Buildings.Fluid.BaseClasses

Information

Extends from Modelica.Fluid.Icons.BaseClassLibrary (Icon for library).

Package Content

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

Buildings.Fluid.BaseClasses.PartialResistance

Information

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 Modelica.Fluid.Interfaces.PartialTwoPortTransport (Partial element transporting fluid between two ports without storage of mass or energy).

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]
Pressure	dp_nominal		Pressure [Pa]
Assumptions
Boolean	allowFlowReversal	system.allowFlowReversal	= true to allow flow reversal, false restricts to design direction (port_a -> port_b)
Advanced
AbsolutePressure	dp_start	0.01*system.p_start	Guess value of dp = port_a.p - port_b.p [Pa]
MassFlowRate	m_flow_start	system.m_flow_start	Guess value of m_flow = port_a.m_flow [kg/s]
MassFlowRate	m_flow_small	1E-4*m_flow_nominal	Small mass flow rate for regularization of zero flow [kg/s]
Boolean	from_dp	true	= 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_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 PartialResistance 
  "Partial model for a hydraulic resistance"
    extends Modelica.Fluid.Interfaces.PartialTwoPortTransport(m_flow_small = 1E-4*m_flow_nominal,
     m_flow(nominal=m_flow_nominal), dp(nominal=dp_nominal, displayUnit="Pa"));


  parameter Boolean from_dp = true 
    "= 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";
  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";
equation 
  // Pressure drop calculation
  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;

  // 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);

end PartialResistance;

Buildings.Fluid.BaseClasses.PartialThreeWayResistance

Information

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.

Parameters

Type	Name	Default	Description
PartialTwoPortTransport	res1	redeclare Modelica.Fluid.Int...	Partial model, to be replaced with a fluid component
PartialTwoPortTransport	res2	redeclare Modelica.Fluid.Int...	Partial model, to be replaced with a fluid component
PartialTwoPortTransport	res3	redeclare Modelica.Fluid.Int...	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	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

Connectors

Type	Name	Description
FluidPort_a	port_1
FluidPort_b	port_2
FluidPort_a	port_3

Modelica definition

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 Modelica.Fluid.Interfaces.PartialTwoPortTransport res1(redeclare 
      package Medium = Medium) 
    "Partial model, to be replaced with a fluid component";
  replaceable Modelica.Fluid.Interfaces.PartialTwoPortTransport res2(redeclare 
      package Medium = Medium) 
    "Partial model, to be replaced with a fluid component";
  replaceable Modelica.Fluid.Interfaces.PartialTwoPortTransport res3(redeclare 
      package Medium = Medium) 
    "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,
    use_portsData=false,
    nPorts=3,
    use_HeatTransfer=false,
    tau=tau,
    m_flow_nominal=mDyn_flow_nominal,
    m_flow_small=1E-4*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=
      system.p_start "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 system.T_start 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";
equation 
  connect(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 then
    connect(res1.port_b, res3.port_b);
    connect(res1.port_b, res2.port_b);
  end if;
end PartialThreeWayResistance;