Extends from Modelica.Fluid.Icons.BaseClassLibrary (Icon for library).
Name | Description |
---|---|
FlowModels | Flow models for pressure drop calculations |
PartialResistance | Partial model for a hydraulic resistance |
PartialThreeWayResistance | Flow splitter with partial resistance model at each port |
Partial model for a flow resistance, possible with variable flow coefficient. The pressure drop is computed by an instance of Buildings.Fluid.BaseClasses.FlowModels.BasicFlowModel, i.e., using a regularized implementation of the equation
m_flow = sign(dp) * k * sqrt(|dp|).
Extends from Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface (Partial model transporting fluid between two ports without storing mass or energy).
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 drop at nominal mass flow rate [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] |
Boolean | from_dp | false | = true, use m_flow = f(dp) else dp = f(m_flow) |
Boolean | linearized | false | = true, use linear relation between m_flow and dp for any flow rate |
Diagnostics | |||
Boolean | show_V_flow | false | = true, if volume flow rate at inflowing port is computed |
Boolean | show_T | false | = true, if actual temperature at port is computed (may lead to events) |
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 PartialResistance "Partial model for a hydraulic resistance" extends Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface( show_T=false, show_V_flow=false); parameter Boolean from_dp = false "= true, use m_flow = f(dp) else dp = f(m_flow)"; parameter Medium.MassFlowRate m_flow_nominal(min=0) "Nominal mass flow rate"; parameter Modelica.SIunits.Pressure dp_nominal(min=0, displayUnit="Pa") "Pressure drop at nominal mass flow rate"; parameter Boolean linearized = false "= true, use linear relation between m_flow and dp for any flow rate"; Real k(unit="") "Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2)"; Medium.MassFlowRate m_flow_turbulent "Turbulent flow if |m_flow| >= m_flow_turbulent, not a parameter because k can be a function of time"; // Modelica.SIunits.Pressure dp_turbulent // "Turbulent flow if |dp| >= dp_small, not a parameter because k can be a function of time"; protected parameter Medium.ThermodynamicState sta0= Medium.setState_pTX(T=Medium.T_default, p=Medium.p_default, X=Medium.X_default); parameter Modelica.SIunits.DynamicViscosity eta_nominal=Medium.dynamicViscosity(sta0) "Dynamic viscosity, used to compute transition to turbulent flow regime"; parameter Modelica.SIunits.SpecificEnthalpy h0=Medium.h_default "Initial value for solver for specific enthalpy"; //specificEnthalpy(sta0) constant Real conv(unit="m.s2/kg") = 1 "Factor, needed to satisfy unit check"; constant Real conv2 = sqrt(conv) "Factor, needed to satisfy unit check"; final parameter Boolean computeFlowResistance=(dp_nominal > Modelica.Constants.eps) "Flag to enable/disable computation of flow resistance"; equation // Pressure drop calculation if computeFlowResistance then if from_dp then m_flow=FlowModels.basicFlowFunction_dp(dp=dp, k=k, m_flow_turbulent=m_flow_turbulent, linearized=linearized); else dp=FlowModels.basicFlowFunction_m_flow(m_flow=m_flow, k=k, m_flow_turbulent=m_flow_turbulent, linearized=linearized); end if; /* homotopy is not yet supported in Dymola 7.4 with Modelica 3.1 if from_dp then m_flow=homotopy(actual=FlowModels.basicFlowFunction_dp(dp=dp, k=k, m_flow_turbulent=m_flow_turbulent, linearized=linearized), simplified=FlowModels.basicFlowFunction_dp(dp=dp, k=k, m_flow_turbulent=m_flow_turbulent, linearized=true)); else dp=homotopy(actual=FlowModels.basicFlowFunction_m_flow(m_flow=m_flow, k=k, m_flow_turbulent=m_flow_turbulent, linearized=linearized), simplified=FlowModels.basicFlowFunction_m_flow(m_flow=m_flow, k=k, m_flow_turbulent=m_flow_turbulent, linearized=true)); end if; */ else dp = 0; end if; // Isenthalpic state transformation (no storage and no loss of energy) port_a.h_outflow = inStream(port_b.h_outflow); port_b.h_outflow = inStream(port_a.h_outflow); // Mass balance (no storage) port_a.m_flow + port_b.m_flow = 0; // Transport of substances port_a.Xi_outflow = inStream(port_b.Xi_outflow); port_b.Xi_outflow = inStream(port_a.Xi_outflow); port_a.C_outflow = inStream(port_b.C_outflow); port_b.C_outflow = inStream(port_a.C_outflow);end PartialResistance;
Partial model for flow resistances with three ports such as a flow mixer/splitter or a three way valve.
If dynamicBalance=true
, then at the junction of the three flows,
a mixing volume will be present. This will introduce a dynamic energy and momentum
balance, which often breaks algebraic loops.
The time constant of the mixing volume is determined by the parameter tau
.
Type | Name | Default | Description |
---|---|---|---|
PartialStaticTwoPortInterface | res1 | redeclare Buildings.Fluid.In... | Partial model, to be replaced with a fluid component |
PartialStaticTwoPortInterface | res2 | redeclare Buildings.Fluid.In... | Partial model, to be replaced with a fluid component |
PartialStaticTwoPortInterface | res3 | redeclare Buildings.Fluid.In... | Partial model, to be replaced with a fluid component |
Advanced | |||
Boolean | from_dp | true | = true, use m_flow = f(dp) else dp = f(m_flow) |
Assumptions | |||
Dynamics | |||
Boolean | dynamicBalance | true | Set to true to use a dynamic balance, which often leads to smaller systems of equations |
Time | tau | 10 | Time constant at nominal flow for dynamic energy and momentum balance [s] |
MassFlowRate | mDyn_flow_nominal | Nominal mass flow rate for dynamic momentum and energy balance [kg/s] | |
Dynamics | energyDynamics | system.energyDynamics | Formulation of energy balance |
Dynamics | massDynamics | system.massDynamics | Formulation of mass balance |
Initialization | |||
AbsolutePressure | p_start | Medium.p_default | 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 Medium.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 |
Type | Name | Description |
---|---|---|
FluidPort_a | port_1 | |
FluidPort_b | port_2 | |
FluidPort_a | port_3 |
partial model PartialThreeWayResistance "Flow splitter with partial resistance model at each port" outer Modelica.Fluid.System system "System properties"; replaceable package Medium = Modelica.Media.Interfaces.PartialMedium "Fluid medium model";Modelica.Fluid.Interfaces.FluidPort_a port_1(redeclare package Medium = Medium, m_flow(min=if (portFlowDirection_1 == Modelica.Fluid.Types.PortFlowDirection.Entering) then 0.0 else -Modelica.Constants.inf, max=if (portFlowDirection_1 == Modelica.Fluid.Types.PortFlowDirection.Leaving) then 0.0 else Modelica.Constants.inf)); Modelica.Fluid.Interfaces.FluidPort_b port_2(redeclare package Medium = Medium, m_flow(min=if (portFlowDirection_2 == Modelica.Fluid.Types.PortFlowDirection.Entering) then 0.0 else -Modelica.Constants.inf, max=if (portFlowDirection_2 == Modelica.Fluid.Types.PortFlowDirection.Leaving) then 0.0 else Modelica.Constants.inf)); Modelica.Fluid.Interfaces.FluidPort_a port_3( redeclare package Medium=Medium, m_flow(min=if (portFlowDirection_3==Modelica.Fluid.Types.PortFlowDirection.Entering) then 0.0 else -Modelica.Constants.inf, max=if (portFlowDirection_3==Modelica.Fluid.Types.PortFlowDirection.Leaving) then 0.0 else Modelica.Constants.inf)); parameter Boolean from_dp = true "= true, use m_flow = f(dp) else dp = f(m_flow)";replaceable Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface res1(redeclare package Medium = Medium, allowFlowReversal=true) "Partial model, to be replaced with a fluid component"; replaceable Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface res2(redeclare package Medium = Medium, allowFlowReversal=true) "Partial model, to be replaced with a fluid component"; replaceable Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface res3(redeclare package Medium = Medium, allowFlowReversal=true) "Partial model, to be replaced with a fluid component"; protected parameter Modelica.Fluid.Types.PortFlowDirection portFlowDirection_1=Modelica.Fluid.Types.PortFlowDirection.Bidirectional "Flow direction for port_1"; parameter Modelica.Fluid.Types.PortFlowDirection portFlowDirection_2=Modelica.Fluid.Types.PortFlowDirection.Bidirectional "Flow direction for port_2"; parameter Modelica.Fluid.Types.PortFlowDirection portFlowDirection_3=Modelica.Fluid.Types.PortFlowDirection.Bidirectional "Flow direction for port_3";public Delays.DelayFirstOrder vol( redeclare package Medium = Medium, nPorts=3, use_HeatTransfer=false, tau=tau, m_flow_nominal=mDyn_flow_nominal, energyDynamics=energyDynamics, massDynamics=massDynamics, p_start=p_start, use_T_start=use_T_start, T_start=T_start, h_start=h_start, X_start=X_start, C_start=C_start) if dynamicBalance "Fluid volume to break algebraic loop"; parameter Boolean dynamicBalance = true "Set to true to use a dynamic balance, which often leads to smaller systems of equations"; parameter Modelica.SIunits.Time tau=10 "Time constant at nominal flow for dynamic energy and momentum balance"; parameter Modelica.SIunits.MassFlowRate mDyn_flow_nominal "Nominal mass flow rate for dynamic momentum and energy balance"; parameter Modelica.Fluid.Types.Dynamics energyDynamics=system.energyDynamics "Formulation of energy balance"; parameter Modelica.Fluid.Types.Dynamics massDynamics=system.massDynamics "Formulation of mass balance"; parameter Modelica.Media.Interfaces.PartialMedium.AbsolutePressure p_start= Medium.p_default "Start value of pressure"; parameter Boolean use_T_start=true "= true, use T_start, otherwise h_start"; parameter Modelica.Media.Interfaces.PartialMedium.Temperature T_start=if use_T_start then Medium.T_default else Medium.temperature_phX( p_start, h_start, X_start) "Start value of temperature"; parameter Modelica.Media.Interfaces.PartialMedium.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 Modelica.Media.Interfaces.PartialMedium.MassFraction X_start[Medium.nX]= Medium.X_default "Start value of mass fractions m_i/m"; parameter Modelica.Media.Interfaces.PartialMedium.ExtraProperty C_start[ Medium.nC]=fill(0, Medium.nC) "Start value of trace substances"; equationconnect(port_1, res1.port_a); connect(res2.port_a, port_2); connect(res3.port_a, port_3); connect(res1.port_b,vol. ports[1]); connect(res2.port_b,vol. ports[2]); connect(res3.port_b,vol. ports[3]); if not dynamicBalance thenconnect(res1.port_b, res3.port_b); connect(res1.port_b, res2.port_b); end if;end PartialThreeWayResistance;