]*vs[i]*vs[i]*crossAreas[i] - rhos[i+1]*vs[i+1]*vs[i+1]*crossAreas[i+1] for i in 1:n-1};
else ...

---

model Fluid.Pipes.BaseClasses.FlowModels.PartialGenericPipeFlow

Component	Version 3.2	Version 3.2.1
dp_small		protected
	=system.dp_small
		start=1
		fixed=false
m_flow_small	=system.m_flow_small	=if system.use_eps_Re then system.eps_m_flow*m_flow_nominal else system.m_flow_small
constantPressureLossCoefficient		protected
continuousFlowReversal		protected
diameters		protected
Res_turbulent_internal		Present
dp_fric_nominal		Present

Equations in Version 3.2	Equations in Version 3.2.1
for i in 1:n-1 loop	initial equation
	if system.use_eps_Re then dp_small = dp_fric_nominal/m_flow_nominal*m_flow_small; else dp_small = system.dp_small; end if; equation  &nbspfor i in 1:n-1 loop
assert(m_flows[i] > -m_flow_small or allowFlowReversal, "Reverting flow occurs even though allowFlowReversal is false"); ... if from_dp and not WallFriction.dp_is_zero then
m_flows = WallFriction.massFlowRate_dp( dps_fg - {g*dheights[i]*rhos_act[i] for i in 1:n-1}, rhos_act, rhos_act, mus_act, mus_act, pathLengths_internal, diameters, (roughnesses[1:n-1]+roughnesses[2:n])/2, dp_small)*nParallel;	m_flows = homotopy( actual= WallFriction.massFlowRate_dp( dps_fg - {g*dheights[i]*rhos_act[i] for i in 1:n-1}, rhos_act, rhos_act, mus_act, mus_act, pathLengths_internal, diameters, (roughnesses[1:n-1]+roughnesses[2:n])/2, dp_small/(n-1), Res_turbulent_internal)*nParallel, simplified= m_flow_nominal/dp_nominal*(dps_fg - g*dheights*rho_nominal));
else
dps_fg = WallFriction.pressureLoss_m_flow( m_flows/nParallel, rhos_act, rhos_act, mus_act, mus_act, pathLengths_internal, diameters, (roughnesses[1:n-1]+roughnesses[2:n])/2, m_flow_small/nParallel) + {g*dheights[i]*rhos_act[i] for i in 1:n-1};	dps_fg = homotopy( actual= WallFriction.pressureLoss_m_flow( m_flows/nParallel, rhos_act, rhos_act, mus_act, mus_act, pathLengths_internal, diameters, (roughnesses[1:n-1]+roughnesses[2:n])/2, m_flow_small/nParallel, Res_turbulent_internal) + {g*dheights[i]*rhos_act[i] for i in 1:n-1}, simplified= dp_nominal/m_flow_nominal*m_flows + g*dheights*rho_nominal);
end if; ... if from_dp and not WallFriction.dp_is_zero then
m_flows = WallFriction.massFlowRate_dp_staticHead( dps_fg, rhos[1:n-1], rhos[2:n], mus[1:n-1], mus[2:n], pathLengths_internal, diameters, g*dheights, (roughnesses[1:n-1]+roughnesses[2:n])/2, dp_small/n)*nParallel;	m_flows = homotopy( actual= WallFriction.massFlowRate_dp_staticHead( dps_fg, rhos[1:n-1], rhos[2:n], mus[1:n-1], mus[2:n], pathLengths_internal, diameters, g*dheights, (roughnesses[1:n-1]+roughnesses[2:n])/2, dp_small/(n-1), Res_turbulent_internal)*nParallel, simplified= m_flow_nominal/dp_nominal*(dps_fg - g*dheights*rho_nominal));
else
dps_fg = WallFriction.pressureLoss_m_flow_staticHead( m_flows/nParallel, rhos[1:n-1], rhos[2:n], mus[1:n-1], mus[2:n], pathLengths_internal, diameters, g*dheights, (roughnesses[1:n-1]+roughnesses[2:n])/2, m_flow_small/nParallel);	dps_fg = homotopy( actual= WallFriction.pressureLoss_m_flow_staticHead( m_flows/nParallel, rhos[1:n-1], rhos[2:n], mus[1:n-1], mus[2:n], pathLengths_internal, diameters, g*dheights, (roughnesses[1:n-1]+roughnesses[2:n])/2, m_flow_small/nParallel, Res_turbulent_internal), simplified= dp_nominal/m_flow_nominal*m_flows + g*dheights*rho_nominal);
end if; ...

---

model Fluid.Pipes.BaseClasses.FlowModels.NominalTurbulentPipeFlow

Component	Version 3.2	Version 3.2.1
dps_fg_turbulent	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
m_flow_turbulent		Present
Res_turbulent_nominal		Present

Equations in Version 3.2	Equations in Version 3.2.1
... pathLengths_nominal[i] = zetas[i]*diameters[i]*(2*    &nbspModelica_3_2.Math.log10(3.7/((roughnesses[i] + roughnesses[i +    &nbsp1])/2/diameters[i])))^2;
	Res_turbulent_nominal[i] = m_flow_turbulent/nParallel / (pi/4*diameters[i]*mus_act[i]);
end for;

---

model Fluid.Pipes.BaseClasses.FlowModels.TurbulentPipeFlow

Component	Version 3.2	Version 3.2.1
use_Re		Present

Equations in Version 3.2	Equations in Version 3.2.1
	initial equation if system.use_eps_Re then dp_nominal = dp_fric_nominal + g*sum(dheights)*rho_nominal; end if;

---

model Fluid.Pipes.BaseClasses.FlowModels.DetailedPipeFlow

Equations in Version 3.2	Equations in Version 3.2.1
	initial equation if system.use_eps_Re then dp_nominal = dp_fric_nominal + g*sum(dheights)*rho_nominal; else dp_nominal = 1e3*dp_small; end if;

---

model Fluid.Pipes.BaseClasses.HeatTransfer.PartialPipeFlowHeatTransfer

Component	Version 3.2	Version 3.2.1
ds	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
mus	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambdas	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity

---

model Fluid.Pipes.BaseClasses.HeatTransfer.LocalPipeFlowHeatTransfer

Equations in Version 3.2	Equations in Version 3.2.1
... Nus_2[i]=smooth(0,1.077*(abs(Res[i])*Prs[i]*diameters[i]/lengths[i]/(if vs[i]>=0 then (i-0.5) else (n-i+0.5)))^(1/3));
Nus[i]=spliceFunction(Nus_turb[i], Nus_lam[i], Res[i]-6150, 3850);	Nus[i]=Modelica.Media.Air.MoistAir.Utilities.spliceFunction(Nus_turb[i], Nus_lam[i], Res[i]-6150, 3850);
end for;

---

package Fluid.Pipes.BaseClasses.WallFriction.PartialWallFriction

Component	Version 3.2	Version 3.2.1
use_Re_turbulent		Present

---

function Fluid.Pipes.BaseClasses.WallFriction.PartialWallFriction.massFlowRate_dp

Component	Version 3.2	Version 3.2.1
Re_turbulent		Present

---

function Fluid.Pipes.BaseClasses.WallFriction.PartialWallFriction.massFlowRate_dp_staticHead

Component	Version 3.2	Version 3.2.1
Re_turbulent		Present

---

function Fluid.Pipes.BaseClasses.WallFriction.PartialWallFriction.pressureLoss_m_flow

Component	Version 3.2	Version 3.2.1
Re_turbulent		Present

---

function Fluid.Pipes.BaseClasses.WallFriction.PartialWallFriction.pressureLoss_m_flow_staticHead

Component	Version 3.2	Version 3.2.1
Re_turbulent		Present

---

function Fluid.Pipes.BaseClasses.WallFriction.QuadraticTurbulent.massFlowRate_dp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
zeta = (length/diameter)/(2*Math.log10(3.7 /(roughness/diameter)))^2; ...

---

function Fluid.Pipes.BaseClasses.WallFriction.QuadraticTurbulent.pressureLoss_m_flow

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
zeta = (length/diameter)/(2*Math.log10(3.7 /(roughness/diameter)))^2; ...

---

function Fluid.Pipes.BaseClasses.WallFriction.QuadraticTurbulent.massFlowRate_dp_staticHead

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
if dp>=dp_a then ...

---

function Fluid.Pipes.BaseClasses.WallFriction.QuadraticTurbulent.pressureLoss_m_flow_staticHead

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
if m_flow>=m_flow_a then ...

---

function Fluid.Pipes.BaseClasses.WallFriction.LaminarAndQuadraticTurbulent.massFlowRate_dp

Component	Version 3.2	Version 3.2.1
Re_turbulent	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
zeta = (length/diameter)/(2*Math.log10(3.7 /(roughness/diameter)))^2; ... yd0 = (rho_a + rho_b)/(k0*(mu_a + mu_b));
dp_turbulent = ((mu_a + mu_b)*diameter*pi/8)^2*Re_turbulent^2/(k_inv*(rho_a+rho_b)/2);	dp_turbulent = max(((mu_a + mu_b)*diameter*pi/8)^2*Re_turbulent^2/(k_inv*(rho_a+rho_b)/2), dp_small);
m_flow = Modelica_3_2.Fluid.Utilities.regRoot2(                &nbspdp,                &nbspdp_turbulent,                &nbsprho_a*k_inv,                &nbsprho_b*k_inv,                &nbspuse_yd0=true,                &nbspyd0=yd0); ...

---

function Fluid.Pipes.BaseClasses.WallFriction.LaminarAndQuadraticTurbulent.pressureLoss_m_flow

Component	Version 3.2	Version 3.2.1
Re_turbulent	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
zeta = (length/diameter)/(2*Math.log10(3.7 /(roughness/diameter)))^2; ... yd0 = k0*(mu_a + mu_b)/(rho_a + rho_b);
m_flow_turbulent = (pi/8)*diameter*(mu_a + mu_b)*Re_turbulent;	m_flow_turbulent = max((pi/8)*diameter*(mu_a + mu_b)*Re_turbulent, m_flow_small);
dp = Modelica_3_2.Fluid.Utilities.regSquare2(                &nbspm_flow,                &nbspm_flow_turbulent,                &nbspk/rho_a,                &nbspk/rho_b,                &nbspuse_yd0=true,                &nbspyd0=yd0); ...

---

function Fluid.Pipes.BaseClasses.WallFriction.LaminarAndQuadraticTurbulent.massFlowRate_dp_staticHead

Component	Version 3.2	Version 3.2.1
Re1	=745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta)	=min(745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta), Re_turbulent)
Re2	constant
	=4000	=Re_turbulent

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
dp_a = max(dp_grav_a, dp_grav_b)+dp_small; ...

---

function Fluid.Pipes.BaseClasses.WallFriction.LaminarAndQuadraticTurbulent.pressureLoss_m_flow_staticHead

Component	Version 3.2	Version 3.2.1
Re1	=745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta)	=min(745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta), Re_turbulent)
Re2	constant
	=4000	=Re_turbulent

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(roughness > 1.e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");	assert(roughness > 1e-10, "roughness > 0 required for quadratic turbulent wall friction characteristic");
m_flow_a = if dp_grav_a<dp_grav_b then    &nbspInternal.m_flow_of_dp_fric(dp_grav_b - dp_grav_a, rho_a, rho_b, mu_a, mu_b, length, diameter, Re1, Re2, Delta)+m_flow_small else    &nbspm_flow_small; ...

---

function Fluid.Pipes.BaseClasses.WallFriction.Detailed.massFlowRate_dp

Component	Version 3.2	Version 3.2.1
Re1	=(745*Math.exp(if Delta <= 0.0065 then 1 else 0.0065/Delta))^0.97	=min((745*Math.exp(if Delta <= 0.0065 then 1 else 0.0065/Delta))^0.97, Re_turbulent)
Re2	=4000	=Re_turbulent

---

function Fluid.Pipes.BaseClasses.WallFriction.Detailed.pressureLoss_m_flow

Component	Version 3.2	Version 3.2.1
Re1	=745*Math.exp(if Delta <= 0.0065 then 1 else 0.0065/Delta)	=min(745*Math.exp(if Delta <= 0.0065 then 1 else 0.0065/Delta), Re_turbulent)
Re2	=4000	=Re_turbulent

---

function Fluid.Pipes.BaseClasses.WallFriction.Detailed.massFlowRate_dp_staticHead

Component	Version 3.2	Version 3.2.1
Re1	=(745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta))^0.97	=min((745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta))^0.97, Re_turbulent)
Re2	constant
	=4000	=Re_turbulent

---

function Fluid.Pipes.BaseClasses.WallFriction.Detailed.pressureLoss_m_flow_staticHead

Component	Version 3.2	Version 3.2.1
Re1	=745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta)	=min(745*exp(if Delta <= 0.0065 then 1 else 0.0065/Delta), Re_turbulent)
Re2	constant
	=4000	=Re_turbulent

---

model Fluid.Pipes.BaseClasses.WallFriction.TestWallFrictionAndGravity

Component	Version 3.2	Version 3.2.1
dp_small	SIunits.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
		protected
m_flow_nominal		Present
dp_fric_nominal		Present

---

model Fluid.Machines.ControlledPump

Component	Version 3.2	Version 3.2.1
p_a_nominal	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_nominal	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Fluid.Machines.BaseClasses.PartialPump

Component	Version 3.2	Version 3.2.1
p_a_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
m_flow_start	=1	=system.m_flow_start
rho_nominal	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
V_flow	=m_flow/rho
V_flow_single	=V_flow/nParallel
s	start=m_flow_start	start=m_flow_start/unit_m_flow
show_NPSHa	Present
state_a	Present
rho_in	Present
NPSHa	Present
NPSPa	Present
NPDPa	Present
V_flow_single_init		Present
delta_head_init		Present
unit_m_flow		Present
monitoring		Present

Equations in Version 3.2	Equations in Version 3.2.1
	V_flow = homotopy(m_flow/rho,                     &nbspm_flow/rho_nominal); V_flow_single = V_flow/nParallel;
if not checkValve then
head = (N/N_nominal)^2*flowCharacteristic(V_flow_single*(N_nominal/N));	head = homotopy((N/N_nominal)^2*flowCharacteristic(V_flow_single*N_nominal/N), N/N_nominal*(flowCharacteristic(0)+delta_head_init*V_flow_single));
s = 0;
elseif s > 0 then head = (N/N_nominal)^2*flowCharacteristic(V_flow_single*(N_nominal/N)); V_flow_single = s*unitMassFlowRate/rho;
else
head = (N/N_nominal)^2*flowCharacteristic(0) - s*unitHead;	head = homotopy(if s > 0 then (N/N_nominal)^2*flowCharacteristic(V_flow_single*N_nominal/N) else (N/N_nominal)^2*flowCharacteristic(0) - s*unitHead, N/N_nominal*(flowCharacteristic(0)+delta_head_init*V_flow_single));
V_flow_single = 0;	V_flow_single = homotopy(if s > 0 then s*unitMassFlowRate/rho else 0, s*unitMassFlowRate/rho_nominal);
end if;
if use_powerCharacteristic then
W_single = (N/N_nominal)^3*(rho/rho_nominal)*powerCharacteristic(V_flow_single*(N_nominal/N));	W_single = homotopy((N/N_nominal)^3*(rho/rho_nominal)*powerCharacteristic(V_flow_single*N_nominal/N), N/N_nominal*V_flow_single/V_flow_single_init*powerCharacteristic(V_flow_single_init));
eta = dp_pump*V_flow_single/W_single;
else
eta = efficiencyCharacteristic(V_flow_single*(N_nominal/N));	eta = homotopy(efficiencyCharacteristic(V_flow_single*(N_nominal/N)), efficiencyCharacteristic(V_flow_single_init));
W_single = dp_pump*V_flow_single/eta;	W_single = homotopy(dp_pump*V_flow_single/eta, dp_pump*V_flow_single_init/eta);
end if; ...

---

function Fluid.Machines.BaseClasses.PumpCharacteristics.linearFlow

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
head := c[1] + V_flow*c[2];	assert(c[2] <= -Modelica.Constants.small, "Wrong pump curve -- head_nominal must be monotonically decreasing with increasing V_flow_nominal", level=AssertionLevel.warning);
	head = c[1] + V_flow*c[2];

---

function Fluid.Machines.BaseClasses.PumpCharacteristics.quadraticFlow

Component	Version 3.2	Version 3.2.1
V_flow_min		Present
V_flow_max		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
head := c[1] + V_flow*c[2] + V_flow^2*c[3];	assert(max(c[2].+2*c[3]*V_flow_nominal) <= -Modelica.Constants.small, "Wrong pump curve -- head_nominal must be monotonically decreasing with increasing V_flow_nominal", level=AssertionLevel.warning);
	if V_flow < V_flow_min then
	head = max(head_nominal) + (V_flow-V_flow_min)*(c[2]+2*c[3]*V_flow_min); elseif V_flow > V_flow_max then head = min(head_nominal) + (V_flow-V_flow_max)*(c[2]+2*c[3]*V_flow_max); else head = c[1] + V_flow*(c[2] + V_flow*c[3]); end if;

---

function Fluid.Machines.BaseClasses.PumpCharacteristics.polynomialFlow

Component	Version 3.2	Version 3.2.1
V_flow_nominal_pow	={{V_flow_nominal[i]^(j - 1) for j in 1:N} for i in 1:N}	={{if j > 1 then V_flow_nominal[i]^(j - 1) else 1 for j in 1:N} for i in 1:N}
V_flow_min		Present
V_flow_max		Present
max_dhdV		Present
poly		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
head := sum(V_flow^(i-1)*c[i] for i in 1:N);	assert(max_dhdV <= -Modelica.Constants.small, "Wrong pump curve -- head_nominal must be monotonically decreasing with increasing V_flow_nominal", level=AssertionLevel.warning);
	if V_flow < V_flow_min then
	poly = c[N]*(N-1); for i in 1:N-2 loop poly = V_flow_min*poly + c[N-i]*(N-i-1); end for; head = max(head_nominal) + (V_flow-V_flow_min)*poly; elseif V_flow > V_flow_max then poly = c[N]*(N-1); for i in 1:N-2 loop poly = V_flow_max*poly + c[N-i]*(N-i-1); end for; head = min(head_nominal) + (V_flow-V_flow_max)*poly; else poly = c[N]; for i in 1:N-1 loop poly = V_flow*poly + c[N-i]; end for; head = poly; end if;

---

model Fluid.Valves.ValveIncompressible

Component	Version 3.2	Version 3.2.1
Re_turbulent		Present
use_Re		Present
dp_turbulent		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if checkValve then
m_flow = relativeFlowCoefficient*Av*sqrt(Medium.density(state_a))* Modelica_3_2.Fluid.Utilities.regRoot2( dp, dp_small, 1.0, 0.0, use_yd0=true, yd0=0.0);	m_flow = homotopy(relativeFlowCoefficient*Av*sqrt(Medium.density(state_a))* Utilities.regRoot2(dp,dp_turbulent,1.0,0.0,use_yd0=true,yd0=0.0), relativeFlowCoefficient*m_flow_nominal*dp/dp_nominal);
elseif not allowFlowReversal then
m_flow = relativeFlowCoefficient*Av*sqrt(Medium.density(state_a))* Utilities.regRoot(dp, dp_small);	m_flow = homotopy(relativeFlowCoefficient*Av*sqrt(Medium.density(state_a))* Utilities.regRoot(dp, dp_turbulent), relativeFlowCoefficient*m_flow_nominal*dp/dp_nominal);
else
m_flow = relativeFlowCoefficient*Av* Modelica_3_2.Fluid.Utilities.regRoot2( dp, dp_small, Medium.density(state_a), Medium.density(state_b));	m_flow = homotopy(relativeFlowCoefficient*Av* Utilities.regRoot2(dp,dp_turbulent,Medium.density(state_a),Medium.density(state_b)), relativeFlowCoefficient*m_flow_nominal*dp/dp_nominal);
end if;

---

model Fluid.Valves.ValveVaporizing

Component	Version 3.2	Version 3.2.1
T_in	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
p_sat	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_in	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_out	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
Re_turbulent		Present
use_Re		Present
dp_turbulent		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if checkValve then
m_flow = valveCharacteristic(opening_actual)*Av*sqrt(Medium.density( state_a))*Modelica_3_2.Fluid.Utilities.regRoot2( dpEff, dp_small, 1.0, 0.0, use_yd0=true, yd0=0.0);	m_flow = homotopy(valveCharacteristic(opening_actual)*Av*sqrt(Medium.density(state_a))* Utilities.regRoot2(dpEff,dp_turbulent,1.0,0.0,use_yd0=true,yd0=0.0), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
elseif not allowFlowReversal then
m_flow = valveCharacteristic(opening_actual)*Av*sqrt(Medium.density(state_a))* Utilities.regRoot(dpEff, dp_small);	m_flow = homotopy(valveCharacteristic(opening_actual)*Av*sqrt(Medium.density(state_a))* Utilities.regRoot(dpEff, dp_turbulent), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
else
m_flow = valveCharacteristic(opening_actual)*Av* Modelica_3_2.Fluid.Utilities.regRoot2( dpEff, dp_small, Medium.density(state_a), Medium.density(state_b));	m_flow = homotopy(valveCharacteristic(opening_actual)*Av* Utilities.regRoot2(dpEff,dp_turbulent,Medium.density(state_a),Medium.density(state_b)), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
end if;

---

model Fluid.Valves.ValveCompressible

Component	Version 3.2	Version 3.2.1
p_nominal	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
Re_turbulent		Present
use_Re		Present
dp_turbulent		Present

Equations in Version 3.2	Equations in Version 3.2.1
...
equation p = noEvent(if dp>=0 then port_a.p else port_b.p);	equation p = max(port_a.p, port_b.p);
Fxt = Fxt_full*xtCharacteristic(opening_actual);
x = dp/p;
xs = smooth(0, if x < -Fxt then -Fxt else if x > Fxt then Fxt else x);	xs = max(-Fxt, min(x, Fxt));
Y = 1 - abs(xs)/(3*Fxt);
if checkValve then
m_flow = valveCharacteristic(opening_actual)*Av*Y*sqrt(Medium.density(state_a))* (if xs>=0 then Utilities.regRoot(p*xs, dp_small) else 0);	m_flow = homotopy(valveCharacteristic(opening_actual)*Av*Y*sqrt(Medium.density(state_a))* (if xs>=0 then Utilities.regRoot(p*xs, dp_turbulent) else 0), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
elseif not allowFlowReversal then
m_flow = valveCharacteristic(opening_actual)*Av*sqrt(Medium.density(state_a))* Utilities.regRoot(p*xs, dp_small);	m_flow = homotopy(valveCharacteristic(opening_actual)*Av*Y*sqrt(Medium.density(state_a))* Utilities.regRoot(p*xs, dp_turbulent), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
else
m_flow = valveCharacteristic(opening_actual)*Av*Y* smooth(0, Utilities.regRoot(p*xs, dp_small)*(if xs>=0 then sqrt(Medium.density(state_a)) else sqrt(Medium.density(state_b))));	m_flow = homotopy(valveCharacteristic(opening_actual)*Av*Y* Utilities.regRoot2(p*xs, dp_turbulent, Medium.density(state_a), Medium.density(state_b)), valveCharacteristic(opening_actual)*m_flow_nominal*dp/dp_nominal);
end if;

---

model Fluid.Valves.ValveDiscrete

Component	Version 3.2	Version 3.2.1
dp_nominal	SIunits.Pressure	SIunits.AbsolutePressure

---

model Fluid.Valves.BaseClasses.PartialValve

Component	Version 3.2	Version 3.2.1
Av	=0
rho_nominal	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
dp_small		protected
	=system.dp_small	=if system.use_eps_Re then dp_nominal/m_flow_nominal*m_flow_small else system.dp_small

---

model Fluid.Fittings.Bends.CurvedBend

Component	Version 3.2	Version 3.2.1
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Fluid.Fittings.Bends.EdgedBend

Component	Version 3.2	Version 3.2.1
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Fluid.Fittings.Orifices.ThickEdgedOrifice

Component	Version 3.2	Version 3.2.1
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Fluid.Fittings.GenericResistances.VolumeFlowRate

Component	Version 3.2	Version 3.2.1
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
d_a	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
d_b	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

model Fluid.Fittings.SimpleGenericOrifice

Component	Version 3.2	Version 3.2.1
dp_nominal	SIunits.AbsolutePressure	SIunits.Pressure
m_flow_nominal	=1	=if system.use_eps_Re then system.m_flow_nominal else 1e2*system.m_flow_small
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
		protected
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
use_Re		Present
Re_turbulent		Present
m_flow_turbulent		Present
dp_turbulent		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if from_dp then
m_flow = Utilities.regRoot2( dp_fg, dp_small, Medium.density(state_a)/BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal), Medium.density(state_b)/BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal));	m_flow = homotopy(Utilities.regRoot2( dp_fg, dp_turbulent, Medium.density(state_a)/BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal), Medium.density(state_b)/BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal)), m_flow_nominal*dp_fg/dp_nominal);
else
dp_fg = Utilities.regSquare2( m_flow, m_flow_small, BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal)/Medium.density(state_a), BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal)/Medium.density(state_b));	dp_fg = homotopy(Utilities.regSquare2( m_flow, m_flow_turbulent, BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal)/Medium.density(state_a), BaseClasses.lossConstant_D_zeta(diameter, zeta_nominal)/Medium.density(state_b)), dp_nominal*m_flow/m_flow_nominal);
end if; ...

---

model Fluid.Fittings.MultiPort

Component	Version 3.2	Version 3.2.1
ports_b_Xi_inStream	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
ports_b_C_inStream	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Fittings.BaseClasses.QuadraticTurbulent.BaseModel

Component	Version 3.2	Version 3.2.1
use_Re	=false	=system.use_eps_Re
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
		protected
m_flow_small	Present
m_flow_nominal		Present
state_nominal		Present
dp_nominal		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if from_dp then
m_flow = if use_Re then massFlowRate_dp_and_Re( dp_fg, Medium.density(state_a), Medium.density(state_b), Medium.dynamicViscosity(state_a), Medium.dynamicViscosity(state_b), data) else massFlowRate_dp(dp_fg, Medium.density(state_a), Medium.density(state_b), data, dp_small);	m_flow = homotopy(if use_Re then massFlowRate_dp_and_Re( dp_fg, Medium.density(state_a), Medium.density(state_b), Medium.dynamicViscosity(state_a), Medium.dynamicViscosity(state_b), data) else massFlowRate_dp(dp_fg, Medium.density(state_a), Medium.density(state_b), data, dp_small), m_flow_nominal*dp_fg/dp_nominal);
else
dp_fg = if use_Re then pressureLoss_m_flow_and_Re( m_flow, Medium.density(state_a), Medium.density(state_b), Medium.dynamicViscosity(state_a), Medium.dynamicViscosity(state_b), data) else pressureLoss_m_flow(m_flow, Medium.density(state_a), Medium.density(state_b), data, m_flow_small);	dp_fg = homotopy(if use_Re then pressureLoss_m_flow_and_Re( m_flow, Medium.density(state_a), Medium.density(state_b), Medium.dynamicViscosity(state_a), Medium.dynamicViscosity(state_b), data) else pressureLoss_m_flow(m_flow, Medium.density(state_a), Medium.density(state_b), data, m_flow_small), dp_nominal*m_flow/m_flow_nominal);
end if; ...

---

model Fluid.Fittings.BaseClasses.QuadraticTurbulent.BaseModelNonconstantCrossSectionArea

Component	Version 3.2	Version 3.2.1
dp_small	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
		protected
m_flow_small	Present
m_flow_nominal		Present
state_nominal		Present
dp_nominal		Present

---

model Fluid.Sources.FixedBoundary

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Sources.Boundary_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Sources.Boundary_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Sources.MassFlowSource_T

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
sum(ports.m_flow) = -m_flow_in_internal;	if Medium.ThermoStates == IndependentVariables.ph or Medium.ThermoStates == IndependentVariables.phX then
	medium.h = Medium.specificEnthalpy(Medium.setState_pTX(medium.p, T_in_internal, X_in_internal)); else
medium.T = T_in_internal;
	end if; sum(ports.m_flow) = -m_flow_in_internal;
medium.Xi = X_in_internal[1:Medium.nXi]; ...

---

model Fluid.Sources.MassFlowSource_h

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
sum(ports.m_flow) = -m_flow_in_internal;	if Medium.ThermoStates == IndependentVariables.ph or Medium.ThermoStates == IndependentVariables.phX then
medium.h = h_in_internal;
medium.Xi = X_in_internal[1:Medium.nXi];	else
ports.C_outflow = fill(C_in_internal, nPorts);	medium.T = Medium.temperature(Medium.setState_phX(medium.p, h_in_internal, X_in_internal));
	end if; sum(ports.m_flow) = -m_flow_in_internal; medium.Xi = X_in_internal[1:Medium.nXi]; ports.C_outflow = fill(C_in_internal, nPorts);

---

model Fluid.Sensors.DensityTwoPort

Component	Version 3.2	Version 3.2.1
rho_a_inflow	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho_b_inflow	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
m_flow_small	Present

---

model Fluid.Sensors.TemperatureTwoPort

Component	Version 3.2	Version 3.2.1
T_a_inflow	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T_b_inflow	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
m_flow_small	Present

---

model Fluid.Sensors.SpecificEnthalpyTwoPort

Component	Version 3.2	Version 3.2.1
m_flow_small	Present

---

model Fluid.Sensors.SpecificEntropyTwoPort

Component	Version 3.2	Version 3.2.1
s_a_inflow	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
s_b_inflow	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
m_flow_small	Present

---

model Fluid.Sensors.TraceSubstances

Component	Version 3.2	Version 3.2.1
CVec	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Sensors.TraceSubstancesTwoPort

Component	Version 3.2	Version 3.2.1
m_flow_small	Present

---

model Fluid.Sensors.VolumeFlowRate

Component	Version 3.2	Version 3.2.1
rho_a_inflow	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
rho_b_inflow	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
m_flow_small	Present

---

model Fluid.Sensors.RelativePressure

Component	Version 3.2	Version 3.2.1
port_a	Present
port_b	Present

Equations in Version 3.2	Equations in Version 3.2.1
port_a.m_flow = 0;	p_rel = port_a.p - port_b.p;
port_b.m_flow = 0; port_a.h_outflow = 0; port_b.h_outflow = 0; port_a.Xi_outflow = zeros(Medium.nXi); port_b.Xi_outflow = zeros(Medium.nXi); port_a.C_outflow = zeros(Medium.nC); port_b.C_outflow = zeros(Medium.nC); p_rel = port_a.p - port_b.p;

---

model Fluid.Sensors.RelativeTemperature

Component	Version 3.2	Version 3.2.1
port_a	Present
port_b	Present

Equations in Version 3.2	Equations in Version 3.2.1
port_a.m_flow = 0;	T_rel = Medium.temperature(Medium.setState_phX(port_a.p, inStream(port_a.h_outflow), inStream(port_a.Xi_outflow))) - Medium.temperature(Medium.setState_phX(port_b.p, inStream(port_b.h_outflow), inStream(port_b.Xi_outflow)));
port_b.m_flow = 0; port_a.h_outflow = 0; port_b.h_outflow = 0; port_a.Xi_outflow = zeros(Medium.nXi); port_b.Xi_outflow = zeros(Medium.nXi); port_a.C_outflow = zeros(Medium.nC); port_b.C_outflow = zeros(Medium.nC); T_rel = Medium.temperature(Medium.setState_phX(port_a.p, inStream(port_a.h_outflow), inStream(port_a.Xi_outflow))) -          &nbspMedium.temperature(Medium.setState_phX(port_b.p, inStream(port_b.h_outflow), inStream(port_b.Xi_outflow)));

---

model Fluid.Sensors.BaseClasses.PartialAbsoluteSensor

Equations in Version 3.2	Equations in Version 3.2.1
port.m_flow = 0;
port.h_outflow = 0;	port.h_outflow = Medium.h_default;
port.Xi_outflow = zeros(Medium.nXi);	port.Xi_outflow = Medium.X_default[1:Medium.nXi];
port.C_outflow = zeros(Medium.nC);

---

model Fluid.Sensors.BaseClasses.PartialFlowSensor

Component	Version 3.2	Version 3.2.1
m_flow_nominal		Present
m_flow_small		Present

---

connector Fluid.Interfaces.FluidPort

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h_outflow	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
Xi_outflow	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C_outflow	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty

---

model Fluid.Interfaces.PartialTwoPortTransport

Component	Version 3.2	Version 3.2.1
dp_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
m_flow_small	=system.m_flow_small	=if system.use_eps_Re then system.eps_m_flow*system.m_flow_nominal else system.m_flow_small
port_a_T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
port_b_T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

model Fluid.Interfaces.PartialLumpedVolume

Component	Version 3.2	Version 3.2.1
p_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_start	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C_start	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty
mbC_flow	Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Media.Interfaces.Types.ExtraPropertyFlowRate

---

model Fluid.Interfaces.PartialDistributedVolume

Component	Version 3.2	Version 3.2.1
p_a_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
p_b_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
ps_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_start	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C_start	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty
Cs	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty
mbC_flows	Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Media.Interfaces.Types.ExtraPropertyFlowRate

---

model Fluid.Interfaces.PartialPressureLoss

Component	Version 3.2	Version 3.2.1
d_a	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
d_b	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
eta_a	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
eta_b	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

---

function Fluid.Dissipation.HeatTransfer.General.kc_approxForcedConvection_KC

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
kc := IN_var.lambda/d_hyd*(if IN_con.target == TYP.Rough then 0.023*Re^(4/5)* Pr^IN_con.exp_Pr else if IN_con.target == TYP.Middle then 0.023*Re^(4/5)*Pr ^(1/3)*(IN_var.eta/IN_var.eta_wall)^0.14 else if IN_con.target == 3 and Pr <= 1.5 then 0.0214*max(1, abs(Re^0.8 - 100))*Pr^0.4 else if IN_con.target == TYP.Finest then 0.012*max(1, abs(Re^0.87 - 280))*Pr^0.4 else 0);	kc := IN_var.lambda/d_hyd*(if IN_con.target == TYP.Rough then 0.023*Re^(4/5)* Pr^IN_con.exp_Pr else if IN_con.target == TYP.Middle then 0.023*Re^(4/5)*Pr ^(1/3)*(IN_var.eta/IN_var.eta_wall)^0.14 else if IN_con.target == TYP.Finest and Pr <= 1.5 then 0.0214*max(1, abs(Re^0.8 - 100))*Pr^0.4 else if IN_con.target == TYP.Finest then 0.012*max(1, abs(Re^0.87 - 280))*Pr^0.4 else 0);

---

function Fluid.Dissipation.HeatTransfer.HelicalPipe.kc_overall

Equations in Version 3.2	Equations in Version 3.2.1
... Nu = kc*IN_con.d_hyd/max(MIN, IN_var.lambda);
	failureStatus = 0;

---

function Fluid.Dissipation.HeatTransfer.StraightPipe.kc_overall

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(true, "No choice of roughness is selected");	assert(false, "No choice of roughness is selected");
end if; ...

---

function Fluid.Dissipation.HeatTransfer.StraightPipe.kc_turbulent

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(true, "No choice of roughness is selected");	assert(false, "No choice of roughness is selected");
end if; ...

---

function Fluid.Dissipation.PressureLoss.Bend.dp_edgedOverall_MFLOW

Component	Version 3.2	Version 3.2.1
v_lam	=Re_lam_leave*IN_var.eta/(IN_var.rho*d_hyd)	=(2*(d_hyd/IN_var.eta)^exp/(A*C1*zeta_LOC*B*(IN_var.rho)^(1 - exp)))^(1/pow)*Fluid.Dissipation.Utilities.Functions.General.SmoothPower(abs(dp), dp_min, 1/pow)
v_smooth	=if abs(dp) > dp_lam then (2*abs(dp))^0.5*(A*C1*zeta_LOC*IN_var.rho)^(-0.5) else (2*(d_hyd/IN_var.eta)^exp/(A*C1*zeta_LOC*B*(IN_var.rho)^(1 - exp)))^(1/pow)*Modelica_3_2.Fluid.Dissipation.Utilities.Functions.General.SmoothPower(abs(dp), dp_min, 1/pow)	=if abs(dp) > dp_lam_max then v_turb else if abs(dp) < dp_lam_trans then v_lam else SMOOTH(dp_lam_max, dp_lam_trans, abs(dp))*v_turb + SMOOTH(dp_lam_trans, dp_lam_max, abs(dp))*v_lam
dp_lam	Present
v_lam_trans		Present
v_lam_max		Present
dp_lam_trans		Present
dp_lam_max		Present
v_turb		Present

---

function Fluid.Dissipation.PressureLoss.Orifice.dp_thickEdgedOverall_DP

Component	Version 3.2	Version 3.2.1
l_bar	SIunits.Length	Real

---

function Fluid.Dissipation.PressureLoss.Orifice.dp_thickEdgedOverall_MFLOW

Component	Version 3.2	Version 3.2.1
l_bar	SIunits.Length	Real

---

function Fluid.Dissipation.PressureLoss.StraightPipe.dp_overall_MFLOW

Component	Version 3.2	Version 3.2.1
Re_turb	=if IN_con.roughness == 1 then (max(MIN, lambda_FRI_calc)/0.3164)^(1/1.75) else -2*sqrt(max(lambda_FRI_calc, MIN))*Modelica_3_2.Math.log10(2.51/sqrt(max(lambda_FRI_calc, MIN)) + k/3.7)	=if IN_con.roughness == Roughness.Neglected then (max(MIN, lambda_FRI_calc)/0.3164)^(1/1.75) else -2*sqrt(max(lambda_FRI_calc, MIN))*Modelica.Math.log10(2.51/sqrt(max(lambda_FRI_calc, MIN)) + k/3.7)

---

record Fluid.Dissipation.PressureLoss.StraightPipe.dp_twoPhaseOverall_IN_con

Component	Version 3.2	Version 3.2.1
voidFractionApproach	Fluid.Dissipation.Utilities.Types.Roughness	Fluid.Dissipation.Utilities.Types.VoidFractionApproach

---

function Fluid.Dissipation.Utilities.Functions.PressureLoss.TwoPhase.dp_twoPhaseGeodetic_DP

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
DP_geo := (eps*rho_g + (1 - eps)*rho_l)*9.81*length*sin(min(PI/2, max(0, abs( phi))));	DP_geo := (eps*rho_g + (1 - eps)*rho_l)*9.81*length*sin(phi);

---

function Fluid.Dissipation.Utilities.Functions.PressureLoss.TwoPhase.dp_twoPhaseMomentum_DP

Component	Version 3.2	Version 3.2.1
voidFractionApproach	Fluid.Dissipation.Utilities.Types.Roughness	Fluid.Dissipation.Utilities.Types.VoidFractionApproach
A_cross	Real	SIunits.Area
dp_mom_cor	=SMOOTH(delta_xflow, 0.05, 0)*abs(mdot_A*meanVelEnd + mdotCorEnd*deltaVelEnd/Across) - abs(mdot_A*meanVelEnd + mdotCorEnd*deltaVelEnd/Across)	=SMOOTH(delta_xflow, 0.05, 0)*abs(mdot_A*meanVelEnd + mdotCorEnd*deltaVelEnd/Across) - abs(mdot_A*meanVelSta + mdotCorEnd*deltaVelSta/Across)

---

function Fluid.Dissipation.Utilities.Functions.PressureLoss.TwoPhase.TwoPhaseDensity

Component	Version 3.2	Version 3.2.1
voidFractionApproach	Fluid.Dissipation.Utilities.Types.Roughness	Fluid.Dissipation.Utilities.Types.VoidFractionApproach

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
rho_2ph := if massFlowRateCorrection then rho_hom else if voidFractionApproach == Modelica_3_2.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Homogeneous then rho_hom else if voidFractionApproach == Modelica_3_2.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Momentum then rho_mom else if voidFractionApproach == Modelica_3_2.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Energy then rho_kin else MIN;	rho_2ph := if not massFlowRateCorrection then rho_hom else if voidFractionApproach == Modelica.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Homogeneous then rho_hom else if voidFractionApproach == Modelica.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Momentum then rho_mom else if voidFractionApproach == Modelica.Fluid.Dissipation.Utilities.Types.VoidFractionApproach.Energy then rho_kin else MIN;

---

function Fluid.Dissipation.Utilities.Functions.General.LambertW

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(y > -1/Modelica_3_2.Math.exp(1), "Lambert-w-function is only valid for inputs y > -1/Modelica.Math.exp(1)!");	assert(y > -1/Modelica.Math.exp(1), "Lambert-w-function is only valid for inputs y > -1/Modelica.Math.exp(1)!");

---

function Fluid.Dissipation.Utilities.Functions.General.Stepsmoother_der

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
dresult := if x >= 0.999*(func - nofunc) + nofunc and func > nofunc or x <= 0.999*(func - nofunc) + nofunc and nofunc > func or x <= 0.001*(func - nofunc) + nofunc and func > nofunc or x >= 0.001*(func - nofunc) + nofunc and nofunc > func then 0 else (1 - Modelica_3_2.Math.tanh(Modelica_3_2.Math.tan(m*x + b)) ^2)*(1 + Modelica_3_2.Math.tan(m*x + b)^2)*m*dx;	dresult := if x >= 0.999*(func - nofunc) + nofunc and func > nofunc or x <= 0.999*(func - nofunc) + nofunc and nofunc > func or x <= 0.001*(func - nofunc) + nofunc and func > nofunc or x >= 0.001*(func - nofunc) + nofunc and nofunc > func then 0 else (1 - Modelica.Math.tanh(Modelica.Math.tan(m* x + b))^2)*(1 + Modelica.Math.tan(m*x + b)^2)*m*dx/2;

---

record Fluid.Dissipation.Utilities.Records.HeatTransfer.TwoPhaseFlowHT_IN_con

Component	Version 3.2	Version 3.2.1
MM	SIunits.MolarMass	Fluid.Dissipation.Utilities.Types.MolarMass_gpmol

---

function Fluid.Utilities.regFun3

Equations in Version 3.2	Equations in Version 3.2.1
... assert(x0<x1, "regFun3(): Data points not sorted appropriately (x0 = "+String(x0)+" > x1 = "+String(x1)+"). Please flip arguments.");
	if y0d*y1d >= 0 then else assert(abs(y0d)<Modelica.Constants.eps or abs(y1d)<Modelica.Constants.eps, "regFun3(): Derivatives at data points do not allow co-monotone interpolation, as both are non-zero, of opposite sign and have an absolute value larger than machine eps (y0d = " +      &nbspString(y0d) + ", y1d = " + String(y1d) + "). Please correct arguments."); end if;
h0 = x1 - x0; ... if abs(Delta0)<=0 then
y = y0;	y = y0 + Delta0*(x-x0);
	c = 0;
elseif abs(y1d + y0d - 2*Delta0) < 100*Modelica_3_2.Constants.eps then
y = (y0d+y1d-2*Delta0)*(x-x0)^3/h0^2+(-2*y0d-y1d+3*Delta0)*(x-x0)^2/h0+y0d*(x-x0)+y0;	y = y0 + (x-x0)*(y0d + (x-x0)/h0*( (-2*y0d-y1d+3*Delta0) + (x-x0)*(y0d+y1d-2*Delta0)/h0));
aux01 = (x0+x1)/2; ... else
y = (y0d+y1d-2*Delta0)*(x-x0)^3/h0^2+(-2*y0d-y1d+3*Delta0)*(x-x0)^2/h0+y0d*(x-x0)+y0;	y = y0 + (x-x0)*(y0d + (x-x0)/h0*( (-2*y0d-y1d+3*Delta0) + (x-x0)*(y0d+y1d-2*Delta0)/h0));
aux01 = (x0+x1)/2; ...

---

model Media.Examples.SimpleLiquidWater

Component	Version 3.2	Version 3.2.1
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

---

model Media.Examples.IdealGasH2O

Component	Version 3.2	Version 3.2.1
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
k	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

model Media.Examples.WaterIF97

Component	Version 3.2	Version 3.2.1
medium	p(start=1.e5, stateSelect=StateSelect.prefer)	p(start=1.e5, fixed=true, stateSelect=StateSelect.prefer)
	h(start=1.0e5, stateSelect=StateSelect.prefer)	h(start=1.0e5, fixed=true, stateSelect=StateSelect.prefer)
V		fixed=true
H_flow_ext	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate

---

model Media.Examples.MixtureGases

Component	Version 3.2	Version 3.2.1
medium1	p(start=1.e5, stateSelect=StateSelect.prefer)	p(start=1.e5, fixed=true, stateSelect=StateSelect.prefer)
	T(start=300, stateSelect=StateSelect.prefer)	T(start=300, fixed=true, stateSelect=StateSelect.prefer)
cp1	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
eta1	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda1	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
medium2	p(start=1.e5, stateSelect=StateSelect.prefer)	p(start=1.e5, fixed=true, stateSelect=StateSelect.prefer)
	T(start=300, stateSelect=StateSelect.prefer)	T(start=300, fixed=true, stateSelect=StateSelect.prefer)
cp2	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
eta2	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda2	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity

---

model Media.Examples.MoistAir

Component	Version 3.2	Version 3.2.1
medium	T(start=274.0)	T(start=274.0, fixed=true)
	p(start=1.0e5)	p(start=1.0e5, fixed=true)
MMx	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
MM	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
unitTime		Present

Equations in Version 3.2	Equations in Version 3.2.1
... state1.T = 300 + 10*time;
state1.X = {time, 1-time};	state1.X = {time,1 - time}/unitTime;
state2.p = 1.e5*(1+time/2);
state2.T = 340 - 20*time;
state2.X = {0.5*time, 1-0.5*time};	state2.X = {0.5*time,1 - 0.5*time}/unitTime;
smoothState = Medium.setSmoothState(m_flow_ext, state1, state2, 0.2); ...

---

model Media.Examples.TwoPhaseWater.ExtendedProperties

Component	Version 3.2	Version 3.2.1
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
eta_d	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
eta_b	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda_d	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
lambda_b	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
cp_d	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cp_b	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
x	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
s_b	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
s_d	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

model Media.Examples.TwoPhaseWater.TestTwoPhaseStates

Component	Version 3.2	Version 3.2.1
medium	p(start=700.0)	p(start=2000.0, fixed=true)
	h(start=8.0e5)	h(start=8.0e5, fixed=true)

---

model Media.Examples.TestOnly.MixIdealGasAir

Component	Version 3.2	Version 3.2.1
medium	T(start=200.0)	T(start=200.0, fixed=true)
	p(start=1.0e5)	p(start=1.0e5, fixed=true)
medium2	T(start=300.0)	T(start=300.0, fixed=true)
	X(start={0.2,0.8})	X(start={0.2,0.8}, fixed=true)
	p(start=2.0e5)	p(start=2.0e5, fixed=true)
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
s2	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

model Media.Examples.TestOnly.FlueGas

Component	Version 3.2	Version 3.2.1
state	T(start=200.0)	T(start=200.0, fixed=true)
	p(start=1.0e5)	p(start=1.0e5, fixed=true)
medium2	T(start=300.0)	T(start=300.0, fixed=true)
	X(start={0.2,0.1,0.3,0.4})	X(start={0.2,0.1,0.3,0.4}, fixed=true)
	p(start=2.0e5)	p(start=2.0e5, fixed=true)
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
s2	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
MMx	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
MM	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

model Media.Examples.TestOnly.IdealGasN2

Component	Version 3.2	Version 3.2.1
H_flow_ext	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate
medium	p(start=1.e5)	p(start=1.e5, fixed=true)
	T(start=300)	T(start=300, fixed=true)
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound

---

model Media.Examples.TestOnly.IdealGasN2Mix

Component	Version 3.2	Version 3.2.1
H_flow_ext	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate
medium	p(start=1.e5)	p(start=1.e5, fixed=true)
	T(start=300)	T(start=300, fixed=true)
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound

---

connector Media.Examples.Tests.Components.FluidPort

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
H_flow	Media.Interfaces.PartialMedium.EnthalpyFlowRate	Media.Interfaces.Types.EnthalpyFlowRate
Xi	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
C	Media.Interfaces.PartialMedium.ExtraProperty	Media.Interfaces.Types.ExtraProperty
mC_flow	Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Media.Interfaces.Types.ExtraPropertyFlowRate

---

model Media.Examples.Tests.Components.PortVolume

Component	Version 3.2	Version 3.2.1
p_start	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
d_start	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T_start	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_start	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_start	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

model Media.Examples.Tests.Components.FixedMassFlowRate

Component	Version 3.2	Version 3.2.1
T_ambient	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_ambient	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_ambient	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

model Media.Examples.Tests.Components.FixedAmbient

Component	Version 3.2	Version 3.2.1
p_ambient	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
d_ambient	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T_ambient	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_ambient	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_ambient	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

model Media.Examples.Tests.Components.ShortPipe

Component	Version 3.2	Version 3.2.1
dp_nominal	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Media.Examples.SolveOneNonlinearEquation.Inverse_sh_T

Component	Version 3.2	Version 3.2.1
h_min	=Medium.h_T(Medium.data, T_min)	=Medium.specificEnthalpy(Medium.setState_pT(p, T_min))
h_max	=Medium.h_T(Medium.data, T_max)	=Medium.specificEnthalpy(Medium.setState_pT(p, T_max))
h1		start=h_min
		fixed=true
s1		start=s_min
		fixed=true

Equations in Version 3.2	Equations in Version 3.2.1
h1 = if time < 0 then h_min else if time > 1 then h_max else h_min + time/timeUnit*(h_max - h_min);	der(h1) = if time < 1.0 then 1/timeUnit*(h_max - h_min) else 0.0;
s1 = if time < 0 then s_min else if time > 1 then s_max else s_min + time/timeUnit*(s_max - s_min);	der(s1) = if time < 1.0 then 1/timeUnit*(s_max - s_min) else 0.0;
Th = Medium.temperature_phX(p, h1, fill(0.0,0)); ...

---

model Media.Examples.SolveOneNonlinearEquation.InverseIncompressible_sh_T

Component	Version 3.2	Version 3.2.1
h1		start=h_min
		fixed=true
s1		start=s_min
		fixed=true

Equations in Version 3.2	Equations in Version 3.2.1
h1 = if time < 0 then h_min else if time > 1 then h_max else h_min + time/timeUnit*(h_max - h_min);	der(h1) = if time < 1.0 then 1/timeUnit*(h_max - h_min) else 0.0;
s1 = if time < 0 then s_min else if time > 1 then s_max else s_min + time/timeUnit*(s_max - s_min);	der(s1) = if time < 1.0 then 1/timeUnit*(s_max - s_min) else 0.0;
Th = Medium.temperature_phX(p, h1, fill(0.0,0)); ...

---

model Media.Examples.SolveOneNonlinearEquation.Inverse_sh_TX

Component	Version 3.2	Version 3.2.1
h_min		parameter
h_max		parameter
s_min		parameter
s_max		parameter
h1		start=h_min
		fixed=true
s1		start=s_min
		fixed=true
X		parameter
		=Medium.reference_X

Equations in Version 3.2	Equations in Version 3.2.1
X = Medium.reference_X;	der(h1) = if time < 1.0 then 1/timeUnit*(h_max - h_min) else 0.0;
h1 = if time < 0 then h_min else if time > 1 then h_max else h_min + time/timeUnit*(h_max - h_min);	der(s1) = if time < 1.0 then 1/timeUnit*(s_max - s_min) else 0.0;
s1 = if time < 0 then s_min else        &nbspif time > 1 then s_max else           &nbsps_min + time/timeUnit*(s_max - s_min);
Th = Medium.temperature_phX(p, h1, X); ...

---

package Media.Interfaces.TemplateMedium

Component	Version 3.2	Version 3.2.1
cp_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

---

record Media.Interfaces.TemplateMedium.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

package Media.Interfaces.PartialMedium

Component	Version 3.2	Version 3.2.1
ThermoStates	Media.Interfaces.PartialMedium.Choices.IndependentVariables	Media.Interfaces.Choices.IndependentVariables
reference_p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
reference_T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
reference_X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
p_default	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T_default	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h_default	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X_default	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

record Media.Interfaces.PartialMedium.FluidConstants

Component	Version 3.2	Version 3.2.1
record		shortClass
iupacName	Present
casRegistryNumber	Present
chemicalFormula	Present
structureFormula	Present
molarMass	Present

---

model Media.Interfaces.PartialMedium.BaseProperties

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
u	Media.Interfaces.PartialMedium.SpecificInternalEnergy	Media.Interfaces.Types.SpecificInternalEnergy
R	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
MM	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

function Media.Interfaces.PartialMedium.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialMedium.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialMedium.setState_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialMedium.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialMedium.dynamicViscosity

Component	Version 3.2	Version 3.2.1
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

---

function Media.Interfaces.PartialMedium.thermalConductivity

Component	Version 3.2	Version 3.2.1
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity

---

function Media.Interfaces.PartialMedium.prandtlNumber

Component	Version 3.2	Version 3.2.1
Pr	Media.Interfaces.PartialMedium.PrandtlNumber	Media.Interfaces.Types.PrandtlNumber

---

function Media.Interfaces.PartialMedium.pressure

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialMedium.temperature

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialMedium.density

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialMedium.specificEnthalpy

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialMedium.specificInternalEnergy

Component	Version 3.2	Version 3.2.1
u	Media.Interfaces.PartialMedium.SpecificEnergy	Media.Interfaces.Types.SpecificEnergy

---

function Media.Interfaces.PartialMedium.specificEntropy

Component	Version 3.2	Version 3.2.1
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

function Media.Interfaces.PartialMedium.specificGibbsEnergy

Component	Version 3.2	Version 3.2.1
g	Media.Interfaces.PartialMedium.SpecificEnergy	Media.Interfaces.Types.SpecificEnergy

---

function Media.Interfaces.PartialMedium.specificHelmholtzEnergy

Component	Version 3.2	Version 3.2.1
f	Media.Interfaces.PartialMedium.SpecificEnergy	Media.Interfaces.Types.SpecificEnergy

---

function Media.Interfaces.PartialMedium.specificHeatCapacityCp

Component	Version 3.2	Version 3.2.1
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

---

function Media.Interfaces.PartialMedium.specificHeatCapacityCv

Component	Version 3.2	Version 3.2.1
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

---

function Media.Interfaces.PartialMedium.isentropicExponent

Component	Version 3.2	Version 3.2.1
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent

---

function Media.Interfaces.PartialMedium.isentropicEnthalpy

Component	Version 3.2	Version 3.2.1
p_downstream	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialMedium.velocityOfSound

Component	Version 3.2	Version 3.2.1
a	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound

---

function Media.Interfaces.PartialMedium.isobaricExpansionCoefficient

Component	Version 3.2	Version 3.2.1
beta	Media.Interfaces.PartialMedium.IsobaricExpansionCoefficient	Media.Interfaces.Types.IsobaricExpansionCoefficient

---

function Media.Interfaces.PartialMedium.density_derp_h

Component	Version 3.2	Version 3.2.1
ddph	Media.Interfaces.PartialMedium.DerDensityByPressure	Media.Interfaces.Types.DerDensityByPressure

---

function Media.Interfaces.PartialMedium.density_derh_p

Component	Version 3.2	Version 3.2.1
ddhp	Media.Interfaces.PartialMedium.DerDensityByEnthalpy	Media.Interfaces.Types.DerDensityByEnthalpy

---

function Media.Interfaces.PartialMedium.density_derp_T

Component	Version 3.2	Version 3.2.1
ddpT	Media.Interfaces.PartialMedium.DerDensityByPressure	Media.Interfaces.Types.DerDensityByPressure

---

function Media.Interfaces.PartialMedium.density_derT_p

Component	Version 3.2	Version 3.2.1
ddTp	Media.Interfaces.PartialMedium.DerDensityByTemperature	Media.Interfaces.Types.DerDensityByTemperature

---

function Media.Interfaces.PartialMedium.density_derX

Component	Version 3.2	Version 3.2.1
dddX	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialMedium.molarMass

Component	Version 3.2	Version 3.2.1
MM	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

function Media.Interfaces.PartialMedium.specificEnthalpy_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialMedium.specificEntropy_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

function Media.Interfaces.PartialMedium.density_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialMedium.temperature_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialMedium.density_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialMedium.temperature_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialMedium.density_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialMedium.specificEnthalpy_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

package Media.Interfaces.PartialMedium.Choices

Component	Version 3.2	Version 3.2.1
package		shortClass

---

function Media.Interfaces.PartialPureSubstance.setState_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialPureSubstance.setState_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialPureSubstance.setState_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

function Media.Interfaces.PartialPureSubstance.setState_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialPureSubstance.density_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialPureSubstance.temperature_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialPureSubstance.pressure_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialPureSubstance.specificEnthalpy_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialPureSubstance.specificEnthalpy_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialPureSubstance.temperature_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialPureSubstance.density_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialPureSubstance.specificEnthalpy_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialPureSubstance.density_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

package Media.Interfaces.PartialLinearFluid

Component	Version 3.2	Version 3.2.1
cp_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
beta_const	Media.Interfaces.PartialMedium.IsobaricExpansionCoefficient	Media.Interfaces.Types.IsobaricExpansionCoefficient
MM_const	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
reference_d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
reference_h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
reference_s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

record Media.Interfaces.PartialLinearFluid.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialLinearFluid.T_ph

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialLinearFluid.T_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

package Media.Interfaces.PartialMixtureMedium

Component	Version 3.2	Version 3.2.1
fluidConstants	Media.Interfaces.PartialMixtureMedium.FluidConstants	Media.Interfaces.PartialMedium.FluidConstants

---

record Media.Interfaces.PartialMixtureMedium.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialMixtureMedium.moleToMassFractions

Component	Version 3.2	Version 3.2.1
MMX	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
Mmix	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

function Media.Interfaces.PartialCondensingGases.saturationPressure

Component	Version 3.2	Version 3.2.1
Tsat	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
psat	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialCondensingGases.enthalpyOfVaporization

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
r0	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialCondensingGases.enthalpyOfLiquid

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialCondensingGases.enthalpyOfGas

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialCondensingGases.enthalpyOfCondensingGas

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialCondensingGases.enthalpyOfNonCondensingGas

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

package Media.Interfaces.PartialTwoPhaseMedium

Component	Version 3.2	Version 3.2.1
smoothModel		=false
onePhase		=false
fluidConstants	Media.Interfaces.PartialTwoPhaseMedium.FluidConstants	Media.Interfaces.PartialMedium.FluidConstants

---

record Media.Interfaces.PartialTwoPhaseMedium.ThermodynamicState

Component	Version 3.2	Version 3.2.1
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

model Media.Interfaces.PartialTwoPhaseMedium.BaseProperties

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.setDewState

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setBubbleState

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_dTX

Component	Version 3.2	Version 3.2.1
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_phX

Component	Version 3.2	Version 3.2.1
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_psX

Component	Version 3.2	Version 3.2.1
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_pTX

Component	Version 3.2	Version 3.2.1
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setSat_T

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.setSat_p

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.bubbleEnthalpy

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.dewEnthalpy

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.bubbleEntropy

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.dewEntropy

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Interfaces.PartialTwoPhaseMedium.bubbleDensity

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
dl	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.dewDensity

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
dv	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationPressure

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationTemperature

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationPressure_sat

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationTemperature_sat

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationTemperature_derp

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
dTp	Real	Media.Interfaces.Types.DerTemperatureByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.saturationTemperature_derp_sat

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
dTp	Real	Media.Interfaces.Types.DerTemperatureByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.surfaceTension

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
sigma	Media.Interfaces.PartialMedium.SurfaceTension	Media.Interfaces.Types.SurfaceTension

---

function Media.Interfaces.PartialTwoPhaseMedium.molarMass

Component	Version 3.2	Version 3.2.1
function	partial

---

function Media.Interfaces.PartialTwoPhaseMedium.dBubbleDensity_dPressure

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
ddldp	Media.Interfaces.PartialMedium.DerDensityByPressure	Media.Interfaces.Types.DerDensityByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.dDewDensity_dPressure

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
ddvdp	Media.Interfaces.PartialMedium.DerDensityByPressure	Media.Interfaces.Types.DerDensityByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.dBubbleEnthalpy_dPressure

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
dhldp	Media.Interfaces.PartialMedium.DerEnthalpyByPressure	Media.Interfaces.Types.DerEnthalpyByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.dDewEnthalpy_dPressure

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties
dhvdp	Media.Interfaces.PartialMedium.DerEnthalpyByPressure	Media.Interfaces.Types.DerEnthalpyByPressure

---

function Media.Interfaces.PartialTwoPhaseMedium.specificEnthalpy_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.temperature_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.density_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.temperature_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.density_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.specificEnthalpy_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_px

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
x	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialTwoPhaseMedium.setState_Tx

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
x	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialTwoPhaseMedium.vapourQuality

Component	Version 3.2	Version 3.2.1
x	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
eps	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.density_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.temperature_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.pressure_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Interfaces.PartialTwoPhaseMedium.specificEnthalpy_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.specificEnthalpy_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.temperature_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialTwoPhaseMedium.density_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Interfaces.PartialTwoPhaseMedium.specificEnthalpy_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialTwoPhaseMedium.density_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

package Media.Interfaces.PartialSimpleMedium

Component	Version 3.2	Version 3.2.1
cp_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
d_const	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
eta_const	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda_const	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
a_const	Media.Interfaces.PartialMedium.VelocityOfSound	Media.Interfaces.Types.VelocityOfSound
T_min	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T_max	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T0	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
MM_const	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

record Media.Interfaces.PartialSimpleMedium.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialSimpleMedium.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleMedium.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleMedium.setState_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state := ThermodynamicState(p=p, T=Modelica_3_2.Math.exp(s/cp_const + Modelica_3_2.Math.log(reference_T))) "here the incompressible limit is used, with cp as heat capacity";	state := ThermodynamicState(p=p, T=Modelica.Math.exp(s/cp_const + Modelica.Math.log(reference_T))) "Here the incompressible limit is used, with cp as heat capacity";

---

function Media.Interfaces.PartialSimpleMedium.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(false,"pressure can not be computed from temperature and density for an incompressible fluid!");	assert(false, "Pressure can not be computed from temperature and density for an incompressible fluid!");

---

function Media.Interfaces.PartialSimpleMedium.specificEnthalpy_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialSimpleMedium.temperature_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialSimpleMedium.density_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

package Media.Interfaces.PartialSimpleIdealGasMedium

Component	Version 3.2	Version 3.2.1
cp_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
cv_const	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
R_gas	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
MM_const	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
eta_const	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda_const	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
T_min	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T_max	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T0	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
fluidConstants		Present

---

record Media.Interfaces.PartialSimpleIdealGasMedium.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialSimpleIdealGasMedium.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleIdealGasMedium.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleIdealGasMedium.setState_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleIdealGasMedium.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Interfaces.PartialSimpleIdealGasMedium.specificInternalEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
u := cp_const*(state.T-T0) - R_gas*state.T;	u := (cp_const - R_gas)*(state.T - T0);

---

function Media.Interfaces.PartialSimpleIdealGasMedium.specificEnthalpy_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Interfaces.PartialSimpleIdealGasMedium.temperature_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Interfaces.PartialSimpleIdealGasMedium.density_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

package Media.Common

Component	Version 3.2	Version 3.2.1
MINPOS	protected
AMIN	protected
AMAX	protected
ANOM	protected
MOLMIN	protected
MOLMAX	protected
MOLNOM	protected
DMIN	protected
	=MINPOS	=1e-6
DMAX	protected
	=1.0e5	=30.0e3
DNOM	protected
LAMMIN	protected
LAMNOM	protected
LAMMAX	protected
ETAMIN	protected
ETAMAX	protected
ETANOM	protected
EMIN	protected
EMAX	protected
ENOM	protected
SMIN	protected
SMAX	protected
SNOM	protected
MDOTMIN	protected
MDOTMAX	protected
MDOTNOM	protected
MASSXMIN	protected
MASSXMAX	protected
MASSXNOM	protected
MMIN	protected
MMAX	protected
MNOM	protected
MMMIN	protected
MMMAX	protected
MMNOM	protected
MOLEYMIN	protected
MOLEYMAX	protected
MOLEYNOM	protected
GMIN	protected
GMAX	protected
GNOM	protected
POWMIN	protected
POWMAX	protected
POWNOM	protected
PMIN	protected
PMAX	protected
PNOM	protected
COMPPMIN	protected
COMPPMAX	protected
COMPPNOM	protected
KAPPAMIN	protected
KAPPAMAX	protected
KAPPANOM	protected
SEMIN	protected
SEMAX	protected
SENOM	protected
SHMIN	protected
SHMAX	protected
SHNOM	protected
SSMIN	protected
SSMAX	protected
SSNOM	protected
CPMIN	protected
CPMAX	protected
CPNOM	protected
TMIN	protected
	=MINPOS	=1.0
TMAX	protected
	=1.0e5	=6000.0
TNOM	protected
LMIN	protected
LMAX	protected
LNOM	protected
VELMIN	protected
VELMAX	protected
VELNOM	protected
VMIN	protected
VMAX	protected
VNOM	protected

---

type Media.Common.Rate

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.MolarFlowRate

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.MolarReactionRate

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.MolarEnthalpy

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerDensityByEntropy

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerEnergyByPressure

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerEnergyByMoles

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerEntropyByTemperature

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerEntropyByPressure

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerEntropyByMoles

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerPressureByDensity

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerPressureBySpecificVolume

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerPressureByTemperature

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerVolumeByTemperature

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerVolumeByPressure

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.DerVolumeByMoles

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.IsenthalpicExponent

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.IsentropicExponent

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.IsobaricVolumeExpansionCoefficient

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.IsochoricPressureCoefficient

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.IsothermalCompressibility

Component	Version 3.2	Version 3.2.1
type	protected

---

type Media.Common.JouleThomsonCoefficient

Component	Version 3.2	Version 3.2.1
type	protected

---

package Media.Common.ThermoFluidSpecial

Component	Version 3.2	Version 3.2.1
package	protected

---

package Media.Air.SimpleAir

Component	Version 3.2	Version 3.2.1
fluidConstants	Present
airConstants		Present

---

function Media.Air.DryAirNasa.dynamicViscosity

Component	Version 3.2	Version 3.2.1
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
eta := Incompressible.TableBased.Polynomials_Temp.evaluate({(-4.96717436974791E-011), 5.06626785714286E-008, 1.72937731092437E-005}, Cv.to_degC(state.T));	eta := 1e-6*Polynomials_Temp.evaluateWithRange( {9.7391102886305869E-15,-3.1353724870333906E-11,4.3004876595642225E-08, -3.8228016291758240E-05,5.0427874367180762E-02,1.7239260139242528E+01}, Cv.to_degC(123.15), Cv.to_degC(1273.15), Cv.to_degC(state.T));

---

function Media.Air.DryAirNasa.thermalConductivity

Component	Version 3.2	Version 3.2.1
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
lambda := Incompressible.TableBased.Polynomials_Temp.evaluate({(-4.8737307422969E-008), 7.67803133753502E-005, 0.0241814385504202},Cv.to_degC(state.T));	lambda := 1e-3*Polynomials_Temp.evaluateWithRange( {6.5691470817717812E-15,-3.4025961923050509E-11,5.3279284846303157E-08, -4.5340839289219472E-05,7.6129675309037664E-02,2.4169481088097051E+01}, Cv.to_degC(123.15), Cv.to_degC(1273.15), Cv.to_degC(state.T));

---

model Media.Air.MoistAir.BaseProperties

Component	Version 3.2	Version 3.2.1
x_water	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
X_liquid	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
X_steam	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
X_air	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
X_sat	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
x_sat	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
p_steam_sat	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

Equations in Version 3.2	Equations in Version 3.2.1
assert(T >= 200.0 and T <= 423.15, " Temperature T is not in the allowed range 200.0 K <= (T =" + String(T) + " K) <= 423.15 K required from medium model \"" + mediumName + "\".");	assert(T >= 190 and T <= 647, " Temperature T is not in the allowed range 190.0 K <= (T =" + String(T) + " K) <= 647.0 K required from medium model \"" + mediumName + "\".");
MM = 1/(Xi[Water]/MMX[Water]+(1.0-Xi[Water])/MMX[Air]); ...

---

function Media.Air.MoistAir.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.Xsaturation

Component	Version 3.2	Version 3.2.1
X_sat	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.xsaturation

Component	Version 3.2	Version 3.2.1
x_sat	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.xsaturation_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
x_sat	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.Air.MoistAir.massFraction_pTphi

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X_steam	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
psat	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Air.MoistAir.saturationPressureLiquid

Component	Version 3.2	Version 3.2.1
Tcritical		Present
pcritical		Present
r1		Present
a		Present
n		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
psat := 611.657*Math.exp(17.2799 - 4102.99/(Tsat - 35.719));	psat := exp(((a[1]*r1^n[1] + a[2]*r1^n[2] + a[3]*r1^n[3] + a[4]*r1^n[4] + a[5]*r1^n[5] + a[6]*r1^n[6])*Tcritical)/Tsat)*pcritical;

---

function Media.Air.MoistAir.saturationPressureLiquid_der

Component	Version 3.2	Version 3.2.1
Tcritical		Present
pcritical		Present
r1		Present
r1_der		Present
a		Present
n		Present
r2		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
psat_der:=611.657*Math.exp(17.2799 - 4102.99/(Tsat - 35.719))*4102.99*dTsat/(Tsat - 35.719)/(Tsat - 35.719);	psat_der := exp((r2*Tcritical)/Tsat)*pcritical*((a[1]*(r1^(n[1] - 1)*n[1] *r1_der) + a[2]*(r1^(n[2] - 1)*n[2]*r1_der) + a[3]*(r1^(n[3] - 1)*n[3]* r1_der) + a[4]*(r1^(n[4] - 1)*n[4]*r1_der) + a[5]*(r1^(n[5] - 1)*n[5]* r1_der) + a[6]*(r1^(n[6] - 1)*n[6]*r1_der))*Tcritical/Tsat - r2* Tcritical*dTsat/Tsat^2);

---

function Media.Air.MoistAir.sublimationPressureIce

Component	Version 3.2	Version 3.2.1
Ttriple		Present
ptriple		Present
r1		Present
a		Present
n		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
psat := 611.657*Math.exp(22.5159*(1.0 - 273.16/Tsat));	psat := exp(a[1] - a[1]*r1^n[1] + a[2] - a[2]*r1^n[2])*ptriple;

---

function Media.Air.MoistAir.sublimationPressureIce_der

Component	Version 3.2	Version 3.2.1
Ttriple		Present
ptriple		Present
r1		Present
r1_der		Present
a		Present
n		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
psat_der:=611.657*Math.exp(22.5159*(1.0 - 273.16/Tsat))*22.5159*273.16*dTsat/Tsat/Tsat;	psat_der := exp(a[1] - a[1]*r1^n[1] + a[2] - a[2]*r1^n[2])*ptriple*(-(a[1] *(r1^(n[1] - 1)*n[1]*r1_der)) - (a[2]*(r1^(n[2] - 1)*n[2]*r1_der)));

---

function Media.Air.MoistAir.saturationPressure_der

Component	Version 3.2	Version 3.2.1
Tsat	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Air.MoistAir.saturationTemperature

Component	Version 3.2	Version 3.2.1
T_min	=200	=190
T_max	=400	=647

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
T:=Internal.solve(p, T_min, T_max);	T := Internal.solve( p, T_min, T_max, f_nonlinear_data=Internal.f_nonlinear_Data());

---

function Media.Air.MoistAir.enthalpyOfVaporization

Component	Version 3.2	Version 3.2.1
Tcritical		Present
dcritical		Present
pcritical		Present
n		Present
a		Present
m		Present
b		Present
o		Present
c		Present
tau		Present
r1		Present
r2		Present
dp		Present
dpp		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
r0:=(2405900-2500500)/(40-0)*(T-273.16)+2500500;	r0 := -(((dp - dpp)*exp(r1)*pcritical*(r2 + r1*tau))/(dp*dpp*tau)) "Difference of equations (7) and (6)";

---

function Media.Air.MoistAir.HeatCapacityOfWater

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
cp_fl	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

---

function Media.Air.MoistAir.enthalpyOfGas

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h := SingleGasNasa.h_Tlow(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5)*X[Water] + SingleGasNasa.h_Tlow(data=dryair, T=T, refChoice=3, h_off=25104.684)*(1.0-X[Water]);	h := Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5)*X[Water] + Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684)*(1.0 - X[Water]);

---

function Media.Air.MoistAir.enthalpyOfCondensingGas

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h := SingleGasNasa.h_Tlow(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5);	h := Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5);

---

function Media.Air.MoistAir.enthalpyOfNonCondensingGas

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h := SingleGasNasa.h_Tlow(data=dryair, T=T, refChoice=3, h_off=25104.684);	h := Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684);

---

function Media.Air.MoistAir.T_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
T := Internal.solve(h, 240, 400, p, X[1:nXi], steam);	T := Internal.solve( h, 190, 647, p, X[1:nXi], steam);

---

function Media.Air.MoistAir.h_pTX

Equations in Version 3.2	Equations in Version 3.2.1
... X_air = 1 - X[Water];
h = {SingleGasNasa.h_Tlow(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5), SingleGasNasa.h_Tlow(data=dryair, T=T, refChoice=3, h_off=25104.684)}* {X_steam, X_air} + enthalpyOfWater(T)*X_liquid;	h = {Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5), Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684)}*{X_steam,X_air} + enthalpyOfWater(T)*X_liquid;

---

function Media.Air.MoistAir.h_pTX_der

Equations in Version 3.2	Equations in Version 3.2.1
... X_sat= min(x_sat*(1 - X[Water]), 1.0);
X_liquid = Utilities.spliceFunction(X[Water] - X_sat, 0.0, X[Water] - X_sat,1e-6);	X_liquid = Utilities.smoothMax( X[Water] - X_sat, 0.0, 1e-5);
X_steam = X[Water] - X_liquid; ... dx_sat= k_mair*(dps*(p-p_steam_sat)-p_steam_sat*(dp-dps))/(p-p_steam_sat)/(p-p_steam_sat);
dX_liq= Utilities.spliceFunction_der(X[Water] - X_sat, 0.0, X[Water] - X_sat,1e-6,(1+x_sat)*dX[Water]-(1-X[Water])*dx_sat,0.0,(1+x_sat)*dX[Water]-(1-X[Water])*dx_sat,0.0);	dX_liq = Utilities.smoothMax_der( X[Water] - X_sat, 0.0, 1e-5, (1 + x_sat)*dX[Water] - (1 - X[Water])*dx_sat, 0, 0);
dX_steam= dX[Water]-dX_liq;
h_der = X_steam* Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow_der( data=steam, T=T, refChoice=3, h_off=46479.819 + 2501014.5, dT=dT) + dX_steam* Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow( data=steam, T=T, refChoice=3, h_off=46479.819 + 2501014.5) + X_air* Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow_der( data=dryair, T=T, refChoice=3, h_off=25104.684, dT=dT) + dX_air* Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow( data=dryair, T=T, refChoice=3, h_off=25104.684) + X_liquid*enthalpyOfWater_der(T=T, dT=dT) + dX_liq*enthalpyOfWater(T);	h_der = X_steam*Modelica.Media.IdealGases.Common.Functions.h_Tlow_der( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5, dT=dT) + dX_steam*Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5) + X_air* Modelica.Media.IdealGases.Common.Functions.h_Tlow_der( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684, dT=dT) + dX_air*Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684) + X_liquid*enthalpyOfWater_der(T=T, dT=dT) + dX_liq*enthalpyOfWater(T);

---

function Media.Air.MoistAir.isentropicEnthalpyApproximation

Component	Version 3.2	Version 3.2.1
p2	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
X := if reducedX then cat(1,state.X,{1-sum(state.X)}) else state.X;	X := state.X;
h = {SingleGasNasa.h_Tlow(data=steam, T=state.T, refChoice=3, h_off=46479.819+2501014.5), SingleGasNasa.h_Tlow(data=dryair, T=state.T, refChoice=3, h_off=25104.684)}*X;	h = {Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=state.T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5), Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=state.T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684)}*X;
h_is = h + gamma/(gamma - 1.0)*(state.T*gasConstant(state))*     ((p2/state.p)^((gamma - 1)/gamma) - 1.0); ...

---

function Media.Air.MoistAir.specificInternalEnergy_pTX

Equations in Version 3.2	Equations in Version 3.2.1
... R_gas= dryair.R*X_air/(1-X_liquid)+steam.R* X_steam/(1-X_liquid);
u = X_steam*SingleGasNasa.h_Tlow(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5)+ X_air*SingleGasNasa.h_Tlow(data=dryair, T=T, refChoice=3, h_off=25104.684) + enthalpyOfWater(T)*X_liquid-R_gas*T;	u = X_steam*Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5) + X_air* Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684) + enthalpyOfWater(T)*X_liquid - R_gas*T;

---

function Media.Air.MoistAir.specificInternalEnergy_pTX_der

Equations in Version 3.2	Equations in Version 3.2.1
... dR_gas= (steam.R*(dX_steam*(1-X_liquid)+dX_liq*X_steam)+dryair.R*(dX_air*(1-X_liquid)+dX_liq*X_air))/(1-X_liquid)/(1-X_liquid);
u_der= X_steam*SingleGasNasa.h_Tlow_der(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5, dT=dT)+ dX_steam*SingleGasNasa.h_Tlow(data=steam, T=T, refChoice=3, h_off=46479.819+2501014.5) + X_air*SingleGasNasa.h_Tlow_der(data=dryair, T=T, refChoice=3, h_off=25104.684, dT=dT) + dX_air*SingleGasNasa.h_Tlow(data=dryair, T=T, refChoice=3, h_off=25104.684) + X_liquid*enthalpyOfWater_der(T=T, dT=dT) + dX_liq*enthalpyOfWater(T) - dR_gas*T-R_gas*dT;	u_der = X_steam*Modelica.Media.IdealGases.Common.Functions.h_Tlow_der( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5, dT=dT) + dX_steam*Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=steam, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=46479.819 + 2501014.5) + X_air* Modelica.Media.IdealGases.Common.Functions.h_Tlow_der( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684, dT=dT) + dX_air*Modelica.Media.IdealGases.Common.Functions.h_Tlow( data=dryair, T=T, refChoice=ReferenceEnthalpy.UserDefined, h_off=25104.684) + X_liquid*enthalpyOfWater_der(T=T, dT=dT) + dX_liq*enthalpyOfWater(T) - dR_gas*T - R_gas*dT;

---

function Media.Air.MoistAir.specificEntropy

Component	Version 3.2	Version 3.2.1
Y	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
s := SingleGasNasa.s0_Tlow(dryair, state.T)*(1 - state.X[Water]) + SingleGasNasa.s0_Tlow(steam, state.T)*state.X[Water] - (state.X[ Water]*Modelica_3_2.Constants.R/MMX[Water]*(if state.X[Water] < Modelica_3_2.Constants.eps then state.X[Water] else Modelica_3_2.Math.log(Y[Water]*state.p/reference_p)) + (1 - state.X[ Water])*Modelica_3_2.Constants.R/MMX[Air]*(if (1 - state.X[Water]) < Modelica_3_2.Constants.eps then (1 - state.X[Water]) else Modelica_3_2.Math.log(Y[Air]*state.p/reference_p)));	s := s_pTX( state.p, state.T, state.X);

---

function Media.Air.MoistAir.specificHeatCapacityCv

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cv:= SingleGasNasa.cp_Tlow(dryair, state.T)*(1-state.X[Water]) + SingleGasNasa.cp_Tlow(steam, state.T)*state.X[Water] - gasConstant(state);	cv := Modelica.Media.IdealGases.Common.Functions.cp_Tlow(dryair, state.T) *(1 - state.X[Water]) + Modelica.Media.IdealGases.Common.Functions.cp_Tlow(steam, state.T)* state.X[Water] - gasConstant(state);

---

function Media.Air.MoistAir.dynamicViscosity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
eta := Polynomials_Temp.evaluate({(-4.96717436974791E-011), 5.06626785714286E-008, 1.72937731092437E-005}, Cv.to_degC(state.T));	eta := 1e-6*Polynomials_Temp.evaluateWithRange( {9.7391102886305869E-15,-3.1353724870333906E-11,4.3004876595642225E-08, -3.8228016291758240E-05,5.0427874367180762E-02,1.7239260139242528E+01}, Cv.to_degC(123.15), Cv.to_degC(1273.15), Cv.to_degC(state.T));

---

function Media.Air.MoistAir.thermalConductivity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
lambda := Polynomials_Temp.evaluate({(-4.8737307422969E-008), 7.67803133753502E-005, 0.0241814385504202}, Cv.to_degC(state.T));	lambda := 1e-3*Polynomials_Temp.evaluateWithRange( {6.5691470817717812E-15,-3.4025961923050509E-11,5.3279284846303157E-08, -4.5340839289219472E-05,7.6129675309037664E-02,2.4169481088097051E+01}, Cv.to_degC(123.15), Cv.to_degC(1273.15), Cv.to_degC(state.T));

---

package Media.IdealGases.Common.SingleGasNasa

Component	Version 3.2	Version 3.2.1
fluidConstants	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.PartialMedium.FluidConstants
excludeEnthalpyOfFormation	Present
referenceChoice	Present
h_offset	Present

---

record Media.IdealGases.Common.SingleGasNasa.ThermodynamicState

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

model Media.IdealGases.Common.SingleGasNasa.BaseProperties

Equations in Version 3.2	Equations in Version 3.2.1
... R = data.R;
h = h_T(data, T, excludeEnthalpyOfFormation, referenceChoice, h_offset);	h = Modelica.Media.IdealGases.Common.Functions.h_T( data, T, Modelica.Media.IdealGases.Common.Functions.excludeEnthalpyOfFormation, Modelica.Media.IdealGases.Common.Functions.referenceChoice, Modelica.Media.IdealGases.Common.Functions.h_offset);
u = h - R*T; ...

---

function Media.IdealGases.Common.SingleGasNasa.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.IdealGases.Common.SingleGasNasa.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.IdealGases.Common.SingleGasNasa.setState_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.IdealGases.Common.SingleGasNasa.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.IdealGases.Common.SingleGasNasa.specificEnthalpy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h := h_T(data,state.T);	h := Modelica.Media.IdealGases.Common.Functions.h_T( data,state.T);

---

function Media.IdealGases.Common.SingleGasNasa.specificInternalEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
u := h_T(data,state.T) - data.R*state.T;	u := Modelica.Media.IdealGases.Common.Functions.h_T( data,state.T) - data.R*state.T;

---

function Media.IdealGases.Common.SingleGasNasa.specificEntropy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
s := s0_T(data, state.T) - data.R*Modelica_3_2.Math.log(state.p/ reference_p);	s := Modelica.Media.IdealGases.Common.Functions.s0_T( data, state.T) - data.R*Modelica.Math.log(state.p/reference_p);

---

function Media.IdealGases.Common.SingleGasNasa.specificGibbsEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
g := h_T(data,state.T) - state.T*specificEntropy(state);	g := Modelica.Media.IdealGases.Common.Functions.h_T( data,state.T) - state.T*specificEntropy(state);

---

function Media.IdealGases.Common.SingleGasNasa.specificHelmholtzEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
f := h_T(data,state.T) - data.R*state.T - state.T*specificEntropy(state);	f := Modelica.Media.IdealGases.Common.Functions.h_T( data,state.T) - data.R*state.T - state.T*specificEntropy(state);

---

function Media.IdealGases.Common.SingleGasNasa.specificHeatCapacityCp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cp := cp_T(data, state.T);	cp := Modelica.Media.IdealGases.Common.Functions.cp_T( data, state.T);

---

function Media.IdealGases.Common.SingleGasNasa.specificHeatCapacityCv

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cv := cp_T(data, state.T) - data.R;	cv := Modelica.Media.IdealGases.Common.Functions.cp_T( data, state.T) - data.R;

---

function Media.IdealGases.Common.SingleGasNasa.velocityOfSound

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
a := sqrt(max(0,data.R*state.T*cp_T(data, state.T)/specificHeatCapacityCv(state)));	a := sqrt(max(0,data.R*state.T*Modelica.Media.IdealGases.Common.Functions.cp_T( data, state.T)/specificHeatCapacityCv(state)));

---

function Media.IdealGases.Common.SingleGasNasa.isentropicEnthalpyApproximation

Component	Version 3.2	Version 3.2.1
exclEnthForm	=excludeEnthalpyOfFormation	=Functions.excludeEnthalpyOfFormation
refChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy
h_off	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h_is := h_T(data,state.T,exclEnthForm,refChoice,h_off) + gamma/(gamma - 1.0)*state.p/density(state)*((p2/state.p)^((gamma - 1)/gamma) - 1.0);	h_is := Modelica.Media.IdealGases.Common.Functions.h_T( data,state.T,exclEnthForm,refChoice,h_off) + gamma/(gamma - 1.0)*state.p/density(state)*((p2/state.p)^((gamma - 1)/gamma) - 1.0);

---

function Media.IdealGases.Common.SingleGasNasa.isentropicEnthalpy

Component	Version 3.2	Version 3.2.1
exclEnthForm	=excludeEnthalpyOfFormation	=Functions.excludeEnthalpyOfFormation
refChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy
h_off	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.IdealGases.Common.SingleGasNasa.dynamicViscosityLowPressure

Component	Version 3.2	Version 3.2.1
mu	Media.Interfaces.PartialMedium.DipoleMoment	Media.Interfaces.Types.DipoleMoment

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
Tstar := 1.2593*T/Tc;	eta := Functions.dynamicViscosityLowPressure(T,Tc,M,Vc,w,mu,k);
Ov = 1.16145*Tstar^(-0.14874) + 0.52487*exp(-0.7732*Tstar) + 2.16178*exp(-2.43787 *Tstar);
eta = Const1_SI*Fc*sqrt(M*T)/(Vc^(2/3)*Ov);

---

function Media.IdealGases.Common.SingleGasNasa.dynamicViscosity

Equations in Version 3.2	Equations in Version 3.2.1
... assert(fluidConstants[1].hasDipoleMoment,   "Failed to compute dynamicViscosity: For the species \"" + mediumName + "\" no critical data is available.");
eta = dynamicViscosityLowPressure(state.T, fluidConstants[1].criticalTemperature, fluidConstants[1].molarMass, fluidConstants[1].criticalMolarVolume, fluidConstants[1].acentricFactor, fluidConstants[1].dipoleMoment);	eta = Modelica.Media.IdealGases.Common.Functions.dynamicViscosityLowPressure( state.T, fluidConstants[1].criticalTemperature, fluidConstants[1].molarMass, fluidConstants[1].criticalMolarVolume, fluidConstants[1].acentricFactor, fluidConstants[1].dipoleMoment);

---

function Media.IdealGases.Common.SingleGasNasa.thermalConductivityEstimate

Component	Version 3.2	Version 3.2.1
Cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
data		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
lambda := if method == 1 then eta*(Cp - data.R + (9/4)*data.R) else eta*(Cp - data.R)*(1.32 + 1.77/((Cp/Modelica_3_2.Constants.R) - 1.0));	lambda := Functions.thermalConductivityEstimate(Cp,eta,method,data);

---

function Media.IdealGases.Common.SingleGasNasa.thermalConductivity

Component	Version 3.2	Version 3.2.1
method	=1	=Functions.methodForThermalConductivity

Equations in Version 3.2	Equations in Version 3.2.1
... assert(fluidConstants[1].hasCriticalData,   "Failed to compute thermalConductivity: For the species \"" + mediumName + "\" no critical data is available.");
lambda = thermalConductivityEstimate(specificHeatCapacityCp(state), dynamicViscosity(state), method=method);	lambda = Modelica.Media.IdealGases.Common.Functions.thermalConductivityEstimate( specificHeatCapacityCp(state), dynamicViscosity(state), method=method,data=data);

---

function Media.IdealGases.Common.SingleGasNasa.T_h

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.IdealGases.Common.SingleGasNasa.T_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

package Media.IdealGases.Common.MixtureGasNasa

Component	Version 3.2	Version 3.2.1
referenceChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy
h_offset	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
MMX	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
methodForThermalConductivity		Present

---

function Media.IdealGases.Common.MixtureGasNasa.setState_pTX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state := if size(X,1) == nX then ThermodynamicState(p=p,T=T, X=X) else ThermodynamicState(p=p,T=T, X=cat(1,X,{1-sum(X)}));	state := if size(X,1) == 0 then ThermodynamicState(p=p,T=T,X=reference_X) else if size(X,1) == nX then ThermodynamicState(p=p,T=T, X=X) else ThermodynamicState(p=p,T=T, X=cat(1,X,{1-sum(X)}));

---

function Media.IdealGases.Common.MixtureGasNasa.setState_phX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state := if size(X,1) == nX then ThermodynamicState(p=p,T=T_hX(h,X),X=X) else ThermodynamicState(p=p,T=T_hX(h,X), X=cat(1,X,{1-sum(X)}));	state := if size(X,1) == 0 then ThermodynamicState(p=p,T=T_hX(h,reference_X),X=reference_X) else if size(X,1) == nX then ThermodynamicState(p=p,T=T_hX(h,X),X=X) else ThermodynamicState(p=p,T=T_hX(h,X), X=cat(1,X,{1-sum(X)}));

---

function Media.IdealGases.Common.MixtureGasNasa.setState_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state := if size(X,1) == nX then ThermodynamicState(p=p,T=T_psX(p,s,X),X=X) else ThermodynamicState(p=p,T=T_psX(p,s,X), X=cat(1,X,{1-sum(X)}));	state := if size(X,1) == 0 then ThermodynamicState(p=p,T=T_psX(p,s,reference_X),X=reference_X) else if size(X,1) == nX then ThermodynamicState(p=p,T=T_psX(p,s,X),X=X) else ThermodynamicState(p=p,T=T_psX(p,s,X), X=cat(1,X,{1-sum(X)}));

---

function Media.IdealGases.Common.MixtureGasNasa.setState_dTX

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state := if size(X,1) == nX then ThermodynamicState(p=d*(data.R*X)*T,T=T,X=X) else ThermodynamicState(p=d*(data.R*cat(1,X,{1-sum(X)}))*T,T=T, X=cat(1,X,{1-sum(X)}));	state := if size(X,1) == 0 then ThermodynamicState(p=d*(data.R*reference_X)*T,T=T,X=reference_X) else if size(X,1) == nX then ThermodynamicState(p=d*(data.R*X)*T,T=T,X=X) else ThermodynamicState(p=d*(data.R*cat(1,X,{1-sum(X)}))*T,T=T, X=cat(1,X,{1-sum(X)}));

---

function Media.IdealGases.Common.MixtureGasNasa.h_TX

Component	Version 3.2	Version 3.2.1
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
refChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h :=(if fixedX then reference_X else X)* {SingleGasNasa.h_T(data[i], T, exclEnthForm, refChoice, h_off) for i in 1:nX};	h :=(if fixedX then reference_X else X)* {Modelica.Media.IdealGases.Common.Functions.h_T( data[i], T, exclEnthForm, refChoice, h_off) for i in 1:nX};

---

function Media.IdealGases.Common.MixtureGasNasa.h_TX_der

Component	Version 3.2	Version 3.2.1
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
refChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
h_der := if fixedX then dT*sum((SingleGasNasa.cp_T(data[i], T)*reference_X[i]) for i in 1:nX) else dT*sum((SingleGasNasa.cp_T(data[i], T)*X[i]) for i in 1:nX)+ sum((SingleGasNasa.h_T(data[i], T)*dX[i]) for i in 1:nX);	h_der := if fixedX then dT*sum((Modelica.Media.IdealGases.Common.Functions.cp_T( data[i], T)*reference_X[i]) for i in 1:nX) else dT*sum((Modelica.Media.IdealGases.Common.Functions.cp_T( data[i], T)*X[i]) for i in 1:nX)+ sum((Modelica.Media.IdealGases.Common.Functions.h_T( data[i], T)*dX[i]) for i in 1:nX);

---

function Media.IdealGases.Common.MixtureGasNasa.specificHeatCapacityCp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cp := {SingleGasNasa.cp_T(data[i], state.T) for i in 1:nX}*state.X;	cp := {Modelica.Media.IdealGases.Common.Functions.cp_T( data[i], state.T) for i in 1:nX}*state.X;

---

function Media.IdealGases.Common.MixtureGasNasa.specificHeatCapacityCv

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cv := {SingleGasNasa.cp_T(data[i], state.T) for i in 1:nX}*state.X -data.R*state.X;	cv := {Modelica.Media.IdealGases.Common.Functions.cp_T( data[i], state.T) for i in 1:nX}*state.X -data.R*state.X;

---

function Media.IdealGases.Common.MixtureGasNasa.s_TX

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
s := sum(SingleGasNasa.s0_T(data[i], T)*X[i] for i in 1:size(X,1));	s := sum(Modelica.Media.IdealGases.Common.Functions.s0_T( data[i], T)*X[i] for i in 1:size(X,1));

---

function Media.IdealGases.Common.MixtureGasNasa.isentropicEnthalpyApproximation

Component	Version 3.2	Version 3.2.1
p2	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h_is	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
h_component	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
gamma	Media.Interfaces.PartialMedium.IsentropicExponent	Media.Interfaces.Types.IsentropicExponent
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

Equations in Version 3.2	Equations in Version 3.2.1
... X := if reducedX then cat(1,state.X,{1-sum(state.X)}) else state.X;
h_component = {SingleGasNasa.h_T(data[i], state.T, excludeEnthalpyOfFormation, referenceChoice, h_offset) for i in 1:nX};	h_component = {Modelica.Media.IdealGases.Common.Functions.h_T( data[i], state.T, excludeEnthalpyOfFormation, referenceChoice, h_offset) for i in 1:nX};
h = h_component*X; ...

---

function Media.IdealGases.Common.MixtureGasNasa.gasMixtureViscosity

Component	Version 3.2	Version 3.2.1
yi	Media.Interfaces.PartialMedium.MoleFraction	Media.Interfaces.Types.MoleFraction
M	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
etam	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

---

function Media.IdealGases.Common.MixtureGasNasa.dynamicViscosity

Component	Version 3.2	Version 3.2.1
etaX	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

Equations in Version 3.2	Equations in Version 3.2.1
... for i in 1:nX loop
etaX[i] = SingleGasNasa.dynamicViscosityLowPressure(state.T, fluidConstants[i].criticalTemperature, fluidConstants[i].molarMass, fluidConstants[i].criticalMolarVolume, fluidConstants[i].acentricFactor, fluidConstants[i].dipoleMoment);	etaX[i] = Modelica.Media.IdealGases.Common.Functions.dynamicViscosityLowPressure( state.T, fluidConstants[i].criticalTemperature, fluidConstants[i].molarMass, fluidConstants[i].criticalMolarVolume, fluidConstants[i].acentricFactor, fluidConstants[i].dipoleMoment);
end for; ...

---

function Media.IdealGases.Common.MixtureGasNasa.mixtureViscosityChung

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Tc	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Vcrit	Media.Interfaces.PartialMedium.MolarVolume	Media.Interfaces.Types.MolarVolume
MolecularWeights	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
y	Media.Interfaces.PartialMedium.MoleFraction	Media.Interfaces.Types.MoleFraction
etaMixture	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity

---

function Media.IdealGases.Common.MixtureGasNasa.lowPressureThermalConductivity

Component	Version 3.2	Version 3.2.1
y	Media.Interfaces.PartialMedium.MoleFraction	Media.Interfaces.Types.MoleFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Tc	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Pc	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
M	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
lambdam	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
gamma	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass

---

function Media.IdealGases.Common.MixtureGasNasa.thermalConductivity

Component	Version 3.2	Version 3.2.1
method	=1	=methodForThermalConductivity
lambdaX	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
cp	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity

Equations in Version 3.2	Equations in Version 3.2.1
... assert(fluidConstants[i].hasCriticalData, "Critical data for "+ fluidConstants[i].chemicalFormula +      " not known. Can not compute thermal conductivity.");
eta[i] = SingleGasNasa.dynamicViscosityLowPressure(state.T, fluidConstants[i].criticalTemperature, fluidConstants[i].molarMass, fluidConstants[i].criticalMolarVolume, fluidConstants[i].acentricFactor, fluidConstants[i].dipoleMoment);	eta[i] = Modelica.Media.IdealGases.Common.Functions.dynamicViscosityLowPressure( state.T, fluidConstants[i].criticalTemperature, fluidConstants[i].molarMass, fluidConstants[i].criticalMolarVolume, fluidConstants[i].acentricFactor, fluidConstants[i].dipoleMoment);
cp[i] = SingleGasNasa.cp_T(data[i],state.T);	cp[i] = Modelica.Media.IdealGases.Common.Functions.cp_T( data[i],state.T);
lambdaX[i] = SingleGasNasa.thermalConductivityEstimate(Cp=cp[i], eta= eta[i], method=method);	lambdaX[i] = Modelica.Media.IdealGases.Common.Functions.thermalConductivityEstimate( Cp=cp[i], eta= eta[i], method=method,data=data[i]);
end for; ...

---

function Media.IdealGases.Common.MixtureGasNasa.density_derX

Component	Version 3.2	Version 3.2.1
dddX	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.IdealGases.Common.MixtureGasNasa.T_hX

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
refChoice	Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Media.Interfaces.Choices.ReferenceEnthalpy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Xfull	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

function Media.IdealGases.Common.MixtureGasNasa.T_psX

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
X	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
Xfull	Media.Interfaces.PartialMedium.MassFraction	Media.Interfaces.Types.MassFraction

---

package Media.IdealGases.Common.FluidData

Component	Version 3.2	Version 3.2.1
N2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
O2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
CL2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
F2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
CO2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
CO	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
H2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
H2O	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
N2O	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
NO	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
NO2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
NH3	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
SO2	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
SO3	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
Ar	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
He	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
Ne	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
CH4	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C2H6	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C3H8	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C4H10_n_butane	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C5H12_n_pentane	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C6H14_n_hexane	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C7H16_n_heptane	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C2H4	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C3H6_propylene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C4H8_1_butene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C5H10_1_pentene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C6H12_1_hexene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C7H14_1_heptene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C2H2_vinylidene	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C6H6	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C8H18_n_octane	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C8H10_ethylbenz	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
CH3OH	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C2H5OH	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C3H7OH	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants
C4H9OH	Media.IdealGases.Common.SingleGasNasa.FluidConstants	Media.Interfaces.Types.IdealGas.FluidConstants

---

model Media.Incompressible.Examples.TestGlycol

Component	Version 3.2	Version 3.2.1
eta	Media.Interfaces.PartialMedium.DynamicViscosity	Media.Interfaces.Types.DynamicViscosity
lambda	Media.Interfaces.PartialMedium.ThermalConductivity	Media.Interfaces.Types.ThermalConductivity
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
cv	Media.Interfaces.PartialMedium.SpecificHeatCapacity	Media.Interfaces.Types.SpecificHeatCapacity
u		Present
h		Present
d		Present

Equations in Version 3.2	Equations in Version 3.2.1
medium.p = 1e5;	medium.p = 1.013e5;
medium.T = Medium.T_min + time/timeUnit*Ta;

---

package Media.Incompressible.TableBased

Component	Version 3.2	Version 3.2.1
T_min	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T_max	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
T0	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
h0	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
s0	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
MM_const	Media.Interfaces.PartialMedium.MolarMass	Media.Interfaces.Types.MolarMass
invTK	=if size(tableViscosity, 1) > 0 then invertTemp(tableViscosity[:, 1], TinK) else fill(0, 0)	=if size(tableViscosity, 1) > 0 then (if TinK then 1 ./ tableViscosity[:, 1] else 1 ./ Cv.from_degC(tableViscosity[:, 1])) else fill(0, neta)
poly_rho	=if hasDensity then Poly.fitting(tableDensity[:, 1], tableDensity[:, 2], npol) else zeros(npol + 1)	=if hasDensity then Poly.fitting(tableDensity[:, 1], tableDensity[:, 2], npolDensity) else zeros(npolDensity + 1)
poly_Cp	=if hasHeatCapacity then Poly.fitting(tableHeatCapacity[:, 1], tableHeatCapacity[:, 2], npol) else zeros(npol + 1)	=if hasHeatCapacity then Poly.fitting(tableHeatCapacity[:, 1], tableHeatCapacity[:, 2], npolHeatCapacity) else zeros(npolHeatCapacity + 1)
poly_eta	=if hasViscosity then Poly.fitting(invTK, Math.log(tableViscosity[:, 2]), npol) else zeros(npol + 1)	=if hasViscosity then Poly.fitting(invTK, Math.log(tableViscosity[:, 2]), npolViscosity) else zeros(npolViscosity + 1)
poly_pVap	=if hasVaporPressure then Poly.fitting(tableVaporPressure[:, 1], tableVaporPressure[:, 2], npol) else zeros(npol + 1)	=if hasVaporPressure then Poly.fitting(tableVaporPressure[:, 1], tableVaporPressure[:, 2], npolVaporPressure) else zeros(npolVaporPressure + 1)
poly_lam	=if size(tableConductivity, 1) > 0 then Poly.fitting(tableConductivity[:, 1], tableConductivity[:, 2], npol) else zeros(npol + 1)	=if size(tableConductivity, 1) > 0 then Poly.fitting(tableConductivity[:, 1], tableConductivity[:, 2], npolConductivity) else zeros(npolConductivity + 1)
npolDensity		Present
npolHeatCapacity		Present
npolViscosity		Present
npolVaporPressure		Present
npolConductivity		Present

---

model Media.Incompressible.TableBased.BaseProperties

Equations in Version 3.2	Equations in Version 3.2.1
... h = if enthalpyOfT then h_T(T) else h_pT(p,T,densityOfT);
if singleState then	u = h - (if singleState then reference_p/d else state.p/d);
u = h_T(T) - reference_p/d; else u = h - p/d; end if;
d = Poly.evaluate(poly_rho,if TinK then T else T_degC); ...

---

function Media.Incompressible.TableBased.setState_dTX

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(false, "for incompressible media with d(T) only, state can not be set from density and temperature");	assert(false, "For incompressible media with d(T) only, state can not be set from density and temperature");

---

function Media.Incompressible.TableBased.setState_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Incompressible.TableBased.setState_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Incompressible.TableBased.setState_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

function Media.Incompressible.TableBased.s_T

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy

---

function Media.Incompressible.TableBased.density_T

Component	Version 3.2	Version 3.2.1
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Incompressible.TableBased.specificInternalEnergy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
u := if enthalpyOfT then h_T(state.T) else h_pT(state.p,state.T) - (if singleState then reference_p/density(state) else state.p/density(state));	u := (if enthalpyOfT then h_T(state.T) else h_pT(state.p,state.T)) - (if singleState then reference_p else state.p)/density(state);

---

function Media.Incompressible.TableBased.T_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Incompressible.TableBased.T_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

package Media.Water

Component	Version 3.2	Version 3.2.1
waterConstants	Media.Interfaces.PartialTwoPhaseMedium.FluidConstants	Media.Interfaces.Types.TwoPhase.FluidConstants
simpleWaterConstants	Present

---

package Media.Water.ConstantPropertyLiquidWater

Component	Version 3.2	Version 3.2.1
simpleWaterConstants		Present

---

record Media.Water.WaterIF97_base.ThermodynamicState

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Media.Water.WaterIF97_base.BaseProperties

Component	Version 3.2	Version 3.2.1
sat	Present

Equations in Version 3.2	Equations in Version 3.2.1
... assert(not ((d < bubbleDensity(sat) and d > dewDensity(sat)) and T <         &nbspfluidConstants[1].criticalTemperature),            "With onePhase=true this model may only be called with one-phase states d > dl or d < dv!"            + "(d = " + String(d) + ", T = " + String(T) + ")");
	end if; end if;
else
assert(true,"no events for pT-model"); end if; end if; else
phase = 0; ...

---

function Media.Water.WaterIF97_base.density_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_base.temperature_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Water.WaterIF97_base.temperature_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Water.WaterIF97_base.density_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_base.pressure_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Water.WaterIF97_base.specificEnthalpy_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_base.specificEnthalpy_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_base.specificEnthalpy_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_base.density_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_base.specificEntropy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	s := if dT_explicit then IF97_Utilities.s_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.s_pT(state.p, state.T) else IF97_Utilities.s_ph( state.p, state.h, state.phase);
s = IF97_Utilities.s_dT(state.d, state.T, state.phase);
elseif pT_explicit then s = IF97_Utilities.s_pT(state.p, state.T); else s = IF97_Utilities.s_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.specificHeatCapacityCp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	cp := if dT_explicit then IF97_Utilities.cp_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.cp_pT(state.p, state.T) else IF97_Utilities.cp_ph( state.p, state.h, state.phase);
cp = IF97_Utilities.cp_dT(state.d, state.T, state.phase);
elseif pT_explicit then cp = IF97_Utilities.cp_pT(state.p, state.T); else cp = IF97_Utilities.cp_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.specificHeatCapacityCv

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	cv := if dT_explicit then IF97_Utilities.cv_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.cv_pT(state.p, state.T) else IF97_Utilities.cv_ph( state.p, state.h, state.phase);
cv = IF97_Utilities.cv_dT(state.d, state.T, state.phase);
elseif pT_explicit then cv = IF97_Utilities.cv_pT(state.p, state.T); else cv = IF97_Utilities.cv_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.isentropicExponent

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	gamma := if dT_explicit then IF97_Utilities.isentropicExponent_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.isentropicExponent_pT(state.p, state.T) else IF97_Utilities.isentropicExponent_ph( state.p, state.h, state.phase);
gamma = IF97_Utilities.isentropicExponent_dT(state.d, state.T, state. phase);
elseif pT_explicit then gamma = IF97_Utilities.isentropicExponent_pT(state.p, state.T); else gamma = IF97_Utilities.isentropicExponent_ph(state.p, state.h, state.        &nbspphase); end if;

---

function Media.Water.WaterIF97_base.isothermalCompressibility

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	kappa := if dT_explicit then IF97_Utilities.kappa_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.kappa_pT(state.p, state.T) else IF97_Utilities.kappa_ph( state.p, state.h, state.phase);
kappa = IF97_Utilities.kappa_dT(state.d, state.T, state.phase);
elseif pT_explicit then kappa = IF97_Utilities.kappa_pT(state.p, state.T); else kappa = IF97_Utilities.kappa_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.isobaricExpansionCoefficient

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	beta := if dT_explicit then IF97_Utilities.beta_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.beta_pT(state.p, state.T) else IF97_Utilities.beta_ph( state.p, state.h, state.phase);
beta = IF97_Utilities.beta_dT(state.d, state.T, state.phase);
elseif pT_explicit then beta = IF97_Utilities.beta_pT(state.p, state.T); else beta = IF97_Utilities.beta_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.velocityOfSound

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	a := if dT_explicit then IF97_Utilities.velocityOfSound_dT( state.d, state.T, state.phase) else if pT_explicit then IF97_Utilities.velocityOfSound_pT(state.p, state.T) else IF97_Utilities.velocityOfSound_ph( state.p, state.h, state.phase);
a = IF97_Utilities.velocityOfSound_dT(state.d, state.T, state.phase);
elseif pT_explicit then a = IF97_Utilities.velocityOfSound_pT(state.p, state.T); else a = IF97_Utilities.velocityOfSound_ph(state.p, state.h, state.phase); end if;

---

function Media.Water.WaterIF97_base.bubbleDensity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if ph_explicit or pT_explicit then	dl := if ph_explicit then IF97_Utilities.BaseIF97.Regions.rhol_p(sat.psat) else IF97_Utilities.BaseIF97.Regions.rhol_T(sat.Tsat);
dl = IF97_Utilities.BaseIF97.Regions.rhol_p(sat.psat);
else dl = IF97_Utilities.BaseIF97.Regions.rhol_T(sat.Tsat); end if;

---

function Media.Water.WaterIF97_base.dewDensity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if ph_explicit or pT_explicit then	dv := if ph_explicit or pT_explicit then IF97_Utilities.BaseIF97.Regions.rhov_p(sat.psat) else IF97_Utilities.BaseIF97.Regions.rhov_T(sat.Tsat);
dv = IF97_Utilities.BaseIF97.Regions.rhov_p(sat.psat);
else dv = IF97_Utilities.BaseIF97.Regions.rhov_T(sat.Tsat); end if;

---

record Media.Water.WaterIF97_fixedregion.ThermodynamicState

Component	Version 3.2	Version 3.2.1
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

model Media.Water.WaterIF97_fixedregion.BaseProperties

Component	Version 3.2	Version 3.2.1
sat	Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Media.Interfaces.Types.SaturationProperties

---

function Media.Water.WaterIF97_fixedregion.density_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_fixedregion.temperature_ph

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Water.WaterIF97_fixedregion.temperature_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature

---

function Media.Water.WaterIF97_fixedregion.density_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_fixedregion.pressure_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure

---

function Media.Water.WaterIF97_fixedregion.specificEnthalpy_dT

Component	Version 3.2	Version 3.2.1
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_fixedregion.specificEnthalpy_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_fixedregion.specificEnthalpy_ps

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
s	Media.Interfaces.PartialMedium.SpecificEntropy	Media.Interfaces.Types.SpecificEntropy
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
h	Media.Interfaces.PartialMedium.SpecificEnthalpy	Media.Interfaces.Types.SpecificEnthalpy

---

function Media.Water.WaterIF97_fixedregion.density_pT

Component	Version 3.2	Version 3.2.1
p	Media.Interfaces.PartialMedium.AbsolutePressure	Media.Interfaces.Types.AbsolutePressure
T	Media.Interfaces.PartialMedium.Temperature	Media.Interfaces.Types.Temperature
phase	Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Media.Interfaces.Types.FixedPhase
d	Media.Interfaces.PartialMedium.Density	Media.Interfaces.Types.Density

---

function Media.Water.WaterIF97_fixedregion.setDewState

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state.phase := phase;	state := ThermodynamicState( phase=phase, p=sat.psat, T=sat.Tsat, h=dewEnthalpy(sat), d=dewDensity(sat));
state.p = sat.psat;
state.T = sat.Tsat; state.h = dewEnthalpy(sat); state.d = dewDensity(sat);

---

function Media.Water.WaterIF97_fixedregion.setBubbleState

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
state.phase := phase;	state := ThermodynamicState( phase=phase, p=sat.psat, T=sat.Tsat, h=bubbleEnthalpy(sat), d=bubbleDensity(sat));
state.p = sat.psat;
state.T = sat.Tsat; state.h = bubbleEnthalpy(sat); state.d = bubbleDensity(sat);

---

function Media.Water.WaterIF97_fixedregion.specificEntropy

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	s := if dT_explicit then IF97_Utilities.s_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.s_pT( state.p, state.T, Region) else IF97_Utilities.s_ph( state.p, state.h, state.phase, Region);
s = IF97_Utilities.s_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then s = IF97_Utilities.s_pT(state.p, state.T, Region); else s = IF97_Utilities.s_ph(state.p, state.h, state.phase, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.specificHeatCapacityCp

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	cp := if dT_explicit then IF97_Utilities.cp_dT( state.d, state.T, Region) else if pT_explicit then IF97_Utilities.cp_pT( state.p, state.T, Region) else IF97_Utilities.cp_ph( state.p, state.h, Region);
cp = IF97_Utilities.cp_dT(state.d, state.T, Region);
elseif pT_explicit then cp = IF97_Utilities.cp_pT(state.p, state.T, Region); else cp = IF97_Utilities.cp_ph(state.p, state.h, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.specificHeatCapacityCv

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	cv := if dT_explicit then IF97_Utilities.cv_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.cv_pT( state.p, state.T, Region) else IF97_Utilities.cv_ph( state.p, state.h, state.phase, Region);
cv = IF97_Utilities.cv_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then cv = IF97_Utilities.cv_pT(state.p, state.T, Region); else cv = IF97_Utilities.cv_ph(state.p, state.h, state.phase, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.isentropicExponent

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	gamma := if dT_explicit then IF97_Utilities.isentropicExponent_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.isentropicExponent_pT( state.p, state.T, Region) else IF97_Utilities.isentropicExponent_ph( state.p, state.h, state.phase, Region);
gamma = IF97_Utilities.isentropicExponent_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then gamma = IF97_Utilities.isentropicExponent_pT(state.p, state.T, Region); else gamma = IF97_Utilities.isentropicExponent_ph(state.p, state.h,          &nbspstate.phase, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.isothermalCompressibility

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	kappa := if dT_explicit then IF97_Utilities.kappa_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.kappa_pT( state.p, state.T, Region) else IF97_Utilities.kappa_ph( state.p, state.h, state.phase, Region);
kappa = IF97_Utilities.kappa_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then kappa = IF97_Utilities.kappa_pT(state.p, state.T, Region); else kappa = IF97_Utilities.kappa_ph(state.p, state.h, state.phase, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.isobaricExpansionCoefficient

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	beta := if dT_explicit then IF97_Utilities.beta_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.beta_pT( state.p, state.T, Region) else IF97_Utilities.beta_ph( state.p, state.h, state.phase, Region);
beta = IF97_Utilities.beta_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then beta = IF97_Utilities.beta_pT(state.p, state.T, Region); else beta = IF97_Utilities.beta_ph(state.p, state.h, state.phase, Region); end if;

---

function Media.Water.WaterIF97_fixedregion.velocityOfSound

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if dT_explicit then	a := if dT_explicit then IF97_Utilities.velocityOfSound_dT( state.d, state.T, state.phase, Region) else if pT_explicit then IF97_Utilities.velocityOfSound_pT( state.p, state.T, Region) else IF97_Utilities.velocityOfSound_ph( state.p, state.h, state.phase, Region);
a = IF97_Utilities.velocityOfSound_dT(state.d, state.T, state.phase, Region);
elseif pT_explicit then a = IF97_Utilities.velocityOfSound_pT(state.p, state.T, Region); else a = IF97_Utilities.velocityOfSound_ph(state.p, state.h, state.phase,        &nbspRegion); end if;

---

function Media.Water.WaterIF97_fixedregion.bubbleDensity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if ph_explicit or pT_explicit then	dl := if ph_explicit or pT_explicit then IF97_Utilities.BaseIF97.Regions.rhol_p(sat.psat) else IF97_Utilities.BaseIF97.Regions.rhol_T(sat.Tsat);
dl = IF97_Utilities.BaseIF97.Regions.rhol_p(sat.psat);
else dl = IF97_Utilities.BaseIF97.Regions.rhol_T(sat.Tsat); end if;

---

function Media.Water.WaterIF97_fixedregion.dewDensity

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if ph_explicit or pT_explicit then	dv := if ph_explicit or pT_explicit then IF97_Utilities.BaseIF97.Regions.rhov_p(sat.psat) else IF97_Utilities.BaseIF97.Regions.rhov_T(sat.Tsat);
dv = IF97_Utilities.BaseIF97.Regions.rhov_p(sat.psat);
else dv = IF97_Utilities.BaseIF97.Regions.rhov_T(sat.Tsat); end if;

---

function Media.Water.IF97_Utilities.BaseIF97.Regions.region_ps

Equations in Version 3.2	Equations in Version 3.2.1
... if region < 0 then
assert(false, "region computation from p and s failed: function called outside the legal region");	assert(false, "Region computation from p and s failed: function called outside the legal region");
else ...

---

function Media.Water.IF97_Utilities.BaseIF97.Regions.region_dT

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(false,"out of valid region for IF97, pressure above region 5!");	assert(false, "Out of valid region for IF97, pressure above region 5!");
end if; ...

---

function Media.Water.IF97_Utilities.BaseIF97.Basic.g2

Equations in Version 3.2	Equations in Version 3.2.1
... g.R = data.RH2O;
assert(p > triple.ptriple, "IF97 medium function g2 called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");	assert(p > 0.0, "IF97 medium function g2 called with too low pressure\n" + "p = " + String(p) + " Pa <= 0.0 Pa");
assert(p <= 100.0e6,     "IF97 medium function g2: the input pressure (= " + String(p) + " Pa) is higher than 100 Mpa"); ...

---

function Media.Water.IF97_Utilities.BaseIF97.Basic.g2metastable

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(p > triple.ptriple, "IF97 medium function g2metastable called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");	assert(p > 0.0, "IF97 medium function g2metastable called with too low pressure\n" + "p = " + String(p) + " Pa <= 0.0 Pa");
assert(p <= 100.0e6,     "IF97 medium function g2metastable: the input pressure (= " + String(p) + " Pa) is higher than 100 Mpa"); ...

---

function Media.Water.IF97_Utilities.BaseIF97.Basic.g5

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(p > triple.ptriple, "IF97 medium function g5 called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");	assert(p > 0.0, "IF97 medium function g5 called with too low pressure\n" + "p = " + String(p) + " Pa <= 0.0 Pa");
assert(p <= data.PLIMIT5,     "IF97 medium function g5: input pressure (= " + String(p) + " Pa) is higher than 10 Mpa in region 5"); ...

---

function Media.Water.IF97_Utilities.BaseIF97.Basic.g2pitau

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(p > triple.ptriple, "IF97 medium function g2pitau called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");	assert(p > 0.0, "IF97 medium function g2pitau called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");
assert(p <= 100.0e6,     "IF97 medium function g2pitau: the input pressure (= " + String(p) + " Pa) is higher than 100 Mpa"); ...

---

function Media.Water.IF97_Utilities.BaseIF97.Basic.g5pitau

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(p > triple.ptriple, "IF97 medium function g5pitau called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");	assert(p > 0.0, "IF97 medium function g5pitau called with too low pressure\n" + "p = " + String(p) + " Pa <= " + String(triple.ptriple) + " Pa (triple point pressure)");
assert(p <= data.PLIMIT5,     "IF97 medium function g5pitau: input pressure (= " + String(p) + " Pa) is higher than 10 Mpa in region 5"); ...

---

function Media.Water.IF97_Utilities.BaseIF97.Transport.cond_dTp

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(false, "the scientific method works only for temperature up to 623.15 K");	assert(false, "The scientific method works only for temperature up to 623.15 K");
end if; ... else
assert(false, "thermal conductivity can only be called in the one-phase regions below 623.15 K\n" + "(p = " + String(p) + " Pa, T = " + String(T) + " K, region = " + String(region) + ")");	assert(false, "Thermal conductivity can only be called in the one-phase regions below 623.15 K\n" + "(p = " + String(p) + " Pa, T = " + String(T) + " K, region = " + String(region) + ")");
end if; ...

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.dofpt3

Component	Version 3.2	Version 3.2.1
damping		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
	found := false;
assert(p >= data.PLIMIT4A,     "BaseIF97.dofpt3: function called outside of region 3! p too low\n" +     "p = " + String(p) + " Pa < " + String(data.PLIMIT4A) + " Pa"); ... supercritical = p > data.PCRIT;
	damping = if supercritical then 1.0 else 1.0; Tmax = Regions.boundary23ofp(p); if supercritical then
dmax = dofp13(p);
dmin = dofp23(p);
Tmax = Regions.boundary23ofp(p);	dguess = dmax - (T - data.TLIMIT1)/(data.TLIMIT1 - Tmax)*(dmax - dmin);
if supercritical then dguess = dmin + (T - data.TLIMIT1)/(data.TLIMIT1 - Tmax)*(dmax -        &nbspdmin);
else ... if liquid then
dguess = 0.5*(Regions.rhol_p_R4b(p) + dmax);	dmax = dofp13(p);
	dmin = Regions.rhol_p_R4b(p); dguess = 1.1*Regions.rhol_T(T)   "Guess: 10 percent more than on the phase boundary for same T";
else
dguess = 0.5*(Regions.rhov_p_R4b(p) + dmin);	dmax = Regions.rhov_p_R4b(p);
	dmin = dofp23(p); dguess = 0.9*Regions.rhov_T(T)   "Guess: 10% less than on the phase boundary for same T";
end if; ... end if;
deld = dp/nDerivs.pd;	deld = dp/nDerivs.pd*damping;
d = d - deld; ... end if;
assert(error <> 1, "error in inverse function dofpt3: iteration failed");	assert(error <> 1, "Error in inverse function dofpt3: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.dtofph3

Component	Version 3.2	Version 3.2.1
found		=false

Equations in Version 3.2	Equations in Version 3.2.1
... subregion = if h < (Regions.hl_p(p) + 10.0) then 1 else        &nbspif h > (Regions.hv_p(p) - 10.0) then 2 else 0;
assert(subregion <> 0,"inverse iteration of dt from ph called in 2 phase region: this can not work");	assert(subregion <> 0, "Inverse iteration of dt from ph called in 2 phase region: this can not work");
else ... end if;
assert(error <> 1, "error in inverse function dtofph3: iteration failed");	assert(error <> 1, "Error in inverse function dtofph3: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.dtofps3

Equations in Version 3.2	Equations in Version 3.2.1
... subregion = if s < (Regions.sl_p(p) + 10.0) then 1 else        &nbspif s > (Regions.sv_p(p) - 10.0) then 2 else 0;
assert(subregion <> 0,"inverse iteration of dt from ps called in 2 phase region: this is illegal!");	assert(subregion <> 0, "Inverse iteration of dt from ps called in 2 phase region: this is illegal!");
else ... end if;
assert(error <> 1, "error in inverse function dtofps3: iteration failed");	assert(error <> 1, "Error in inverse function dtofps3: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.dtofpsdt3

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(error <> 1, "error in inverse function dtofpsdt3: iteration failed");	assert(error <> 1, "Error in inverse function dtofpsdt3: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.pofdt125

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(error <> 1, "error in inverse function pofdt125: iteration failed");	assert(error <> 1, "Error in inverse function pofdt125: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.tofph5

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(error <> 1, "error in inverse function tofph5: iteration failed");	assert(error <> 1, "Error in inverse function tofph5: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.tofps5

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(error <> 1, "error in inverse function tofps5: iteration failed");	assert(error <> 1, "Error in inverse function tofps5: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.Inverses.tofpst5

Equations in Version 3.2	Equations in Version 3.2.1
... end if;
assert(error <> 1, "error in inverse function tofpst5: iteration failed");	assert(error <> 1, "Error in inverse function tofpst5: iteration failed");

---

function Media.Water.IF97_Utilities.BaseIF97.extraDerivs_ph

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(phase ==1, "extraDerivs_ph: properties are not implemented in 2 phase region");	assert(phase == 1, "ExtraDerivs_ph: properties are not implemented in 2 phase region");
region = Regions.region_ph(p=p,h= h,phase= phase); ...

---

function Media.Water.IF97_Utilities.waterBaseProp_ph

Equations in Version 3.2	Equations in Version 3.2.1
... aux.pt = aux.R*aux.rho*f.delta*(f.fdelta - f.tau*f.fdeltatau);
aux.cv = abs(aux.R*(-f.tau*f.tau*f.ftautau)) "can be close to neg. infinity near critical point";	aux.cv = abs(aux.R*(-f.tau*f.tau*f.ftautau)) "Can be close to neg. infinity near critical point";
aux.cp = (aux.rho*aux.rho*aux.pd*aux.cv + aux.T*aux.pt*aux.pt)/(aux.rho*aux.rho*aux.pd); ... (aux.T,error) = BaseIF97.Inverses.tofph5(p=aux.p,h= aux.h,reldh= 1.0e-7);
assert(error == 0, "error in inverse iteration of steam tables");	assert(error == 0, "Error in inverse iteration of steam tables");
g = BaseIF97.Basic.g5(aux.p, aux.T); ... else
assert(false, "error in region computation of IF97 steam tables" + "(p = " + String(p) + ", h = " + String(h) + ")");	assert(false, "Error in region computation of IF97 steam tables" + "(p = " + String(p) + ", h = " + String(h) + ")");
end if; ...

---

function Media.Water.IF97_Utilities.waterBaseProp_ps

Equations in Version 3.2	Equations in Version 3.2.1
... aux.x = 0.0;
	aux.dpT = -aux.vt/aux.vp;
elseif (aux.region == 2) then ... aux.x = 1.0;
	aux.dpT = -aux.vt/aux.vp;
elseif (aux.region == 3) then ... aux.x = 0.0;
	aux.dpT = aux.pt;
elseif (aux.region == 4) then ... (aux.T,error) = BaseIF97.Inverses.tofps5(p=p,s=s,relds= 1.0e-7);
assert(error == 0, "error in inverse iteration of steam tables");	assert(error == 0, "Error in inverse iteration of steam tables");
g = BaseIF97.Basic.g5(p, aux.T); ... aux.cv = aux.R*(-g.tau*g.tau*g.gtautau + ((g.gpi - g.tau*g.gtaupi)*(g.gpi - g.tau*g.gtaupi)/g.gpipi));
	aux.dpT = -aux.vt/aux.vp; aux.x = 1.0;
else
assert(false, "error in region computation of IF97 steam tables" + "(p = " + String(p) + ", s = " + String(s) + ")");	assert(false, "Error in region computation of IF97 steam tables" + "(p = " + String(p) + ", s = " + String(s) + ")");
end if; ...

---

function Media.Water.IF97_Utilities.regionAssertReal

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(check, "this function can not be called with two-phase inputs!");	assert(check, "This function can not be called with two-phase inputs!");

---

function Media.Water.IF97_Utilities.waterBaseProp_pT

Equations in Version 3.2	Equations in Version 3.2.1
... aux.x = 0.0;
	aux.dpT = -aux.vt/aux.vp;
elseif (aux.region == 2) then ... aux.x = 1.0;
	aux.dpT = -aux.vt/aux.vp;
elseif (aux.region == 3) then ... aux.x = 0.0;
	aux.dpT = aux.pt;
elseif (aux.region == 5) then ... aux.cv = aux.R*(-g.tau*g.tau*g.gtautau + ((g.gpi - g.tau*g.gtaupi)*(g.gpi - g.tau*g.gtaupi)/g.gpipi));
	aux.x = 1.0; aux.dpT = -aux.vt/aux.vp;
else
assert(false, "error in region computation of IF97 steam tables" + "(p = " + String(p) + ", T = " + String(T) + ")");	assert(false, "Error in region computation of IF97 steam tables" + "(p = " + String(p) + ", T = " + String(T) + ")");
end if; ...

---

function Media.Water.IF97_Utilities.waterBaseProp_dT

Equations in Version 3.2	Equations in Version 3.2.1
... else
assert(false, "error in region computation of IF97 steam tables" + "(rho = " + String(rho) + ", T = " + String(T) + ")");	assert(false, "Error in region computation of IF97 steam tables" + "(rho = " + String(rho) + ", T = " + String(T) + ")");
end if; ...

---

model Thermal.FluidHeatFlow.Examples.SimpleCooling

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor	T(start=TAmb)	T(start=TAmb, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.ParallelCooling

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe1		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		V_flow(start=0)
		T0fixed=true
pipe2		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		V_flow(start=0)
		T0fixed=true
pipe3		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor1	T(start=TAmb)	T(start=TAmb, fixed=true)
heatCapacitor2	T(start=TAmb)	T(start=TAmb, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.IndirectCooling

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
outerPump		constantVolumeFlow=1
ambient2		constantAmbientPressure=0
heatCapacitor	T(start=TAmb)	T(start=TAmb, fixed=true)
pipe1		h_g=0
		T0fixed=true
innerPump		constantVolumeFlow=1
outerPipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
innerPipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true

---

model Thermal.FluidHeatFlow.Examples.PumpAndValve

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
idealPump		V_flow0=2
		V_flow(start=0)
		wNominal(displayUnit="rad/s") = 1
		dp0(displayUnit="Pa") = 2
valve		m=0
		y1=1
		Kv1=1
		kv0=0.01
		dp0(displayUnit="Pa") = 1
		rho0=10
		frictionLoss=0
pipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor	T(start=TAmb)	T(start=TAmb, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.PumpDropOut

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor	T(start=TAmb)	T(start=TAmb, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.ParallelPumpDropOut

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe1		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		V_flow(start=0)
		T0fixed=true
pipe2		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		V_flow(start=0)
		T0fixed=true
pipe3		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor1	T(start=TAmb)	T(start=TAmb, fixed=true)
heatCapacitor2	T(start=TAmb)	T(start=TAmb, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.OneMass

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor	T(start=TMass)	T(start=TMass, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.TwoMass

Component	Version 3.2	Version 3.2.1
ambient1		constantAmbientPressure=0
pump		constantVolumeFlow=1
pipe1		V_flow(start=0)
		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
pipe2		V_flow(start=0)
		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
pipe3		V_flowLaminar=0.1
		dpLaminar(displayUnit="Pa") = 0.1
		V_flowNominal=1
		dpNominal(displayUnit="Pa") = 1
		h_g=0
		T0fixed=true
ambient2		constantAmbientPressure=0
heatCapacitor1	T(start=TMass1)	T(start=TMass1, fixed=true)
heatCapacitor2	T(start=TMass2)	T(start=TMass2, fixed=true)

---

model Thermal.FluidHeatFlow.Examples.Utilities.DoubleRamp

Component	Version 3.2	Version 3.2.1
offset	start=1
		=1
startTime	start=0.2
		=0.2
interval	start=0.2
		=0.2
height_1	start=-1
		=-1
duration_1	start=0.2
		=0.2
height_2	start=1
		=1
duration_2	start=0.2
		=0.2

---

model Thermal.FluidHeatFlow.Interfaces.Partials.TwoPort

Component	Version 3.2	Version 3.2.1
dp	=flowPort_a.p - flowPort_b.p
V_flow	=flowPort_a.m_flow/medium.rho
T		fixed=T0fixed
T_a	=flowPort_a.h/medium.cp
T_b	=flowPort_b.h/medium.cp
dT	=if noEvent(V_flow >= 0) then T - T_a else T_b - T
h	=medium.cp*T
T_q	=T - noEvent(sign(V_flow))*(1 - tapT)*dT
T0fixed		Present

Equations in Version 3.2	Equations in Version 3.2.1
	dp=flowPort_a.p - flowPort_b.p; V_flow=flowPort_a.m_flow/medium.rho; T_a=flowPort_a.h/medium.cp; T_b=flowPort_b.h/medium.cp; dT=if noEvent(V_flow>=0) then T-T_a else T_b-T; h = medium.cp*T; T_q = T - noEvent(sign(V_flow))*(1 - tapT)*dT;
flowPort_a.m_flow + flowPort_b.m_flow = 0; ...

---

model Thermal.FluidHeatFlow.Interfaces.Partials.Ambient

Component	Version 3.2	Version 3.2.1
T_port	=flowPort.h/medium.cp
h	=medium.cp*T

Equations in Version 3.2	Equations in Version 3.2.1
flowPort.H_flow = semiLinear(flowPort.m_flow,flowPort.h,h);	T_port=flowPort.h/medium.cp;
	h = medium.cp*T; flowPort.H_flow = semiLinear(flowPort.m_flow,flowPort.h,h);

---

model Thermal.HeatTransfer.Examples.ControlledTemperature

Component	Version 3.2	Version 3.2.1
TRes	=heatingResistor.heatPort.T	=heatingResistor.T_heatPort
heatingResistor	T_ref=from_degC(20)	T_ref=293.15
	alpha=1/(235 + 20)	alpha=1/255

---

model Thermal.HeatTransfer.Examples.Motor

Component	Version 3.2	Version 3.2.1
windingLosses	T_ref=from_degC(95)	T_ref=368.15

---

model Thermal.HeatTransfer.Components.Convection

Component	Version 3.2	Version 3.2.1
Gc		unit="W/K"

---

model Thermal.HeatTransfer.Sensors.TemperatureSensor

Component	Version 3.2	Version 3.2.1
T		unit="K"

---

model Thermal.HeatTransfer.Sensors.RelTemperatureSensor

Component	Version 3.2	Version 3.2.1
T_rel		unit="K"
		displayUnit="K"

---

model Thermal.HeatTransfer.Sensors.HeatFlowSensor

Component	Version 3.2	Version 3.2.1
Q_flow		unit="W"

---

model Thermal.HeatTransfer.Sensors.ConditionalFixedHeatFlowSensor

Component	Version 3.2	Version 3.2.1
Q_flow		unit="W"

---

model Thermal.HeatTransfer.Sources.PrescribedTemperature

Component	Version 3.2	Version 3.2.1
T		unit="K"

---

model Thermal.HeatTransfer.Sources.PrescribedHeatFlow

Component	Version 3.2	Version 3.2.1
Q_flow		unit="W"

---

model Thermal.HeatTransfer.Celsius.ToKelvin

Component	Version 3.2	Version 3.2.1
Celsius		unit="degC"
Kelvin		unit="K"

Equations in Version 3.2	Equations in Version 3.2.1
Kelvin = from_degC(Celsius);	Kelvin = Modelica.SIunits.Conversions.from_degC(Celsius);

---

model Thermal.HeatTransfer.Celsius.FromKelvin

Component	Version 3.2	Version 3.2.1
Kelvin		unit="K"
Celsius		unit="degC"

Equations in Version 3.2	Equations in Version 3.2.1
Celsius = to_degC(Kelvin);	Celsius = Modelica.SIunits.Conversions.to_degC(Kelvin);

---

model Thermal.HeatTransfer.Celsius.FixedTemperature

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degC(T);	port.T = Modelica.SIunits.Conversions.from_degC(T);

---

model Thermal.HeatTransfer.Celsius.PrescribedTemperature

Component	Version 3.2	Version 3.2.1
T		unit="degC"

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degC(T);	port.T = Modelica.SIunits.Conversions.from_degC(T);

---

model Thermal.HeatTransfer.Celsius.TemperatureSensor

Component	Version 3.2	Version 3.2.1
T		unit="degC"

Equations in Version 3.2	Equations in Version 3.2.1
T = to_degC(port.T);	T = Modelica.SIunits.Conversions.to_degC(port.T);
port.Q_flow = 0;

---

model Thermal.HeatTransfer.Fahrenheit.ToKelvin

Component	Version 3.2	Version 3.2.1
Fahrenheit		unit="degF"
Kelvin		unit="K"

Equations in Version 3.2	Equations in Version 3.2.1
Kelvin = from_degF(Fahrenheit);	Kelvin = Modelica.SIunits.Conversions.from_degF(Fahrenheit);

---

model Thermal.HeatTransfer.Fahrenheit.FromKelvin

Component	Version 3.2	Version 3.2.1
Kelvin		unit="K"
Fahrenheit		unit="degF"

Equations in Version 3.2	Equations in Version 3.2.1
Fahrenheit = to_degF(Kelvin);	Fahrenheit = Modelica.SIunits.Conversions.to_degF(Kelvin);

---

model Thermal.HeatTransfer.Fahrenheit.FixedTemperature

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degF(T);	port.T = Modelica.SIunits.Conversions.from_degF(T);

---

model Thermal.HeatTransfer.Fahrenheit.PrescribedTemperature

Component	Version 3.2	Version 3.2.1
T		unit="degF"

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degF(T);	port.T = Modelica.SIunits.Conversions.from_degF(T);

---

model Thermal.HeatTransfer.Fahrenheit.TemperatureSensor

Equations in Version 3.2	Equations in Version 3.2.1
T = to_degF(port.T);	T = Modelica.SIunits.Conversions.to_degF(port.T);
port.Q_flow = 0;

---

model Thermal.HeatTransfer.Rankine.ToKelvin

Component	Version 3.2	Version 3.2.1
Rankine		unit="degRk"
Kelvin		unit="K"

Equations in Version 3.2	Equations in Version 3.2.1
Kelvin = from_degRk(Rankine);	Kelvin = Modelica.SIunits.Conversions.from_degRk(Rankine);

---

model Thermal.HeatTransfer.Rankine.FromKelvin

Component	Version 3.2	Version 3.2.1
Kelvin		unit="K"
Rankine		unit="degRk"

Equations in Version 3.2	Equations in Version 3.2.1
Rankine = to_degRk(Kelvin);	Rankine = Modelica.SIunits.Conversions.to_degRk(Kelvin);

---

model Thermal.HeatTransfer.Rankine.FixedTemperature

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degRk(T);	port.T = Modelica.SIunits.Conversions.from_degRk(T);

---

model Thermal.HeatTransfer.Rankine.PrescribedTemperature

Component	Version 3.2	Version 3.2.1
T		unit="degRk"

Equations in Version 3.2	Equations in Version 3.2.1
port.T = from_degRk(T);	port.T = Modelica.SIunits.Conversions.from_degRk(T);

---

model Thermal.HeatTransfer.Rankine.TemperatureSensor

Equations in Version 3.2	Equations in Version 3.2.1
T = to_degRk(port.T);	T = Modelica.SIunits.Conversions.to_degRk(port.T);
port.Q_flow = 0;

---

function Math.Vectors.norm

Component	Version 3.2	Version 3.2.1
result		=0.0
eps		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if p == 2 then	if size(v,1) > 0 then
	if p >= 2-eps and p <= 2+eps then
result= sqrt(v*v);
elseif p == Modelica_3_2.Constants.inf then	elseif p >= Modelica.Constants.inf then
result= max(abs(v));
elseif p == 1 then	elseif p >= 1-eps and p <= 1+eps then
result= sum(abs(v));
	elseif p >= 1 then result = (sum(abs(v[i])^p for i in 1:size(v, 1)))^(1/p);
else
result= (sum(abs(v[i])^p for i in 1:size(v, 1)))^(1/p);	assert(false, "Optional argument \"p\" (= " + String(p) + ") of function \"norm\" >= 1 required");
end if;
	end if;

---

function Math.Vectors.normalize

Component	Version 3.2	Version 3.2.1
eps		min=0.0

---

function Math.Vectors.interpolate

Equations in Version 3.2	Equations in Version 3.2.1
... y2 = y[i+1];
assert(x2 > x1, "Abszissa table vector values must be increasing");	assert(x2 > x1, "Abscissa table vector values must be increasing");
yi = y1 + (y2 - y1)*(xi - x1)/(x2 - x1); ...

---

function Math.Vectors.Utilities.householderVector

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(norm_b > 0, "Vector b in function housholderVector is zero vector, but at least one element should be different from zero");	assert(norm_b > 0, "Vector b in function householderVector is zero vector, but at least one element should be different from zero");
assert(norm_a > 0, "Vector a in function housholderVector is zero vector, but at least one element should be different from zero");	assert(norm_a > 0, "Vector a in function householderVector is zero vector, but at least one element should be different from zero");
alpha = if norm(a + norm_a/norm_b*b,2) > norm(a - norm_a/norm_b*b,2) then norm_a/norm_b else -norm_a/norm_b; ...

---

function Math.Vectors.Utilities.roots

Equations in Version 3.2	Equations in Version 3.2.1
... if n > 0 then
assert(abs(p[1]) > 0, "Computing the roots of a polynomial with function \"Modelica.Math.Vectors.Utilities.roots\"\n" + "failed because the first element of the coefficient vector is zero, but should not be.");	assert(abs(p[1]) > 0, "Computing the roots of a polynomial with function \"Modelica.Math.Vectors.Utilities.roots\"\n" + "failed because the first element of the coefficient vector is zero, but should not be.");
A[1, :] = -p[2:np]/p[1]; ...

---

function Math.Matrices.QR

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
assert(nrow >= ncol, "\nInput matrix A[" + String(nrow) + "," + String(ncol) + "] has more columns as rows. This is not allowed when calling Modelica.Matrices.QR(A).");	assert(nrow >= ncol, "\nInput matrix A[" + String(nrow) + "," + String(ncol) + "] has more columns as rows. This is not allowed when calling Modelica.Matrices.QR(A).");
if pivoting then ...

---

function Math.Matrices.realSchur

Equations in Version 3.2	Equations in Version 3.2.1
... if size(A, 1) > 1 then
(S,QZ,alphaReal,alphaImag) = Matrices.LAPACK.dgees(A);	(S,QZ,alphaReal,alphaImag,info) = Matrices.LAPACK.dgees(A);
assert(info == 0, "The output info of LAPACK.dgees should be zero, else if\n     &nbspinfo < 0: if info = -i, the i-th argument of dgees had an illegal value\n     &nbspinfo > 0: if INFO = i, and i is                <= N: the QR algorithm failed to compute all the                     &nbspeigenvalues; elements 1:ILO-1 and i+1:N of WR and WI                     &nbspcontain those eigenvalues which have converged; if                     &nbspJOBVS = 'V', VS contains the matrix which reduces A                     &nbspto its partially converged Schur form.\n"); ... S = A;
if size(A, 1) > 0 then	QZ = fill(1, size(A, 1), size(A, 2));
QZ = [1];	alphaReal = fill(1, size(A, 1));
alphaReal = {1};	alphaImag = fill(0, size(A, 1));
alphaImag = {0};	end if;
else
QZ = fill(1, 0, 0); alphaReal = fill(1, 0); alphaImag = fill(0, 0); end if; end if;

---

function Math.Matrices.conditionNumber

Component	Version 3.2	Version 3.2.1
eps2		Present

Equations in Version 3.2	Equations in Version 3.2.1
... if min(size(A)) > 0 then
if p == 2 then	if p >= 2-eps2 and p <= 2+eps2 then
s = Modelica_3_2.Math.Matrices.singularValues(A); ...

---

function Math.Matrices.norm

Component	Version 3.2	Version 3.2.1
eps		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
if p == 1 then	if min(size(A)) > 0 then
	if p >= 1-eps and p <= 1+eps then
for i in 1:size(A, 2) loop ... end for;
elseif p == 2 then	elseif p >= 2-eps and p <= 2+eps then
result = max(singularValues(A));
elseif p == Modelica_3_2.Constants.inf then	elseif p >= Modelica.Constants.inf then
for i in 1:size(A, 1) loop ... else
assert(false, "Optional argument \"p\" of function \"norm\" must be 1, 2 or Modelica.Constants.inf");	assert(false, "Optional argument \"p\" (= " + String(p) + ") of function \"norm\" must be 1, 2 or Modelica.Constants.inf");
end if;
	end if;

---

function Math.Matrices.frobeniusNorm

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
result := if min(size(A))>0 then sqrt(sum(A.*A)) else -1e100;	result := if min(size(A)) > 0 then sqrt(sum(A .* A)) else 0.0;

---

function Math.Matrices.continuousSylvester

Equations in Version 3.2	Equations in Version 3.2.1
... (X,scale,info) = Matrices.LAPACK.dtrsyl(S, T, Chat);
assert(info == 0, "Solving of Sylvester equation with Matrices.continuousSylvester was not successful.\n The value of info is " + String(info) + ", but should be zero. A value unequal to zero means:\n < 0: if INFO = -i, the i-th argument had an illegal value\n = 1: A and B have common or very close eigenvalues; perturbed values were used to solve the equation (but the matrices A and B are unchanged).");	assert(info == 0, "Solving of Sylvester equation with Matrices.continuousSylvester was not successful.\n The value of info is " + String(info) + ", but should be zero. A value unequal to zero means:\n < 0: if INFO = -i, the i-th argument had an illegal value\n = 1: A and B have common or very close eigenvalues; perturbed values were used to solve the equation (but the matrices A and B are unchanged).");
X = if AisSchur and BisSchur then scale*X else if AisSchur then scale*X*        &nbsptranspose(V) else if BisSchur then scale*U*X else scale*U*X*transpose(V); ...

---

function Math.Matrices.LAPACK.dgeev

Component	Version 3.2	Version 3.2.1
dummy		Present

Equations in Version 3.2	Equations in Version 3.2.1
external "Fortran 77" dgeev("N", "V", n, Awork, n, eigenReal, eigenImag, eigenVectors, n, eigenVectors, n, work, size(work, 1), info);	external "Fortran 77" dgeev( "N", "V", n, Awork, n, eigenReal, eigenImag, dummy, 1, eigenVectors, n, work, size(work, 1), info);

---

function Math.Matrices.LAPACK.dgees

Component	Version 3.2	Version 3.2.1
dummyFunctionPointerNotUsed		Present
lwork		Present
work		Present

Equations in Version 3.2	Equations in Version 3.2.1
external "FORTRAN 77" c_inter_dgees("V", "N", n, T, lda, sdim, eval_real, eval_imag, Z, lda, bwork, info);	external"FORTRAN 77" dgees("V","N",dummyFunctionPointerNotUsed,n,T,lda,sdim,eval_real,eval_imag,Z,lda,work,lwork,bwork,info);

---

function Math.Matrices.LAPACK.dlange

Component	Version 3.2	Version 3.2.1
lda	=max(1, m)	=max(1, size(A, 1))

Equations in Version 3.2	Equations in Version 3.2.1
external "Fortran 77" dlange2(norm, m, n, A, lda, work, anorm);	external "Fortran 77" anorm = dlange( norm, m, n, A, lda, work);

---

function Math.Matrices.LAPACK.dgeevx

Component	Version 3.2	Version 3.2.1
iwork		Present

Equations in Version 3.2	Equations in Version 3.2.1
external "Fortran 77" dgeevx( "B", "V", "V", "E", n, AS, n, alphaReal, alphaImag, lEigenVectors, n, rEigenVectors, n, ilo, ihi, scale, abnrm, rconde, rcondv, work, lwork, info);	external "Fortran 77" dgeevx( "B", "V", "V", "E", n, AS, n, alphaReal, alphaImag, lEigenVectors, n, rEigenVectors, n, ilo, ihi, scale, abnrm, rconde, rcondv, work, lwork, iwork, info);

---

function Math.Matrices.Utilities.eigenvaluesHessenberg

Component	Version 3.2	Version 3.2.1
n	Present
ilo	Present
ihi	Present
Z	Present

---

function Math.Nonlinear.Examples.quadratureLobatto1

Equations in Version 3.2	Equations in Version 3.2.1
... I_err = abs(I_numerical - I_analytical);
print("Function 1 ( integral(sin(x)*dx) from x=0 to x=1): "); ...

---

function Math.Nonlinear.Examples.quadratureLobatto2

Equations in Version 3.2	Equations in Version 3.2.1
... I[3] = Modelica_3_2.Math.Nonlinear.quadratureLobatto(            &nbspfunction      &nbspModelica_3_2.Math.Nonlinear.Examples.UtilityFunctions.fun6(k=k),            &nbspa3,            &nbspb3,            &nbspTolerance);
print("Function 1 (integral(sin(x)*dx)): "); ...

---

function Math.Nonlinear.Examples.solveNonlinearEquations1

Equations in Version 3.2	Equations in Version 3.2.1
... u_err = abs(u_numerical - u_analytical);
print("Solve 3 nonlinear equations with relative tolerance = " + String(tolerance) +"\n"); ...

---

function Math.Nonlinear.Examples.solveNonlinearEquations2

Equations in Version 3.2	Equations in Version 3.2.1
... u[3] = Modelica_3_2.Math.Nonlinear.solveOneNonlinearEquation(            &nbspfunction      &nbspModelica_3_2.Math.Nonlinear.Examples.UtilityFunctions.fun3(p=p, m=       &nbspm), u_min3,            &nbspu_max3,            &nbsptolerance);
print("Solve 3 nonlinear equations with relative tolerance = " + String(tolerance) +"\n"); ...

---

function Math.Nonlinear.solveOneNonlinearEquation

Equations in Version 3.2	Equations in Version 3.2.1
... if fa > 0.0 and fb > 0.0 or fa < 0.0 and fb < 0.0 then
error( "The arguments u_min and u_max to solveOneNonlinearEquation(..)\n" + "do not bracket the root of the single non-linear equation:\n" + " u_min = " + String(u_min) + "\n" + " u_max = " + String(u_max) + "\n" + " fa = f(u_min) = " + String(fa) + "\n" + " fb = f(u_max) = " + String(fb) + "\n" + "fa and fb must have opposite sign which is not the case");	error( "The arguments u_min and u_max provided in the function call\n"+ " solveOneNonlinearEquation(f,u_min,u_max)\n" + "do not bracket the root of the single non-linear equation 0=f(u):\n" + " u_min = " + String(u_min) + "\n" + " u_max = " + String(u_max) + "\n" + " fa = f(u_min) = " + String(fa) + "\n" + " fb = f(u_max) = " + String(fb) + "\n" + "fa and fb must have opposite sign which is not the case");
end if; ...

---

function Math.BooleanVectors.oneTrue

Component	Version 3.2	Version 3.2.1
count	Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
for i in 1:size(b,1) loop	result := countTrue(b) == 1;
count = if b[i] then count+1 else count;
end for; result = count == 1;

---

function Math.atan3

Component	Version 3.2	Version 3.2.1
pi		constant
pi2		Present

Equations in Version 3.2	Equations in Version 3.2.1
... w :=Math.atan2(u1, u2);
y = w + 2*pi*div(abs(w-y0)+pi,2*pi)*(if y0 > w then +1 else -1);	if y0 == 0 then
	y = w;
	else y = w + pi2*integer((pi+y0-w)/pi2); end if;

---

model Utilities.Examples.readRealParameterModel

Component	Version 3.2	Version 3.2.1
file	="Modelica/Resources/Data/Utilities/Examples_readRealParameters.txt"	=Modelica.Utilities.Files.loadResource("modelica://Modelica/Resources/Data/Utilities/Examples_readRealParameters.txt")

---

function Utilities.Strings.findLast

Component	Version 3.2	Version 3.2.1
iMax		Present

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
i := if startIndex == 0 then lenString-lenSearchString+1 else startIndex;	i := if startIndex == 0 or startIndex > iMax then iMax else startIndex;
index = 0; ...

---

package Utilities.Internal.FileSystem

Component	Version 3.2	Version 3.2.1
package	protected

---

package Constants

Component	Version 3.2	Version 3.2.1
eps	=1.e-15	=ModelicaServices.Machine.eps
small	=1.e-60	=ModelicaServices.Machine.small
inf	=1.e+60	=ModelicaServices.Machine.inf
Integer_inf	=2147483647	=ModelicaServices.Machine.Integer_inf

---

function SIunits.Conversions.to_cm2

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
cm2 := 0.0001*m2;	cm2 := 10000*m2;

---

function SIunits.Conversions.from_cm2

Equations in Version 3.2	Equations in Version 3.2.1
algorithm
m2 :=10000*cm2;	m2 := 0.0001*cm2;

---

Class	Version 3.2	Version 3.2.1
Modelica_3_2.Blocks.Logical.And	model	block
Modelica_3_2.Blocks.Logical.Or	model	block
Modelica_3_2.Blocks.Logical.Xor	model	block
Modelica_3_2.Blocks.Logical.Nor	model	block
Modelica_3_2.Blocks.Logical.Nand	model	block
Modelica_3_2.Blocks.Logical.Not	model	block
Modelica_3_2.Blocks.Logical.Pre	model	block
Modelica_3_2.Blocks.Logical.Edge	model	block
Modelica_3_2.Blocks.Logical.FallingEdge	model	block
Modelica_3_2.Blocks.Logical.Change	model	block
Modelica_3_2.Blocks.Sources.CombiTimeTable	model	block
Modelica_3_2.Blocks.Tables.CombiTable1D	model	block
Modelica_3_2.Blocks.Tables.CombiTable1Ds	model	block
Modelica_3_2.Blocks.Tables.CombiTable2D	model	block
Modelica_3_2.Icons.TypeComplex	record	operator	record
Modelica_3_2.Icons.SignalBus	connector	expandable	connector
Modelica_3_2.Icons.SignalSubBus	connector	expandable	connector
Modelica_3_2.SIunits.ComplexCurrent	record	operator	record
Modelica_3_2.SIunits.ComplexCurrentSlope	record	operator	record
Modelica_3_2.SIunits.ComplexCurrentDensity	record	operator	record
Modelica_3_2.SIunits.ComplexElectricPotential	record	operator	record
Modelica_3_2.SIunits.ComplexPotentialDifference	record	operator	record
Modelica_3_2.SIunits.ComplexVoltage	record	operator	record
Modelica_3_2.SIunits.ComplexVoltageSlope	record	operator	record
Modelica_3_2.SIunits.ComplexElectricFieldStrength	record	operator	record
Modelica_3_2.SIunits.ComplexElectricFluxDensity	record	operator	record
Modelica_3_2.SIunits.ComplexElectricFlux	record	operator	record
Modelica_3_2.SIunits.ComplexMagneticFieldStrength	record	operator	record
Modelica_3_2.SIunits.ComplexMagneticPotential	record	operator	record
Modelica_3_2.SIunits.ComplexMagneticPotentialDifference	record	operator	record
Modelica_3_2.SIunits.ComplexMagnetomotiveForce	record	operator	record
Modelica_3_2.SIunits.ComplexMagneticFluxDensity	record	operator	record
Modelica_3_2.SIunits.ComplexMagneticFlux	record	operator	record
Modelica_3_2.SIunits.ComplexReluctance	record	operator	record
Modelica_3_2.SIunits.ComplexImpedance	record	operator	record
Modelica_3_2.SIunits.ComplexAdmittance	record	operator	record
Modelica_3_2.SIunits.ComplexPower	record	operator	record
package Modelica_3_2.UsersGuide.Conventions.ModelicaCode	Present
class Modelica_3_2.UsersGuide.ReleaseNotes.Version_3_2_BugFixes	Present
class Modelica_3_2.UsersGuide.ModelicaLicense2	Present
connector Modelica_3_2.StateGraph.Examples.Utilities.inflow1	Present
connector Modelica_3_2.StateGraph.Examples.Utilities.inflow2	Present
connector Modelica_3_2.StateGraph.Examples.Utilities.outflow1	Present
connector Modelica_3_2.StateGraph.Examples.Utilities.outflow2	Present
package Modelica_3_2.Magnetic.FundamentalWave.BasicMachines.Functions	Present
block Modelica_3_2.Fluid.Examples.AST_BatchPlant.BaseClasses.TriggeredTrapezoid	Present
function Modelica_3_2.Fluid.Machines.BaseClasses.assertPositiveDifference	Present
package Modelica_3_2.Media.Examples.TestOnly.TestMedia	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.IndependentVariables	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.Init	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.ReferenceEnthalpy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.ReferenceEntropy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.pd	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Choices.Th	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.AbsolutePressure	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Density	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DynamicViscosity	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.EnthalpyFlowRate	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.MassFraction	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.MoleFraction	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.MolarMass	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.MolarVolume	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.IsentropicExponent	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SpecificEnergy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SpecificInternalEnergy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SpecificEnthalpy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SpecificEntropy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SpecificHeatCapacity	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.SurfaceTension	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.Temperature	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.ThermalConductivity	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.PrandtlNumber	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.VelocityOfSound	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.ExtraProperty	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.CumulativeExtraProperty	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.ExtraPropertyFlowRate	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.IsobaricExpansionCoefficient	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DipoleMoment	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DerDensityByPressure	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DerDensityByEnthalpy	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DerEnthalpyByPressure	Present
type Modelica_3_2.Media.Interfaces.PartialMedium.DerDensityByTemperature	Present
record Modelica_3_2.Media.Interfaces.PartialMixtureMedium.FluidConstants	Present
record Modelica_3_2.Media.Interfaces.PartialTwoPhaseMedium.FluidLimits	Present
record Modelica_3_2.Media.Interfaces.PartialTwoPhaseMedium.FluidConstants	Present
record Modelica_3_2.Media.Interfaces.PartialTwoPhaseMedium.SaturationProperties	Present
type Modelica_3_2.Media.Interfaces.PartialTwoPhaseMedium.FixedPhase	Present
record Modelica_3_2.Media.Interfaces.PartialSimpleIdealGasMedium.FluidConstants	Present
record Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.FluidConstants	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.cp_T	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.cp_Tlow	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.cp_Tlow_der	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_T	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_T_der	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.h_Tlow_der	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.s0_T	Present
function Modelica_3_2.Media.IdealGases.Common.SingleGasNasa.s0_Tlow	Present
record Modelica_3_2.Media.IdealGases.Common.MixtureGasNasa.FluidConstants	Present
package Modelica_3_2.Utilities.Internal.PartialModelicaServices	Present
package Modelica.UsersGuide.Conventions.ModelicaCode		Present
class Modelica.UsersGuide.ReleaseNotes.Version_3_2_1		Present
class Modelica.UsersGuide.ModelicaLicense2		Present
block Modelica.Blocks.Logical.RSFlipFlop		Present
block Modelica.Blocks.Math.MinMax		Present
block Modelica.Blocks.Math.LinearDependency		Present
block Modelica.Blocks.Nonlinear.SlewRateLimiter		Present
block Modelica.Blocks.Sources.Cosine		Present
class Modelica.Blocks.Types.ExternalCombiTimeTable		Present
class Modelica.Blocks.Types.ExternalCombiTable1D		Present
class Modelica.Blocks.Types.ExternalCombiTable2D		Present
package Modelica.Blocks.Icons		Present
connector Modelica.StateGraph.Examples.Utilities.Inflow1		Present
connector Modelica.StateGraph.Examples.Utilities.Inflow2		Present
connector Modelica.StateGraph.Examples.Utilities.Outflow1		Present
connector Modelica.StateGraph.Examples.Utilities.Outflow2		Present
model Modelica.Electrical.Analog.Sources.CosineVoltage		Present
model Modelica.Electrical.Analog.Sources.CosineCurrent		Present
model Modelica.Electrical.Digital.Examples.MUX2x1		Present
model Modelica.Electrical.Digital.Examples.RAM		Present
block Modelica.Electrical.Digital.Converters.LogicToX01		Present
block Modelica.Electrical.Digital.Converters.LogicToX01Z		Present
package Modelica.Electrical.Digital.Memories		Present
package Modelica.Electrical.Digital.Multiplexers		Present
model Modelica.Electrical.Machines.Examples.AsynchronousInductionMachines.AIMC_Initialize		Present
model Modelica.Electrical.Machines.Examples.SynchronousInductionMachines.SMPM_VoltageSource		Present
model Modelica.Electrical.Machines.Examples.SynchronousInductionMachines.SMEE_Rectifier		Present
model Modelica.Electrical.Machines.BasicMachines.Components.PermanentMagnetWithLosses		Present
model Modelica.Electrical.Machines.Losses.InductionMachines.PermanentMagnetLosses		Present
record Modelica.Electrical.Machines.Losses.PermanentMagnetLossParameters		Present
package Modelica.Electrical.Machines.Utilities.ParameterRecords		Present
model Modelica.Electrical.Machines.Utilities.VoltageController		Present
block Modelica.Electrical.Machines.Utilities.ToDQ		Present
block Modelica.Electrical.Machines.Utilities.FromDQ		Present
model Modelica.Electrical.MultiPhase.Examples.TestSensors		Present
model Modelica.Electrical.MultiPhase.Sensors.VoltageQuasiRMSSensor		Present
model Modelica.Electrical.MultiPhase.Sensors.CurrentQuasiRMSSensor		Present
model Modelica.Electrical.MultiPhase.Sources.CosineVoltage		Present
model Modelica.Electrical.MultiPhase.Sources.CosineCurrent		Present
package Modelica.Electrical.MultiPhase.Blocks		Present
package Modelica.Electrical.MultiPhase.Functions		Present
model Modelica.Electrical.Spice3.Examples.CoupledInductors		Present
model Modelica.Electrical.Spice3.Examples.CascodeCircuit		Present
model Modelica.Electrical.Spice3.Examples.Spice3BenchmarkDifferentialPair		Present
model Modelica.Electrical.Spice3.Examples.Spice3BenchmarkMosfetCharacterization		Present
model Modelica.Electrical.Spice3.Examples.Spice3BenchmarkRtlInverter		Present
model Modelica.Electrical.Spice3.Examples.Spice3BenchmarkFourBitBinaryAdder		Present
model Modelica.Electrical.Spice3.Basic.K_CoupledInductors		Present
model Modelica.Electrical.Spice3.Semiconductors.M_NMOS2		Present
model Modelica.Electrical.Spice3.Semiconductors.M_PMOS2		Present
record Modelica.Electrical.Spice3.Semiconductors.ModelcardMOS2		Present
model Modelica.Electrical.Spice3.Semiconductors.J_PJFJFET		Present
model Modelica.Electrical.Spice3.Semiconductors.J_NJFJFET		Present
record Modelica.Electrical.Spice3.Semiconductors.ModelcardJFET		Present
model Modelica.Electrical.Spice3.Semiconductors.C_Capacitor		Present
record Modelica.Electrical.Spice3.Semiconductors.ModelcardCAPACITOR		Present
connector Modelica.Electrical.Spice3.Interfaces.InductiveCouplePinIn		Present
connector Modelica.Electrical.Spice3.Interfaces.InductiveCouplePinOut		Present
model Modelica.Electrical.Spice3.Interfaces.ConditionalSubstrate		Present
function Modelica.Electrical.Spice3.Internal.Functions.junction2SPICE3MOSFETRevised		Present
function Modelica.Electrical.Spice3.Internal.Functions.junctionCapRevised		Present
function Modelica.Electrical.Spice3.Internal.Functions.saturationCurDepTempSPICE3JFET		Present
function Modelica.Electrical.Spice3.Internal.Functions.capDepGeom		Present
function Modelica.Electrical.Spice3.Internal.Functions.junction2SPICE3BJT		Present
function Modelica.Electrical.Spice3.Internal.Functions.energyGapDepTemp_old		Present
function Modelica.Electrical.Spice3.Internal.SpiceRoot.limitJunctionVoltageRevised		Present
function Modelica.Electrical.Spice3.Internal.SpiceRoot.initJunctionVoltagesRevised		Present
function Modelica.Electrical.Spice3.Internal.Mosfet.mosfetRenameParametersDev		Present
function Modelica.Electrical.Spice3.Internal.Mos.mos2CalcInitEquationsRevised		Present
function Modelica.Electrical.Spice3.Internal.Mos.mos2CalcCalcTempDependenciesRevised		Present
function Modelica.Electrical.Spice3.Internal.Mos.mos2CalcNoBypassCodeRevised		Present
function Modelica.Electrical.Spice3.Internal.Mos2.mos2ModelLineParamsInitEquationsRevised		Present
function Modelica.Electrical.Spice3.Internal.Mos2.drainCurRevised		Present
function Modelica.Electrical.Spice3.Internal.Mos2.mos2RenameParametersRevised		Present
model Modelica.Electrical.Spice3.Internal.BJT2		Present
record Modelica.Electrical.Spice3.Internal.ModelcardBJT2		Present
model Modelica.Electrical.Spice3.Internal.JFET		Present
record Modelica.Electrical.Spice3.Internal.ModelcardJFET		Present
model Modelica.Electrical.Spice3.Internal.C_SEMI		Present
record Modelica.Electrical.Spice3.Internal.ModelcardC		Present
record Modelica.Electrical.Spice3.Internal.MaterialParameters		Present
package Modelica.Electrical.Spice3.Internal.Bjt		Present
package Modelica.Electrical.Spice3.Internal.Fet		Present
package Modelica.Electrical.Spice3.Internal.Jfet		Present
package Modelica.Electrical.Spice3.Internal.Csemiconductor		Present
package Modelica.Electrical.Spice3.Types		Present
class Modelica.Magnetic.FundamentalWave.UsersGuide.MultiPhase		Present
class Modelica.Magnetic.FundamentalWave.UsersGuide.Parameters		Present
model Modelica.Magnetic.FundamentalWave.Examples.Components.SinglePhaseInductance		Present
model Modelica.Magnetic.FundamentalWave.Examples.Components.MultiPhaseInductance		Present
model Modelica.Magnetic.FundamentalWave.Examples.BasicMachines.AIMC_DOL_MultiPhase		Present
model Modelica.Magnetic.FundamentalWave.Examples.BasicMachines.AIMS_Start_MultiPhase		Present
model Modelica.Magnetic.FundamentalWave.Examples.BasicMachines.SMPM_Inverter_MultiPhase		Present
model Modelica.Magnetic.FundamentalWave.Examples.BasicMachines.SMEE_Generator_MultiPhase		Present
model Modelica.Magnetic.FundamentalWave.Examples.BasicMachines.SMR_Inverter_MultiPhase		Present
model Modelica.Magnetic.FundamentalWave.BasicMachines.Components.PermanentMagnet		Present
package Modelica.Mechanics.MultiBody.Examples.Constraints		Present
model Modelica.Mechanics.MultiBody.Joints.Internal.InitPosition		Present
model Modelica.Mechanics.MultiBody.Joints.Internal.InitAngle		Present
model Modelica.Mechanics.MultiBody.Joints.Internal.InitAngularVelocity		Present
package Modelica.Mechanics.MultiBody.Joints.Constraints		Present
model Modelica.Mechanics.MultiBody.Sensors.TransformAbsoluteVector		Present
model Modelica.Mechanics.MultiBody.Sensors.TransformRelativeVector		Present
class Modelica.Mechanics.MultiBody.Icons.MotorIcon		Present
class Modelica.Mechanics.Rotational.UsersGuide.StateSelection		Present
model Modelica.Mechanics.Rotational.Examples.GenerationOfFMUs		Present
package Modelica.Mechanics.Rotational.Examples.Utilities		Present
model Modelica.Mechanics.Rotational.Components.TorqueToAngleAdaptor		Present
model Modelica.Mechanics.Rotational.Components.AngleToTorqueAdaptor		Present
model Modelica.Mechanics.Rotational.Sensors.MultiSensor		Present
model Modelica.Mechanics.Translational.Sensors.MultiSensor		Present
package Modelica.Fluid.Machines.BaseClasses.PumpMonitoring		Present
model Modelica.Fluid.Sources.BaseClasses.PartialFlowSource		Present
model Modelica.Fluid.Sensors.BaseClasses.PartialRelativeSensor		Present
model Modelica.Fluid.Sensors.MassFractions		Present
model Modelica.Fluid.Sensors.MassFractionsTwoPort		Present
type Modelica.Fluid.Dissipation.Utilities.Types.MolarMass_gpmol		Present
package Modelica.Media.Examples.ReferenceAir		Present
package Modelica.Media.Examples.R134a		Present
package Modelica.Media.Interfaces.PartialRealCondensingGases		Present
package Modelica.Media.Interfaces.Choices		Present
package Modelica.Media.Interfaces.Types		Present
record Modelica.Media.Common.FundamentalConstants		Present
record Modelica.Media.Common.AuxiliaryProperties		Present
record Modelica.Media.Common.GibbsDerivs2		Present
record Modelica.Media.Common.NewtonDerivatives_dT		Present
function Modelica.Media.Common.Gibbs2_ph		Present
function Modelica.Media.Common.Gibbs2_dT		Present
function Modelica.Media.Common.Gibbs2_ps		Present
function Modelica.Media.Air.MoistAir.Utilities.smoothMax		Present
function Modelica.Media.Air.MoistAir.Utilities.smoothMax_der		Present
function Modelica.Media.Air.MoistAir.velocityOfSound		Present
function Modelica.Media.Air.MoistAir.isobaricExpansionCoefficient		Present
function Modelica.Media.Air.MoistAir.isothermalCompressibility		Present
function Modelica.Media.Air.MoistAir.density_derp_h		Present
function Modelica.Media.Air.MoistAir.density_derh_p		Present
function Modelica.Media.Air.MoistAir.density_derp_T		Present
function Modelica.Media.Air.MoistAir.density_derT_p		Present
function Modelica.Media.Air.MoistAir.density_derX		Present
function Modelica.Media.Air.MoistAir.molarMass		Present
function Modelica.Media.Air.MoistAir.T_psX		Present
function Modelica.Media.Air.MoistAir.setState_psX		Present
function Modelica.Media.Air.MoistAir.s_pTX		Present
function Modelica.Media.Air.MoistAir.s_pTX_der		Present
function Modelica.Media.Air.MoistAir.isentropicEnthalpy		Present
package Modelica.Media.Air.ReferenceAir		Present
package Modelica.Media.Air.ReferenceMoistAir		Present
package Modelica.Media.IdealGases.Common.Functions		Present
function Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange		Present
function Modelica.Media.Incompressible.TableBased.Polynomials_Temp.evaluateWithRange_der		Present
package Modelica.Media.R134a		Present
model Modelica.Thermal.HeatTransfer.Components.ThermalResistor		Present
model Modelica.Thermal.HeatTransfer.Components.ConvectiveResistor		Present
function Modelica.Math.Vectors.normalizeWithAssert		Present
function Modelica.Math.BooleanVectors.countTrue		Present
function Modelica.Math.BooleanVectors.enumerate		Present
function Modelica.Math.BooleanVectors.index		Present
package Modelica.Math.Icons		Present
function Modelica.Math.isPowerOf2		Present
function Modelica.Utilities.Files.loadResource		Present
function Modelica.Utilities.Strings.isEmpty		Present
package Modelica.Utilities.Internal.PartialModelicaServices		Present
package Modelica.Icons.UtilitiesPackage		Present
package Modelica.Icons.TypesPackage		Present
package Modelica.Icons.IconsPackage		Present
package Modelica.Icons.InternalPackage		Present
function Modelica.SIunits.Conversions.to_unit1		Present
package Modelica.SIunits.Icons		Present
type Modelica.SIunits.PressureDifference		Present
type Modelica.SIunits.DerPressureByDensity		Present
type Modelica.SIunits.DerPressureByTemperature		Present
type Modelica.SIunits.LoudnessLevel		Present
type Modelica.SIunits.Loudness		Present
type Modelica.SIunits.MolarDensity		Present
type Modelica.SIunits.MolarEnergy		Present
type Modelica.SIunits.MolarEnthalpy		Present
type Modelica.SIunits.TimeAging		Present
type Modelica.SIunits.ChargeAging		Present
type Modelica.SIunits.PerUnit		Present