| Name | Description |
|---|---|
| Fixed flow resistance with dp and m_flow as parameter | |
| Pipe with no flow friction and no heat transfer | |
| Flow splitter with fixed resistance at each port | |
| Collection of models that illustrate model use and test models |
Buildings.Fluid.FixedResistances.FixedResistanceDpM
This is a model of a resistance with a fixed flow coefficient
k = m ⁄ √ΔP.
Near the origin, the square root relation is regularized to ensure that the derivative is bounded.Extends from Buildings.Fluid.BaseClasses.PartialResistance (Partial model for a hydraulic resistance).
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Boolean | use_dh | false | Set to true to specify hydraulic diameter |
| Length | dh | 1 | Hydraulic diameter [m] |
| Real | ReC | 4000 | Reynolds number where transition to turbulent starts |
| Real | deltaM | 0.3 | Fraction of nominal mass flow rate where transition to turbulent occurs |
| 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) |
model FixedResistanceDpM
"Fixed flow resistance with dp and m_flow as parameter"
extends Buildings.Fluid.BaseClasses.PartialResistance;
parameter Boolean use_dh = false "Set to true to specify hydraulic diameter";
parameter Modelica.SIunits.Length dh=1 "Hydraulic diameter";
parameter Real ReC=4000
"Reynolds number where transition to turbulent starts";
parameter Real deltaM(min=0.01) = 0.3
"Fraction of nominal mass flow rate where transition to turbulent occurs";
initial equation
assert(m_flow_nominal > 0, "m_flow_nominal must be positive. Check parameters.");
if ( m_flow_turbulent > m_flow_nominal) then
Modelica.Utilities.Streams.print("Warning: In FixedResistanceDpM, m_flow_nominal is smaller than m_flow_turbulent."
+ "\n"
+ " m_flow_nominal = " + realString(m_flow_nominal) + "\n"
+ " dh = " + realString(dh) + "\n"
+ " To fix, set dh < " +
realString( 4*m_flow_nominal/eta_nominal/Modelica.Constants.pi/ReC) + "\n"
+ " Suggested value: dh = " +
realString(1/10*4*m_flow_nominal/eta_nominal/Modelica.Constants.pi/ReC));
end if;
equation
// if computeFlowResistance = false, then equations of this model are disabled.
if computeFlowResistance then
m_flow_turbulent = if use_dh then
eta_nominal*dh/4*Modelica.Constants.pi*ReC else
deltaM * m_flow_nominal;
if linearized then
k = m_flow_nominal / dp_nominal / conv2;
else
k = m_flow_nominal / sqrt(dp_nominal);
end if;
else
m_flow_turbulent = 0;
k = 0;
end if;
end FixedResistanceDpM;
Buildings.Fluid.FixedResistances.LosslessPipe
Model of a pipe with no flow resistance and no heat loss.
This model can be used to replace a replaceable pipe model
in flow legs in which no friction should be modeled, such as
in the outlet port of a three way valve.
Extends from Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface (Partial model transporting fluid between two ports without storing mass or energy), Buildings.BaseClasses.BaseIcon (Base icon).
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Medium in the component | |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal | Nominal mass flow rate [kg/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) |
| 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 | 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) |
model LosslessPipe "Pipe with no flow friction and no heat transfer"
extends Buildings.Fluid.Interfaces.PartialStaticTwoPortInterface(
show_T=false, show_V_flow=false);
extends Buildings.BaseClasses.BaseIcon;
final parameter Boolean from_dp=true "Used to satisfy replaceable models";
equation
dp=0;
// 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 LosslessPipe;
Buildings.Fluid.FixedResistances.SplitterFixedResistanceDpM
Model of a flow splitter or mixer with a fixed resistance in each flow leg.
Extends from Buildings.Fluid.BaseClasses.PartialThreeWayResistance (Flow splitter with partial resistance model at each port).
| Type | Name | Default | Description |
|---|---|---|---|
| replaceable package Medium | PartialMedium | Fluid medium model | |
| Boolean | use_dh | false | Set to true to specify hydraulic diameter |
| Real | deltaM | 0.3 | Fraction of nominal mass flow rate where transition to turbulent occurs |
| Length | dh[3] | {1,1,1} | Hydraulic diameter [m] |
| Real | ReC[3] | {4000,4000,4000} | Reynolds number where transition to turbulent starts |
| Nominal condition | |||
| MassFlowRate | m_flow_nominal[3] | Mass flow rate [kg/s] | |
| Pressure | dp_nominal[3] | Pressure [Pa] | |
| Advanced | |||
| 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 |
| 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 | sum(m_flow_nominal[:]/3) | 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 |
model SplitterFixedResistanceDpM
"Flow splitter with fixed resistance at each port"
extends Buildings.Fluid.BaseClasses.PartialThreeWayResistance(
mDyn_flow_nominal = sum(m_flow_nominal[:]/3),
redeclare Buildings.Fluid.FixedResistances.FixedResistanceDpM res1(
redeclare package Medium=Medium,
from_dp=from_dp, m_flow_nominal=m_flow_nominal[1], dp_nominal=dp_nominal[1],
ReC=ReC[1], dh=dh[1],
linearized=linearized, deltaM=deltaM),
redeclare Buildings.Fluid.FixedResistances.FixedResistanceDpM res2(
redeclare package Medium=Medium,
from_dp=from_dp, m_flow_nominal=m_flow_nominal[2], dp_nominal=dp_nominal[2],
ReC=ReC[2], dh=dh[2],
linearized=linearized, deltaM=deltaM),
redeclare Buildings.Fluid.FixedResistances.FixedResistanceDpM res3(
redeclare package Medium=Medium,
from_dp=from_dp, m_flow_nominal=m_flow_nominal[3], dp_nominal=dp_nominal[3],
ReC=ReC[3], dh=dh[3],
linearized=linearized, deltaM=deltaM));
parameter Boolean use_dh = false "Set to true to specify hydraulic diameter";
parameter Modelica.SIunits.MassFlowRate[3] m_flow_nominal(each min=0)
"Mass flow rate";
parameter Modelica.SIunits.Pressure[3] dp_nominal(each min=0, each
displayUnit = "Pa") "Pressure";
parameter Real deltaM(min=0) = 0.3
"Fraction of nominal mass flow rate where transition to turbulent occurs";
parameter Modelica.SIunits.Length[3] dh={1, 1, 1} "Hydraulic diameter";
parameter Real[3] ReC={4000, 4000, 4000}
"Reynolds number where transition to turbulent starts";
parameter Boolean linearized = false
"= true, use linear relation between m_flow and dp for any flow rate";
end SplitterFixedResistanceDpM;