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Annex60.Fluid.BaseClasses

Package with base classes for Annex60.Fluid

Information

This package contains base classes that are used to construct the models in Annex60.Fluid.

Extends from Modelica.Icons.BasesPackage (Icon for packages containing base classes).

Package Content

Name Description
Annex60.Fluid.BaseClasses.IndexMassFraction IndexMassFraction Computes the index of a substance in the mass fraction vector Xi
Annex60.Fluid.BaseClasses.PartialResistance PartialResistance Partial model for a hydraulic resistance
Annex60.Fluid.BaseClasses.PartialThreeWayResistance PartialThreeWayResistance Flow splitter with partial resistance model at each port
Annex60.Fluid.BaseClasses.FlowModels FlowModels Flow models for pressure drop calculations

Annex60.Fluid.BaseClasses.IndexMassFraction

Computes the index of a substance in the mass fraction vector Xi

Information

This block computes the index that the subtance with name substanceName has in the mass fraction vector X. If the medium model has no component called substanceName, then the block writes an error message and terminates the simulation.

This block is used for example to obtain the index of the subtance 'water' to obtain the water vapor concentration, or to measure any other mass fraction.

Parameters

TypeNameDefaultDescription
replaceable package MediumModelica.Media.Interfaces.Pa...Medium model
StringsubstanceName""Name of species substance

Connectors

TypeNameDescription
replaceable package MediumMedium model

Modelica definition

block IndexMassFraction "Computes the index of a substance in the mass fraction vector Xi" replaceable package Medium = Modelica.Media.Interfaces.PartialCondensingGases "Medium model"; parameter String substanceName="" "Name of species substance"; protected parameter Integer i_x(fixed=false) "Index of substance"; initial algorithm // Compute index of species vector that carries the substance name i_x :=-1; for i in 1:Medium.nXi loop if Modelica.Utilities.Strings.isEqual(string1=Medium.substanceNames[i], string2=substanceName, caseSensitive=false) then i_x :=i; end if; end for; assert(i_x > 0, "Substance '" + substanceName + "' is not present in medium '" + Medium.mediumName + "'.\n" + "Change medium model to one that has '" + substanceName + "' as a substance."); end IndexMassFraction;

Annex60.Fluid.BaseClasses.PartialResistance Annex60.Fluid.BaseClasses.PartialResistance

Partial model for a hydraulic resistance

Annex60.Fluid.BaseClasses.PartialResistance

Information

Partial model for a flow resistance, possible with variable flow coefficient. Models that extend this class need to implement an equation that relates m_flow and dp, and they need to assign the parameter m_flow_turbulent.

See for example Annex60.Fluid.FixedResistances.PressureDrop for a model that extends this base class.

Extends from Annex60.Fluid.Interfaces.PartialTwoPortInterface (Partial model transporting fluid between two ports without storing mass or energy).

Parameters

TypeNameDefaultDescription
replaceable package MediumPartialMediumMedium in the component
MassFlowRatem_flow_turbulent Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s]
Nominal condition
MassFlowRatem_flow_nominal Nominal mass flow rate [kg/s]
PressureDifferencedp_nominal Pressure drop at nominal mass flow rate [Pa]
Assumptions
BooleanallowFlowReversaltrue= false to simplify equations, assuming, but not enforcing, no flow reversal
Advanced
MassFlowRatem_flow_small1E-4*abs(m_flow_nominal)Small mass flow rate for regularization of zero flow [kg/s]
Booleanfrom_dpfalse= true, use m_flow = f(dp) else dp = f(m_flow)
BooleanhomotopyInitializationtrue= true, use homotopy method
Booleanlinearizedfalse= true, use linear relation between m_flow and dp for any flow rate
Diagnostics
Booleanshow_Tfalse= true, if actual temperature at port is computed

Connectors

TypeNameDescription
FluidPort_aport_aFluid connector a (positive design flow direction is from port_a to port_b)
FluidPort_bport_bFluid connector b (positive design flow direction is from port_a to port_b)

Modelica definition

partial model PartialResistance "Partial model for a hydraulic resistance" extends Annex60.Fluid.Interfaces.PartialTwoPortInterface( show_T=false, dp(nominal=if dp_nominal_pos > Modelica.Constants.eps then dp_nominal_pos else 1), m_flow( nominal=if m_flow_nominal_pos > Modelica.Constants.eps then m_flow_nominal_pos else 1), final m_flow_small = 1E-4*abs(m_flow_nominal)); parameter Boolean from_dp = false "= true, use m_flow = f(dp) else dp = f(m_flow)"; parameter Modelica.SIunits.PressureDifference dp_nominal(displayUnit="Pa") "Pressure drop at nominal mass flow rate"; parameter Boolean homotopyInitialization = true "= true, use homotopy method"; parameter Boolean linearized = false "= true, use linear relation between m_flow and dp for any flow rate"; parameter Modelica.SIunits.MassFlowRate m_flow_turbulent(min=0) "Turbulent flow if |m_flow| >= m_flow_turbulent"; protected parameter Medium.ThermodynamicState sta_default= Medium.setState_pTX(T=Medium.T_default, p=Medium.p_default, X=Medium.X_default); parameter Modelica.SIunits.DynamicViscosity eta_default=Medium.dynamicViscosity(sta_default) "Dynamic viscosity, used to compute transition to turbulent flow regime"; final parameter Modelica.SIunits.MassFlowRate m_flow_nominal_pos = abs(m_flow_nominal) "Absolute value of nominal flow rate"; final parameter Modelica.SIunits.PressureDifference dp_nominal_pos(displayUnit="Pa") = abs(dp_nominal) "Absolute value of nominal pressure difference"; equation // Isenthalpic state transformation (no storage and no loss of energy) port_a.h_outflow = if allowFlowReversal then inStream(port_b.h_outflow) else Medium.h_default; 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 = 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 PartialResistance;

Annex60.Fluid.BaseClasses.PartialThreeWayResistance Annex60.Fluid.BaseClasses.PartialThreeWayResistance

Flow splitter with partial resistance model at each port

Annex60.Fluid.BaseClasses.PartialThreeWayResistance

Information

Partial model for flow resistances with three ports such as a flow mixer/splitter or a three way valve.

If energyDynamics ≠ Modelica.Fluid.Types.Dynamics.SteadyState, 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.

Extends from Annex60.Fluid.Interfaces.LumpedVolumeDeclarations (Declarations for lumped volumes).

Parameters

TypeNameDefaultDescription
replaceable package MediumPartialMediumMedium in the component
PartialTwoPortInterfaceres1redeclare Annex60.Fluid.Inte...Partial model, to be replaced with a fluid component
PartialTwoPortInterfaceres2redeclare Annex60.Fluid.Inte...Partial model, to be replaced with a fluid component
PartialTwoPortInterfaceres3redeclare Annex60.Fluid.Inte...Partial model, to be replaced with a fluid component
Dynamics
Equations
DynamicsenergyDynamicsModelica.Fluid.Types.Dynamic...Type of energy balance: dynamic (3 initialization options) or steady state
DynamicsmassDynamicsenergyDynamicsType of mass balance: dynamic (3 initialization options) or steady state
MassFlowRatemDyn_flow_nominal Nominal mass flow rate for dynamic momentum and energy balance [kg/s]
RealmSenFac1Factor for scaling the sensible thermal mass of the volume
Nominal condition
Timetau10Time constant at nominal flow for dynamic energy and momentum balance [s]
Initialization
AbsolutePressurep_startMedium.p_defaultStart value of pressure [Pa]
TemperatureT_startMedium.T_defaultStart value of temperature [K]
MassFractionX_start[Medium.nX]Medium.X_defaultStart value of mass fractions m_i/m [kg/kg]
ExtraPropertyC_start[Medium.nC]fill(0, Medium.nC)Start value of trace substances
ExtraPropertyC_nominal[Medium.nC]fill(1E-2, Medium.nC)Nominal value of trace substances. (Set to typical order of magnitude.)
Advanced
Booleanfrom_dptrue= true, use m_flow = f(dp) else dp = f(m_flow)
PortFlowDirectionportFlowDirection_1Modelica.Fluid.Types.PortFlo...Flow direction for port_1
PortFlowDirectionportFlowDirection_2Modelica.Fluid.Types.PortFlo...Flow direction for port_2
PortFlowDirectionportFlowDirection_3Modelica.Fluid.Types.PortFlo...Flow direction for port_3

Connectors

TypeNameDescription
FluidPort_aport_1First port, typically inlet
FluidPort_bport_2Second port, typically outlet
FluidPort_aport_3Third port, can be either inlet or outlet

Modelica definition

partial model PartialThreeWayResistance "Flow splitter with partial resistance model at each port" extends Annex60.Fluid.Interfaces.LumpedVolumeDeclarations( final mSenFac=1); 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)) "First port, typically inlet"; 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)) "Second port, typically outlet"; 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)) "Third port, can be either inlet or outlet"; 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 Boolean from_dp = true "= true, use m_flow = f(dp) else dp = f(m_flow)"; 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"; replaceable Annex60.Fluid.Interfaces.PartialTwoPortInterface res1 constrainedby Annex60.Fluid.Interfaces.PartialTwoPortInterface( redeclare final package Medium = Medium, allowFlowReversal=portFlowDirection_1 == Modelica.Fluid.Types.PortFlowDirection.Bidirectional) "Partial model, to be replaced with a fluid component"; replaceable Annex60.Fluid.Interfaces.PartialTwoPortInterface res2 constrainedby Annex60.Fluid.Interfaces.PartialTwoPortInterface( redeclare final package Medium = Medium, allowFlowReversal=portFlowDirection_2 == Modelica.Fluid.Types.PortFlowDirection.Bidirectional) "Partial model, to be replaced with a fluid component"; replaceable Annex60.Fluid.Interfaces.PartialTwoPortInterface res3 constrainedby Annex60.Fluid.Interfaces.PartialTwoPortInterface( redeclare final package Medium = Medium, allowFlowReversal=portFlowDirection_3 == Modelica.Fluid.Types.PortFlowDirection.Bidirectional) "Partial model, to be replaced with a fluid component"; Annex60.Fluid.Delays.DelayFirstOrder vol( redeclare final package Medium = Medium, final nPorts=3, final tau=tau, final m_flow_nominal=mDyn_flow_nominal, final energyDynamics=energyDynamics, final massDynamics=massDynamics, final p_start=p_start, final T_start=T_start, final X_start=X_start, final C_start=C_start, final allowFlowReversal=true, final prescribedHeatFlowRate=false) if have_controlVolume "Fluid volume to break algebraic loop"; protected parameter Boolean have_controlVolume= energyDynamics <> Modelica.Fluid.Types.Dynamics.SteadyState or massDynamics <> Modelica.Fluid.Types.Dynamics.SteadyState "Boolean flag used to remove conditional components"; Modelica.Fluid.Interfaces.FluidPort_a port_internal( redeclare package Medium = Medium) if not have_controlVolume "Internal dummy port for easier connection of conditional connections"; equation if portFlowDirection_1==Modelica.Fluid.Types.PortFlowDirection.Leaving then if not have_controlVolume then connect(res1.port_a, port_internal); else connect(res1.port_a, vol.ports[1]); end if; connect(port_1, res1.port_b); else if not have_controlVolume then connect(res1.port_b, port_internal); else connect(res1.port_b, vol.ports[1]); end if; connect(port_1, res1.port_a); end if; if portFlowDirection_2==Modelica.Fluid.Types.PortFlowDirection.Leaving then if not have_controlVolume then connect(res2.port_a, port_internal); else connect(res2.port_a, vol.ports[2]); end if; connect(port_2, res2.port_b); else if not have_controlVolume then connect(res2.port_b, port_internal); else connect(res2.port_b, vol.ports[2]); end if; connect(port_2, res2.port_a); end if; if portFlowDirection_3==Modelica.Fluid.Types.PortFlowDirection.Leaving then if not have_controlVolume then connect(res3.port_a, port_internal); else connect(res3.port_a, vol.ports[3]); end if; connect(port_3, res3.port_b); else if not have_controlVolume then connect(res3.port_b, port_internal); else connect(res3.port_b, vol.ports[3]); end if; connect(port_3, res3.port_a); end if; end PartialThreeWayResistance;

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