Extends from Modelica_Fluid.Icons.BaseClassLibrary (Icon for library).
Name | Description |
---|---|
FourPortFlowResistanceParameters | Parameters for flow resistance for models with four ports |
PartialDynamicFourPortTransformer | Partial model transporting two fluid streams between four ports with storing mass or energy |
PartialDynamicTwoPortTransformer | Partial model transporting one fluid stream with storing mass or energy |
PartialFourPort | Partial model with four ports |
PartialStaticFourPortHeatMassTransfer | Partial model transporting two fluid streams between four ports without storing mass or energy |
PartialStaticFourPortInterface | Partial model transporting fluid between two ports without storing mass or energy |
PartialStaticTwoPortHeatMassTransfer | Partial model transporting fluid between two ports without storing mass or energy |
PartialStaticTwoPortInterface | Partial model transporting fluid between two ports without storing mass or energy |
TwoPortFlowResistanceParameters | Parameters for flow resistance for models with two ports |
Type | Name | Default | Description |
---|---|---|---|
Nominal condition | |||
Pressure | dp1_nominal | Pressure [Pa] | |
Pressure | dp2_nominal | Pressure [Pa] | |
Flow resistance | |||
Medium 1 | |||
Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp1 | true | = 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 | true | = 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 |
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 = true "= true, use m_flow = f(dp) else dp = f(m_flow)"; parameter Modelica.SIunits.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 = true "= true, use m_flow = f(dp) else dp = f(m_flow)"; parameter Modelica.SIunits.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"; end FourPortFlowResistanceParameters;
This component transports two fluid streams between four ports. It provides the basic model for implementing a dynamic heat exchanger. It is used by HeatExchangers.BaseClasses.HexElement. The variable names follow the conventions used in Modelica_Fluid.HeatExchangers.BasicHX.
Extends from Buildings.Fluids.Interfaces.PartialStaticFourPortInterface (Partial model transporting fluid between two ports without storing mass or energy), Buildings.Fluids.Interfaces.FourPortFlowResistanceParameters (Parameters for flow resistance for models with four ports).
Type | Name | Default | Description |
---|---|---|---|
replaceable package Medium1 | PartialMedium | Medium 1 in the component | |
replaceable package Medium2 | PartialMedium | Medium 2 in the component | |
MixingVolumeDryAir | vol2 | redeclare Buildings.Fluids.M... | Volume for fluid 2 |
Nominal condition | |||
MassFlowRate | m1_flow_nominal | Nominal mass flow rate [kg/s] | |
MassFlowRate | m2_flow_nominal | m1_flow_nominal | Nominal mass flow rate [kg/s] |
Pressure | dp1_nominal | Pressure [Pa] | |
Pressure | dp2_nominal | Pressure [Pa] | |
Time | tau1 | 60 | Time constant at nominal flow [s] |
Time | tau2 | 60 | Time constant at nominal flow [s] |
Initialization | |||
MassFlowRate | m1_flow.start | 0 | Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction) [kg/s] |
Pressure | dp1.start | 0 | Pressure difference between port_a1 and port_b1 [Pa] |
MassFlowRate | m2_flow.start | 0 | Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction) [kg/s] |
Pressure | dp2.start | 0 | Pressure difference between port_a2 and port_b2 [Pa] |
Assumptions | |||
Boolean | allowFlowReversal1 | system.allowFlowReversal | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
Boolean | allowFlowReversal2 | system.allowFlowReversal | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
Advanced | |||
MassFlowRate | m1_flow_small | 1E-4*m1_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
MassFlowRate | m2_flow_small | 1E-4*m2_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a1_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b1_start | p_a1_start | Guess value for outlet pressure [Pa] |
AbsolutePressure | p_a2_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b2_start | p_a2_start | Guess value for outlet pressure [Pa] |
Flow resistance | |||
Medium 1 | |||
Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp1 | true | = 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 | true | = 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 |
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) |
partial model PartialDynamicFourPortTransformer "Partial model transporting two fluid streams between four ports with storing mass or energy" extends Buildings.Fluids.Interfaces.PartialStaticFourPortInterface; extends Buildings.Fluids.Interfaces.FourPortFlowResistanceParameters( final computeFlowResistance1=true, final computeFlowResistance2=true); import Modelica.Constants; Buildings.Fluids.MixingVolumes.MixingVolume vol1( redeclare package Medium = Medium1, nPorts = 2, V=m1_flow_nominal*tau1/rho1_nominal, medium(T(stateSelect=StateSelect.always)), final use_HeatTransfer=true, redeclare model HeatTransfer = Modelica_Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer) "Volume for fluid 1"; replaceable Buildings.Fluids.MixingVolumes.MixingVolumeDryAir vol2( redeclare package Medium = Medium2, nPorts = 2, V=m2_flow_nominal*tau2/rho2_nominal, final use_HeatTransfer=true, redeclare model HeatTransfer = Modelica_Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer(surfaceAreas={1})) constrainedby Buildings.Fluids.MixingVolumes.BaseClasses.PartialMixingVolumeWaterPort "Volume for fluid 2"; parameter Modelica.SIunits.Time tau1 = 60 "Time constant at nominal flow"; parameter Modelica.SIunits.Time tau2 = 60 "Time constant at nominal flow"; Modelica.SIunits.HeatFlowRate Q1_flow= if vol1.use_HeatTransfer then sum(vol1.heatPort.Q_flow) else 0 "Heat flow rate into medium 1"; Modelica.SIunits.HeatFlowRate Q2_flow= if vol2.use_HeatTransfer then sum(vol2.heatPort.Q_flow) else 0 "Heat flow rate into medium 2"; protected parameter Medium1.ThermodynamicState sta1_nominal=Medium1.setState_pTX( T=Medium1.T_default, p=Medium1.p_default, X=Medium1.X_default); parameter Modelica.SIunits.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.SIunits.Density rho2_nominal=Medium2.density(sta2_nominal) "Density, used to compute fluid volume"; public FixedResistances.FixedResistanceDpM preDro1( redeclare package Medium = Medium1, final use_dh=false, final m_flow_nominal=m1_flow_nominal, final deltaM=deltaM1, final allowFlowReversal=allowFlowReversal1, final m_flow_small=m1_flow_small, final show_T=false, final show_V_flow=show_V_flow, final from_dp=from_dp1, final linearized=linearizeFlowResistance1, final dp_nominal=dp1_nominal, final dh=1, final ReC=4000) "Pressure drop model for fluid 1"; FixedResistances.FixedResistanceDpM preDro2( redeclare package Medium = Medium2, final use_dh=false, final m_flow_nominal=m2_flow_nominal, final deltaM=deltaM2, final allowFlowReversal=allowFlowReversal2, final m_flow_small=m2_flow_small, final show_T=false, final show_V_flow=show_V_flow, final from_dp=from_dp2, final linearized=linearizeFlowResistance2, final dp_nominal=dp2_nominal, final dh=1, final ReC=4000) "Pressure drop model for fluid 2"; equation assert(vol1.use_HeatTransfer == true, "Wrong parameter for vol1."); assert(vol2.use_HeatTransfer == true, "Wrong parameter for vol2."); 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 PartialDynamicFourPortTransformer;
This component transports one fluid stream. It provides the basic model for implementing a dynamic heater such as a boiler. It is used by Buildings.Fluids.Boilers.BoilerPolynomial. The variable names follow the conventions used in Modelica_Fluid.HeatExchangers.BasicHX.
Extends from Buildings.Fluids.Interfaces.PartialStaticTwoPortInterface (Partial model transporting fluid between two ports without storing mass or energy), Buildings.Fluids.Interfaces.TwoPortFlowResistanceParameters (Parameters for flow resistance for models with two ports).
Type | Name | Default | Description |
---|---|---|---|
replaceable package Medium | PartialMedium | Medium in the component | |
Nominal condition | |||
MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
Pressure | dp_nominal | Pressure [Pa] | |
Time | tau | 300 | Time constant at nominal flow [s] |
Initialization | |||
MassFlowRate | m_flow.start | 0 | Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] |
Pressure | dp.start | 0 | Pressure difference between port_a and port_b [Pa] |
Assumptions | |||
Boolean | allowFlowReversal | system.allowFlowReversal | = true to allow flow reversal, false restricts to design direction (port_a -> port_b) |
Dynamics | |||
Dynamics | energyDynamics | system.energyDynamics | Formulation of energy balance |
Dynamics | massDynamics | energyDynamics | Formulation of mass balance |
Advanced | |||
MassFlowRate | m_flow_small | 1E-4*m_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b_start | p_a_start | Guess value for outlet pressure [Pa] |
AbsolutePressure | p_start | system.p_start | Start value of pressure [Pa] |
Boolean | use_T_start | true | = true, use T_start, otherwise h_start |
Temperature | T_start | if use_T_start then system.T... | Start value of temperature [K] |
SpecificEnthalpy | h_start | if use_T_start then Medium.s... | Start value of specific enthalpy [J/kg] |
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 |
Flow resistance | |||
Boolean | computeFlowResistance | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp | true | = 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 |
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) |
partial model PartialDynamicTwoPortTransformer "Partial model transporting one fluid stream with storing mass or energy" extends Buildings.Fluids.Interfaces.PartialStaticTwoPortInterface; extends Buildings.Fluids.Interfaces.TwoPortFlowResistanceParameters( final computeFlowResistance=true); import Modelica.Constants; Buildings.Fluids.MixingVolumes.MixingVolume vol( redeclare package Medium = Medium, nPorts = 2, V=m_flow_nominal*tau/rho_nominal, final use_HeatTransfer=true, redeclare model HeatTransfer = Modelica_Fluid.Vessels.BaseClasses.HeatTransfer.IdealHeatTransfer, final energyDynamics=energyDynamics, final massDynamics=massDynamics, final p_start=p_start, final use_T_start=use_T_start, final T_start=T_start, final h_start=h_start, final X_start=X_start, final C_start=C_start) "Volume for fluid stream"; parameter Modelica.SIunits.Time tau = 300 "Time constant at nominal flow"; // Assumptions parameter Modelica_Fluid.Types.Dynamics energyDynamics=system.energyDynamics "Formulation of energy balance"; parameter Modelica_Fluid.Types.Dynamics massDynamics=energyDynamics "Formulation of mass balance"; final parameter Modelica_Fluid.Types.Dynamics substanceDynamics=massDynamics "Formulation of substance balance"; final parameter Modelica_Fluid.Types.Dynamics traceDynamics=massDynamics "Formulation of trace substance balance"; // Initialization parameter Medium.AbsolutePressure p_start = system.p_start "Start value of pressure"; parameter Boolean use_T_start = true "= true, use T_start, otherwise h_start"; parameter Medium.Temperature T_start= if use_T_start then system.T_start else Medium.temperature_phX(p_start,h_start,X_start) "Start value of temperature"; parameter Medium.SpecificEnthalpy h_start= if use_T_start then Medium.specificEnthalpy_pTX(p_start, T_start, X_start) else Medium.h_default "Start value of specific enthalpy"; parameter Medium.MassFraction X_start[Medium.nX] = 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"; Modelica.Thermal.HeatTransfer.Sensors.TemperatureSensor temSen( T(final quantity="ThermodynamicTemperature", final unit = "K", displayUnit = "degC", min=0)) "Temperature sensor of metal"; protected parameter Medium.ThermodynamicState sta_nominal=Medium.setState_pTX( T=Medium.T_default, p=Medium.p_default, X=Medium.X_default); parameter Modelica.SIunits.Density rho_nominal=Medium.density(sta_nominal) "Density, used to compute fluid volume"; public Buildings.Fluids.FixedResistances.FixedResistanceDpM preDro( redeclare package Medium = Medium, final use_dh=false, final m_flow_nominal=m_flow_nominal, final deltaM=deltaM, final allowFlowReversal=allowFlowReversal, final m_flow_small=m_flow_small, final show_T=false, final show_V_flow=show_V_flow, final from_dp=from_dp, final linearized=linearizeFlowResistance, final dp_nominal=dp_nominal) "Pressure drop model"; equation assert(vol.use_HeatTransfer == true, "Wrong parameter for vol."); connect(temSen.port, vol.heatPort); connect(vol.ports[2], port_b); connect(port_a, preDro.port_a); connect(preDro.port_b, vol.ports[1]); end PartialDynamicTwoPortTransformer;
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.
An extending model providing direct access to internal storage of mass or energy through port_a or port_b (or port_a2 and port_b2) should redefine the protected parameters port_a1_exposesState and port_b1_exposesState appropriately. This will be visualized at the port icons, in order to improve the understanding of fluid model diagrams.
This partial model is identical to
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) |
partial model PartialFourPort "Partial model with four ports" import Modelica.Constants; outer Modelica_Fluid.System system "System wide properties"; 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 = system.allowFlowReversal "= true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b)"; parameter Boolean allowFlowReversal2 = system.allowFlowReversal "= 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 package Medium = Medium1, m_flow(min=if allowFlowReversal1 then -Constants.inf else 0)) "Fluid connector a1 (positive design flow direction is from port_a1 to port_b1)"; Modelica_Fluid.Interfaces.FluidPort_b port_b1( redeclare package Medium = Medium1, m_flow(max=if allowFlowReversal1 then +Constants.inf else 0)) "Fluid connector b1 (positive design flow direction is from port_a1 to port_b1)"; Modelica_Fluid.Interfaces.FluidPort_a port_a2( redeclare package Medium = Medium2, m_flow(min=if allowFlowReversal2 then -Constants.inf else 0)) "Fluid connector a2 (positive design flow direction is from port_a2 to port_b2)"; Modelica_Fluid.Interfaces.FluidPort_b port_b2( redeclare package Medium = Medium2, m_flow(max=if allowFlowReversal2 then +Constants.inf else 0)) "Fluid connector b2 (positive design flow direction is from port_a2 to port_b2)"; // Model structure, e.g. used for visualization protected parameter Boolean port_a1_exposesState = false "= true if port_a1 exposes the state of a fluid volume"; parameter Boolean port_b1_exposesState = false "= true if port_b1 exposes the state of a fluid volume"; parameter Boolean port_a2_exposesState = false "= true if port_a1 exposes the state of a fluid volume"; parameter Boolean port_b2_exposesState = false "= true if port_b1 exposes the state of a fluid volume"; end PartialFourPort;
This component transports two fluid streams between four ports, without storing mass or energy. It is similar to Buildings.Fluids.Interfaces.PartialStaticTwoPortHeatMassTransfer, but it has four ports instead of two. See the documentation of Buildings.Fluids.Interfaces.PartialStaticTwoPortHeatMassTransfer for how to use this partial model.
Extends from Buildings.Fluids.Interfaces.PartialStaticFourPortInterface (Partial model transporting fluid between two ports without storing mass or energy), Buildings.Fluids.Interfaces.FourPortFlowResistanceParameters (Parameters for flow resistance for models with four ports).
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 | m1_flow_nominal | Nominal mass flow rate [kg/s] |
Pressure | dp1_nominal | Pressure [Pa] | |
Pressure | dp2_nominal | Pressure [Pa] | |
Initialization | |||
MassFlowRate | m1_flow.start | 0 | Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction) [kg/s] |
Pressure | dp1.start | 0 | Pressure difference between port_a1 and port_b1 [Pa] |
MassFlowRate | m2_flow.start | 0 | Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction) [kg/s] |
Pressure | dp2.start | 0 | Pressure difference between port_a2 and port_b2 [Pa] |
Assumptions | |||
Boolean | allowFlowReversal1 | system.allowFlowReversal | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
Boolean | allowFlowReversal2 | system.allowFlowReversal | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
Advanced | |||
MassFlowRate | m1_flow_small | 1E-4*m1_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
MassFlowRate | m2_flow_small | 1E-4*m2_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a1_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b1_start | p_a1_start | Guess value for outlet pressure [Pa] |
AbsolutePressure | p_a2_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b2_start | p_a2_start | Guess value for outlet pressure [Pa] |
Flow resistance | |||
Medium 1 | |||
Boolean | computeFlowResistance1 | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp1 | true | = 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 | true | = 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 |
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) |
partial model PartialStaticFourPortHeatMassTransfer "Partial model transporting two fluid streams between four ports without storing mass or energy" extends Buildings.Fluids.Interfaces.PartialStaticFourPortInterface; extends Buildings.Fluids.Interfaces.FourPortFlowResistanceParameters( final computeFlowResistance1=true, final computeFlowResistance2=true); import Modelica.Constants; Modelica.SIunits.HeatFlowRate Q1_flow "Heat transfered into the medium 1"; Medium1.MassFlowRate mXi1_flow[Medium1.nXi] "Mass flow rates of independent substances added to the medium 1"; Modelica.SIunits.HeatFlowRate Q2_flow "Heat transfered into the medium 2"; Medium2.MassFlowRate mXi2_flow[Medium2.nXi] "Mass flow rates of independent substances added to the medium 2"; equation // Energy balance (no storage, no heat loss/gain) port_a1.m_flow*port_a1.h_outflow + port_b1.m_flow*inStream(port_b1.h_outflow) = -Q1_flow; port_a1.m_flow*port_b1.h_outflow + port_b1.m_flow*inStream(port_a1.h_outflow) = Q1_flow; port_a2.m_flow*port_a2.h_outflow + port_b2.m_flow*inStream(port_b2.h_outflow) = -Q2_flow; port_a2.m_flow*port_b2.h_outflow + port_b2.m_flow*inStream(port_a2.h_outflow) = Q2_flow; // Mass balance (no storage) port_a1.m_flow + port_b1.m_flow = -sum(mXi1_flow); port_a2.m_flow + port_b2.m_flow = -sum(mXi2_flow); port_a1.m_flow*port_a1.Xi_outflow + port_b1.m_flow*inStream(port_b1.Xi_outflow) = -mXi1_flow; port_a1.m_flow*port_b1.Xi_outflow + port_b1.m_flow*inStream(port_a1.Xi_outflow) = mXi1_flow; port_a2.m_flow*port_a2.Xi_outflow + port_b2.m_flow*inStream(port_b2.Xi_outflow) = -mXi2_flow; port_a2.m_flow*port_b2.Xi_outflow + port_b2.m_flow*inStream(port_a2.Xi_outflow) = mXi2_flow; // Transport of trace substances port_a1.C_outflow = inStream(port_b1.C_outflow); port_b1.C_outflow = inStream(port_a1.C_outflow); port_a2.C_outflow = inStream(port_b2.C_outflow); port_b2.C_outflow = inStream(port_a2.C_outflow); // Pressure drop calculation // Medium 1 if computeFlowResistance1 then if from_dp1 then m1_flow = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_dp( dp=dp1, k=m1_flow_nominal/sqrt(dp1_nominal), m_flow_turbulent=deltaM1 * m1_flow_nominal, linearized=linearizeFlowResistance1); else dp1 = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_m_flow( m_flow=m1_flow, k=m1_flow_nominal/sqrt(dp1_nominal), m_flow_turbulent=deltaM1 * m1_flow_nominal, linearized=linearizeFlowResistance1); end if; else dp1 = 0; end if; // Medium 2 if computeFlowResistance2 then if from_dp2 then m2_flow = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_dp( dp=dp2, k=m2_flow_nominal/sqrt(dp2_nominal), m_flow_turbulent=deltaM2 * m2_flow_nominal, linearized=linearizeFlowResistance2); else dp2 = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_m_flow( m_flow=m2_flow, k=m2_flow_nominal/sqrt(dp2_nominal), m_flow_turbulent=deltaM2 * m2_flow_nominal, linearized=linearizeFlowResistance2); end if; else dp2 = 0; end if; end PartialStaticFourPortHeatMassTransfer;
This component defines the interface for models that
transport two fluid streams between four ports.
It is similar to
,
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.
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 | m1_flow_nominal | Nominal mass flow rate [kg/s] |
Assumptions | |||
Boolean | allowFlowReversal1 | system.allowFlowReversal | = true to allow flow reversal in medium 1, false restricts to design direction (port_a -> port_b) |
Boolean | allowFlowReversal2 | system.allowFlowReversal | = true to allow flow reversal in medium 2, false restricts to design direction (port_a -> port_b) |
Advanced | |||
MassFlowRate | m1_flow_small | 1E-4*m1_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
MassFlowRate | m2_flow_small | 1E-4*m2_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a1_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b1_start | p_a1_start | Guess value for outlet pressure [Pa] |
AbsolutePressure | p_a2_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b2_start | p_a2_start | Guess value for outlet pressure [Pa] |
partial model PartialStaticFourPortInterface "Partial model transporting fluid between two ports without storing mass or energy" import Modelica.Constants; extends Buildings.Fluids.Interfaces.PartialFourPort( port_a1( p(start=p_a1_start), m_flow(min = if allowFlowReversal1 then -Constants.inf else 0)), port_b1( p(start=p_b1_start), m_flow(max = if allowFlowReversal1 then +Constants.inf else 0)), port_a2( p(start=p_a2_start), m_flow(min = if allowFlowReversal2 then -Constants.inf else 0)), port_b2( p(start=p_b2_start), m_flow(max = if allowFlowReversal2 then +Constants.inf else 0))); parameter Modelica.SIunits.MassFlowRate m1_flow_nominal(min=0) "Nominal mass flow rate"; parameter Modelica.SIunits.MassFlowRate m2_flow_nominal(min=0) = m1_flow_nominal "Nominal mass flow rate"; parameter Medium1.MassFlowRate m1_flow_small(min=0) = 1E-4*m1_flow_nominal "Small mass flow rate for regularization of zero flow"; parameter Medium2.MassFlowRate m2_flow_small(min=0) = 1E-4*m2_flow_nominal "Small mass flow rate for regularization of zero flow"; // Initialization parameter Medium1.AbsolutePressure p_a1_start=system.p_start "Guess value for inlet pressure"; parameter Medium1.AbsolutePressure p_b1_start=p_a1_start "Guess value for outlet pressure"; parameter Medium2.AbsolutePressure p_a2_start=system.p_start "Guess value for inlet pressure"; parameter Medium2.AbsolutePressure p_b2_start=p_a2_start "Guess value for outlet pressure"; // Diagnostics // parameter Boolean show_T = true // "= true, if temperatures at port_a and port_b are computed" annotation 7; parameter Boolean show_V_flow = true "= true, if volume flow rate at inflowing port is computed"; Modelica.SIunits.VolumeFlowRate V1_flow= m1_flow/Modelica_Fluid.Utilities.regStep(m1_flow, Medium1.density(state_a1_inflow), Medium1.density(state_b1_inflow), m1_flow_small) if show_V_flow "Volume flow rate at inflowing port (positive when flow from port_a1 to port_b1)"; Modelica.SIunits.VolumeFlowRate V2_flow= m2_flow/Modelica_Fluid.Utilities.regStep(m2_flow, Medium2.density(state_a2_inflow), Medium2.density(state_b2_inflow), m2_flow_small) if show_V_flow "Volume flow rate at inflowing port (positive when flow from port_a2 to port_b2)"; Medium1.MassFlowRate m1_flow(start=0) "Mass flow rate from port_a1 to port_b1 (m1_flow > 0 is design flow direction)"; Modelica.SIunits.Pressure dp1(start=0, displayUnit="Pa") "Pressure difference between port_a1 and port_b1"; Medium2.MassFlowRate m2_flow(start=0) "Mass flow rate from port_a2 to port_b2 (m2_flow > 0 is design flow direction)"; Modelica.SIunits.Pressure dp2(start=0, displayUnit="Pa") "Pressure difference between port_a2 and port_b2"; Medium1.ThermodynamicState sta_a1= Medium1.setState_phX(port_a1.p, actualStream(port_a1.h_outflow), actualStream(port_a1.Xi_outflow)) "Medium properties in port_a1"; Medium1.ThermodynamicState sta_b1= Medium1.setState_phX(port_b1.p, actualStream(port_b1.h_outflow), actualStream(port_b1.Xi_outflow)) "Medium properties in port_b1"; Medium2.ThermodynamicState sta_a2= Medium2.setState_phX(port_a2.p, actualStream(port_a2.h_outflow), actualStream(port_a2.Xi_outflow)) "Medium properties in port_a2"; Medium2.ThermodynamicState sta_b2= Medium2.setState_phX(port_b2.p, actualStream(port_b2.h_outflow), actualStream(port_b2.Xi_outflow)) "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"; equation // Design direction of mass flow rate m1_flow = port_a1.m_flow; m2_flow = port_a2.m_flow; // Pressure difference between ports dp1 = port_a1.p - port_b1.p; dp2 = port_a2.p - port_b2.p; end PartialStaticFourPortInterface;
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.
Depending on the parameter settings, 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.
When using this partial component, an equation for the energy and mass balances need to be added, such as
mWat_flow = u * m_flow_nominal; Q_flow = Medium.enthalpyOfLiquid(TWat) * mWat_flow; for i in 1:Medium.nXi loop mXi_flow[i] = if ( i == Medium.Water) then mWat_flow else 0; end for;Extends from Buildings.Fluids.Interfaces.PartialStaticTwoPortInterface (Partial model transporting fluid between two ports without storing mass or energy), Buildings.Fluids.Interfaces.TwoPortFlowResistanceParameters (Parameters for flow resistance for models with two ports).
Type | Name | Default | Description |
---|---|---|---|
replaceable package Medium | PartialMedium | Medium in the component | |
Nominal condition | |||
MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/s] | |
Pressure | dp_nominal | Pressure [Pa] | |
Initialization | |||
MassFlowRate | m_flow.start | 0 | Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction) [kg/s] |
Pressure | dp.start | 0 | Pressure difference between port_a and port_b [Pa] |
Assumptions | |||
Boolean | allowFlowReversal | system.allowFlowReversal | = true to allow flow reversal, false restricts to design direction (port_a -> port_b) |
Advanced | |||
MassFlowRate | m_flow_small | 1E-4*m_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b_start | p_a_start | Guess value for outlet pressure [Pa] |
Flow resistance | |||
Boolean | computeFlowResistance | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp | true | = 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 |
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) |
partial model PartialStaticTwoPortHeatMassTransfer "Partial model transporting fluid between two ports without storing mass or energy" extends Buildings.Fluids.Interfaces.PartialStaticTwoPortInterface; extends Buildings.Fluids.Interfaces.TwoPortFlowResistanceParameters( final computeFlowResistance=true); import Modelica.Constants; Modelica.SIunits.HeatFlowRate Q_flow "Heat transfered into the medium"; Medium.MassFlowRate mXi_flow[Medium.nXi] "Mass flow rates of independent substances added to the medium"; equation // Energy balance (no storage, no heat loss/gain) port_a.m_flow*port_a.h_outflow + port_b.m_flow*inStream(port_b.h_outflow) = -Q_flow; port_a.m_flow*port_b.h_outflow + port_b.m_flow*inStream(port_a.h_outflow) = Q_flow; // Mass balance (no storage) port_a.m_flow + port_b.m_flow = -sum(mXi_flow); port_a.m_flow*port_a.Xi_outflow + port_b.m_flow*inStream(port_b.Xi_outflow) = -mXi_flow; port_a.m_flow*port_b.Xi_outflow + port_b.m_flow*inStream(port_a.Xi_outflow) = mXi_flow; // Transport of trace substances port_a.C_outflow = inStream(port_b.C_outflow); port_b.C_outflow = inStream(port_a.C_outflow); // Pressure drop calculation if computeFlowResistance then if from_dp then m_flow = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_dp( dp=dp, k=m_flow_nominal/sqrt(dp_nominal), m_flow_turbulent=deltaM * m_flow_nominal, linearized=linearizeFlowResistance); else dp = Buildings.Fluids.BaseClasses.FlowModels.basicFlowFunction_m_flow( m_flow=m_flow, k=m_flow_nominal/sqrt(dp_nominal), m_flow_turbulent=deltaM * m_flow_nominal, linearized=linearizeFlowResistance); end if; else dp = 0; end if; end PartialStaticTwoPortHeatMassTransfer;
This component defines the interface for models that transports a fluid between two 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 model is used by other models in this package that add heat transfer, mass transfer and pressure drop equations. See for example Buildings.Fluids.Interfaces.PartialStaticTwoPortHeatMassTransfer.
Extends from Modelica_Fluid.Interfaces.PartialTwoPort (Partial component with two ports).
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 | system.allowFlowReversal | = true to allow flow reversal, false restricts to design direction (port_a -> port_b) |
Advanced | |||
MassFlowRate | m_flow_small | 1E-4*m_flow_nominal | Small mass flow rate for regularization of zero flow [kg/s] |
Diagnostics | |||
Boolean | show_V_flow | true | = true, if volume flow rate at inflowing port is computed |
Initialization | |||
AbsolutePressure | p_a_start | system.p_start | Guess value for inlet pressure [Pa] |
AbsolutePressure | p_b_start | p_a_start | Guess value for outlet pressure [Pa] |
partial model PartialStaticTwoPortInterface "Partial model transporting fluid between two ports without storing mass or energy" import Modelica.Constants; extends Modelica_Fluid.Interfaces.PartialTwoPort( port_a( p(start=p_a_start), m_flow(min = if allowFlowReversal then -Constants.inf else 0)), port_b( p(start=p_b_start), m_flow(max = if allowFlowReversal then +Constants.inf else 0))); parameter Medium.MassFlowRate m_flow_nominal(min=0) "Nominal mass flow rate"; parameter Medium.MassFlowRate m_flow_small(min=0) = 1E-4*m_flow_nominal "Small mass flow rate for regularization of zero flow"; // Initialization parameter Medium.AbsolutePressure p_a_start=system.p_start "Guess value for inlet pressure"; parameter Medium.AbsolutePressure p_b_start=p_a_start "Guess value for outlet pressure"; // Diagnostics // parameter Boolean show_T = true // "= true, if temperatures at port_a and port_b are computed" annotation 4; parameter Boolean show_V_flow = true "= true, if volume flow rate at inflowing port is computed"; Modelica.SIunits.VolumeFlowRate V_flow= m_flow/Modelica_Fluid.Utilities.regStep(m_flow, Medium.density(state_a_inflow), Medium.density(state_b_inflow), 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(state_a), 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(state_b), 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"; */ Medium.MassFlowRate m_flow(start=0) "Mass flow rate from port_a to port_b (m_flow > 0 is design flow direction)"; Modelica.SIunits.Pressure dp(start=0, displayUnit="Pa") "Pressure difference between port_a and port_b"; Medium.ThermodynamicState sta_a= Medium.setState_phX(port_a.p, actualStream(port_a.h_outflow), actualStream(port_a.Xi_outflow)) "Medium properties in port_a"; Medium.ThermodynamicState sta_b= Medium.setState_phX(port_b.p, actualStream(port_b.h_outflow), actualStream(port_b.Xi_outflow)) "Medium properties in port_b"; protected Medium.ThermodynamicState state_a_inflow= Medium.setState_phX(port_a.p, inStream(port_a.h_outflow), inStream(port_a.Xi_outflow)) "state for medium inflowing through port_a"; Medium.ThermodynamicState state_b_inflow= Medium.setState_phX(port_b.p, inStream(port_b.h_outflow), inStream(port_b.Xi_outflow)) "state for medium inflowing through port_b"; equation // medium_a.state=sta_a; // medium_a.Xi = actualStream(port_a.Xi_outflow); // Design direction of mass flow rate m_flow = port_a.m_flow; // Pressure difference between ports dp = port_a.p - port_b.p; end PartialStaticTwoPortInterface;
Type | Name | Default | Description |
---|---|---|---|
Nominal condition | |||
Pressure | dp_nominal | Pressure [Pa] | |
Flow resistance | |||
Boolean | computeFlowResistance | true | =true, compute flow resistance. Set to false to assume no friction |
Boolean | from_dp | true | = 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 |
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 = true "= true, use m_flow = f(dp) else dp = f(m_flow)"; parameter Modelica.SIunits.Pressure dp_nominal(min=0, displayUnit="Pa") "Pressure"; 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;