Buildings.Fluid.Interfaces
Package with interfaces for fluid models
Information
This package contains basic classes that are used to build component models that change the state of the fluid. The classes are not directly usable, but can be extended when building a new model.
Extends from Modelica.Icons.InterfacesPackage (Icon for packages containing interfaces).
Package Content
| Name | Description |
|---|---|
 UsersGuide
|
User's Guide |
 ConservationEquation
|
Lumped volume with mass and energy balance |
 EightPort
|
Partial model with eight ports |
 EightPortHeatMassExchanger
|
Model transporting four fluid streams between eight ports with storing mass or energy |
 FourPortHeatMassExchanger
|
Model transporting two fluid streams between four ports with storing mass or energy |
 LumpedVolumeDeclarations
|
Declarations for lumped volumes |
| PartialEightPortInterface
|
Partial model with eight ports and declaration of quantities that are used by many models |
 PartialFourPort
|
Partial model with four ports |
| PartialFourPortInterface
|
Partial model with four ports and declaration of quantities that are used by many models |
 PartialFourPortParallel
|
Partial model with four ports for components with parallel flow |
 PartialTwoPort
|
Partial component with two ports |
| PartialTwoPortInterface
|
Partial model with two ports and declaration of quantities that are used by many models |
| PartialTwoPortTransport
|
Partial element transporting fluid between two ports without storage of mass or energy |
 PartialTwoPortVector
|
Partial component with two ports, one of which being vectorized |
 PrescribedOutlet
|
Component that assigns the outlet fluid property at port_a based on an input signal |
| StaticFourPortHeatMassExchanger
|
Partial model transporting two fluid streams between four ports without storing mass or energy |
 StaticTwoPortConservationEquation
|
Partial model for static energy and mass conservation equations |
| StaticTwoPortHeatMassExchanger
|
Partial model transporting fluid between two ports without storing mass or energy |
 TwoPortHeatMassExchanger
|
Partial model transporting one fluid stream with storing mass or energy |
 EightPortFlowResistanceParameters
|
Parameters for flow resistance for models with height ports |
| FourPortFlowResistanceParameters
|
Parameters for flow resistance for models with four ports |
| TwoPortFlowResistanceParameters
|
Parameters for flow resistance for models with two ports |
 Examples
|
Collection of models that illustrate model use and test models |
Buildings.Fluid.Interfaces.ConservationEquation
Lumped volume with mass and energy balance
Information
Basic model for an ideally mixed fluid volume with the ability to store mass and energy. It implements a dynamic or a steady-state conservation equation for energy and mass fractions. The model has zero pressure drop between its ports.
If the constant simplify_mWat_flow = true then adding
moisture does not increase the mass of the volume or the leaving mass flow rate.
It does however change the mass fraction medium.Xi.
This allows to decouple the moisture balance from the pressure drop equations.
If simplify_mWat_flow = false, then
the outlet mass flow rate is
mout = min (1 + Δ Xw),
where
Δ Xw is the change in water vapor mass
fraction across the component. In this case,
this component couples
the energy calculation to the
pressure drop versus mass flow rate calculations.
However, in typical building HVAC systems,
Δ Xw < 0.005 kg/kg.
Hence, by tolerating a relative error of 0.005 in the mass balance,
one can decouple these equations.
Decoupling these equations avoids having
to compute the energy balance of the humidifier
and its upstream components when solving for the
pressure drop of downstream components.
Therefore, the default value is simplify_mWat_flow = true.
Typical use and important parameters
Set the parameter use_mWat_flow_in=true to enable an
input connector for mWat_flow.
Otherwise, the model uses mWat_flow = 0.
If the constant simplify_mWat_flow = true, which is its default value,
then the equation
port_a.m_flow + port_b.m_flow = - mWat_flow;
is simplified as
port_a.m_flow + port_b.m_flow = 0;
This causes an error in the mass balance of about 0.5%, but generally leads to
simpler equations because the pressure drop equations are then decoupled from the
mass exchange in this component.
The model
Buildings.Fluid.MixingVolumes.Validation.MixingVolumeAdiabaticCooling
shows that the relative error on the temperature difference between these
two options of simplify_mWat_flow is less than
0.1%.
Implementation
When extending or instantiating this model, the input
fluidVolume, which is the actual volume occupied by the fluid,
needs to be assigned.
For most components, this can be set to a parameter.
-
Q_flow, which is the sensible plus latent heat flow rate added to the medium, -
mWat_flow, which is the moisture mass flow rate added to the medium, and -
C_flow, which is the trace substance mass flow rate added to the medium.
The model can be used as a dynamic model or as a steady-state model. However, for a steady-state model with exactly two fluid ports connected, the model Buildings.Fluid.Interfaces.StaticTwoPortConservationEquation provides a more efficient implementation.
For a model that instantiates this model, see Buildings.Fluid.MixingVolumes.MixingVolume.
Extends from Buildings.Fluid.Interfaces.LumpedVolumeDeclarations (Declarations for lumped volumes).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Volume | fluidVolume | Volume [m3] | |
| Dynamics | |||
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Type of energy balance: dynamic (3 initialization options) or steady state |
| Real | mSenFac | 1 | Factor for scaling the sensible thermal mass of the volume |
| Advanced | |||
| Dynamics | |||
| Dynamics | massDynamics | energyDynamics | Type of mass balance: dynamic (3 initialization options) or steady state, must be steady state if energyDynamics is steady state |
| Boolean | initialize_p | not Medium.singleState | = true to set up initial equations for pressure |
| Boolean | use_mWat_flow | false | Set to true to enable input connector for moisture mass flow rate |
| Boolean | use_C_flow | false | Set to true to enable input connector for trace substance |
| Initialization | |||
| AbsolutePressure | p_start | Medium.p_default | Start value of pressure [Pa] |
| Temperature | T_start | Medium.T_default | Start value of temperature [K] |
| MassFraction | X_start[Medium.nX] | Medium.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C_start[Medium.nC] | fill(0, Medium.nC) | Start value of trace substances |
| ExtraProperty | C_nominal[Medium.nC] | fill(1E-2, Medium.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
Connectors
| Type | Name | Description |
|---|---|---|
| input RealInput | Q_flow | Sensible plus latent heat flow rate transferred into the medium [W] |
| input RealInput | mWat_flow | Moisture mass flow rate added to the medium [kg/s] |
| input RealInput | C_flow[Medium.nC] | Trace substance mass flow rate added to the medium |
| output RealOutput | hOut | Leaving specific enthalpy of the component [J/kg] |
| output RealOutput | XiOut[Medium.nXi] | Leaving species concentration of the component [1] |
| output RealOutput | COut[Medium.nC] | Leaving trace substances of the component |
| output RealOutput | UOut | Internal energy of the component [J] |
| output RealOutput | mXiOut[Medium.nXi] | Species mass of the component [kg] |
| output RealOutput | mOut | Mass of the component [kg] |
| output RealOutput | mCOut[Medium.nC] | Trace substance mass of the component [kg] |
| VesselFluidPorts_b | ports[nPorts] | Fluid inlets and outlets |
Modelica definition
model ConservationEquation "Lumped volume with mass and energy balance"
extends Buildings.Fluid.Interfaces.LumpedVolumeDeclarations;
// Constants
parameter Boolean initialize_p = not Medium.singleState
"= true to set up initial equations for pressure";
constant Boolean simplify_mWat_flow = true
"Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1";
// Port definitions
parameter Integer nPorts=0 "Number of ports";
parameter Boolean use_mWat_flow = false
"Set to true to enable input connector for moisture mass flow rate";
parameter Boolean use_C_flow = false
"Set to true to enable input connector for trace substance";
Modelica.Blocks.Interfaces.RealInput Q_flow(unit="W")
"Sensible plus latent heat flow rate transferred into the medium";
Modelica.Blocks.Interfaces.RealInput mWat_flow(final quantity="MassFlowRate",
unit="kg/s")
if use_mWat_flow "Moisture mass flow rate added to the medium";
Modelica.Blocks.Interfaces.RealInput[Medium.nC] C_flow
if use_C_flow "Trace substance mass flow rate added to the medium";
// Outputs that are needed in models that use this model
Modelica.Blocks.Interfaces.RealOutput hOut(unit="J/kg",
start=hStart)
"Leaving specific enthalpy of the component";
Modelica.Blocks.Interfaces.RealOutput XiOut[Medium.nXi](each unit="1",
each min=0,
each max=1)
"Leaving species concentration of the component";
Modelica.Blocks.Interfaces.RealOutput COut[Medium.nC](each min=0)
"Leaving trace substances of the component";
Modelica.Blocks.Interfaces.RealOutput UOut(unit="J")
"Internal energy of the component";
Modelica.Blocks.Interfaces.RealOutput mXiOut[Medium.nXi](each min=0, each unit="kg")
"Species mass of the component";
Modelica.Blocks.Interfaces.RealOutput mOut(min=0, unit="kg")
"Mass of the component";
Modelica.Blocks.Interfaces.RealOutput mCOut[Medium.nC](each min=0, each unit="kg")
"Trace substance mass of the component";
Modelica.Fluid.Vessels.BaseClasses.VesselFluidPorts_b ports[nPorts](
redeclare each final package Medium = Medium) "Fluid inlets and outlets";
// Set nominal attributes where literal values can be used.
Medium.BaseProperties medium(
p(start=p_start),
h(start=hStart),
T(start=T_start),
Xi(
each stateSelect=if medium.preferredMediumStates then StateSelect.prefer else StateSelect.default,
start=X_start[1:Medium.nXi]),
X(start=X_start),
d(start=rho_start)) "Medium properties";
Modelica.Units.SI.Energy U(
start=fluidVolume*rho_start*
Medium.specificInternalEnergy(Medium.setState_pTX(
T=T_start,
p=p_start,
X=X_start[1:Medium.nXi])) + (T_start - Medium.reference_T)*CSen,
nominal=1E5) "Internal energy of fluid";
Modelica.Units.SI.Mass m(start=fluidVolume*rho_start, stateSelect=if
massDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
StateSelect.default else StateSelect.prefer) "Mass of fluid";
Modelica.Units.SI.Mass[Medium.nXi] mXi(
each stateSelect=StateSelect.never,
start=fluidVolume*rho_start*X_start[1:Medium.nXi])
"Masses of independent components in the fluid";
Modelica.Units.SI.Mass[Medium.nC] mC(start=fluidVolume*rho_start*C_start)
"Masses of trace substances in the fluid";
// C need to be added here because unlike for Xi, which has medium.Xi,
// there is no variable medium.C
Medium.ExtraProperty C[Medium.nC](nominal=C_nominal)
"Trace substance mixture content";
Modelica.Units.SI.MassFlowRate mb_flow "Mass flows across boundaries";
Modelica.Units.SI.MassFlowRate[Medium.nXi] mbXi_flow
"Substance mass flows across boundaries";
Medium.ExtraPropertyFlowRate[Medium.nC] mbC_flow
"Trace substance mass flows across boundaries";
Modelica.Units.SI.EnthalpyFlowRate Hb_flow
"Enthalpy flow across boundaries or energy source/sink";
// Parameters that need to be defined by an extending class
parameter Modelica.Units.SI.Volume fluidVolume "Volume";
final parameter Modelica.Units.SI.HeatCapacity CSen=(mSenFac - 1)*rho_default
*cp_default*fluidVolume
"Aditional heat capacity for implementing mFactor";
protected
Medium.EnthalpyFlowRate ports_H_flow[nPorts];
Modelica.Units.SI.MassFlowRate ports_mXi_flow[nPorts,Medium.nXi];
Medium.ExtraPropertyFlowRate ports_mC_flow[nPorts,Medium.nC];
parameter Modelica.Units.SI.SpecificHeatCapacity cp_default=
Medium.specificHeatCapacityCp(state=state_default)
"Heat capacity, to compute additional dry mass";
parameter Modelica.Units.SI.Density rho_start=Medium.density(
Medium.setState_pTX(
T=T_start,
p=p_start,
X=X_start[1:Medium.nXi])) "Density, used to compute fluid mass";
// Parameter for avoiding extra overhead calculations when CSen==0
final parameter Boolean computeCSen = abs(mSenFac-1) > Modelica.Constants.eps;
final parameter Medium.ThermodynamicState state_default = Medium.setState_pTX(
T=Medium.T_default,
p=Medium.p_default,
X=Medium.X_default[1:Medium.nXi]) "Medium state at default values";
// Density at medium default values, used to compute the size of control volumes
final parameter Modelica.Units.SI.Density rho_default=Medium.density(state=
state_default) "Density, used to compute fluid mass";
// Parameter that is used to construct the vector mXi_flow
final parameter Real s[Medium.nXi] = {if Modelica.Utilities.Strings.isEqual(
string1=Medium.substanceNames[i],
string2="Water",
caseSensitive=false)
then 1 else 0 for i in 1:Medium.nXi}
"Vector with zero everywhere except where species is";
parameter Modelica.Units.SI.SpecificEnthalpy hStart=
Medium.specificEnthalpy_pTX(
p_start,
T_start,
X_start) "Start value for specific enthalpy";
// Set _simplify_mWat_flow == false for Glycol47; otherwise Dymola 2018FD01
// cannot differentiate the equations.
constant Boolean _simplify_mWat_flow = simplify_mWat_flow and Medium.nX > 1
"If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified";
// Conditional connectors
Modelica.Blocks.Interfaces.RealInput mWat_flow_internal(unit="kg/s")
"Needed to connect to conditional connector";
Modelica.Blocks.Interfaces.RealInput C_flow_internal[Medium.nC]
"Needed to connect to conditional connector";
initial equation
// Assert that the substance with name 'water' has been found.
if use_mWat_flow then
assert(Medium.nXi == 0 or abs(sum(s) - 1) < 1e-5, "In " + getInstanceName()
+ ":
If Medium.nXi > 1, then substance 'water' must be present for one component of '"
+ Medium.mediumName + "'.
Check medium model.");
end if;
// Make sure that if energyDynamics is SteadyState, then
// massDynamics is also SteadyState.
// Otherwise, the system of ordinary differential equations may be inconsistent.
if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
assert(massDynamics == energyDynamics, "In " + getInstanceName() + ":
If 'massDynamics == Modelica.Fluid.Types.Dynamics.SteadyState', then it is
required that 'energyDynamics==Modelica.Fluid.Types.Dynamics.SteadyState'.
Otherwise, the system of equations may not be consistent.
You need to select other parameter values.");
end if;
// initialization of balances
if energyDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
medium.T = T_start;
else
if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(medium.T) = 0;
end if;
end if;
if massDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
if initialize_p then
medium.p = p_start;
end if;
else
if massDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
if initialize_p then
der(medium.p) = 0;
end if;
end if;
end if;
if substanceDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
medium.Xi = X_start[1:Medium.nXi];
else
if substanceDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(medium.Xi) = zeros(Medium.nXi);
end if;
end if;
if traceDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
C = C_start[1:Medium.nC];
else
if traceDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(C) = zeros(Medium.nC);
end if;
end if;
equation
// Conditional connectors
connect(mWat_flow, mWat_flow_internal);
if not use_mWat_flow then
mWat_flow_internal = 0;
end if;
connect(C_flow, C_flow_internal);
if not use_C_flow then
C_flow_internal = zeros(Medium.nC);
end if;
// Total quantities
if massDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
m = fluidVolume*rho_start;
else
if _simplify_mWat_flow then
// If moisture is neglected in mass balance, assume for computation
// of the mass of air that the air is at Medium.X_default.
m = fluidVolume*Medium.density(Medium.setState_phX(
p = medium.p,
h = hOut,
X = Medium.X_default));
else
// Use actual density
m = fluidVolume*medium.d;
end if;
end if;
mXi = m*medium.Xi;
if computeCSen then
U = m*medium.u + CSen*(medium.T-Medium.reference_T);
else
U = m*medium.u;
end if;
mC = m*C;
hOut = medium.h;
XiOut = medium.Xi;
COut = C;
for i in 1:nPorts loop
//The semiLinear function should be used for the equations below
//for allowing min/max simplifications.
//See https://github.com/ibpsa/modelica-ibpsa/issues/216 for a discussion and motivation
ports_H_flow[i] = semiLinear(ports[i].m_flow, inStream(ports[i].h_outflow), ports[i].h_outflow)
"Enthalpy flow";
for j in 1:Medium.nXi loop
ports_mXi_flow[i,j] = semiLinear(ports[i].m_flow, inStream(ports[i].Xi_outflow[j]), ports[i].Xi_outflow[j])
"Component mass flow";
end for;
for j in 1:Medium.nC loop
ports_mC_flow[i,j] = semiLinear(ports[i].m_flow, inStream(ports[i].C_outflow[j]), ports[i].C_outflow[j])
"Trace substance mass flow";
end for;
end for;
for i in 1:Medium.nXi loop
mbXi_flow[i] = sum(ports_mXi_flow[:,i]);
end for;
for i in 1:Medium.nC loop
mbC_flow[i] = sum(ports_mC_flow[:,i]);
end for;
mb_flow = sum(ports.m_flow);
Hb_flow = sum(ports_H_flow);
// Energy and mass balances
if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
0 = Hb_flow + Q_flow;
else
der(U) = Hb_flow + Q_flow;
end if;
if massDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
0 = mb_flow + (if simplify_mWat_flow then 0 else mWat_flow_internal);
else
der(m) = mb_flow + (if simplify_mWat_flow then 0 else mWat_flow_internal);
end if;
if substanceDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
zeros(Medium.nXi) = mbXi_flow + mWat_flow_internal * s;
else
der(medium.Xi) = (mbXi_flow + mWat_flow_internal * s)/m;
end if;
if traceDynamics == Modelica.Fluid.Types.Dynamics.SteadyState then
zeros(Medium.nC) = mbC_flow + C_flow_internal;
else
der(mC) = mbC_flow + C_flow_internal;
end if;
// Properties of outgoing flows
for i in 1:nPorts loop
ports[i].p = medium.p;
ports[i].h_outflow = medium.h;
ports[i].Xi_outflow = medium.Xi;
ports[i].C_outflow = C;
end for;
UOut=U;
mXiOut=mXi;
mOut=m;
mCOut=mC;
end ConservationEquation;
Buildings.Fluid.Interfaces.EightPort
Partial model with eight ports
Information
This model defines an interface for components with eight ports. The parameters allowFlowReversal1,
allowFlowReversal2, allowFlowReversal3 and allowFlowReversal4
may be used by models that extend this model to treat flow reversal.
This model is identical to Modelica.Fluid.Interfaces.PartialTwoPort, except that it has eight ports.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | Modelica.Media.Interfaces.Pa... | Medium 1 in the component | |
| replaceable package Medium2 | Modelica.Media.Interfaces.Pa... | Medium 2 in the component | |
| replaceable package Medium3 | Modelica.Media.Interfaces.Pa... | Medium 3 in the component | |
| replaceable package Medium4 | Modelica.Media.Interfaces.Pa... | Medium 4 in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal2 | true | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal3 | true | = true to allow flow reversal in medium 3, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal4 | true | = true to allow flow reversal in medium 4, false restricts to design direction (port_a -> port_b) |
| Advanced | |||
| Initialization | |||
| SpecificEnthalpy | h_outflow_a1_start | Medium1.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b1_start | Medium1.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a2_start | Medium2.h_default | Start value for enthalpy flowing out of port a2 [J/kg] |
| SpecificEnthalpy | h_outflow_b2_start | Medium2.h_default | Start value for enthalpy flowing out of port b2 [J/kg] |
| SpecificEnthalpy | h_outflow_a3_start | Medium3.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b3_start | Medium3.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a4_start | Medium4.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b4_start | Medium4.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium1 | Medium 1 in the component | |
| replaceable package Medium2 | Medium 2 in the component | |
| replaceable package Medium3 | Medium 3 in the component | |
| replaceable package Medium4 | Medium 4 in the component | |
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_a | port_a3 | Fluid connector a1 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_b | port_b3 | Fluid connector b2 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_a | port_a4 | Fluid connector a1 (positive design flow direction is from port_a4 to port_b4) |
| FluidPort_b | port_b4 | Fluid connector b2 (positive design flow direction is from port_a4 to port_b4) |
Modelica definition
partial model EightPort "Partial model with eight ports"
replaceable package Medium1 =
Modelica.Media.Interfaces.PartialMedium "Medium 1 in the component";
replaceable package Medium2 =
Modelica.Media.Interfaces.PartialMedium "Medium 2 in the component";
replaceable package Medium3 =
Modelica.Media.Interfaces.PartialMedium "Medium 3 in the component";
replaceable package Medium4 =
Modelica.Media.Interfaces.PartialMedium "Medium 4 in the component";
parameter Boolean allowFlowReversal1 = true
"= true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b)";
parameter Boolean allowFlowReversal2 = true
"= true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b)";
parameter Boolean allowFlowReversal3 = true
"= true to allow flow reversal in medium 3, false restricts to design direction (port_a -> port_b)";
parameter Boolean allowFlowReversal4 = true
"= true to allow flow reversal in medium 4, false restricts to design direction (port_a -> port_b)";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_a1_start=Medium1.h_default
"Start value for enthalpy flowing out of port a1";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_b1_start=Medium1.h_default
"Start value for enthalpy flowing out of port b1";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_a2_start=Medium2.h_default
"Start value for enthalpy flowing out of port a2";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_b2_start=Medium2.h_default
"Start value for enthalpy flowing out of port b2";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_a3_start=Medium3.h_default
"Start value for enthalpy flowing out of port a1";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_b3_start=Medium3.h_default
"Start value for enthalpy flowing out of port b1";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_a4_start=Medium4.h_default
"Start value for enthalpy flowing out of port a1";
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_b4_start=Medium4.h_default
"Start value for enthalpy flowing out of port b1";
Modelica.Fluid.Interfaces.FluidPort_a port_a1(
redeclare final package Medium = Medium1,
m_flow(min=if allowFlowReversal1 then -Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_a1_start))
"Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_b port_b1(
redeclare final package Medium = Medium1,
m_flow(max=if allowFlowReversal1 then +Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_b1_start))
"Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_a port_a2(
redeclare final package Medium = Medium2,
m_flow(min=if allowFlowReversal2 then -Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_a2_start))
"Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)";
Modelica.Fluid.Interfaces.FluidPort_b port_b2(
redeclare final package Medium = Medium2,
m_flow(max=if allowFlowReversal2 then +Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_b2_start))
"Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)";
Modelica.Fluid.Interfaces.FluidPort_a port_a3(
redeclare final package Medium = Medium3,
m_flow(min=if allowFlowReversal3 then -Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_a3_start))
"Fluid connector a1 (positive design flow direction is from port_a3 to port_b3)";
Modelica.Fluid.Interfaces.FluidPort_b port_b3(
redeclare final package Medium = Medium3,
m_flow(max=if allowFlowReversal3 then +Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_b3_start))
"Fluid connector b2 (positive design flow direction is from port_a3 to port_b3)";
Modelica.Fluid.Interfaces.FluidPort_a port_a4(
redeclare final package Medium = Medium4,
m_flow(min=if allowFlowReversal4 then -Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_a4_start))
"Fluid connector a1 (positive design flow direction is from port_a4 to port_b4)";
Modelica.Fluid.Interfaces.FluidPort_b port_b4(
redeclare final package Medium = Medium4,
m_flow(max=if allowFlowReversal4 then +Modelica.Constants.inf else 0),
h_outflow(start=h_outflow_b4_start))
"Fluid connector b2 (positive design flow direction is from port_a4 to port_b4)";
end EightPort;
Buildings.Fluid.Interfaces.EightPortHeatMassExchanger
Model transporting four fluid streams between eight ports with storing mass or energy
Information
This component transports four fluid streams between eight ports. It provides the basic model for implementing a dynamic heat exchanger.
The model can be used as-is, although there will be no heat or mass transfer between the four fluid streams. To add heat transfer, heat flow can be added to the heat port of the four volumes.
Implementation
The variable names follow the conventions used in Modelica.Fluid.Examples.HeatExchanger.BaseClasses.BasicHX.
Extends from Buildings.Fluid.Interfaces.PartialEightPortInterface (Partial model with eight ports and declaration of quantities that are used by many models), Buildings.Fluid.Interfaces.EightPortFlowResistanceParameters (Parameters for flow resistance for models with height ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
| replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
| replaceable package Medium3 | PartialMedium | Medium 3 in the component | |
| replaceable package Medium4 | PartialMedium | Medium 4 in the component | |
| Nominal condition | |||
| MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m2_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m3_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m4_flow_nominal | Nominal mass flow rate [kg/s] | |
| Pressure | dp1_nominal | Pressure [Pa] | |
| Pressure | dp2_nominal | Pressure [Pa] | |
| Pressure | dp3_nominal | Pressure [Pa] | |
| Pressure | dp4_nominal | Pressure [Pa] | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal2 | true | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal3 | true | = true to allow flow reversal in medium 3, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal4 | true | = true to allow flow reversal in medium 4, false restricts to design direction (port_a -> port_b) |
| Advanced | |||
| Initialization | |||
| SpecificEnthalpy | h_outflow_a1_start | h1_outflow_start | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b1_start | h1_outflow_start | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a2_start | h2_outflow_start | Start value for enthalpy flowing out of port a2 [J/kg] |
| SpecificEnthalpy | h_outflow_b2_start | h2_outflow_start | Start value for enthalpy flowing out of port b2 [J/kg] |
| SpecificEnthalpy | h_outflow_a3_start | h3_outflow_start | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b3_start | h3_outflow_start | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a4_start | h4_outflow_start | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b4_start | h4_outflow_start | Start value for enthalpy flowing out of port b1 [J/kg] |
| MassFlowRate | m1_flow_small | 1E-4*abs(m1_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m2_flow_small | 1E-4*abs(m2_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m3_flow_small | 1E-4*abs(m3_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m4_flow_small | 1E-4*abs(m4_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Flow resistance | |||
| Medium 1 | |||
| Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp1 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance1 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM1 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 2 | |||
| Boolean | computeFlowResistance2 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp2 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance2 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM2 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 3 | |||
| Boolean | computeFlowResistance3 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp3 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance3 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM3 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 4 | |||
| Boolean | computeFlowResistance4 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp4 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance4 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM4 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Dynamics | |||
| Nominal condition | |||
| Time | tau1 | 30 | Time constant at nominal flow [s] |
| Time | tau2 | 30 | Time constant at nominal flow [s] |
| Time | tau3 | 30 | Time constant at nominal flow [s] |
| Time | tau4 | 30 | Time constant at nominal flow [s] |
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Formulation of energy balance |
| Initialization | |||
| Medium 1 | |||
| AbsolutePressure | p1_start | Medium1.p_default | Start value of pressure [Pa] |
| Temperature | T1_start | Medium1.T_default | Start value of temperature [K] |
| MassFraction | X1_start[Medium1.nX] | Medium1.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C1_start[Medium1.nC] | fill(0, Medium1.nC) | Start value of trace substances |
| ExtraProperty | C1_nominal[Medium1.nC] | fill(1E-2, Medium1.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
| Medium 2 | |||
| AbsolutePressure | p2_start | Medium2.p_default | Start value of pressure [Pa] |
| Temperature | T2_start | Medium2.T_default | Start value of temperature [K] |
| MassFraction | X2_start[Medium2.nX] | Medium2.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C2_start[Medium2.nC] | fill(0, Medium2.nC) | Start value of trace substances |
| ExtraProperty | C2_nominal[Medium2.nC] | fill(1E-2, Medium2.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
| Medium 3 | |||
| AbsolutePressure | p3_start | Medium3.p_default | Start value of pressure [Pa] |
| Temperature | T3_start | Medium3.T_default | Start value of temperature [K] |
| MassFraction | X3_start[Medium3.nX] | Medium3.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C3_start[Medium3.nC] | fill(0, Medium3.nC) | Start value of trace substances |
| ExtraProperty | C3_nominal[Medium3.nC] | fill(1E-2, Medium3.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
| Medium 4 | |||
| AbsolutePressure | p4_start | Medium4.p_default | Start value of pressure [Pa] |
| Temperature | T4_start | Medium4.T_default | Start value of temperature [K] |
| MassFraction | X4_start[Medium4.nX] | Medium4.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C4_start[Medium4.nC] | fill(0, Medium4.nC) | Start value of trace substances |
| ExtraProperty | C4_nominal[Medium4.nC] | fill(1E-2, Medium4.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_a | port_a3 | Fluid connector a1 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_b | port_b3 | Fluid connector b2 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_a | port_a4 | Fluid connector a1 (positive design flow direction is from port_a4 to port_b4) |
| FluidPort_b | port_b4 | Fluid connector b2 (positive design flow direction is from port_a4 to port_b4) |
Modelica definition
model EightPortHeatMassExchanger
"Model transporting four fluid streams between eight ports with storing mass or energy"
extends Buildings.Fluid.Interfaces.PartialEightPortInterface(
final h_outflow_a1_start = h1_outflow_start,
final h_outflow_b1_start = h1_outflow_start,
final h_outflow_a2_start = h2_outflow_start,
final h_outflow_b2_start = h2_outflow_start,
final h_outflow_a3_start = h3_outflow_start,
final h_outflow_b3_start = h3_outflow_start,
final h_outflow_a4_start = h4_outflow_start,
final h_outflow_b4_start = h4_outflow_start);
extends Buildings.Fluid.Interfaces.EightPortFlowResistanceParameters(
final computeFlowResistance1=true, final computeFlowResistance2=true,final computeFlowResistance3=true, final computeFlowResistance4=true);
constant Boolean homotopyInitialization = true "= true, use homotopy method";
parameter Modelica.Units.SI.Time tau1=30 "Time constant at nominal flow";
parameter Modelica.Units.SI.Time tau2=30 "Time constant at nominal flow";
parameter Modelica.Units.SI.Time tau3=30 "Time constant at nominal flow";
parameter Modelica.Units.SI.Time tau4=30 "Time constant at nominal flow";
// Assumptions
parameter Modelica.Fluid.Types.Dynamics energyDynamics=Modelica.Fluid.Types.Dynamics.DynamicFreeInitial
"Formulation of energy balance";
// Initialization
parameter Medium1.AbsolutePressure p1_start = Medium1.p_default
"Start value of pressure";
parameter Medium1.Temperature T1_start = Medium1.T_default
"Start value of temperature";
parameter Medium1.MassFraction X1_start[Medium1.nX] = Medium1.X_default
"Start value of mass fractions m_i/m";
parameter Medium1.ExtraProperty C1_start[Medium1.nC](
quantity=Medium1.extraPropertiesNames)=fill(0, Medium1.nC)
"Start value of trace substances";
parameter Medium1.ExtraProperty C1_nominal[Medium1.nC](
quantity=Medium1.extraPropertiesNames) = fill(1E-2, Medium1.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
parameter Medium2.AbsolutePressure p2_start = Medium2.p_default
"Start value of pressure";
parameter Medium2.Temperature T2_start = Medium2.T_default
"Start value of temperature";
parameter Medium2.MassFraction X2_start[Medium2.nX] = Medium2.X_default
"Start value of mass fractions m_i/m";
parameter Medium2.ExtraProperty C2_start[Medium2.nC](
quantity=Medium2.extraPropertiesNames)=fill(0, Medium2.nC)
"Start value of trace substances";
parameter Medium2.ExtraProperty C2_nominal[Medium2.nC](
quantity=Medium2.extraPropertiesNames) = fill(1E-2, Medium2.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
parameter Medium3.AbsolutePressure p3_start = Medium3.p_default
"Start value of pressure";
parameter Medium3.Temperature T3_start = Medium3.T_default
"Start value of temperature";
parameter Medium3.MassFraction X3_start[Medium3.nX] = Medium3.X_default
"Start value of mass fractions m_i/m";
parameter Medium3.ExtraProperty C3_start[Medium3.nC](
quantity=Medium3.extraPropertiesNames)=fill(0, Medium3.nC)
"Start value of trace substances";
parameter Medium3.ExtraProperty C3_nominal[Medium3.nC](
quantity=Medium3.extraPropertiesNames) = fill(1E-2, Medium3.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
parameter Medium4.AbsolutePressure p4_start = Medium4.p_default
"Start value of pressure";
parameter Medium4.Temperature T4_start = Medium4.T_default
"Start value of temperature";
parameter Medium4.MassFraction X4_start[Medium4.nX] = Medium4.X_default
"Start value of mass fractions m_i/m";
parameter Medium4.ExtraProperty C4_start[Medium4.nC](
quantity=Medium4.extraPropertiesNames)=fill(0, Medium4.nC)
"Start value of trace substances";
parameter Medium4.ExtraProperty C4_nominal[Medium4.nC](
quantity=Medium4.extraPropertiesNames) = fill(1E-2, Medium4.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
Modelica.Units.SI.HeatFlowRate Q1_flow=vol1.heatPort.Q_flow
"Heat flow rate into medium 1";
Modelica.Units.SI.HeatFlowRate Q2_flow=vol2.heatPort.Q_flow
"Heat flow rate into medium 2";
Modelica.Units.SI.HeatFlowRate Q3_flow=vol3.heatPort.Q_flow
"Heat flow rate into medium 1";
Modelica.Units.SI.HeatFlowRate Q4_flow=vol4.heatPort.Q_flow
"Heat flow rate into medium 2";
Buildings.Fluid.MixingVolumes.MixingVolume vol1(
redeclare final package Medium = Medium1,
nPorts = 2,
V=m1_flow_nominal*tau1/rho1_nominal,
final m_flow_nominal=m1_flow_nominal,
energyDynamics=if tau1 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau1 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p1_start,
final T_start=T1_start,
final X_start=X1_start,
final C_start=C1_start,
final C_nominal=C1_nominal) "Volume for fluid 1";
Buildings.Fluid.MixingVolumes.MixingVolume vol2(
redeclare final package Medium = Medium2,
nPorts=2,
energyDynamics=if tau2 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau2 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p2_start,
final T_start=T2_start,
final X_start=X2_start,
final C_start=C2_start,
final C_nominal=C2_nominal,
final m_flow_nominal=m2_flow_nominal,
V=m2_flow_nominal*tau2/rho2_nominal) "Volume for fluid 2";
Buildings.Fluid.MixingVolumes.MixingVolume vol3(
redeclare final package Medium = Medium3,
energyDynamics=if tau3 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau3 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p3_start,
final T_start=T3_start,
final X_start=X3_start,
final C_start=C3_start,
final C_nominal=C3_nominal,
final m_flow_nominal=m3_flow_nominal,
V=m3_flow_nominal*tau3/rho3_nominal,
nPorts=2) "Volume for fluid 3";
Buildings.Fluid.MixingVolumes.MixingVolume vol4(
redeclare final package Medium = Medium4,
nPorts=2,
energyDynamics=if tau4 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau4 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p4_start,
final T_start=T4_start,
final X_start=X4_start,
final C_start=C4_start,
final C_nominal=C4_nominal,
final m_flow_nominal=m4_flow_nominal,
V=m4_flow_nominal*tau4/rho4_nominal) "Volume for fluid 4";
Buildings.Fluid.FixedResistances.PressureDrop preDro1(
redeclare final package Medium = Medium1,
final m_flow_nominal=m1_flow_nominal,
final deltaM=deltaM1,
final allowFlowReversal=allowFlowReversal1,
final show_T=false,
final from_dp=from_dp1,
final linearized=linearizeFlowResistance1,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp1_nominal) "Pressure drop model for fluid 1";
Buildings.Fluid.FixedResistances.PressureDrop preDro2(
redeclare final package Medium = Medium2,
final m_flow_nominal=m2_flow_nominal,
final deltaM=deltaM2,
final allowFlowReversal=allowFlowReversal2,
final show_T=false,
final from_dp=from_dp2,
final linearized=linearizeFlowResistance2,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp2_nominal) "Pressure drop model for fluid 2";
Buildings.Fluid.FixedResistances.PressureDrop preDro3(
redeclare final package Medium = Medium3,
final m_flow_nominal=m3_flow_nominal,
final deltaM=deltaM3,
final allowFlowReversal=allowFlowReversal3,
final show_T=false,
final from_dp=from_dp3,
final linearized=linearizeFlowResistance3,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp3_nominal) "Pressure drop model for fluid 3";
Buildings.Fluid.FixedResistances.PressureDrop preDro4(
redeclare final package Medium = Medium4,
final m_flow_nominal=m4_flow_nominal,
final deltaM=deltaM4,
final allowFlowReversal=allowFlowReversal4,
final show_T=false,
final from_dp=from_dp4,
final linearized=linearizeFlowResistance4,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp4_nominal) "Pressure drop model for fluid 4";
protected
parameter Medium1.ThermodynamicState sta1_nominal=Medium1.setState_pTX(
T=Medium1.T_default, p=Medium1.p_default, X=Medium1.X_default);
parameter Modelica.Units.SI.Density rho1_nominal=Medium1.density(sta1_nominal)
"Density, used to compute fluid volume";
parameter Medium2.ThermodynamicState sta2_nominal=Medium2.setState_pTX(
T=Medium2.T_default, p=Medium2.p_default, X=Medium2.X_default);
parameter Modelica.Units.SI.Density rho2_nominal=Medium2.density(sta2_nominal)
"Density, used to compute fluid volume";
parameter Medium1.ThermodynamicState sta3_nominal=Medium3.setState_pTX(
T=Medium3.T_default, p=Medium3.p_default, X=Medium3.X_default);
parameter Modelica.Units.SI.Density rho3_nominal=Medium3.density(sta3_nominal)
"Density, used to compute fluid volume";
parameter Medium4.ThermodynamicState sta4_nominal=Medium4.setState_pTX(
T=Medium4.T_default, p=Medium4.p_default, X=Medium4.X_default);
parameter Modelica.Units.SI.Density rho4_nominal=Medium4.density(sta4_nominal)
"Density, used to compute fluid volume";
parameter Medium1.ThermodynamicState sta1_start=Medium1.setState_pTX(
T=T1_start, p=p1_start, X=X1_start);
parameter Modelica.Units.SI.SpecificEnthalpy h1_outflow_start=
Medium1.specificEnthalpy(sta1_start)
"Start value for outflowing enthalpy";
parameter Medium2.ThermodynamicState sta2_start=Medium2.setState_pTX(
T=T2_start, p=p2_start, X=X2_start);
parameter Modelica.Units.SI.SpecificEnthalpy h2_outflow_start=
Medium2.specificEnthalpy(sta2_start)
"Start value for outflowing enthalpy";
parameter Medium3.ThermodynamicState sta3_start=Medium3.setState_pTX(
T=T3_start, p=p3_start, X=X3_start);
parameter Modelica.Units.SI.SpecificEnthalpy h3_outflow_start=
Medium3.specificEnthalpy(sta3_start)
"Start value for outflowing enthalpy";
parameter Medium4.ThermodynamicState sta4_start=Medium4.setState_pTX(
T=T4_start, p=p4_start, X=X4_start);
parameter Modelica.Units.SI.SpecificEnthalpy h4_outflow_start=
Medium4.specificEnthalpy(sta4_start)
"Start value for outflowing enthalpy";
initial algorithm
// Check for tau1
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau1 > Modelica.Constants.eps,
"The parameter tau1, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau1 = " + String(tau1) + "\n");
// Check for tau2
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau2 > Modelica.Constants.eps,
"The parameter tau2, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau2 = " + String(tau2) + "\n");
// Check for tau1
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau3 > Modelica.Constants.eps,
"The parameter tau3, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau3 = " + String(tau3) + "\n");
// Check for tau2
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau4 > Modelica.Constants.eps,
"The parameter tau4, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau4 = " + String(tau4) + "\n");
assert(homotopyInitialization, "In " + getInstanceName() +
": The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.",
level = AssertionLevel.warning);
equation
connect(vol1.ports[2], port_b1);
connect(port_a1, preDro1.port_a);
connect(preDro1.port_b, vol1.ports[1]);
connect(port_a2, preDro2.port_a);
connect(preDro4.port_a, port_a4);
connect(preDro4.port_b, vol4.ports[1]);
connect(port_b4, vol4.ports[2]);
connect(port_a3, preDro3.port_a);
connect(preDro3.port_b, vol3.ports[1]);
connect(port_b3, vol3.ports[2]);
connect(port_b2, vol2.ports[1]);
connect(preDro2.port_b, vol2.ports[2]);
end EightPortHeatMassExchanger;
Buildings.Fluid.Interfaces.FourPortHeatMassExchanger
Model transporting two fluid streams between four ports with storing mass or energy
Information
This component transports two fluid streams between four ports. It provides the basic model for implementing a dynamic heat exchanger.
The model can be used as-is, although there will be no heat or mass transfer
between the two fluid streams.
To add heat transfer, heat flow can be added to the heat port of the two volumes.
See for example
Buildings.Fluid.Chillers.Carnot_y.
To add moisture input into (or moisture output from) volume vol2,
the model can be replaced with
Buildings.Fluid.MixingVolumes.MixingVolumeMoistAir.
Implementation
The variable names follow the conventions used in Modelica.Fluid.Examples.HeatExchanger.BaseClasses.BasicHX.
Extends from Buildings.Fluid.Interfaces.PartialFourPortInterface (Partial model with four ports and declaration of quantities that are used by many models), Buildings.Fluid.Interfaces.FourPortFlowResistanceParameters (Parameters for flow resistance for models with four ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
| replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
| MixingVolumeHeatPort | vol1 | redeclare Buildings.Fluid.Mi... | Volume for fluid 1 |
| MixingVolume | vol2 | redeclare Buildings.Fluid.Mi... | Volume for fluid 2 |
| Nominal condition | |||
| MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m2_flow_nominal | Nominal mass flow rate [kg/s] | |
| PressureDifference | dp1_nominal | Pressure difference [Pa] | |
| PressureDifference | dp2_nominal | Pressure difference [Pa] | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 |
| Boolean | allowFlowReversal2 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 |
| Advanced | |||
| MassFlowRate | m1_flow_small | 1E-4*abs(m1_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m2_flow_small | 1E-4*abs(m2_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Flow resistance | |||
| Medium 1 | |||
| Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp1 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance1 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM1 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 2 | |||
| Boolean | computeFlowResistance2 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp2 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance2 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM2 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Dynamics | |||
| Nominal condition | |||
| Time | tau1 | 30 | Time constant at nominal flow [s] |
| Time | tau2 | 30 | Time constant at nominal flow [s] |
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Type of energy balance: dynamic (3 initialization options) or steady state |
| Initialization | |||
| Medium 1 | |||
| AbsolutePressure | p1_start | Medium1.p_default | Start value of pressure [Pa] |
| Temperature | T1_start | Medium1.T_default | Start value of temperature [K] |
| MassFraction | X1_start[Medium1.nX] | Medium1.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C1_start[Medium1.nC] | fill(0, Medium1.nC) | Start value of trace substances |
| ExtraProperty | C1_nominal[Medium1.nC] | fill(1E-2, Medium1.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
| Medium 2 | |||
| AbsolutePressure | p2_start | Medium2.p_default | Start value of pressure [Pa] |
| Temperature | T2_start | Medium2.T_default | Start value of temperature [K] |
| MassFraction | X2_start[Medium2.nX] | Medium2.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C2_start[Medium2.nC] | fill(0, Medium2.nC) | Start value of trace substances |
| ExtraProperty | C2_nominal[Medium2.nC] | fill(1E-2, Medium2.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
Modelica definition
model FourPortHeatMassExchanger
"Model transporting two fluid streams between four ports with storing mass or energy"
extends Buildings.Fluid.Interfaces.PartialFourPortInterface(
port_a1(h_outflow(start=h1_outflow_start)),
port_b1(h_outflow(start=h1_outflow_start)),
port_a2(h_outflow(start=h2_outflow_start)),
port_b2(h_outflow(start=h2_outflow_start)));
extends Buildings.Fluid.Interfaces.FourPortFlowResistanceParameters(
final computeFlowResistance1=true, final computeFlowResistance2=true);
constant Boolean homotopyInitialization = true "= true, use homotopy method";
parameter Modelica.Units.SI.Time tau1=30 "Time constant at nominal flow";
parameter Modelica.Units.SI.Time tau2=30 "Time constant at nominal flow";
// Assumptions
parameter Modelica.Fluid.Types.Dynamics energyDynamics=Modelica.Fluid.Types.Dynamics.DynamicFreeInitial
"Type of energy balance: dynamic (3 initialization options) or steady state";
// Initialization
parameter Medium1.AbsolutePressure p1_start = Medium1.p_default
"Start value of pressure";
parameter Medium1.Temperature T1_start = Medium1.T_default
"Start value of temperature";
parameter Medium1.MassFraction X1_start[Medium1.nX] = Medium1.X_default
"Start value of mass fractions m_i/m";
parameter Medium1.ExtraProperty C1_start[Medium1.nC](
final quantity=Medium1.extraPropertiesNames)=fill(0, Medium1.nC)
"Start value of trace substances";
parameter Medium1.ExtraProperty C1_nominal[Medium1.nC](
final quantity=Medium1.extraPropertiesNames) = fill(1E-2, Medium1.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
parameter Medium2.AbsolutePressure p2_start = Medium2.p_default
"Start value of pressure";
parameter Medium2.Temperature T2_start = Medium2.T_default
"Start value of temperature";
parameter Medium2.MassFraction X2_start[Medium2.nX] = Medium2.X_default
"Start value of mass fractions m_i/m";
parameter Medium2.ExtraProperty C2_start[Medium2.nC](
final quantity=Medium2.extraPropertiesNames)=fill(0, Medium2.nC)
"Start value of trace substances";
parameter Medium2.ExtraProperty C2_nominal[Medium2.nC](
final quantity=Medium2.extraPropertiesNames) = fill(1E-2, Medium2.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
Modelica.Units.SI.HeatFlowRate Q1_flow=vol1.heatPort.Q_flow
"Heat flow rate into medium 1";
Modelica.Units.SI.HeatFlowRate Q2_flow=vol2.heatPort.Q_flow
"Heat flow rate into medium 2";
replaceable Buildings.Fluid.MixingVolumes.BaseClasses.MixingVolumeHeatPort vol1
constrainedby Buildings.Fluid.MixingVolumes.BaseClasses.MixingVolumeHeatPort
( redeclare final package Medium = Medium1,
nPorts = 2,
V=m1_flow_nominal*tau1/rho1_nominal,
final allowFlowReversal=allowFlowReversal1,
final m_flow_nominal=m1_flow_nominal,
energyDynamics=if tau1 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau1 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p1_start,
final T_start=T1_start,
final X_start=X1_start,
final C_start=C1_start,
final C_nominal=C1_nominal,
mSenFac=1) "Volume for fluid 1";
replaceable Buildings.Fluid.MixingVolumes.MixingVolume vol2
constrainedby Buildings.Fluid.MixingVolumes.BaseClasses.MixingVolumeHeatPort
( redeclare final package Medium = Medium2,
nPorts = 2,
V=m2_flow_nominal*tau2/rho2_nominal,
final allowFlowReversal=allowFlowReversal2,
mSenFac=1,
final m_flow_nominal = m2_flow_nominal,
energyDynamics=if tau2 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
massDynamics=if tau2 > Modelica.Constants.eps
then energyDynamics else
Modelica.Fluid.Types.Dynamics.SteadyState,
final p_start=p2_start,
final T_start=T2_start,
final X_start=X2_start,
final C_start=C2_start,
final C_nominal=C2_nominal) "Volume for fluid 2";
Buildings.Fluid.FixedResistances.PressureDrop preDro1(
redeclare final package Medium = Medium1,
final m_flow_nominal=m1_flow_nominal,
final deltaM=deltaM1,
final allowFlowReversal=allowFlowReversal1,
final show_T=false,
final from_dp=from_dp1,
final linearized=linearizeFlowResistance1,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp1_nominal) "Flow resistance of fluid 1";
Buildings.Fluid.FixedResistances.PressureDrop preDro2(
redeclare final package Medium = Medium2,
final m_flow_nominal=m2_flow_nominal,
final deltaM=deltaM2,
final allowFlowReversal=allowFlowReversal2,
final show_T=false,
final from_dp=from_dp2,
final linearized=linearizeFlowResistance2,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp2_nominal) "Flow resistance of fluid 2";
protected
parameter Medium1.ThermodynamicState sta1_nominal=Medium1.setState_pTX(
T=Medium1.T_default, p=Medium1.p_default, X=Medium1.X_default);
parameter Modelica.Units.SI.Density rho1_nominal=Medium1.density(sta1_nominal)
"Density, used to compute fluid volume";
parameter Medium2.ThermodynamicState sta2_nominal=Medium2.setState_pTX(
T=Medium2.T_default, p=Medium2.p_default, X=Medium2.X_default);
parameter Modelica.Units.SI.Density rho2_nominal=Medium2.density(sta2_nominal)
"Density, used to compute fluid volume";
parameter Medium1.ThermodynamicState sta1_start=Medium1.setState_pTX(
T=T1_start, p=p1_start, X=X1_start);
parameter Modelica.Units.SI.SpecificEnthalpy h1_outflow_start=
Medium1.specificEnthalpy(sta1_start)
"Start value for outflowing enthalpy";
parameter Medium2.ThermodynamicState sta2_start=Medium2.setState_pTX(
T=T2_start, p=p2_start, X=X2_start);
parameter Modelica.Units.SI.SpecificEnthalpy h2_outflow_start=
Medium2.specificEnthalpy(sta2_start)
"Start value for outflowing enthalpy";
initial equation
// Check for tau1
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau1 > Modelica.Constants.eps,
"The parameter tau1, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau1 = " + String(tau1) + "\n");
// Check for tau2
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau2 > Modelica.Constants.eps,
"The parameter tau2, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau2 = " + String(tau2) + "\n");
assert(homotopyInitialization, "In " + getInstanceName() +
": The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.",
level = AssertionLevel.warning);
equation
connect(vol1.ports[2], port_b1);
connect(vol2.ports[2], port_b2);
connect(port_a1, preDro1.port_a);
connect(preDro1.port_b, vol1.ports[1]);
connect(port_a2, preDro2.port_a);
connect(preDro2.port_b, vol2.ports[1]);
end FourPortHeatMassExchanger;
Buildings.Fluid.Interfaces.LumpedVolumeDeclarations
Declarations for lumped volumes
Information
This class contains parameters and medium properties that are used in the lumped volume model, and in models that extend the lumped volume model.
These parameters are used for example by Buildings.Fluid.Interfaces.ConservationEquation, Buildings.Fluid.MixingVolumes.MixingVolume and Buildings.Fluid.HeatExchangers.Radiators.RadiatorEN442_2.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | Modelica.Media.Interfaces.Pa... | Medium in the component | |
| Dynamics | |||
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Type of energy balance: dynamic (3 initialization options) or steady state |
| Real | mSenFac | 1 | Factor for scaling the sensible thermal mass of the volume |
| Advanced | |||
| Dynamics | |||
| Dynamics | massDynamics | energyDynamics | Type of mass balance: dynamic (3 initialization options) or steady state, must be steady state if energyDynamics is steady state |
| Initialization | |||
| AbsolutePressure | p_start | Medium.p_default | Start value of pressure [Pa] |
| Temperature | T_start | Medium.T_default | Start value of temperature [K] |
| MassFraction | X_start[Medium.nX] | Medium.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C_start[Medium.nC] | fill(0, Medium.nC) | Start value of trace substances |
| ExtraProperty | C_nominal[Medium.nC] | fill(1E-2, Medium.nC) | Nominal value of trace substances. (Set to typical order of magnitude.) |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium | Medium in the component | |
Modelica definition
block LumpedVolumeDeclarations "Declarations for lumped volumes"
replaceable package Medium =
Modelica.Media.Interfaces.PartialMedium "Medium in the component";
// Assumptions
parameter Modelica.Fluid.Types.Dynamics energyDynamics=Modelica.Fluid.Types.Dynamics.DynamicFreeInitial
"Type of energy balance: dynamic (3 initialization options) or steady state";
parameter Modelica.Fluid.Types.Dynamics massDynamics=energyDynamics
"Type of mass balance: dynamic (3 initialization options) or steady state, must be steady state if energyDynamics is steady state";
final parameter Modelica.Fluid.Types.Dynamics substanceDynamics=energyDynamics
"Type of independent mass fraction balance: dynamic (3 initialization options) or steady state";
final parameter Modelica.Fluid.Types.Dynamics traceDynamics=energyDynamics
"Type of trace substance balance: dynamic (3 initialization options) or steady state";
// Initialization
parameter Medium.AbsolutePressure p_start = Medium.p_default
"Start value of pressure";
parameter Medium.Temperature T_start=Medium.T_default
"Start value of temperature";
parameter Medium.MassFraction X_start[Medium.nX](
quantity=Medium.substanceNames) = Medium.X_default
"Start value of mass fractions m_i/m";
parameter Medium.ExtraProperty C_start[Medium.nC](
quantity=Medium.extraPropertiesNames)=fill(0, Medium.nC)
"Start value of trace substances";
parameter Medium.ExtraProperty C_nominal[Medium.nC](
quantity=Medium.extraPropertiesNames) = fill(1E-2, Medium.nC)
"Nominal value of trace substances. (Set to typical order of magnitude.)";
parameter Real mSenFac(min=1)=1
"Factor for scaling the sensible thermal mass of the volume";
// The parameter below is evaluated by OCT during compilation, and
// if false, the assert statement won't be optimized away during
// code generation.
protected
final parameter Boolean wrongEnergyMassBalanceConfiguration=
not (energyDynamics <> Modelica.Fluid.Types.Dynamics.SteadyState or
massDynamics == Modelica.Fluid.Types.Dynamics.SteadyState)
"True if configuration of energy and mass balance is wrong.";
initial equation
if wrongEnergyMassBalanceConfiguration then
assert(not wrongEnergyMassBalanceConfiguration,
"In " + getInstanceName() +
": energyDynamics is selected as steady state, and therefore massDynamics must also be steady-state.");
end if;
end LumpedVolumeDeclarations;
Buildings.Fluid.Interfaces.PartialEightPortInterface
Partial model with eight ports and declaration of quantities that are used by many models
Information
This component defines the interface for models with eight fluid ports and four fluid streams. It is similar to Buildings.Fluid.Interfaces.PartialTwoPortInterface, but it has eight ports instead of two.
The model is used by other models in this package that add heat transfer, mass transfer and pressure drop equations.
Extends from Buildings.Fluid.Interfaces.EightPort (Partial model with eight ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
| replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
| replaceable package Medium3 | PartialMedium | Medium 3 in the component | |
| replaceable package Medium4 | PartialMedium | Medium 4 in the component | |
| Nominal condition | |||
| MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m2_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m3_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m4_flow_nominal | Nominal mass flow rate [kg/s] | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal2 | true | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal3 | true | = true to allow flow reversal in medium 3, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal4 | true | = true to allow flow reversal in medium 4, false restricts to design direction (port_a -> port_b) |
| Advanced | |||
| Initialization | |||
| SpecificEnthalpy | h_outflow_a1_start | Medium1.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b1_start | Medium1.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a2_start | Medium2.h_default | Start value for enthalpy flowing out of port a2 [J/kg] |
| SpecificEnthalpy | h_outflow_b2_start | Medium2.h_default | Start value for enthalpy flowing out of port b2 [J/kg] |
| SpecificEnthalpy | h_outflow_a3_start | Medium3.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b3_start | Medium3.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
| SpecificEnthalpy | h_outflow_a4_start | Medium4.h_default | Start value for enthalpy flowing out of port a1 [J/kg] |
| SpecificEnthalpy | h_outflow_b4_start | Medium4.h_default | Start value for enthalpy flowing out of port b1 [J/kg] |
| MassFlowRate | m1_flow_small | 1E-4*abs(m1_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m2_flow_small | 1E-4*abs(m2_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m3_flow_small | 1E-4*abs(m3_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m4_flow_small | 1E-4*abs(m4_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_a | port_a3 | Fluid connector a1 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_b | port_b3 | Fluid connector b2 (positive design flow direction is from port_a3 to port_b3) |
| FluidPort_a | port_a4 | Fluid connector a1 (positive design flow direction is from port_a4 to port_b4) |
| FluidPort_b | port_b4 | Fluid connector b2 (positive design flow direction is from port_a4 to port_b4) |
Modelica definition
partial model PartialEightPortInterface
"Partial model with eight ports and declaration of quantities that are used by many models"
extends Buildings.Fluid.Interfaces.EightPort;
parameter Modelica.Units.SI.MassFlowRate m1_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Modelica.Units.SI.MassFlowRate m2_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Modelica.Units.SI.MassFlowRate m3_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Modelica.Units.SI.MassFlowRate m4_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Medium1.MassFlowRate m1_flow_small(min=0) = 1E-4*abs(m1_flow_nominal)
"Small mass flow rate for regularization of zero flow";
parameter Medium2.MassFlowRate m2_flow_small(min=0) = 1E-4*abs(m2_flow_nominal)
"Small mass flow rate for regularization of zero flow";
parameter Medium3.MassFlowRate m3_flow_small(min=0) = 1E-4*abs(m3_flow_nominal)
"Small mass flow rate for regularization of zero flow";
parameter Medium4.MassFlowRate m4_flow_small(min=0) = 1E-4*abs(m4_flow_nominal)
"Small mass flow rate for regularization of zero flow";
// Diagnostics
parameter Boolean show_T = false
"= true, if actual temperature at port is computed";
Medium1.MassFlowRate m1_flow = port_a1.m_flow
"Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction)";
Modelica.Units.SI.Pressure dp1(displayUnit="Pa") = port_a1.p - port_b1.p
"Pressure difference between port_a1 and port_b1";
Medium2.MassFlowRate m2_flow = port_a2.m_flow
"Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction)";
Modelica.Units.SI.Pressure dp2(displayUnit="Pa") = port_a2.p - port_b2.p
"Pressure difference between port_a2 and port_b2";
Medium3.MassFlowRate m3_flow = port_a3.m_flow
"Mass flow rate from port_a3 to port_b3 (m3_flow > 0 is design flow direction)";
Modelica.Units.SI.Pressure dp3(displayUnit="Pa") = port_a3.p - port_b3.p
"Pressure difference between port_a3 and port_b3";
Medium4.MassFlowRate m4_flow = port_a4.m_flow
"Mass flow rate from port_a4 to port_b4 (m4_flow > 0 is design flow direction)";
Modelica.Units.SI.Pressure dp4(displayUnit="Pa") = port_a4.p - port_b4.p
"Pressure difference between port_a4 and port_b4";
Medium1.ThermodynamicState sta_a1=
if allowFlowReversal1 then
Medium1.setState_phX(port_a1.p,
noEvent(actualStream(port_a1.h_outflow)),
noEvent(actualStream(port_a1.Xi_outflow)))
else
Medium1.setState_phX(port_a1.p,
inStream(port_a1.h_outflow),
inStream(port_a1.Xi_outflow))
if show_T "Medium properties in port_a1";
Medium1.ThermodynamicState sta_b1=
if allowFlowReversal1 then
Medium1.setState_phX(port_b1.p,
noEvent(actualStream(port_b1.h_outflow)),
noEvent(actualStream(port_b1.Xi_outflow)))
else
Medium1.setState_phX(port_b1.p,
port_b1.h_outflow,
port_b1.Xi_outflow)
if show_T "Medium properties in port_b1";
Medium2.ThermodynamicState sta_a2=
if allowFlowReversal2 then
Medium2.setState_phX(port_a2.p,
noEvent(actualStream(port_a2.h_outflow)),
noEvent(actualStream(port_a2.Xi_outflow)))
else
Medium2.setState_phX(port_a2.p,
inStream(port_a2.h_outflow),
inStream(port_a2.Xi_outflow))
if show_T "Medium properties in port_a2";
Medium2.ThermodynamicState sta_b2=
if allowFlowReversal2 then
Medium2.setState_phX(port_b2.p,
noEvent(actualStream(port_b2.h_outflow)),
noEvent(actualStream(port_b2.Xi_outflow)))
else
Medium2.setState_phX(port_b2.p,
port_b2.h_outflow,
port_b2.Xi_outflow)
if show_T "Medium properties in port_b2";
Medium3.ThermodynamicState sta_a3=
if allowFlowReversal3 then
Medium3.setState_phX(port_a3.p,
noEvent(actualStream(port_a3.h_outflow)),
noEvent(actualStream(port_a3.Xi_outflow)))
else
Medium3.setState_phX(port_a3.p,
inStream(port_a3.h_outflow),
inStream(port_a3.Xi_outflow))
if show_T "Medium properties in port_a3";
Medium3.ThermodynamicState sta_b3=
if allowFlowReversal3 then
Medium3.setState_phX(port_b3.p,
noEvent(actualStream(port_b3.h_outflow)),
noEvent(actualStream(port_b3.Xi_outflow)))
else
Medium3.setState_phX(port_b3.p,
port_b3.h_outflow,
port_b3.Xi_outflow)
if show_T "Medium properties in port_b3";
Medium4.ThermodynamicState sta_a4=
if allowFlowReversal4 then
Medium4.setState_phX(port_a4.p,
noEvent(actualStream(port_a4.h_outflow)),
noEvent(actualStream(port_a4.Xi_outflow)))
else
Medium4.setState_phX(port_a4.p,
inStream(port_a4.h_outflow),
inStream(port_a4.Xi_outflow))
if show_T "Medium properties in port_a4";
Medium4.ThermodynamicState sta_b4=
if allowFlowReversal4 then
Medium4.setState_phX(port_b4.p,
noEvent(actualStream(port_b4.h_outflow)),
noEvent(actualStream(port_b4.Xi_outflow)))
else
Medium4.setState_phX(port_b4.p,
port_b4.h_outflow,
port_b4.Xi_outflow)
if show_T "Medium properties in port_b4";
protected
Medium1.ThermodynamicState state_a1_inflow=
Medium1.setState_phX(port_a1.p, inStream(port_a1.h_outflow), inStream(port_a1.Xi_outflow))
"state for medium inflowing through port_a1";
Medium1.ThermodynamicState state_b1_inflow=
Medium1.setState_phX(port_b1.p, inStream(port_b1.h_outflow), inStream(port_b1.Xi_outflow))
"state for medium inflowing through port_b1";
Medium2.ThermodynamicState state_a2_inflow=
Medium2.setState_phX(port_a2.p, inStream(port_a2.h_outflow), inStream(port_a2.Xi_outflow))
"state for medium inflowing through port_a2";
Medium2.ThermodynamicState state_b2_inflow=
Medium2.setState_phX(port_b2.p, inStream(port_b2.h_outflow), inStream(port_b2.Xi_outflow))
"state for medium inflowing through port_b2";
Medium3.ThermodynamicState state_a3_inflow=
Medium3.setState_phX(port_a3.p, inStream(port_a3.h_outflow), inStream(port_a3.Xi_outflow))
"state for medium inflowing through port_a3";
Medium3.ThermodynamicState state_b3_inflow=
Medium3.setState_phX(port_b3.p, inStream(port_b3.h_outflow), inStream(port_b3.Xi_outflow))
"state for medium inflowing through port_b3";
Medium4.ThermodynamicState state_a4_inflow=
Medium4.setState_phX(port_a4.p, inStream(port_a4.h_outflow), inStream(port_a4.Xi_outflow))
"state for medium inflowing through port_a4";
Medium4.ThermodynamicState state_b4_inflow=
Medium4.setState_phX(port_b4.p, inStream(port_b4.h_outflow), inStream(port_b4.Xi_outflow))
"state for medium inflowing through port_b4";
end PartialEightPortInterface;
Buildings.Fluid.Interfaces.PartialFourPort
Partial model with four ports
Information
This model defines an interface for components with four ports.
The parameters allowFlowReversal1 and
allowFlowReversal2 may be used by models that extend
this model to treat flow reversal.
This model is identical to Modelica.Fluid.Interfaces.PartialTwoPort, except for the fowllowing:
- it has four ports, and
-
the parameters
port_a_exposesState,port_b_exposesStateandshowDesignFlowDirectionare not implemented.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | Modelica.Media.Interfaces.Pa... | Medium 1 in the component | |
| replaceable package Medium2 | Modelica.Media.Interfaces.Pa... | Medium 2 in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 |
| Boolean | allowFlowReversal2 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium1 | Medium 1 in the component | |
| replaceable package Medium2 | Medium 2 in the component | |
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
Modelica definition
partial model PartialFourPort "Partial model with four ports"
replaceable package Medium1 =
Modelica.Media.Interfaces.PartialMedium "Medium 1 in the component";
replaceable package Medium2 =
Modelica.Media.Interfaces.PartialMedium "Medium 2 in the component";
parameter Boolean allowFlowReversal1 = true
"= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1";
parameter Boolean allowFlowReversal2 = true
"= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2";
Modelica.Fluid.Interfaces.FluidPort_a port_a1(
redeclare final package Medium = Medium1,
m_flow(min=if allowFlowReversal1 then -Modelica.Constants.inf else 0),
h_outflow(start = Medium1.h_default, nominal = Medium1.h_default))
"Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_b port_b1(
redeclare final package Medium = Medium1,
m_flow(max=if allowFlowReversal1 then +Modelica.Constants.inf else 0),
h_outflow(start = Medium1.h_default, nominal = Medium1.h_default))
"Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_a port_a2(
redeclare final package Medium = Medium2,
m_flow(min=if allowFlowReversal2 then -Modelica.Constants.inf else 0),
h_outflow(start = Medium2.h_default, nominal = Medium2.h_default))
"Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)";
Modelica.Fluid.Interfaces.FluidPort_b port_b2(
redeclare final package Medium = Medium2,
m_flow(max=if allowFlowReversal2 then +Modelica.Constants.inf else 0),
h_outflow(start = Medium2.h_default, nominal = Medium2.h_default))
"Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)";
end PartialFourPort;
Buildings.Fluid.Interfaces.PartialFourPortInterface
Partial model with four ports and declaration of quantities that are used by many models
Information
This component defines the interface for models with four fluid ports and two fluid streams. It is similar to Buildings.Fluid.Interfaces.PartialTwoPortInterface, but it has four ports instead of two.
The model is used by other models in this package that add heat transfer, mass transfer and pressure drop equations.
Extends from Buildings.Fluid.Interfaces.PartialFourPort (Partial model with four ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
| replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
| Nominal condition | |||
| MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m2_flow_nominal | Nominal mass flow rate [kg/s] | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 |
| Boolean | allowFlowReversal2 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 |
| Advanced | |||
| MassFlowRate | m1_flow_small | 1E-4*abs(m1_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m2_flow_small | 1E-4*abs(m2_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
Modelica definition
partial model PartialFourPortInterface
"Partial model with four ports and declaration of quantities that are used by many models"
extends Buildings.Fluid.Interfaces.PartialFourPort;
parameter Modelica.Units.SI.MassFlowRate m1_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Modelica.Units.SI.MassFlowRate m2_flow_nominal(min=0)
"Nominal mass flow rate";
parameter Medium1.MassFlowRate m1_flow_small(min=0) = 1E-4*abs(m1_flow_nominal)
"Small mass flow rate for regularization of zero flow";
parameter Medium2.MassFlowRate m2_flow_small(min=0) = 1E-4*abs(m2_flow_nominal)
"Small mass flow rate for regularization of zero flow";
// Diagnostics
parameter Boolean show_T = false
"= true, if actual temperature at port is computed";
Medium1.MassFlowRate m1_flow = port_a1.m_flow
"Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction)";
Modelica.Units.SI.PressureDifference dp1(displayUnit="Pa") = port_a1.p - port_b1.p
"Pressure difference between port_a1 and port_b1";
Medium2.MassFlowRate m2_flow = port_a2.m_flow
"Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction)";
Modelica.Units.SI.PressureDifference dp2(displayUnit="Pa") = port_a2.p - port_b2.p
"Pressure difference between port_a2 and port_b2";
Medium1.ThermodynamicState sta_a1=
if allowFlowReversal1 then
Medium1.setState_phX(port_a1.p,
noEvent(actualStream(port_a1.h_outflow)),
noEvent(actualStream(port_a1.Xi_outflow)))
else
Medium1.setState_phX(port_a1.p,
inStream(port_a1.h_outflow),
inStream(port_a1.Xi_outflow))
if show_T "Medium properties in port_a1";
Medium1.ThermodynamicState sta_b1=
if allowFlowReversal1 then
Medium1.setState_phX(port_b1.p,
noEvent(actualStream(port_b1.h_outflow)),
noEvent(actualStream(port_b1.Xi_outflow)))
else
Medium1.setState_phX(port_b1.p,
port_b1.h_outflow,
port_b1.Xi_outflow)
if show_T "Medium properties in port_b1";
Medium2.ThermodynamicState sta_a2=
if allowFlowReversal2 then
Medium2.setState_phX(port_a2.p,
noEvent(actualStream(port_a2.h_outflow)),
noEvent(actualStream(port_a2.Xi_outflow)))
else
Medium2.setState_phX(port_a2.p,
inStream(port_a2.h_outflow),
inStream(port_a2.Xi_outflow))
if show_T "Medium properties in port_a2";
Medium2.ThermodynamicState sta_b2=
if allowFlowReversal2 then
Medium2.setState_phX(port_b2.p,
noEvent(actualStream(port_b2.h_outflow)),
noEvent(actualStream(port_b2.Xi_outflow)))
else
Medium2.setState_phX(port_b2.p,
port_b2.h_outflow,
port_b2.Xi_outflow)
if show_T "Medium properties in port_b2";
protected
Medium1.ThermodynamicState state_a1_inflow=
Medium1.setState_phX(port_a1.p, inStream(port_a1.h_outflow), inStream(port_a1.Xi_outflow))
"state for medium inflowing through port_a1";
Medium1.ThermodynamicState state_b1_inflow=
Medium1.setState_phX(port_b1.p, inStream(port_b1.h_outflow), inStream(port_b1.Xi_outflow))
"state for medium inflowing through port_b1";
Medium2.ThermodynamicState state_a2_inflow=
Medium2.setState_phX(port_a2.p, inStream(port_a2.h_outflow), inStream(port_a2.Xi_outflow))
"state for medium inflowing through port_a2";
Medium2.ThermodynamicState state_b2_inflow=
Medium2.setState_phX(port_b2.p, inStream(port_b2.h_outflow), inStream(port_b2.Xi_outflow))
"state for medium inflowing through port_b2";
end PartialFourPortInterface;
Buildings.Fluid.Interfaces.PartialFourPortParallel
Partial model with four ports for components with parallel flow
Information
This model defines an interface for components with four ports
in which flows occur in parallel.
The parameters allowFlowReversal1 and allowFlowReversal2
may be used by models that extend this model to treat flow reversal.
This model is identical to Modelica.Fluid.Interfaces.PartialTwoPort, except for the following:
- it has four ports, and
- the parameter
showDesignFlowDirectionis not implemented.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | Modelica.Media.Interfaces.Pa... | Medium 1 in the component | |
| replaceable package Medium2 | Modelica.Media.Interfaces.Pa... | Medium 2 in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
| Boolean | allowFlowReversal2 | true | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium1 | Medium 1 in the component | |
| replaceable package Medium2 | Medium 2 in the component | |
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
Modelica definition
partial model PartialFourPortParallel
"Partial model with four ports for components with parallel flow"
replaceable package Medium1 =
Modelica.Media.Interfaces.PartialMedium "Medium 1 in the component";
replaceable package Medium2 =
Modelica.Media.Interfaces.PartialMedium "Medium 2 in the component";
parameter Boolean allowFlowReversal1 = true
"= true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b)";
parameter Boolean allowFlowReversal2 = true
"= true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b)";
Modelica.Fluid.Interfaces.FluidPort_a port_a1(
redeclare final package Medium = Medium1,
m_flow(min=if allowFlowReversal1 then -Modelica.Constants.inf else 0),
h_outflow(start = Medium1.h_default, nominal = Medium1.h_default))
"Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_b port_b1(
redeclare final package Medium = Medium1,
m_flow(max=if allowFlowReversal1 then +Modelica.Constants.inf else 0),
h_outflow(start = Medium1.h_default, nominal = Medium1.h_default))
"Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)";
Modelica.Fluid.Interfaces.FluidPort_a port_a2(
redeclare final package Medium = Medium2,
m_flow(min=if allowFlowReversal2 then -Modelica.Constants.inf else 0),
h_outflow(start = Medium2.h_default, nominal = Medium2.h_default))
"Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)";
Modelica.Fluid.Interfaces.FluidPort_b port_b2(
redeclare final package Medium = Medium2,
m_flow(max=if allowFlowReversal2 then +Modelica.Constants.inf else 0),
h_outflow(start = Medium2.h_default, nominal = Medium2.h_default))
"Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)";
end PartialFourPortParallel;
Buildings.Fluid.Interfaces.PartialTwoPort
Partial component with two ports
Information
This partial model defines an interface for components with two ports.
The treatment of the design flow direction and of flow reversal are predefined based on the parameter allowFlowReversal.
The component may transport fluid and may have internal storage for a given fluid Medium.
Implementation
This model is similar to
Modelica.Fluid.Interfaces.PartialTwoPort
but it does not use the outer system declaration.
This declaration is omitted as in building energy simulation,
many models use multiple media, an in practice,
users have not used this global definition to assign parameters.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | Modelica.Media.Interfaces.Pa... | Medium in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium | Medium in the component | |
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
Modelica definition
partial model PartialTwoPort "Partial component with two ports"
replaceable package Medium =
Modelica.Media.Interfaces.PartialMedium "Medium in the component";
parameter Boolean allowFlowReversal = true
"= false to simplify equations, assuming, but not enforcing, no flow reversal";
Modelica.Fluid.Interfaces.FluidPort_a port_a(
redeclare final package Medium = Medium,
m_flow(min=if allowFlowReversal then -Modelica.Constants.inf else 0),
h_outflow(start = Medium.h_default, nominal = Medium.h_default))
"Fluid connector a (positive design flow direction is from port_a to port_b)";
Modelica.Fluid.Interfaces.FluidPort_b port_b(
redeclare final package Medium = Medium,
m_flow(max=if allowFlowReversal then +Modelica.Constants.inf else 0),
h_outflow(start = Medium.h_default, nominal = Medium.h_default))
"Fluid connector b (positive design flow direction is from port_a to port_b)";
end PartialTwoPort;
Buildings.Fluid.Interfaces.PartialTwoPortInterface
Partial model with two ports and declaration of quantities that are used by many models
Information
This component defines the interface for models with two fluid ports. It is similar to Modelica.Fluid.Interfaces.PartialTwoPortTransport, but it does not include the species balance
port_b.Xi_outflow = inStream(port_a.Xi_outflow);
Thus, it can be used as a base class for a heat and mass transfer component
The partial model extends
Buildings.Fluid.Interfaces.PartialTwoPort
and adds quantities that are used by many models such as
m_flow_nominal, m_flow and dp.
The model is used by other models in this package that add heat transfer, mass transfer and pressure drop equations. See for example Buildings.Fluid.Interfaces.StaticTwoPortHeatMassExchanger.
Extends from Buildings.Fluid.Interfaces.PartialTwoPort (Partial component with two ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| MassFlowRate | m_flow_small | 1E-4*abs(m_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
Modelica definition
partial model PartialTwoPortInterface
"Partial model with two ports and declaration of quantities that are used by many models"
extends Buildings.Fluid.Interfaces.PartialTwoPort(
port_a(p(start=Medium.p_default)),
port_b(p(start=Medium.p_default)));
parameter Modelica.Units.SI.MassFlowRate m_flow_nominal
"Nominal mass flow rate";
parameter Modelica.Units.SI.MassFlowRate m_flow_small(min=0) = 1E-4*abs(
m_flow_nominal) "Small mass flow rate for regularization of zero flow";
// Diagnostics
parameter Boolean show_T = false
"= true, if actual temperature at port is computed";
Modelica.Units.SI.MassFlowRate m_flow(start=_m_flow_start) = port_a.m_flow
"Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction)";
Modelica.Units.SI.PressureDifference dp(
start=_dp_start,
displayUnit="Pa") = port_a.p - port_b.p
"Pressure difference between port_a and port_b";
Medium.ThermodynamicState sta_a=
if allowFlowReversal then
Medium.setState_phX(port_a.p,
noEvent(actualStream(port_a.h_outflow)),
noEvent(actualStream(port_a.Xi_outflow)))
else
Medium.setState_phX(port_a.p,
noEvent(inStream(port_a.h_outflow)),
noEvent(inStream(port_a.Xi_outflow)))
if show_T "Medium properties in port_a";
Medium.ThermodynamicState sta_b=
if allowFlowReversal then
Medium.setState_phX(port_b.p,
noEvent(actualStream(port_b.h_outflow)),
noEvent(actualStream(port_b.Xi_outflow)))
else
Medium.setState_phX(port_b.p,
noEvent(port_b.h_outflow),
noEvent(port_b.Xi_outflow))
if show_T "Medium properties in port_b";
protected
final parameter Modelica.Units.SI.MassFlowRate _m_flow_start=0
"Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window";
final parameter Modelica.Units.SI.PressureDifference _dp_start(displayUnit=
"Pa") = 0
"Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window";
end PartialTwoPortInterface;
Buildings.Fluid.Interfaces.PartialTwoPortTransport
Partial element transporting fluid between two ports without storage of mass or energy
Information
This component transports fluid between its two ports, without storing mass or energy.
Energy may be exchanged with the environment though, e.g., in the form of work.
PartialTwoPortTransport is intended as base class for devices like orifices, valves and simple fluid machines.
Three equations need to be added by an extending class using this component:
- The momentum balance specifying the relationship between the pressure drop
dpand the mass flow ratem_flow, port_b.h_outflowfor flow in design direction, andport_a.h_outflowfor flow in reverse direction.
Moreover appropriate values shall be assigned to the following parameters:
dp_startfor a guess of the pressure dropm_flow_smallfor regularization of zero flow.
Implementation
This is similar to
Modelica.Fluid.Interfaces.PartialTwoPortTransport
except that it does not use the outer system declaration.
This declaration is omitted as in building energy simulation,
many models use multiple media, and in practice,
users have not used this global definition to assign parameters.
Extends from Buildings.Fluid.Interfaces.PartialTwoPort (Partial component with two ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| PressureDifference | dp_start | 0 | Guess value of dp = port_a.p - port_b.p [Pa] |
| MassFlowRate | m_flow_start | 0 | Guess value of m_flow = port_a.m_flow [kg/s] |
| MassFlowRate | m_flow_small | Small mass flow rate for regularization of zero flow [kg/s] | |
| Diagnostics | |||
| Boolean | show_T | true | = true, if temperatures at port_a and port_b are computed |
| Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
Modelica definition
partial model PartialTwoPortTransport
"Partial element transporting fluid between two ports without storage of mass or energy"
extends Buildings.Fluid.Interfaces.PartialTwoPort;
// Advanced
// Note: value of dp_start shall be refined by derived model,
// based on local dp_nominal
parameter Modelica.Units.SI.PressureDifference dp_start(displayUnit="Pa") = 0
"Guess value of dp = port_a.p - port_b.p";
parameter Medium.MassFlowRate m_flow_start = 0
"Guess value of m_flow = port_a.m_flow";
// Note: value of m_flow_small shall be refined by derived model,
// based on local m_flow_nominal
parameter Medium.MassFlowRate m_flow_small
"Small mass flow rate for regularization of zero flow";
// Diagnostics
parameter Boolean show_T = true
"= true, if temperatures at port_a and port_b are computed";
parameter Boolean show_V_flow = true
"= true, if volume flow rate at inflowing port is computed";
// Variables
Medium.MassFlowRate m_flow(
min=if allowFlowReversal then -Modelica.Constants.inf else 0,
start = m_flow_start) "Mass flow rate in design flow direction";
Modelica.Units.SI.PressureDifference dp(start=dp_start, displayUnit="Pa")
"Pressure difference between port_a and port_b (= port_a.p - port_b.p)";
Modelica.Units.SI.VolumeFlowRate V_flow=m_flow/
Modelica.Fluid.Utilities.regStep(
m_flow,
Medium.density(Medium.setState_phX(
p=port_a.p,
h=inStream(port_a.h_outflow),
X=inStream(port_a.Xi_outflow))),
Medium.density(Medium.setState_phX(
p=port_b.p,
h=inStream(port_b.h_outflow),
X=inStream(port_b.Xi_outflow))),
m_flow_small) if show_V_flow
"Volume flow rate at inflowing port (positive when flow from port_a to port_b)";
Medium.Temperature port_a_T=
Modelica.Fluid.Utilities.regStep(port_a.m_flow,
Medium.temperature(
Medium.setState_phX(
p = port_a.p,
h = inStream(port_a.h_outflow),
X = inStream(port_a.Xi_outflow))),
Medium.temperature(Medium.setState_phX(port_a.p, port_a.h_outflow, port_a.Xi_outflow)),
m_flow_small) if show_T
"Temperature close to port_a, if show_T = true";
Medium.Temperature port_b_T=
Modelica.Fluid.Utilities.regStep(port_b.m_flow,
Medium.temperature(
Medium.setState_phX(
p = port_b.p,
h = inStream(port_b.h_outflow),
X = inStream(port_b.Xi_outflow))),
Medium.temperature(Medium.setState_phX(port_b.p, port_b.h_outflow, port_b.Xi_outflow)),
m_flow_small) if show_T
"Temperature close to port_b, if show_T = true";
equation
// Pressure drop in design flow direction
dp = port_a.p - port_b.p;
// Design direction of mass flow rate
m_flow = port_a.m_flow;
assert(m_flow > -m_flow_small or allowFlowReversal,
"Reverting flow occurs even though allowFlowReversal is false");
// Mass balance (no storage)
port_a.m_flow + port_b.m_flow = 0;
// Transport of substances
port_a.Xi_outflow = if allowFlowReversal then inStream(port_b.Xi_outflow) else Medium.X_default[1:Medium.nXi];
port_b.Xi_outflow = inStream(port_a.Xi_outflow);
port_a.C_outflow = if allowFlowReversal then inStream(port_b.C_outflow) else zeros(Medium.nC);
port_b.C_outflow = inStream(port_a.C_outflow);
end PartialTwoPortTransport;
Buildings.Fluid.Interfaces.PartialTwoPortVector
Partial component with two ports, one of which being vectorized
Information
This partial model defines an interface for components with two ports, of which one is vectorized.
The treatment of the design flow direction and of flow reversal are
determined based on the parameter allowFlowReversal.
The component may transport fluid and may have internal storage.
Implementation
This model is similar to
Modelica.Fluid.Interfaces.PartialTwoPort
but it does not use the outer system declaration.
This declaration is omitted as in building energy simulation,
many models use multiple media, and in practice,
users have not used this global definition to assign parameters.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | Modelica.Media.Interfaces.Pa... | Medium in the component | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = true to allow flow reversal, false restricts to design direction (port_a -> port_b) |
| Advanced | |||
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| replaceable package Medium | Medium in the component | |
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to ports_b) |
| FluidPorts_b | ports_b[nPorts] | Fluid connectors b (positive design flow direction is from port_a to ports_b) |
Modelica definition
partial model PartialTwoPortVector "Partial component with two ports, one of which being vectorized"
replaceable package Medium =
Modelica.Media.Interfaces.PartialMedium "Medium in the component";
parameter Integer nPorts "Number of ports";
parameter Boolean allowFlowReversal=true
"= true to allow flow reversal, false restricts to design direction (port_a -> port_b)";
Modelica.Fluid.Interfaces.FluidPort_a port_a(
redeclare final package Medium = Medium,
m_flow(min=if allowFlowReversal then -Modelica.Constants.inf else 0),
h_outflow(start=Medium.h_default, nominal=Medium.h_default))
"Fluid connector a (positive design flow direction is from port_a to ports_b)";
Modelica.Fluid.Interfaces.FluidPorts_b ports_b[nPorts](
redeclare each package Medium = Medium,
each m_flow(max=if allowFlowReversal then +Modelica.Constants.inf else 0),
each h_outflow(start=Medium.h_default, nominal=Medium.h_default))
"Fluid connectors b (positive design flow direction is from port_a to ports_b)";
// Diagnostics
parameter Boolean show_T = false
"= true, if actual temperature at port is computed";
Medium.ThermodynamicState sta_a=
Medium.setState_phX(port_a.p,
noEvent(actualStream(port_a.h_outflow)),
noEvent(actualStream(port_a.Xi_outflow)))
if show_T "Medium properties in port_a";
Medium.ThermodynamicState sta_b[nPorts]=
Medium.setState_phX(ports_b.p,
noEvent(actualStream(ports_b.h_outflow)),
noEvent(actualStream(ports_b.Xi_outflow)))
if show_T "Medium properties in ports_b";
end PartialTwoPortVector;
Buildings.Fluid.Interfaces.PrescribedOutlet
Component that assigns the outlet fluid property at port_a based on an input signal
Information
This model sets the temperature or the water vapor mass fraction
of the medium that leaves port_a
to the value given by the input TSet or X_wSet,
subject to optional limitations on the capacity
for heating and cooling, or limitations on the humidification or dehumidification
moisture mass flow rate.
Also, optionally the model allows to take into account first order dynamics.
If the parameters energyDynamics is not equal to
Modelica.Fluid.Types.Dynamics.SteadyState,
the component models the dynamic response using a first order differential equation.
The time constant of the component is equal to the parameter tau.
This time constant is adjusted based on the mass flow rate using
τeff = τ |ṁ| ⁄ ṁnom
where τeff is the effective time constant for the given mass flow rate ṁ and τ is the time constant at the nominal mass flow rate ṁnom. This type of dynamics is equal to the dynamics that a completely mixed control volume would have.
This model has no pressure drop. See Buildings.Fluid.HeatExchangers.PrescribedOutlet for a model that instantiates this model and that has a pressure drop.
In case of reverse flow,
the fluid that leaves port_a has the same
properties as the fluid that enters port_b.
Extends from Buildings.Fluid.Interfaces.PartialTwoPortInterface (Partial model with two ports and declaration of quantities that are used by many models).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| HeatFlowRate | QMax_flow | Modelica.Constants.inf | Maximum heat flow rate for heating (positive) [W] |
| HeatFlowRate | QMin_flow | -Modelica.Constants.inf | Maximum heat flow rate for cooling (negative) [W] |
| MassFlowRate | mWatMax_flow | Modelica.Constants.inf | Maximum water mass flow rate addition (positive) [kg/s] |
| MassFlowRate | mWatMin_flow | -Modelica.Constants.inf | Maximum water mass flow rate removal (negative) [kg/s] |
| Boolean | use_TSet | true | Set to false to disable temperature set point |
| Boolean | use_X_wSet | true | Set to false to disable water vapor set point |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| MassFlowRate | m_flow_small | 1E-4*abs(m_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Dynamics | |||
| Time | tau | 10 | Time constant at nominal flow rate (used if energyDynamics not equal Modelica.Fluid.Types.Dynamics.SteadyState) [s] |
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Type of energy balance: dynamic (3 initialization options) or steady state |
| Initialization | |||
| Temperature | T_start | Medium.T_default | Start value of temperature [K] |
| MassFraction | X_start[Medium.nX] | Medium.X_default | Start value of mass fractions m_i/m [1] |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
| input RealInput | TSet | Set point temperature of the fluid that leaves port_b [K] |
| input RealInput | X_wSet | Set point for water vapor mass fraction of the fluid that leaves port_b [1] |
| output RealOutput | Q_flow | Heat flow rate added to the fluid (if flow is from port_a to port_b) [W] |
| output RealOutput | mWat_flow | Water vapor mass flow rate added to the fluid (if flow is from port_a to port_b) [kg/s] |
Modelica definition
model PrescribedOutlet
"Component that assigns the outlet fluid property at port_a based on an input signal"
extends Buildings.Fluid.Interfaces.PartialTwoPortInterface;
parameter Modelica.Units.SI.HeatFlowRate QMax_flow(min=0) = Modelica.Constants.inf
"Maximum heat flow rate for heating (positive)";
parameter Modelica.Units.SI.HeatFlowRate QMin_flow(max=0) = -Modelica.Constants.inf
"Maximum heat flow rate for cooling (negative)";
parameter Modelica.Units.SI.MassFlowRate mWatMax_flow(min=0) = Modelica.Constants.inf
"Maximum water mass flow rate addition (positive)";
parameter Modelica.Units.SI.MassFlowRate mWatMin_flow(max=0) = -Modelica.Constants.inf
"Maximum water mass flow rate removal (negative)";
parameter Modelica.Units.SI.Time tau(min=0) = 10
"Time constant at nominal flow rate (used if energyDynamics not equal Modelica.Fluid.Types.Dynamics.SteadyState)";
parameter Modelica.Units.SI.Temperature T_start=Medium.T_default
"Start value of temperature";
parameter Modelica.Units.SI.MassFraction X_start[Medium.nX]=Medium.X_default
"Start value of mass fractions m_i/m";
// Dynamics
parameter Modelica.Fluid.Types.Dynamics energyDynamics=Modelica.Fluid.Types.Dynamics.SteadyState
"Type of energy balance: dynamic (3 initialization options) or steady state";
parameter Boolean use_TSet = true
"Set to false to disable temperature set point";
parameter Boolean use_X_wSet = true
"Set to false to disable water vapor set point";
Modelica.Blocks.Interfaces.RealInput TSet(unit="K", displayUnit="degC") if use_TSet
"Set point temperature of the fluid that leaves port_b";
Modelica.Blocks.Interfaces.RealInput X_wSet(unit="1") if use_X_wSet
"Set point for water vapor mass fraction of the fluid that leaves port_b";
Modelica.Blocks.Interfaces.RealOutput Q_flow(unit="W")
"Heat flow rate added to the fluid (if flow is from port_a to port_b)";
Modelica.Blocks.Interfaces.RealOutput mWat_flow(unit="kg/s")
"Water vapor mass flow rate added to the fluid (if flow is from port_a to port_b)";
protected
parameter Modelica.Units.SI.SpecificHeatCapacity cp_default=
Medium.specificHeatCapacityCp(Medium.setState_pTX(
p=Medium.p_default,
T=Medium.T_default,
X=Medium.X_default)) "Specific heat capacity at default medium state";
parameter Boolean restrictHeat = QMax_flow < Modelica.Constants.inf/10.0
"Flag, true if maximum heating power is restricted";
parameter Boolean restrictCool = QMin_flow > -Modelica.Constants.inf/10.0
"Flag, true if maximum cooling power is restricted";
parameter Boolean restrictHumi = mWatMax_flow < Modelica.Constants.inf/10.0
"Flag, true if maximum humidification is restricted";
parameter Boolean restrictDehu = mWatMin_flow > -Modelica.Constants.inf/10.0
"Flag, true if maximum dehumidification is restricted";
parameter Modelica.Units.SI.SpecificEnthalpy deltaH=cp_default*1E-6
"Small value for deltaH used for regularization";
parameter Modelica.Units.SI.MassFraction deltaXi=1E-6
"Small mass fraction used for regularization";
Modelica.Units.SI.MassFlowRate m_flow_pos
"Mass flow rate, or zero if reverse flow";
Modelica.Units.SI.MassFlowRate m_flow_non_zero
"Mass flow rate bounded away from zero";
Modelica.Units.SI.SpecificEnthalpy hSet
"Set point for enthalpy leaving port_b";
Modelica.Units.SI.Temperature T
"Temperature of outlet state assuming unlimited capacity and taking dynamics into account";
Modelica.Units.SI.MassFraction Xi
"Water vapor mass fraction of outlet state assuming unlimited capacity and taking dynamics into account";
Modelica.Units.SI.MassFraction Xi_instream[Medium.nXi]
"Instreaming water vapor mass fraction at port_a";
Modelica.Units.SI.MassFraction Xi_outflow
"Outstreaming water vapor mass fraction at port_a";
Modelica.Units.SI.SpecificEnthalpy dhAct
"Actual enthalpy difference from port_a to port_b";
Real dXiAct(final unit="1")
"Actual mass fraction difference from port_a to port_b";
Real k(start=1)
"Gain to take flow rate into account for sensor time constant";
Real mNor_flow "Normalized mass flow rate";
Modelica.Blocks.Interfaces.RealInput TSet_internal(unit="K", displayUnit="degC")
"Internal connector for set point temperature of the fluid that leaves port_b";
Modelica.Blocks.Interfaces.RealInput X_wSet_internal(unit="1")
"Internal connector for set point for water vapor mass fraction of the fluid that leaves port_b";
initial equation
// Set initial conditions, unless use_{T,Xi}Set = false in which case
// it is not a state.
if use_TSet then
if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(T) = 0;
elseif energyDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
T = T_start;
end if;
end if;
if use_X_wSet then
if energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyStateInitial then
der(Xi) = 0;
elseif energyDynamics == Modelica.Fluid.Types.Dynamics.FixedInitial then
Xi = X_start[1];
end if;
end if;
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau > Modelica.Constants.eps,
"The parameter tau, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau = " + String(tau) + "\n");
if use_X_wSet then
assert(Medium.nX > 1, "If use_X_wSet = true, require a medium with water vapor, such as Buildings.Media.Air");
end if;
equation
// Conditional connectors
if not use_TSet then
TSet_internal = 293.15;
end if;
connect(TSet, TSet_internal);
if not use_X_wSet then
X_wSet_internal = 0.01;
end if;
connect(X_wSet, X_wSet_internal);
if ((use_TSet or use_X_wSet) and energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) then
mNor_flow = port_a.m_flow/m_flow_nominal;
k = Modelica.Fluid.Utilities.regStep(x=port_a.m_flow,
y1= mNor_flow,
y2=-mNor_flow,
x_small=m_flow_small);
else
mNor_flow = 1;
k = 1;
end if;
if use_TSet and energyDynamics <> Modelica.Fluid.Types.Dynamics.SteadyState then
der(T) = (TSet_internal-T)*k/tau;
else
T = TSet_internal;
end if;
if use_X_wSet and energyDynamics <> Modelica.Fluid.Types.Dynamics.SteadyState then
der(Xi) = (X_wSet_internal-Xi)*k/tau;
else
Xi = X_wSet_internal;
end if;
Xi_instream = inStream(port_a.Xi_outflow);
// Set point without any capacity limitation
hSet = if use_TSet then Medium.specificEnthalpy(
Medium.setState_pTX(
p = port_a.p,
T = T,
X = Xi_instream + fill(dXiAct, Medium.nXi)))
else Medium.h_default;
m_flow_pos = Buildings.Utilities.Math.Functions.smoothMax(
x1=m_flow,
x2=0,
deltaX=m_flow_small);
if not restrictHeat and not restrictCool and
not restrictHumi and not restrictDehu then
m_flow_non_zero = Modelica.Constants.eps;
else
m_flow_non_zero = Buildings.Utilities.Math.Functions.smoothMax(
x1 = port_a.m_flow,
x2 = m_flow_small,
deltaX=m_flow_small/2);
end if;
// Compute mass fraction leaving the component.
// Below, we use sum(Xi_instream) as Xi anyway has only one element.
// However, scalar(Xi_instream) would not work as dim(Xi_instream) = 0
// if the medium is not a mixture.
// Note that the computations for the mass fraction and for the
// enthalpy change are identical. In a development version, they were
// put in a function, but this led to large nonlinear systems of equations.
if use_X_wSet then
if not restrictHumi and not restrictDehu then
// No capacity limit
dXiAct = Xi_outflow-sum(Xi_instream);
Xi_outflow = Xi;
mWat_flow = m_flow_pos*(Xi - sum(Xi_instream));
else
if restrictHumi and restrictDehu then
// Capacity limits for heating and cooling
dXiAct =Buildings.Utilities.Math.Functions.smoothLimit(
x=Xi - sum(Xi_instream),
l=mWatMin_flow/m_flow_non_zero,
u=mWatMax_flow/m_flow_non_zero,
deltaX=deltaXi);
elseif restrictHumi then
// Capacity limit for heating only
dXiAct =Buildings.Utilities.Math.Functions.smoothMin(
x1=Xi - sum(Xi_instream),
x2=mWatMax_flow/m_flow_non_zero,
deltaX=deltaXi);
else
// Capacity limit for cooling only
dXiAct =Buildings.Utilities.Math.Functions.smoothMax(
x1=Xi - sum(Xi_instream),
x2=mWatMin_flow/m_flow_non_zero,
deltaX=deltaXi);
end if;
Xi_outflow = sum(Xi_instream) + dXiAct;
mWat_flow = m_flow_pos*dXiAct;
end if;
port_b.Xi_outflow = fill(Xi_outflow, Medium.nXi);
else
Xi_outflow = sum(Xi_instream);
mWat_flow = 0;
dXiAct = 0;
port_b.Xi_outflow = Xi_instream;
end if;
// Compute enthalpy leaving the component.
if use_TSet then
if not restrictHeat and not restrictCool then
// No capacity limit
dhAct = 0;
port_b.h_outflow = hSet;
Q_flow = m_flow_pos*(hSet - inStream(port_a.h_outflow));
else
if restrictHeat and restrictCool then
// Capacity limits for heating and cooling
dhAct =Buildings.Utilities.Math.Functions.smoothLimit(
x=hSet - inStream(port_a.h_outflow),
l=QMin_flow/m_flow_non_zero,
u=QMax_flow/m_flow_non_zero,
deltaX=deltaH);
elseif restrictHeat then
// Capacity limit for heating only
dhAct =Buildings.Utilities.Math.Functions.smoothMin(
x1=hSet - inStream(port_a.h_outflow),
x2=QMax_flow/m_flow_non_zero,
deltaX=deltaH);
else
// Capacity limit for cooling only
dhAct =Buildings.Utilities.Math.Functions.smoothMax(
x1=hSet - inStream(port_a.h_outflow),
x2=QMin_flow/m_flow_non_zero,
deltaX=deltaH);
end if;
port_b.h_outflow = inStream(port_a.h_outflow) + dhAct;
Q_flow = m_flow_pos*dhAct;
end if;
else
port_b.h_outflow = inStream(port_a.h_outflow);
Q_flow = 0;
dhAct = 0;
end if;
// Outflowing property at port_a is unaffected by this model.
if allowFlowReversal then
port_a.h_outflow = inStream(port_b.h_outflow);
port_a.Xi_outflow = inStream(port_b.Xi_outflow);
port_a.C_outflow = inStream(port_b.C_outflow);
else
port_a.h_outflow = Medium.h_default;
port_a.Xi_outflow = Medium.X_default[1:Medium.nXi];
port_a.C_outflow = zeros(Medium.nC);
end if;
// No pressure drop
dp = 0;
// Mass balance (no storage)
port_a.m_flow + port_b.m_flow = 0;
// Transport of substances
port_b.C_outflow = inStream(port_a.C_outflow);
if not allowFlowReversal then
assert(m_flow > -m_flow_small,
"Reverting flow occurs even though allowFlowReversal is false");
end if;
end PrescribedOutlet;
Buildings.Fluid.Interfaces.StaticFourPortHeatMassExchanger
Partial model transporting two fluid streams between four ports without storing mass or energy
Information
This component transports two fluid streams between four ports, without storing mass or energy. It is similar to Buildings.Fluid.Interfaces.StaticTwoPortHeatMassExchanger, but it has four ports instead of two.
If dpN_nominal > Modelica.Constants.eps,
where N denotes the fluid 1 or 2,
then the model computes
pressure drop due to flow friction in the respective fluid stream.
The pressure drop is defined by a quadratic function that goes through
the point (mN_flow_nominal, dpN_nominal).
At |mN_flow| < deltaMN * mN_flow_nominal,
the pressure drop vs. flow relation is linearized.
If the parameter linearizeFlowResistanceN is set to true,
then the whole pressure drop vs. flow resistance curve is linearized.
Implementation
This model uses inputs and constants that need to be set by models
that extend or instantiate this model.
The following inputs need to be assigned, where N denotes 1 or
2:
-
QN_flow, which is the sensible and latent heat flow rate added to the medium N. -
mWatN_flow, which is the moisture mass flow rate added to the medium N.
Set the constant sensibleOnlyN=true if the model that extends
or instantiates this model sets mWatN_flow = 0.
Note that the model does not implement 0 = Q1_flow + Q2_flow or
0 = mXi1_flow + mXi2_flow. If there is no heat or mass transfer
with the environment, then a model that extends this model needs to provide these
equations.
Extends from Buildings.Fluid.Interfaces.PartialFourPortInterface (Partial model with four ports and declaration of quantities that are used by many models), Buildings.Fluid.Interfaces.FourPortFlowResistanceParameters (Parameters for flow resistance for models with four ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
| replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
| Boolean | sensibleOnly1 | Set to true if sensible exchange only for medium 1 | |
| Boolean | sensibleOnly2 | Set to true if sensible exchange only for medium 2 | |
| Nominal condition | |||
| MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
| MassFlowRate | m2_flow_nominal | Nominal mass flow rate [kg/s] | |
| PressureDifference | dp1_nominal | Pressure difference [Pa] | |
| PressureDifference | dp2_nominal | Pressure difference [Pa] | |
| Assumptions | |||
| Boolean | allowFlowReversal1 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 |
| Boolean | allowFlowReversal2 | true | = false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 |
| Advanced | |||
| MassFlowRate | m1_flow_small | 1E-4*abs(m1_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| MassFlowRate | m2_flow_small | 1E-4*abs(m2_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Flow resistance | |||
| Medium 1 | |||
| Boolean | computeFlowResistance1 | (dp1_nominal > Modelica.Cons... | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp1 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance1 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM1 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 2 | |||
| Boolean | computeFlowResistance2 | (dp2_nominal > Modelica.Cons... | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp2 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance2 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM2 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a1 | Fluid connector a1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_b | port_b1 | Fluid connector b1 (positive design flow direction is from port_a1 to port_b1) |
| FluidPort_a | port_a2 | Fluid connector a2 (positive design flow direction is from port_a2 to port_b2) |
| FluidPort_b | port_b2 | Fluid connector b2 (positive design flow direction is from port_a2 to port_b2) |
Modelica definition
model StaticFourPortHeatMassExchanger
"Partial model transporting two fluid streams between four ports without storing mass or energy"
extends Buildings.Fluid.Interfaces.PartialFourPortInterface;
extends Buildings.Fluid.Interfaces.FourPortFlowResistanceParameters(
final computeFlowResistance1=(dp1_nominal > Modelica.Constants.eps),
final computeFlowResistance2=(dp2_nominal > Modelica.Constants.eps));
constant Boolean prescribedHeatFlowRate1 = false
"Set to true if the heat flow rate into fluid 1 is not a function of the component temperature";
constant Boolean prescribedHeatFlowRate2 = false
"Set to true if the heat flow rate into fluid 2 is not a function of the component temperature";
constant Boolean homotopyInitialization = true "= true, use homotopy method";
// Q1_flow is sensible plus latent heat flow rate
input Modelica.Units.SI.HeatFlowRate Q1_flow
"Heat transferred into the medium 1";
input Medium1.MassFlowRate mWat1_flow
"Moisture mass flow rate added to the medium 1";
// Q2_flow is sensible plus latent heat flow rate
input Modelica.Units.SI.HeatFlowRate Q2_flow
"Heat transferred into the medium 2";
input Medium2.MassFlowRate mWat2_flow
"Moisture mass flow rate added to the medium 2";
constant Boolean sensibleOnly1
"Set to true if sensible exchange only for medium 1";
constant Boolean sensibleOnly2
"Set to true if sensible exchange only for medium 2";
protected
Buildings.Fluid.Interfaces.StaticTwoPortHeatMassExchanger bal1(
redeclare final package Medium=Medium1,
final sensibleOnly = sensibleOnly1,
final prescribedHeatFlowRate=prescribedHeatFlowRate1,
final m_flow_nominal = m1_flow_nominal,
final dp_nominal = dp1_nominal,
final allowFlowReversal = allowFlowReversal1,
final m_flow_small = m1_flow_small,
final homotopyInitialization = homotopyInitialization,
final from_dp = from_dp1,
final linearizeFlowResistance = linearizeFlowResistance1,
final deltaM = deltaM1,
final Q_flow = Q1_flow,
final mWat_flow = mWat1_flow)
"Model for heat, mass, species, trace substance and pressure balance of stream 1";
Buildings.Fluid.Interfaces.StaticTwoPortHeatMassExchanger bal2(
redeclare final package Medium=Medium2,
final sensibleOnly = sensibleOnly2,
final prescribedHeatFlowRate=prescribedHeatFlowRate2,
final m_flow_nominal = m2_flow_nominal,
final dp_nominal = dp2_nominal,
final allowFlowReversal = allowFlowReversal2,
final m_flow_small = m2_flow_small,
final homotopyInitialization = homotopyInitialization,
final from_dp = from_dp2,
final linearizeFlowResistance = linearizeFlowResistance2,
final deltaM = deltaM2,
final Q_flow = Q2_flow,
final mWat_flow = mWat2_flow)
"Model for heat, mass, species, trace substance and pressure balance of stream 2";
initial equation
assert(homotopyInitialization, "In " + getInstanceName() +
": The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.",
level = AssertionLevel.warning);
equation
connect(bal1.port_a, port_a1);
connect(bal1.port_b, port_b1);
connect(bal2.port_a, port_a2);
connect(bal2.port_b, port_b2);
end StaticFourPortHeatMassExchanger;
Buildings.Fluid.Interfaces.StaticTwoPortConservationEquation
Partial model for static energy and mass conservation equations
Information
This model transports fluid between its two ports, without storing mass or energy. It implements a steady-state conservation equation for energy and mass fractions. The model has zero pressure drop between its ports.
Typical use and important parameters
Set the parameter use_mWat_flow_in=true to enable an
input connector for mWat_flow.
Otherwise, the model uses mWat_flow = 0.
If the constant simplify_mWat_flow = true, which is its default value,
then the equation
port_a.m_flow + port_b.m_flow = - mWat_flow;
is simplified as
port_a.m_flow + port_b.m_flow = 0;
This causes an error in the mass balance of about 0.5%, but generally leads to simpler equations because the pressure drop equations are then decoupled from the mass exchange in this component.
To increase the numerical robustness of the model, the constant
prescribedHeatFlowRate can be set.
Use the following settings:
- Set
prescribedHeatFlowRate=trueif the only means of heat transfer at theheatPortis a prescribed heat flow rate that is not a function of the temperature difference between the medium and an ambient temperature. Examples include an ideal electrical heater, a pump that rejects heat into the fluid stream, or a chiller that removes heat based on a performance curve. If theheatPortis not connected, then setprescribedHeatFlowRate=trueas in this case,heatPort.Q_flow=0. - Set
prescribedHeatFlowRate=falseif there is heat flow at theheatPortcomputed as K * (T-heatPort.T), for some temperature T and some conductance K, which may itself be a function of temperature or mass flow rate.
If there is a combination of K * (T-heatPort.T) and a prescribed heat flow rate, for example a solar collector that dissipates heat to the ambient and receives heat from the solar radiation, then setprescribedHeatFlowRate=false.
If prescribedHeatFlow=true, then energy and mass balance
equations are formulated to guard against numerical problems near
zero flow that can occur if Q_flow or m_flow
are the results of an iterative solver.
Implementation
Input connectors of the model are
-
Q_flow, which is the sensible plus latent heat flow rate added to the medium, -
mWat_flow, which is the moisture mass flow rate added to the medium, and -
C_flow, which is the trace substance mass flow rate added to the medium.
The model can only be used as a steady-state model with two fluid ports. For a model with a dynamic balance, and more fluid ports, use Buildings.Fluid.Interfaces.ConservationEquation.
Extends from Buildings.Fluid.Interfaces.PartialTwoPortInterface (Partial model with two ports and declaration of quantities that are used by many models).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| MassFlowRate | m_flow_small | 1E-4*abs(m_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Boolean | use_mWat_flow | false | Set to true to enable input connector for moisture mass flow rate |
| Boolean | use_C_flow | false | Set to true to enable input connector for trace substance |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
| input RealInput | Q_flow | Sensible plus latent heat flow rate transferred into the medium [W] |
| input RealInput | mWat_flow | Moisture mass flow rate added to the medium [kg/s] |
| input RealInput | C_flow[Medium.nC] | Trace substance mass flow rate added to the medium |
| output RealOutput | hOut | Leaving specific enthalpy of the component [J/kg] |
| output RealOutput | XiOut[Medium.nXi] | Leaving species concentration of the component [1] |
| output RealOutput | COut[Medium.nC] | Leaving trace substances of the component |
Modelica definition
model StaticTwoPortConservationEquation
"Partial model for static energy and mass conservation equations"
extends Buildings.Fluid.Interfaces.PartialTwoPortInterface;
constant Boolean simplify_mWat_flow = true
"Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero";
constant Boolean prescribedHeatFlowRate = false
"Set to true if the heat flow rate is not a function of a temperature difference to the fluid temperature";
parameter Boolean use_mWat_flow = false
"Set to true to enable input connector for moisture mass flow rate";
parameter Boolean use_C_flow = false
"Set to true to enable input connector for trace substance";
Modelica.Blocks.Interfaces.RealInput Q_flow(unit="W")
"Sensible plus latent heat flow rate transferred into the medium";
Modelica.Blocks.Interfaces.RealInput mWat_flow(final quantity="MassFlowRate",
unit="kg/s")
if use_mWat_flow "Moisture mass flow rate added to the medium";
Modelica.Blocks.Interfaces.RealInput[Medium.nC] C_flow
if use_C_flow "Trace substance mass flow rate added to the medium";
// Outputs that are needed in models that extend this model
Modelica.Blocks.Interfaces.RealOutput hOut(final unit="J/kg")
"Leaving specific enthalpy of the component";
Modelica.Blocks.Interfaces.RealOutput XiOut[Medium.nXi](each unit="1",
each min=0,
each max=1,
nominal=0.01*ones(Medium.nXi))
"Leaving species concentration of the component";
Modelica.Blocks.Interfaces.RealOutput COut[Medium.nC](each min=0)
"Leaving trace substances of the component";
protected
final parameter Boolean use_m_flowInv=
(prescribedHeatFlowRate or use_mWat_flow or use_C_flow)
"Flag, true if m_flowInv is used in the model";
final parameter Real s[Medium.nXi] = {if Modelica.Utilities.Strings.isEqual(string1=Medium.substanceNames[i],
string2="Water",
caseSensitive=false)
then 1 else 0 for i in 1:Medium.nXi}
"Vector with zero everywhere except where species is";
Real m_flowInv(unit="s/kg") "Regularization of 1/m_flow of port_a";
Modelica.Units.SI.MassFlowRate mXi_flow[Medium.nXi]
"Mass flow rates of independent substances added to the medium";
// Parameters for inverseXRegularized.
// These are assigned here for efficiency reason.
// Otherwise, they would need to be computed each time
// the function is invocated.
final parameter Real deltaReg = m_flow_small/1E3
"Smoothing region for inverseXRegularized";
final parameter Real deltaInvReg = 1/deltaReg
"Inverse value of delta for inverseXRegularized";
final parameter Real aReg = -15*deltaInvReg
"Polynomial coefficient for inverseXRegularized";
final parameter Real bReg = 119*deltaInvReg^2
"Polynomial coefficient for inverseXRegularized";
final parameter Real cReg = -361*deltaInvReg^3
"Polynomial coefficient for inverseXRegularized";
final parameter Real dReg = 534*deltaInvReg^4
"Polynomial coefficient for inverseXRegularized";
final parameter Real eReg = -380*deltaInvReg^5
"Polynomial coefficient for inverseXRegularized";
final parameter Real fReg = 104*deltaInvReg^6
"Polynomial coefficient for inverseXRegularized";
final parameter Medium.ThermodynamicState state_default = Medium.setState_pTX(
T=Medium.T_default,
p=Medium.p_default,
X=Medium.X_default[1:Medium.nXi]) "Medium state at default values";
// Density at medium default values, used to compute the size of control volumes
final parameter Modelica.Units.SI.SpecificHeatCapacity cp_default=
Medium.specificHeatCapacityCp(state=state_default)
"Specific heat capacity, used to verify energy conservation";
constant Modelica.Units.SI.TemperatureDifference dTMax(min=1) = 200
"Maximum temperature difference across the StaticTwoPortConservationEquation";
// Conditional connectors
Modelica.Blocks.Interfaces.RealInput mWat_flow_internal(unit="kg/s")
"Needed to connect to conditional connector";
Modelica.Blocks.Interfaces.RealInput C_flow_internal[Medium.nC]
"Needed to connect to conditional connector";
initial equation
// Assert that the substance with name 'water' has been found.
if use_mWat_flow then
assert(Medium.nXi == 0 or abs(sum(s)-1) < 1e-5,
"If Medium.nXi > 1, then substance 'water' must be present for one component.'"
+ Medium.mediumName + "'.\n"
+ "Check medium model.");
end if;
equation
// Conditional connectors
connect(mWat_flow, mWat_flow_internal);
if not use_mWat_flow then
mWat_flow_internal = 0;
end if;
connect(C_flow, C_flow_internal);
if not use_C_flow then
C_flow_internal = zeros(Medium.nC);
end if;
// Species flow rate from connector mWat_flow
mXi_flow = mWat_flow_internal * s;
// Regularization of m_flow around the origin to avoid a division by zero
// m_flowInv is only used if prescribedHeatFlowRate == true, or
// if the input connectors mWat_flow or C_flow are enabled.
if use_m_flowInv then
m_flowInv = Buildings.Utilities.Math.Functions.inverseXRegularized(
x=port_a.m_flow,
delta=deltaReg, deltaInv=deltaInvReg,
a=aReg, b=bReg, c=cReg, d=dReg, e=eReg, f=fReg);
else
// m_flowInv is not used.
m_flowInv = 0;
end if;
if prescribedHeatFlowRate then
assert(noEvent( abs(Q_flow) < dTMax*cp_default*max(m_flow_small/1E3, abs(m_flow))),
"In " + getInstanceName() + ":
The heat flow rate equals " + String(Q_flow) +
" W and the mass flow rate equals " + String(m_flow) + " kg/s,
which results in a temperature difference " +
String(abs(Q_flow)/ (cp_default*max(m_flow_small/1E3, abs(m_flow)))) +
" K > dTMax=" +String(dTMax) + " K.
This may indicate that energy is not conserved for small mass flow rates.
The implementation may require prescribedHeatFlowRate = false.");
end if;
if allowFlowReversal then
// Formulate hOut using spliceFunction. This avoids an event iteration.
// The introduced error is small because deltax=m_flow_small/1e3
hOut = Buildings.Utilities.Math.Functions.regStep(y1=port_b.h_outflow,
y2=port_a.h_outflow,
x=port_a.m_flow,
x_small=m_flow_small/1E3);
XiOut = Buildings.Utilities.Math.Functions.regStep(y1=port_b.Xi_outflow,
y2=port_a.Xi_outflow,
x=port_a.m_flow,
x_small=m_flow_small/1E3);
COut = Buildings.Utilities.Math.Functions.regStep(y1=port_b.C_outflow,
y2=port_a.C_outflow,
x=port_a.m_flow,
x_small=m_flow_small/1E3);
else
hOut = port_b.h_outflow;
XiOut = port_b.Xi_outflow;
COut = port_b.C_outflow;
end if;
//////////////////////////////////////////////////////////////////////////////////////////
// Energy balance and mass balance
// Mass balance (no storage)
port_a.m_flow + port_b.m_flow = if simplify_mWat_flow then 0 else -mWat_flow_internal;
// Substance balance
// a) forward flow
if use_m_flowInv then
port_b.Xi_outflow = inStream(port_a.Xi_outflow) + mXi_flow * m_flowInv;
else // no water is added
assert(use_mWat_flow == false, "In " + getInstanceName() + ": Wrong implementation for forward flow.");
port_b.Xi_outflow = inStream(port_a.Xi_outflow);
end if;
// b) backward flow
if allowFlowReversal then
if use_m_flowInv then
port_a.Xi_outflow = inStream(port_b.Xi_outflow) - mXi_flow * m_flowInv;
else // no water added
assert(use_mWat_flow == false, "In " + getInstanceName() + ": Wrong implementation for reverse flow.");
port_a.Xi_outflow = inStream(port_b.Xi_outflow);
end if;
else // no flow reversal
port_a.Xi_outflow = Medium.X_default[1:Medium.nXi];
end if;
// Energy balance.
// This equation is approximate since m_flow = port_a.m_flow is used for the mass flow rate
// at both ports. Since mWat_flow_internal << m_flow, the error is small.
if prescribedHeatFlowRate then
port_b.h_outflow = inStream(port_a.h_outflow) + Q_flow * m_flowInv;
if allowFlowReversal then
port_a.h_outflow = inStream(port_b.h_outflow) - Q_flow * m_flowInv;
else
port_a.h_outflow = Medium.h_default;
end if;
else
// Case with prescribedHeatFlowRate == false.
// port_b.h_outflow is known and the equation needs to be solved for Q_flow.
// Hence, we cannot use m_flowInv as for m_flow=0, any Q_flow would satisfiy
// Q_flow * m_flowInv = 0.
// The same applies for port_b.Xi_outflow and mXi_flow.
port_a.m_flow * (inStream(port_a.h_outflow) - port_b.h_outflow) = -Q_flow;
if allowFlowReversal then
port_a.m_flow * (inStream(port_b.h_outflow) - port_a.h_outflow) = +Q_flow;
else
// When allowFlowReversal = false, the downstream enthalpy does not matter.
// Therefore a dummy value is used to avoid algebraic loops
port_a.h_outflow = Medium.h_default;
end if;
end if;
// Transport of trace substances
if use_m_flowInv and use_C_flow then
port_b.C_outflow = inStream(port_a.C_outflow) + C_flow_internal * m_flowInv;
else // no trace substance added.
assert(not use_C_flow, "In " + getInstanceName() + ": Wrong implementation of trace substance balance for forward flow.");
port_b.C_outflow = inStream(port_a.C_outflow);
end if;
if allowFlowReversal then
if use_C_flow then
port_a.C_outflow = inStream(port_b.C_outflow) - C_flow_internal * m_flowInv;
else
port_a.C_outflow = inStream(port_b.C_outflow);
end if;
else
port_a.C_outflow = zeros(Medium.nC);
end if;
////////////////////////////////////////////////////////////////////////////
// No pressure drop in this model
port_a.p = port_b.p;
end StaticTwoPortConservationEquation;
Buildings.Fluid.Interfaces.StaticTwoPortHeatMassExchanger
Partial model transporting fluid between two ports without storing mass or energy
Information
This component transports fluid between its two ports, without storing mass or energy. It is based on Modelica.Fluid.Interfaces.PartialTwoPortTransport but it does use a different implementation for handling reverse flow because in this component, mass flow rate can be added or removed from the medium.
If dp_nominal > Modelica.Constants.eps, this component computes
pressure drop due to flow friction.
The pressure drop is defined by a quadratic function that goes through
the point (m_flow_nominal, dp_nominal). At |m_flow| < deltaM * m_flow_nominal,
the pressure drop vs. flow relation is linearized.
If the parameter linearizeFlowResistance is set to true,
then the whole pressure drop vs. flow resistance curve is linearized.
Implementation
This model uses inputs and constants that need to be set by models that extend or instantiate this model. The following inputs need to be assigned:-
Q_flow, which is the sensible and latent heat flow rate added to the medium. -
mWat_flow, which is the moisture mass flow rate added to the medium.
Set the constant sensibleOnly=true if the model that extends
or instantiates this model sets mWat_flow = 0.
To increase the numerical robustness of the model, the constant
prescribedHeatFlowRate can be set.
Use the following settings:
- Set
prescribedHeatFlowRate=trueif the only means of heat transfer at theheatPortis a prescribed heat flow rate that is not a function of the temperature difference between the medium and an ambient temperature. Examples include an ideal electrical heater, a pump that rejects heat into the fluid stream, or a chiller that removes heat based on a performance curve. If theheatPortis not connected, then setprescribedHeatFlowRate=trueas in this case,heatPort.Q_flow=0. - Set
prescribedHeatFlowRate=falseif there is heat flow at theheatPortcomputed as K * (T-heatPort.T), for some temperature T and some conductance K, which may itself be a function of temperature or mass flow rate.
If there is a combination of K * (T-heatPort.T) and a prescribed heat flow rate, for example a solar collector that dissipates heat to the ambient and receives heat from the solar radiation, then setprescribedHeatFlowRate=false.
If prescribedHeatFlow=true, then energy and mass balance
equations are formulated to guard against numerical problems near
zero flow that can occur if Q_flow or m_flow
are the results of an iterative solver.
Extends from Buildings.Fluid.Interfaces.PartialTwoPortInterface (Partial model with two ports and declaration of quantities that are used by many models), Buildings.Fluid.Interfaces.TwoPortFlowResistanceParameters (Parameters for flow resistance for models with two ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Boolean | sensibleOnly | Set to true if sensible exchange only | |
| Boolean | prescribedHeatFlowRate | Set to true if the heat flow rate is not a function of the component temperature | |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
| PressureDifference | dp_nominal | Pressure difference [Pa] | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| MassFlowRate | m_flow_small | 1E-4*abs(m_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Flow resistance | |||
| Boolean | computeFlowResistance | (abs(dp_nominal) > Modelica.... | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
| output RealOutput | hOut | Leaving temperature of the component [J/kg] |
| output RealOutput | XiOut[Medium.nXi] | Leaving species concentration of the component [1] |
| output RealOutput | COut[Medium.nC] | Leaving trace substances of the component |
Modelica definition
model StaticTwoPortHeatMassExchanger
"Partial model transporting fluid between two ports without storing mass or energy"
extends Buildings.Fluid.Interfaces.PartialTwoPortInterface;
extends Buildings.Fluid.Interfaces.TwoPortFlowResistanceParameters(
final computeFlowResistance=(abs(dp_nominal) > Modelica.Constants.eps));
constant Boolean sensibleOnly "Set to true if sensible exchange only";
constant Boolean prescribedHeatFlowRate
"Set to true if the heat flow rate is not a function of the component temperature";
constant Boolean homotopyInitialization = true "= true, use homotopy method";
// Model inputs
// Q_flow is the sensible plus latent heat flow rate
input Modelica.Units.SI.HeatFlowRate Q_flow
"Heat transferred into the medium";
input Modelica.Units.SI.MassFlowRate mWat_flow
"Moisture mass flow rate added to the medium";
// Models for conservation equations and pressure drop
Buildings.Fluid.Interfaces.StaticTwoPortConservationEquation vol(
redeclare final package Medium = Medium,
final use_mWat_flow = not sensibleOnly,
final prescribedHeatFlowRate = prescribedHeatFlowRate,
final m_flow_nominal = m_flow_nominal,
final allowFlowReversal=allowFlowReversal,
final m_flow_small=m_flow_small)
"Control volume for steady-state energy and mass balance";
Buildings.Fluid.FixedResistances.PressureDrop preDro(
redeclare final package Medium = Medium,
final m_flow_nominal=m_flow_nominal,
final deltaM=deltaM,
final allowFlowReversal=allowFlowReversal,
final show_T=false,
final from_dp=from_dp,
final linearized=linearizeFlowResistance,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp_nominal) "Flow resistance";
// Outputs that are needed in models that extend this model
Modelica.Blocks.Interfaces.RealOutput hOut(unit="J/kg")
"Leaving temperature of the component";
Modelica.Blocks.Interfaces.RealOutput XiOut[Medium.nXi](each unit="1",
each min=0,
each max=1)
"Leaving species concentration of the component";
Modelica.Blocks.Interfaces.RealOutput COut[Medium.nC](each min=0)
"Leaving trace substances of the component";
protected
Modelica.Blocks.Sources.RealExpression heaInp(y=Q_flow)
"Block to set heat input into volume";
Modelica.Blocks.Sources.RealExpression
masExc(final y=mWat_flow) "Block to set moisture exchange in volume";
initial equation
assert(homotopyInitialization, "In " + getInstanceName() +
": The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.",
level = AssertionLevel.warning);
equation
connect(vol.hOut, hOut);
connect(vol.XiOut, XiOut);
connect(vol.COut, COut);
connect(port_a,preDro. port_a);
connect(preDro.port_b, vol.port_a);
connect(vol.port_b, port_b);
connect(heaInp.y, vol.Q_flow);
connect(masExc.y, vol.mWat_flow);
end StaticTwoPortHeatMassExchanger;
Buildings.Fluid.Interfaces.TwoPortHeatMassExchanger
Partial model transporting one fluid stream with storing mass or energy
Information
This component transports one fluid stream.
It provides the basic model for implementing dynamic and steady-state
models that exchange heat and water vapor with the fluid stream.
The model also computes the pressure drop due to the flow resistance.
By setting the parameter dp_nominal=0, the computation
of the pressure drop can be avoided.
The variable vol.heatPort.T always has the value of
the temperature of the medium that leaves the component.
For the actual temperatures at the port, the variables sta_a.T
and sta_b.T can be used. These two variables are provided by
the base class
Buildings.Fluid.Interfaces.PartialTwoPortInterface.
- the ideal heater or cooler Buildings.Fluid.HeatExchangers.HeaterCooler_u, and
- the ideal humidifier Buildings.Fluid.Humidifiers.Humidifier_u.
Implementation
The variable names follow the conventions used in Modelica.Fluid.Examples.HeatExchanger.BaseClasses.BasicHX .
Extends from Buildings.Fluid.Interfaces.PartialTwoPortInterface (Partial model with two ports and declaration of quantities that are used by many models), Buildings.Fluid.Interfaces.TwoPortFlowResistanceParameters (Parameters for flow resistance for models with two ports).
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| MixingVolume | vol | redeclare Buildings.Fluid.Mi... | Volume for fluid stream |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
| PressureDifference | dp_nominal | Pressure difference [Pa] | |
| Assumptions | |||
| Boolean | allowFlowReversal | true | = false to simplify equations, assuming, but not enforcing, no flow reversal |
| Advanced | |||
| MassFlowRate | m_flow_small | 1E-4*abs(m_flow_nominal) | Small mass flow rate for regularization of zero flow [kg/s] |
| Diagnostics | |||
| Boolean | show_T | false | = true, if actual temperature at port is computed |
| Flow resistance | |||
| Boolean | computeFlowResistance | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Dynamics | |||
| Nominal condition | |||
| Time | tau | 30 | Time constant at nominal flow (if energyDynamics <> SteadyState) [s] |
| Conservation equations | |||
| Dynamics | energyDynamics | Modelica.Fluid.Types.Dynamic... | Type of energy balance: dynamic (3 initialization options) or steady state |
| Initialization | |||
| AbsolutePressure | p_start | Medium.p_default | Start value of pressure [Pa] |
| Temperature | T_start | Medium.T_default | Start value of temperature [K] |
| MassFraction | X_start[Medium.nX] | Medium.X_default | Start value of mass fractions m_i/m [kg/kg] |
| ExtraProperty | C_start[Medium.nC] | fill(0, Medium.nC) | Start value of trace substances |
Connectors
| Type | Name | Description |
|---|---|---|
| FluidPort_a | port_a | Fluid connector a (positive design flow direction is from port_a to port_b) |
| FluidPort_b | port_b | Fluid connector b (positive design flow direction is from port_a to port_b) |
Modelica definition
model TwoPortHeatMassExchanger
"Partial model transporting one fluid stream with storing mass or energy"
extends Buildings.Fluid.Interfaces.PartialTwoPortInterface(
port_a(h_outflow(start=h_outflow_start)),
port_b(h_outflow(start=h_outflow_start)));
extends Buildings.Fluid.Interfaces.TwoPortFlowResistanceParameters(
final computeFlowResistance=true);
constant Boolean homotopyInitialization = true "= true, use homotopy method";
parameter Modelica.Units.SI.Time tau=30
"Time constant at nominal flow (if energyDynamics <> SteadyState)";
// Dynamics
parameter Modelica.Fluid.Types.Dynamics energyDynamics=Modelica.Fluid.Types.Dynamics.DynamicFreeInitial
"Type of energy balance: dynamic (3 initialization options) or steady state";
// Initialization
parameter Medium.AbsolutePressure p_start = Medium.p_default
"Start value of pressure";
parameter Medium.Temperature T_start = Medium.T_default
"Start value of temperature";
parameter Medium.MassFraction X_start[Medium.nX](
final quantity=Medium.substanceNames) = Medium.X_default
"Start value of mass fractions m_i/m";
parameter Medium.ExtraProperty C_start[Medium.nC](
final quantity=Medium.extraPropertiesNames)=fill(0, Medium.nC)
"Start value of trace substances";
replaceable Buildings.Fluid.MixingVolumes.MixingVolume vol
constrainedby Buildings.Fluid.MixingVolumes.BaseClasses.PartialMixingVolume(
redeclare final package Medium = Medium,
nPorts = 2,
V=m_flow_nominal*tau/rho_default,
final allowFlowReversal=allowFlowReversal,
final mSenFac=1,
final m_flow_nominal = m_flow_nominal,
final energyDynamics=energyDynamics,
final massDynamics=energyDynamics,
final p_start=p_start,
final T_start=T_start,
final X_start=X_start,
final C_start=C_start) "Volume for fluid stream";
Buildings.Fluid.FixedResistances.PressureDrop preDro(
redeclare final package Medium = Medium,
final m_flow_nominal=m_flow_nominal,
final deltaM=deltaM,
final allowFlowReversal=allowFlowReversal,
final show_T=false,
final from_dp=from_dp,
final linearized=linearizeFlowResistance,
final homotopyInitialization=homotopyInitialization,
final dp_nominal=dp_nominal) "Flow resistance";
protected
parameter Medium.ThermodynamicState sta_default=Medium.setState_pTX(
T=Medium.T_default, p=Medium.p_default, X=Medium.X_default);
parameter Modelica.Units.SI.Density rho_default=Medium.density(sta_default)
"Density, used to compute fluid volume";
parameter Medium.ThermodynamicState sta_start=Medium.setState_pTX(
T=T_start, p=p_start, X=X_start);
parameter Modelica.Units.SI.SpecificEnthalpy h_outflow_start=
Medium.specificEnthalpy(sta_start) "Start value for outflowing enthalpy";
initial algorithm
assert((energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState) or
tau > Modelica.Constants.eps,
"The parameter tau, or the volume of the model from which tau may be derived, is unreasonably small.
You need to set energyDynamics == Modelica.Fluid.Types.Dynamics.SteadyState to model steady-state.
Received tau = " + String(tau) + "\n");
assert(homotopyInitialization, "In " + getInstanceName() +
": The constant homotopyInitialization has been modified from its default value. This constant will be removed in future releases.",
level = AssertionLevel.warning);
equation
connect(vol.ports[2], port_b);
connect(port_a, preDro.port_a);
connect(preDro.port_b, vol.ports[1]);
end TwoPortHeatMassExchanger;
Buildings.Fluid.Interfaces.EightPortFlowResistanceParameters
Parameters for flow resistance for models with height ports
Information
This class contains parameters that are used to compute the pressure drop in components that have four fluid streams. Note that the nominal mass flow rate is not declared here because the model PartialHeightPortInterface already declares it.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Nominal condition | |||
| Pressure | dp1_nominal | Pressure [Pa] | |
| Pressure | dp2_nominal | Pressure [Pa] | |
| Pressure | dp3_nominal | Pressure [Pa] | |
| Pressure | dp4_nominal | Pressure [Pa] | |
| Flow resistance | |||
| Medium 1 | |||
| Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp1 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance1 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM1 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 2 | |||
| Boolean | computeFlowResistance2 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp2 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance2 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM2 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 3 | |||
| Boolean | computeFlowResistance3 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp3 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance3 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM3 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 4 | |||
| Boolean | computeFlowResistance4 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp4 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance4 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM4 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
Modelica definition
record EightPortFlowResistanceParameters
"Parameters for flow resistance for models with height ports"
parameter Boolean computeFlowResistance1 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp1 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.Pressure dp1_nominal(min=0, displayUnit="Pa")
"Pressure";
parameter Boolean linearizeFlowResistance1 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM1 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
parameter Boolean computeFlowResistance2 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp2 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.Pressure dp2_nominal(min=0, displayUnit="Pa")
"Pressure";
parameter Boolean linearizeFlowResistance2 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM2 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
parameter Boolean computeFlowResistance3 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp3 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.Pressure dp3_nominal(min=0, displayUnit="Pa")
"Pressure";
parameter Boolean linearizeFlowResistance3 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM3 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
parameter Boolean computeFlowResistance4 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp4 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.Pressure dp4_nominal(min=0, displayUnit="Pa")
"Pressure";
parameter Boolean linearizeFlowResistance4 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM4 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
end EightPortFlowResistanceParameters;
Buildings.Fluid.Interfaces.FourPortFlowResistanceParameters
Parameters for flow resistance for models with four ports
Information
This class contains parameters that are used to compute the pressure drop in components that have two fluid streams. Note that the nominal mass flow rate is not declared here because the model PartialFourPortInterface already declares it.
Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Nominal condition | |||
| PressureDifference | dp1_nominal | Pressure difference [Pa] | |
| PressureDifference | dp2_nominal | Pressure difference [Pa] | |
| Flow resistance | |||
| Medium 1 | |||
| Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp1 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance1 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM1 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
| Medium 2 | |||
| Boolean | computeFlowResistance2 | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp2 | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance2 | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM2 | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
Modelica definition
record FourPortFlowResistanceParameters
"Parameters for flow resistance for models with four ports"
parameter Boolean computeFlowResistance1 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp1 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.PressureDifference dp1_nominal(min=0, displayUnit
="Pa") "Pressure difference";
parameter Boolean linearizeFlowResistance1 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM1 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
parameter Boolean computeFlowResistance2 = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp2 = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.PressureDifference dp2_nominal(min=0, displayUnit
="Pa") "Pressure difference";
parameter Boolean linearizeFlowResistance2 = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM2 = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
end FourPortFlowResistanceParameters;
Buildings.Fluid.Interfaces.TwoPortFlowResistanceParameters
Parameters for flow resistance for models with two ports
Information
This class contains parameters that are used to compute the pressure drop in models that have one fluid stream. Note that the nominal mass flow rate is not declared here because the model PartialTwoPortInterface already declares it.Parameters
| Type | Name | Default | Description |
|---|---|---|---|
| Nominal condition | |||
| PressureDifference | dp_nominal | Pressure difference [Pa] | |
| Flow resistance | |||
| Boolean | computeFlowResistance | true | =true, compute flow resistance. Set to false to assume no friction |
| Boolean | from_dp | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
| Boolean | linearizeFlowResistance | false | = true, use linear relation between m_flow and dp for any flow rate |
| Real | deltaM | 0.1 | Fraction of nominal flow rate where flow transitions to laminar |
Modelica definition
record TwoPortFlowResistanceParameters
"Parameters for flow resistance for models with two ports"
parameter Boolean computeFlowResistance = true
"=true, compute flow resistance. Set to false to assume no friction";
parameter Boolean from_dp = false
"= true, use m_flow = f(dp) else dp = f(m_flow)";
parameter Modelica.Units.SI.PressureDifference dp_nominal(min=0, displayUnit=
"Pa") "Pressure difference";
parameter Boolean linearizeFlowResistance = false
"= true, use linear relation between m_flow and dp for any flow rate";
parameter Real deltaM = 0.1
"Fraction of nominal flow rate where flow transitions to laminar";
end TwoPortFlowResistanceParameters;