Collection of models that illustrate model use and test models
Information
This package contains examples for the use of models that can be found in
Buildings.Fluid.HeatExchangers.
Extends from Modelica.Icons.ExamplesPackage (Icon for packages containing runnable examples).
Package Content
| Name |
Description |
 DryCoilCounterFlowMassFlow
|
Model of a cooling coil that tests variable mass flow rates |
| DryCoilCounterFlowPControl
|
Model that demonstrates use of a heat exchanger without condensation and with feedback control |
| DryCoilDiscretized
|
Model that demonstrates use of a finite volume model of a heat exchanger without condensation |
| DryCoilDiscretizedPControl
|
Model that demonstrates use of a finite volume model of a heat exchanger without condensation and with feedback control |
| DryEffectivenessNTU
|
Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation |
| DryEffectivenessNTUMassFlow
|
Model of epsilon-NTU dry coil that tests variable mass flow rates |
| DryEffectivenessNTUPControl
|
Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation with feedback control |
| Heater_T
|
Example model for the heater with prescribed outlet temperature |
| Heater_u
|
Example model for the heater with prescribed heat input |
| WetCoilCounterFlowMassFlow
|
Model of a cooling coil that tests variable mass flow rates |
| WetCoilCounterFlowPControl
|
Model that demonstrates use of a heat exchanger with condensation and with feedback control |
| WetCoilDiscretizedPControl
|
Model that demonstrates use of a finite volume model of a heat exchanger with condensation and feedback control |
 BaseClasses
|
Package with base classes for Buildings.Fluid.HeatExchangers.Examples |
Model of a cooling coil that tests variable mass flow rates
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.DryCoilCounterFlow
for different inlet conditions.
Extends from Modelica.Icons.Example (Icon for runnable examples), Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow (Partial model of epsilon-NTU coil that tests variable mass flow rates).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | Nominal water inlet temperature [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | Nominal water outlet temperature [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | Nominal air inlet temperature [K] |
| Temperature | T_b2_nominal | 15 + 273.15 | Nominal air outlet temperature [K] |
| HeatFlowRate | Q_flow_nominal | m1_flow_nominal*4200*(T_a1_n... | Nominal heat transfer [W] |
| MassFlowRate | m1_flow_nominal | 0.1 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryCoilCounterFlowMassFlow
"Model of a cooling coil that tests variable mass flow rates"
extends Modelica.Icons.Example;
extends Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow
(
sou_1(nPorts=1),
sin_1(nPorts=1),
sou_2(nPorts=1),
sin_2(nPorts=1));
DryCoilCounterFlow hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
show_T=true,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
dp2_nominal(displayUnit="Pa") = 200,
allowFlowReversal1=true,
allowFlowReversal2=true,
dp1_nominal(displayUnit="Pa") = 3000,
UA_nominal=Q_flow_nominal/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial);
Sensors.RelativeHumidityTwoPort senRelHum(
redeclare package Medium
= Medium2, m_flow_nominal=m2_flow_nominal);
equation
connect(sou_1.ports[1], hex.port_a1);
connect(hex.port_b1, sin_1.ports[1]);
connect(hex.port_a2, sou_2.ports[1]);
connect(senRelHum.port_a, hex.port_b2);
connect(senRelHum.port_b, sin_2.ports[1]);
end DryCoilCounterFlowMassFlow;
Model that demonstrates use of a heat exchanger without condensation and with feedback control
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.DryCoilCounterFlow.
The valve on the water-side is regulated to track a setpoint temperature
for the air outlet.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | [K] |
| Temperature | T_b2_nominal | 15 + 273.15 | [K] |
| MassFlowRate | m1_flow_nominal | 0.1 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryCoilCounterFlowPControl
"Model that demonstrates use of a heat exchanger without condensation and with feedback control"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water;
package Medium2 =
Buildings.Media.Air;
parameter Modelica.SIunits.Temperature T_a1_nominal=5 + 273.15;
parameter Modelica.SIunits.Temperature T_b1_nominal=10 + 273.15;
parameter Modelica.SIunits.Temperature T_a2_nominal=30 + 273.15;
parameter Modelica.SIunits.Temperature T_b2_nominal=15 + 273.15;
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal=0.1
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal=m1_flow_nominal*4200/
1000*(T_a1_nominal - T_b1_nominal)/(T_b2_nominal - T_a2_nominal)
"Nominal mass flow rate medium 2";
Buildings.Fluid.Sources.Boundary_pT sin_2(
redeclare package Medium = Medium2,
nPorts=1,
use_p_in=false,
p(displayUnit="Pa") = 101325,
T=303.15);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare package Medium = Medium2,
nPorts=1,
T=T_a2_nominal,
X={0.02,1 - 0.02},
use_T_in=true,
use_X_in=true,
p(displayUnit="Pa") = 101325 + 300);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare package Medium = Medium1,
nPorts=1,
use_p_in=false,
p=300000,
T=293.15);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
nPorts=1,
use_T_in=true,
p=300000 + 12000);
Fluid.FixedResistances.FixedResistanceDpM res_2(
from_dp=true,
redeclare package Medium = Medium2,
dp_nominal=100,
m_flow_nominal=m2_flow_nominal);
Fluid.FixedResistances.FixedResistanceDpM res_1(
from_dp=true,
redeclare package Medium = Medium1,
dp_nominal=3000,
m_flow_nominal=m1_flow_nominal);
Buildings.Fluid.Sensors.TemperatureTwoPort temSen(
redeclare package Medium =
Medium2, m_flow_nominal=m2_flow_nominal);
Buildings.Fluid.Actuators.Valves.TwoWayEqualPercentage val(
redeclare package Medium = Medium1,
m_flow_nominal=m1_flow_nominal,
dpValve_nominal=6000)
"Valve model";
Modelica.Blocks.Sources.TimeTable TSet(table=[0,288.15; 600,288.15; 600,
298.15; 1200,298.15; 1800,283.15; 2400,283.15; 2400,288.15])
"Setpoint temperature";
Buildings.Fluid.HeatExchangers.DryCoilCounterFlow hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
dp2_nominal(displayUnit="Pa") = 200,
allowFlowReversal1=true,
allowFlowReversal2=true,
dp1_nominal(displayUnit="Pa") = 3000,
UA_nominal=m1_flow_nominal*4200*(T_a1_nominal - T_b1_nominal)/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
show_T=true,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial);
Modelica.Blocks.Sources.Constant const(k=0.8);
Buildings.Utilities.Psychrometrics.X_pTphi x_pTphi(use_p_in=false);
Modelica.Blocks.Sources.Constant const1(k=T_a2_nominal);
Buildings.Controls.Continuous.LimPID con(
Td=1,
reverseAction=true,
yMin=0,
controllerType=Modelica.Blocks.Types.SimpleController.PI,
k=0.1,
Ti=60)
"Controller";
Modelica.Blocks.Sources.Ramp TWat(
height=30,
offset=T_a1_nominal,
startTime=300,
duration=2000)
"Water temperature, raised to high value at t=3000 s";
equation
connect(hex.port_b1, res_1.port_a);
connect(val.port_b, hex.port_a1);
connect(sou_1.ports[1], val.port_a);
connect(sin_1.ports[1], res_1.port_b);
connect(sin_2.ports[1], res_2.port_b);
connect(sou_2.ports[1], hex.port_a2);
connect(temSen.port_b, res_2.port_a);
connect(x_pTphi.X, sou_2.X_in);
connect(const.y, x_pTphi.phi);
connect(const1.y, x_pTphi.T);
connect(const1.y, sou_2.T_in);
connect(TSet.y, con.u_s);
connect(temSen.T, con.u_m);
connect(TWat.y, sou_1.T_in);
connect(con.y, val.y);
connect(temSen.port_a, hex.port_b2);
end DryCoilCounterFlowPControl;
Model that demonstrates use of a finite volume model of a heat exchanger without condensation
Information
This model tests
Buildings.Fluid.HeatExchangers.DryCoilDiscretized
for different inlet conditions.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 60 + 273.15 | [K] |
| Temperature | T_b1_nominal | 40 + 273.15 | [K] |
| Temperature | T_a2_nominal | 5 + 273.15 | [K] |
| Temperature | T_b2_nominal | 20 + 273.15 | [K] |
| MassFlowRate | m1_flow_nominal | 5 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryCoilDiscretized
"Model that demonstrates use of a finite volume model of a heat exchanger without condensation"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water;
package Medium2 =
Buildings.Media.Air;
parameter Modelica.SIunits.Temperature T_a1_nominal = 60+273.15;
parameter Modelica.SIunits.Temperature T_b1_nominal = 40+273.15;
parameter Modelica.SIunits.Temperature T_a2_nominal = 5+273.15;
parameter Modelica.SIunits.Temperature T_b2_nominal = 20+273.15;
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal = 5
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal=
m1_flow_nominal*4200/1000*(T_a1_nominal-T_b1_nominal)/(T_b2_nominal-T_a2_nominal)
"Nominal mass flow rate medium 2";
Buildings.Fluid.HeatExchangers.DryCoilDiscretized hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
nPipPar=1,
nPipSeg=3,
nReg=2,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
UA_nominal=m1_flow_nominal*4200*(T_a1_nominal-T_b1_nominal)/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
dp2_nominal=200,
dp1_nominal=5000,
show_T=true,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial,
from_dp1=true,
from_dp2=true);
Sources.MassFlowSource_T sin_2(
redeclare package Medium = Medium2,
nPorts=1,
use_m_flow_in=true,
T=303.15);
Modelica.Blocks.Sources.Ramp PIn(
offset=101525,
height=-199,
duration=60,
startTime=120);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare package Medium = Medium2,
use_p_in=true,
use_T_in=true,
T=283.15,
nPorts=1);
Modelica.Blocks.Sources.Ramp TWat(
duration=60,
startTime=60,
height=5,
offset=273.15 + 60)
"Water temperature";
Modelica.Blocks.Sources.Constant TDb(k=273.15 + 5)
"Drybulb temperature";
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare package Medium = Medium1,
p=300000,
T=293.15,
use_p_in=true,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
p=300000 + 5000,
use_T_in=true,
T=293.15,
nPorts=1);
Modelica.Blocks.Sources.Ramp PSin_1(
startTime=240,
offset=300000,
height=4990,
duration=60);
Modelica.Blocks.Sources.Ramp m_flow_2(
duration=60,
startTime=120,
height=28 - 0.124,
offset=-28)
"Mass flow rate on air side";
equation
connect(PIn.y,sou_2. p_in);
connect(TDb.y, sou_2.T_in);
connect(TWat.y, sou_1.T_in);
connect(PSin_1.y, sin_1.p_in);
connect(sou_1.ports[1], hex.port_a1);
connect(sou_2.ports[1], hex.port_a2);
connect(sin_2.ports[1], hex.port_b2);
connect(hex.port_b1, sin_1.ports[1]);
connect(m_flow_2.y, sin_2.m_flow_in);
end DryCoilDiscretized;
Model that demonstrates use of a finite volume model of a heat exchanger without condensation and with feedback control
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.DryCoilDiscretized.
The valve on the water-side is regulated to track a setpoint temperature
for the air outlet.
Note that between the controller output and the valve is a model of a motor
that has hysteresis. The events generated by the motor model can lead to a
significantly higher computing time. In most applications, this level
of modeling detail is not justified.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 60 + 273.15 | [K] |
| Temperature | T_b1_nominal | 50 + 273.15 | [K] |
| Temperature | T_a2_nominal | 20 + 273.15 | [K] |
| Temperature | T_b2_nominal | 40 + 273.15 | [K] |
| MassFlowRate | m1_flow_nominal | 5 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryCoilDiscretizedPControl
"Model that demonstrates use of a finite volume model of a heat exchanger without condensation and with feedback control"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water "Medium model for water";
package Medium2 =
Buildings.Media.Air "Medium model for air";
parameter Modelica.SIunits.Temperature T_a1_nominal = 60+273.15;
parameter Modelica.SIunits.Temperature T_b1_nominal = 50+273.15;
parameter Modelica.SIunits.Temperature T_a2_nominal = 20+273.15;
parameter Modelica.SIunits.Temperature T_b2_nominal = 40+273.15;
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal = 5
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal=
m1_flow_nominal*4200/1000*(T_a1_nominal-T_b1_nominal)/(T_b2_nominal-T_a2_nominal)
"Nominal mass flow rate medium 2";
Sources.MassFlowSource_T sin_2(
redeclare
package Medium = Medium2,
nPorts=1,
m_flow=-10.5,
T=303.15);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare
package Medium = Medium2,
nPorts=1,
use_p_in=false,
use_T_in=false,
p(displayUnit="Pa") = 101625,
T=T_a2_nominal);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare
package Medium = Medium1,
p=300000,
T=293.15,
use_p_in=true,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
p=300000 + 9000,
nPorts=1,
use_T_in=false,
T=T_a1_nominal);
Modelica.Blocks.Sources.Ramp PSin_1(
duration=60,
height=5000,
startTime=240,
offset=300000);
Buildings.Fluid.Sensors.TemperatureTwoPort temSen(
redeclare package Medium =
Medium2, m_flow_nominal=m2_flow_nominal);
Buildings.Fluid.Actuators.Valves.TwoWayEqualPercentage val(
redeclare package Medium = Medium1,
l=0.005,
m_flow_nominal=m1_flow_nominal,
filteredOpening=false,
dpFixed_nominal=2000 + 3000,
dpValve_nominal=6000)
"Valve model";
Modelica.Blocks.Sources.TimeTable TSet(table=[0,298.15; 600,298.15; 600,
303.15; 1200,303.15; 1800,298.15; 2400,298.15; 2400,304.15])
"Setpoint temperature";
Buildings.Fluid.HeatExchangers.DryCoilDiscretized hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
show_T=true,
nPipPar=1,
nPipSeg=3,
nReg=4,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
UA_nominal=m1_flow_nominal*4200*(T_a1_nominal-T_b1_nominal)/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
dp1_nominal(displayUnit="Pa") = 0,
dp2_nominal(displayUnit="Pa") = 300,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial,
from_dp1=true,
from_dp2=true);
Buildings.Fluid.Actuators.Motors.IdealMotor mot(tOpe=60)
"Motor model";
Buildings.Controls.Continuous.LimPID con(
k=1,
Ti=60,
controllerType=Modelica.Blocks.Types.SimpleController.P,
Td=60)
"Controller";
equation
connect(PSin_1.y, sin_1.p_in);
connect(val.port_b, hex.port_a1);
connect(sou_1.ports[1], val.port_a);
connect(sou_2.ports[1], hex.port_a2);
connect(mot.y, val.y);
connect(hex.port_b2, temSen.port_a);
connect(TSet.y, con.u_s);
connect(temSen.T, con.u_m);
connect(con.y, mot.u);
connect(hex.port_b1, sin_1.ports[1]);
connect(temSen.port_b, sin_2.ports[1]);
end DryCoilDiscretizedPControl;
Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation
Information
This model tests
Buildings.Fluid.HeatExchangers.DryffectivenessNTU
for different inlet conditions.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| SpecificHeatCapacity | cp1 | Medium1.specificHeatCapacity... | Specific heat capacity of medium 2 [J/(kg.K)] |
| SpecificHeatCapacity | cp2 | Medium2.specificHeatCapacity... | Specific heat capacity of medium 2 [J/(kg.K)] |
| MassFlowRate | m1_flow | 5 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow | m1_flow*cp1/cp2 | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryEffectivenessNTU
"Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water;
package Medium2 =
Buildings.Media.Air;
parameter Modelica.SIunits.SpecificHeatCapacity cp1=
Medium1.specificHeatCapacityCp(
Medium1.setState_pTX(Medium1.p_default, Medium1.T_default, Medium1.X_default))
"Specific heat capacity of medium 2";
parameter Modelica.SIunits.SpecificHeatCapacity cp2=
Medium2.specificHeatCapacityCp(
Medium2.setState_pTX(Medium2.p_default, Medium2.T_default, Medium2.X_default))
"Specific heat capacity of medium 2";
parameter Modelica.SIunits.MassFlowRate m1_flow = 5
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow = m1_flow*cp1/
cp2
"Nominal mass flow rate medium 2";
Buildings.Fluid.Sources.Boundary_pT sin_2(
redeclare
package Medium = Medium2,
use_p_in=true,
nPorts=5,
T=273.15 + 10);
Modelica.Blocks.Sources.Ramp PIn(
height=200,
duration=60,
offset=101325,
startTime=100);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare
package Medium = Medium2, T=273.15 + 5,
use_p_in=true,
use_T_in=true,
nPorts=5);
Modelica.Blocks.Sources.Ramp TWat(
height=10,
duration=60,
offset=273.15 + 30,
startTime=60)
"Water temperature";
Modelica.Blocks.Sources.Constant TDb(k=293.15)
"Drybulb temperature";
Modelica.Blocks.Sources.Constant POut(k=101325);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare
package Medium = Medium1,
use_p_in=true,
nPorts=5,
p=300000,
T=273.15 + 25);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
p=300000 + 5000,
T=273.15 + 50,
use_T_in=true,
nPorts=5);
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hexPar(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
dp1_nominal=500,
dp2_nominal=10,
m1_flow_nominal=m1_flow,
m2_flow_nominal=m2_flow,
Q_flow_nominal=m2_flow*cp2*(24 - 20),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.ParallelFlow,
show_T=true,
T_a1_nominal=303.15,
T_a2_nominal=293.15);
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hexCou(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
dp1_nominal=500,
dp2_nominal=10,
m1_flow_nominal=m1_flow,
m2_flow_nominal=m2_flow,
Q_flow_nominal=m2_flow*cp2*(24 - 20),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CounterFlow,
show_T=true,
T_a1_nominal=303.15,
T_a2_nominal=293.15);
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hexCroC1Mix(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
dp1_nominal=500,
dp2_nominal=10,
m1_flow_nominal=m1_flow,
m2_flow_nominal=m2_flow,
Q_flow_nominal=m2_flow*cp2*(24 - 20),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CrossFlowStream1MixedStream2Unmixed,
show_T=true,
T_a1_nominal=303.15,
T_a2_nominal=293.15);
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hexCroC1Unm(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
dp1_nominal=500,
dp2_nominal=10,
m1_flow_nominal=m1_flow,
m2_flow_nominal=m2_flow,
Q_flow_nominal=m2_flow*cp2*(24 - 20),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CrossFlowStream1UnmixedStream2Mixed,
show_T=true,
T_a1_nominal=303.15,
T_a2_nominal=293.15);
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hexCroUnm(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
dp1_nominal=500,
dp2_nominal=10,
m1_flow_nominal=m1_flow,
m2_flow_nominal=m2_flow,
Q_flow_nominal=m2_flow*cp2*(24 - 20),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CrossFlowUnmixed,
show_T=true,
T_a1_nominal=303.15,
T_a2_nominal=293.15);
Modelica.Blocks.Sources.Trapezoid trapezoid(
amplitude=5000,
rising=10,
width=100,
falling=10,
period=3600,
offset=300000);
equation
connect(PIn.y,sou_2. p_in);
connect(TDb.y, sou_2.T_in);
connect(TWat.y, sou_1.T_in);
connect(sou_1.ports[1], hexPar.port_a1);
connect(hexPar.port_a2, sou_2.ports[1]);
connect(POut.y, sin_2.p_in);
connect(hexPar.port_b1, sin_1.ports[1]);
connect(sin_2.ports[1], hexPar.port_b2);
connect(hexCou.port_a1, sou_1.ports[2]);
connect(hexCroC1Mix.port_a1, sou_1.ports[3]);
connect(hexCroC1Unm.port_a1, sou_1.ports[4]);
connect(hexCou.port_b2, sin_2.ports[2]);
connect(hexCroC1Mix.port_b2, sin_2.ports[3]);
connect(hexCroC1Unm.port_b2, sin_2.ports[4]);
connect(hexCou.port_b1, sin_1.ports[2]);
connect(hexCroC1Mix.port_b1, sin_1.ports[3]);
connect(hexCroC1Unm.port_b1, sin_1.ports[4]);
connect(hexCou.port_a2, sou_2.ports[2]);
connect(hexCroC1Mix.port_a2, sou_2.ports[3]);
connect(hexCroC1Unm.port_a2, sou_2.ports[4]);
connect(hexCroUnm.port_a1, sou_1.ports[5]);
connect(hexCroUnm.port_b2, sin_2.ports[5]);
connect(hexCroUnm.port_b1, sin_1.ports[5]);
connect(hexCroUnm.port_a2, sou_2.ports[5]);
connect(trapezoid.y, sin_1.p_in);
end DryEffectivenessNTU;
Model of epsilon-NTU dry coil that tests variable mass flow rates
Information
This model tests
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU
for different mass flow rates.
Extends from Modelica.Icons.Example (Icon for runnable examples), Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow (Partial model of epsilon-NTU coil that tests variable mass flow rates).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | Nominal water inlet temperature [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | Nominal water outlet temperature [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | Nominal air inlet temperature [K] |
| Temperature | T_b2_nominal | 15 + 273.15 | Nominal air outlet temperature [K] |
| HeatFlowRate | Q_flow_nominal | m1_flow_nominal*4200*(T_a1_n... | Nominal heat transfer [W] |
| MassFlowRate | m1_flow_nominal | 0.1 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryEffectivenessNTUMassFlow
"Model of epsilon-NTU dry coil that tests variable mass flow rates"
extends Modelica.Icons.Example;
extends Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow
(
sou_1(nPorts=1),
sin_1(nPorts=1),
sou_2(nPorts=1),
sin_2(nPorts=1));
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
dp2_nominal(displayUnit="Pa") = 200,
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CounterFlow,
allowFlowReversal1=true,
allowFlowReversal2=true,
dp1_nominal(displayUnit="Pa") = 3000,
Q_flow_nominal=Q_flow_nominal,
T_a1_nominal=T_a1_nominal,
T_a2_nominal=T_a2_nominal,
show_T=true);
Buildings.Fluid.Sensors.RelativeHumidityTwoPort senRelHum(
redeclare package Medium
= Medium2, m_flow_nominal=m2_flow_nominal,
initType=Modelica.Blocks.Types.Init.InitialState);
equation
connect(sou_1.ports[1], hex.port_a1);
connect(hex.port_b1, sin_1.ports[1]);
connect(hex.port_a2, sou_2.ports[1]);
connect(senRelHum.port_a, hex.port_b2);
connect(senRelHum.port_b, sin_2.ports[1]);
end DryEffectivenessNTUMassFlow;
Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation with feedback control
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU.
The valve on the water-side is regulated to track a setpoint temperature
for the air outlet.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 60 + 273.15 | Temperature at nominal conditions as port a1 [K] |
| Temperature | T_b1_nominal | 50 + 273.15 | Temperature at nominal conditions as port b1 [K] |
| Temperature | T_a2_nominal | 20 + 273.15 | Temperature at nominal conditions as port a2 [K] |
| Temperature | T_b2_nominal | 40 + 273.15 | Temperature at nominal conditions as port b2 [K] |
| MassFlowRate | m1_flow_nominal | 5 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model DryEffectivenessNTUPControl
"Model that demonstrates use of a heat exchanger without condensation that uses the epsilon-NTU relation with feedback control"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water "Medium model for water";
package Medium2 =
Buildings.Media.Air "Medium model for air";
parameter Modelica.SIunits.Temperature T_a1_nominal = 60+273.15
"Temperature at nominal conditions as port a1";
parameter Modelica.SIunits.Temperature T_b1_nominal = 50+273.15
"Temperature at nominal conditions as port b1";
parameter Modelica.SIunits.Temperature T_a2_nominal = 20+273.15
"Temperature at nominal conditions as port a2";
parameter Modelica.SIunits.Temperature T_b2_nominal = 40+273.15
"Temperature at nominal conditions as port b2";
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal = 5
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal = m1_flow_nominal*4200/1000*(T_a1_nominal-T_b1_nominal)/(T_b2_nominal-T_a2_nominal)
"Nominal mass flow rate medium 2";
Buildings.Fluid.Sources.Boundary_pT sin_2(
redeclare
package Medium = Medium2,
use_p_in=false,
p(displayUnit="Pa") = 101325,
T=303.15,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare
package Medium = Medium2,
nPorts=1,
use_p_in=false,
use_T_in=false,
p(displayUnit="Pa") = 101625,
T=T_a2_nominal);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare
package Medium = Medium1,
use_p_in=false,
p=300000,
T=293.15,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
p=300000 + 9000,
nPorts=1,
use_T_in=false,
T=T_a1_nominal);
Buildings.Fluid.Sensors.TemperatureTwoPort temSen(
redeclare package Medium =
Medium2, m_flow_nominal=m2_flow_nominal);
Buildings.Fluid.Actuators.Valves.TwoWayEqualPercentage val(
redeclare package Medium = Medium1,
l=0.005,
m_flow_nominal=m1_flow_nominal,
dpFixed_nominal=2000 + 3000,
dpValve_nominal=6000)
"Valve model";
Buildings.Controls.Continuous.LimPID P(
controllerType=Modelica.Blocks.Types.SimpleController.PI,
Ti=30,
k=0.1,
Td=1);
Modelica.Blocks.Sources.Pulse TSet(
amplitude=5,
period=3600,
offset=273.15 + 22)
"Setpoint temperature";
Buildings.Fluid.HeatExchangers.DryEffectivenessNTU hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
show_T=true,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
Q_flow_nominal=m1_flow_nominal*4200*(T_a1_nominal-T_b1_nominal),
configuration=Buildings.Fluid.Types.HeatExchangerConfiguration.CounterFlow,
T_a1_nominal=T_a1_nominal,
T_a2_nominal=T_a2_nominal,
dp1_nominal(displayUnit="Pa") = 0,
dp2_nominal(displayUnit="Pa") = 200 + 100);
equation
connect(val.port_b, hex.port_a1);
connect(sou_1.ports[1], val.port_a);
connect(sou_2.ports[1], hex.port_a2);
connect(hex.port_b2, temSen.port_a);
connect(TSet.y, P.u_s);
connect(temSen.T, P.u_m);
connect(P.y, val.y);
connect(hex.port_b1, sin_1.ports[1]);
connect(temSen.port_b, sin_2.ports[1]);
end DryEffectivenessNTUPControl;
Example model for the heater with prescribed outlet temperature
Information
This example illustrates how to use the heater model that takes as an
input the leaving fluid temperature.
The model consist of an air volume with heat loss to the ambient.
The set point of the air temperature is different between night and day.
The heater tracks the set point temperature, except for the periods in
which the air temperature is above the set point.
See
Buildings.Fluid.HeatExchangers.Examples.Heater_u
for a model that takes the heating power as an input.
Extends from Modelica.Icons.Example (Icon for runnable examples), Buildings.Fluid.HeatExchangers.Examples.BaseClasses.Heater (Base class for example model for the heater and cooler).
Parameters
| Type | Name | Default | Description |
|---|
| Volume | VRoo | 6*6*2.7 | Room volume [m3] |
| MassFlowRate | m_flow_nominal | VRoo*1.2*6/3600 | Nominal mass flow rate [kg/s] |
| HeatFlowRate | Q_flow_nominal | 30*6*6 | Nominal heat loss of the room [W] |
Modelica definition
model Heater_T
"Example model for the heater with prescribed outlet temperature"
extends Modelica.Icons.Example;
extends Buildings.Fluid.HeatExchangers.Examples.BaseClasses.Heater;
Buildings.Fluid.HeatExchangers.HeaterCooler_T hea(
redeclare package Medium = Medium,
m_flow_nominal=m_flow_nominal,
dp_nominal=1000,
Q_flow_maxCool=0,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial,
Q_flow_maxHeat=Q_flow_nominal)
"Heater";
Controls.SetPoints.Table tab(table=[0,273.15 + 15; 1,273.15 + 30]);
equation
connect(fan.port_b, hea.port_a);
connect(hea.port_b, THeaOut.port_a);
connect(conPI.y, tab.u);
connect(tab.y, hea.TSet);
end Heater_T;
Example model for the heater with prescribed heat input
Information
This example illustrates how to use the heater model that takes as an
input the heat added to the medium.
The model consist of an air volume with heat loss to the ambient.
The set point of the air temperature is different between night and day.
The heater tracks the set point temperature, except for the periods in
which the air temperature is above the set point.
See
Buildings.Fluid.HeatExchangers.Examples.Heater_T
for a model that takes the leaving air temperature as an input.
Extends from Modelica.Icons.Example (Icon for runnable examples), Buildings.Fluid.HeatExchangers.Examples.BaseClasses.Heater (Base class for example model for the heater and cooler).
Parameters
| Type | Name | Default | Description |
|---|
| Volume | VRoo | 6*6*2.7 | Room volume [m3] |
| MassFlowRate | m_flow_nominal | VRoo*1.2*6/3600 | Nominal mass flow rate [kg/s] |
| HeatFlowRate | Q_flow_nominal | 30*6*6 | Nominal heat loss of the room [W] |
Modelica definition
model Heater_u
"Example model for the heater with prescribed heat input"
extends Modelica.Icons.Example;
extends Buildings.Fluid.HeatExchangers.Examples.BaseClasses.Heater;
HeaterCooler_u hea(
redeclare package Medium = Medium,
m_flow_nominal=m_flow_nominal,
dp_nominal=1000,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial,
Q_flow_nominal=Q_flow_nominal)
"Heater";
equation
connect(fan.port_b, hea.port_a);
connect(hea.port_b, THeaOut.port_a);
connect(conPI.y, hea.u);
end Heater_u;
Model of a cooling coil that tests variable mass flow rates
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.WetCoilCounterFlow
for different inlet conditions.
Extends from Modelica.Icons.Example (Icon for runnable examples), Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow (Partial model of epsilon-NTU coil that tests variable mass flow rates).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | Nominal water inlet temperature [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | Nominal water outlet temperature [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | Nominal air inlet temperature [K] |
| Temperature | T_b2_nominal | 15 + 273.15 | Nominal air outlet temperature [K] |
| HeatFlowRate | Q_flow_nominal | m1_flow_nominal*4200*(T_a1_n... | Nominal heat transfer [W] |
| MassFlowRate | m1_flow_nominal | 0.1 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model WetCoilCounterFlowMassFlow
"Model of a cooling coil that tests variable mass flow rates"
extends Modelica.Icons.Example;
extends Buildings.Fluid.HeatExchangers.Examples.BaseClasses.EffectivenessNTUMassFlow
(
sou_1(nPorts=1),
sin_1(nPorts=1),
sou_2(nPorts=1),
sin_2(nPorts=1));
WetCoilCounterFlow hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
dp2_nominal(displayUnit="Pa") = 200,
allowFlowReversal1=true,
allowFlowReversal2=true,
dp1_nominal(displayUnit="Pa") = 3000,
UA_nominal=Q_flow_nominal/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
show_T=true,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial);
Sensors.RelativeHumidityTwoPort senRelHum(
redeclare package Medium = Medium2,
m_flow_nominal=m2_flow_nominal);
equation
connect(sou_1.ports[1], hex.port_a1);
connect(hex.port_b1, sin_1.ports[1]);
connect(hex.port_a2, sou_2.ports[1]);
connect(hex.port_b2, senRelHum.port_a);
connect(senRelHum.port_b, sin_2.ports[1]);
end WetCoilCounterFlowMassFlow;
Model that demonstrates use of a heat exchanger with condensation and with feedback control
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.WetCoilCounterFlow.
The valve on the water-side is regulated to track a setpoint temperature
for the air outlet.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | [K] |
| Temperature | T_b2_nominal | 15 + 273.15 | [K] |
| MassFlowRate | m1_flow_nominal | 0.1 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model WetCoilCounterFlowPControl
"Model that demonstrates use of a heat exchanger with condensation and with feedback control"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water;
package Medium2 =
Buildings.Media.Air;
//package Medium2 = Buildings.Media.GasesPTDecoupled.MoistAir;
//package Medium2 = Buildings.Media.Air;
//package Medium2 = Buildings.Media.GasesConstantDensity.MoistAir;
parameter Modelica.SIunits.Temperature T_a1_nominal=5 + 273.15;
parameter Modelica.SIunits.Temperature T_b1_nominal=10 + 273.15;
parameter Modelica.SIunits.Temperature T_a2_nominal=30 + 273.15;
parameter Modelica.SIunits.Temperature T_b2_nominal=15 + 273.15;
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal=0.1
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal=m1_flow_nominal*4200/
1000*(T_a1_nominal - T_b1_nominal)/(T_b2_nominal - T_a2_nominal)
"Nominal mass flow rate medium 2";
Buildings.Fluid.Sources.Boundary_pT sin_2(
redeclare package Medium = Medium2,
nPorts=1,
use_p_in=false,
p(displayUnit="Pa") = 101325,
T=303.15);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare package Medium = Medium2,
nPorts=1,
T=T_a2_nominal,
X={0.02,1 - 0.02},
use_T_in=true,
use_X_in=true,
p(displayUnit="Pa") = 101325 + 300);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare package Medium = Medium1,
nPorts=1,
use_p_in=false,
p=300000,
T=293.15);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
nPorts=1,
use_T_in=true,
p=300000 + 12000);
Fluid.FixedResistances.FixedResistanceDpM res_2(
from_dp=true,
redeclare package Medium = Medium2,
dp_nominal=100,
m_flow_nominal=m2_flow_nominal);
Fluid.FixedResistances.FixedResistanceDpM res_1(
from_dp=true,
redeclare package Medium = Medium1,
dp_nominal=3000,
m_flow_nominal=m1_flow_nominal);
Buildings.Fluid.Sensors.TemperatureTwoPort temSen(
redeclare package Medium =
Medium2, m_flow_nominal=m2_flow_nominal);
Buildings.Fluid.Actuators.Valves.TwoWayEqualPercentage val(
redeclare package Medium = Medium1,
m_flow_nominal=m1_flow_nominal,
dpValve_nominal=6000)
"Valve model";
Modelica.Blocks.Sources.TimeTable TSet(table=[0,288.15; 600,288.15; 600,
298.15; 1200,298.15; 1800,283.15; 2400,283.15; 2400,288.15])
"Setpoint temperature";
Buildings.Fluid.HeatExchangers.WetCoilCounterFlow hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
dp2_nominal(displayUnit="Pa") = 200,
allowFlowReversal1=true,
allowFlowReversal2=true,
dp1_nominal(displayUnit="Pa") = 3000,
UA_nominal=2*m1_flow_nominal*4200*(T_a1_nominal - T_b1_nominal)/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
show_T=true,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial);
Modelica.Blocks.Sources.Constant const(k=0.8);
Buildings.Utilities.Psychrometrics.X_pTphi x_pTphi(use_p_in=false);
Modelica.Blocks.Sources.Constant const1(k=T_a2_nominal);
Buildings.Controls.Continuous.LimPID con(
Td=1,
reverseAction=true,
yMin=0,
controllerType=Modelica.Blocks.Types.SimpleController.PI,
k=0.1,
Ti=60)
"Controller";
Modelica.Blocks.Sources.Ramp TWat(
height=30,
offset=T_a1_nominal,
startTime=300,
duration=2000)
"Water temperature, raised to high value at t=3000 s";
equation
connect(hex.port_b1, res_1.port_a);
connect(val.port_b, hex.port_a1);
connect(sou_1.ports[1], val.port_a);
connect(sin_1.ports[1], res_1.port_b);
connect(sin_2.ports[1], res_2.port_b);
connect(sou_2.ports[1], hex.port_a2);
connect(hex.port_b2, temSen.port_a);
connect(temSen.port_b, res_2.port_a);
connect(x_pTphi.X, sou_2.X_in);
connect(const.y, x_pTphi.phi);
connect(const1.y, x_pTphi.T);
connect(const1.y, sou_2.T_in);
connect(TSet.y, con.u_s);
connect(temSen.T, con.u_m);
connect(TWat.y, sou_1.T_in);
connect(con.y, val.y);
end WetCoilCounterFlowPControl;
Model that demonstrates use of a finite volume model of a heat exchanger with condensation and feedback control
Information
This model demonstrates the use of
Buildings.Fluid.HeatExchangers.DryCoilDiscretized.
The valve on the water-side is regulated to track a setpoint temperature
for the air outlet.
Note that between the controller output and the valve is a model of a motor
that has hysteresis. The events generated by the motor model can lead to a
significantly higher computing time. In most applications, this level
of modeling detail is not justified.
Extends from Modelica.Icons.Example (Icon for runnable examples).
Parameters
| Type | Name | Default | Description |
|---|
| Temperature | T_a1_nominal | 5 + 273.15 | [K] |
| Temperature | T_b1_nominal | 10 + 273.15 | [K] |
| Temperature | T_a2_nominal | 30 + 273.15 | [K] |
| Temperature | T_b2_nominal | 10 + 273.15 | [K] |
| MassFlowRate | m1_flow_nominal | 5 | Nominal mass flow rate medium 1 [kg/s] |
| MassFlowRate | m2_flow_nominal | m1_flow_nominal*4200/1000*(T... | Nominal mass flow rate medium 2 [kg/s] |
Modelica definition
model WetCoilDiscretizedPControl
"Model that demonstrates use of a finite volume model of a heat exchanger with condensation and feedback control"
extends Modelica.Icons.Example;
package Medium1 =
Buildings.Media.Water;
package Medium2 =
Buildings.Media.Air;
parameter Modelica.SIunits.Temperature T_a1_nominal = 5+273.15;
parameter Modelica.SIunits.Temperature T_b1_nominal = 10+273.15;
parameter Modelica.SIunits.Temperature T_a2_nominal = 30+273.15;
parameter Modelica.SIunits.Temperature T_b2_nominal = 10+273.15;
parameter Modelica.SIunits.MassFlowRate m1_flow_nominal = 5
"Nominal mass flow rate medium 1";
parameter Modelica.SIunits.MassFlowRate m2_flow_nominal = m1_flow_nominal*4200/1000*(T_a1_nominal-T_b1_nominal)/(T_b2_nominal-T_a2_nominal)
"Nominal mass flow rate medium 2";
Buildings.Fluid.Sources.Boundary_pT sin_2(
redeclare package Medium = Medium2,
use_p_in=false,
p=101325,
T=303.15,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_2(
redeclare package Medium = Medium2,
nPorts=1,
use_p_in=false,
use_T_in=true,
p(displayUnit="Pa") = 101525,
T=293.15);
Buildings.Fluid.Sources.Boundary_pT sin_1(
redeclare package Medium = Medium1,
p=300000,
T=293.15,
use_p_in=true,
nPorts=1);
Buildings.Fluid.Sources.Boundary_pT sou_1(
redeclare package Medium = Medium1,
nPorts=1,
use_T_in=true,
p=300000 + 7000,
T=278.15);
Modelica.Blocks.Sources.Ramp PSin(
duration=60,
height=5000,
startTime=240,
offset=300000);
Buildings.Fluid.Sensors.TemperatureTwoPort temSen(
redeclare package Medium = Medium2,
m_flow_nominal=m2_flow_nominal);
Buildings.Fluid.Actuators.Valves.TwoWayLinear val(
redeclare package Medium = Medium1,
m_flow_nominal=m1_flow_nominal,
filteredOpening=false,
dpFixed_nominal=2000,
dpValve_nominal=5000);
Modelica.Blocks.Sources.TimeTable TSet(table=[0,293.15; 600,293.15; 600,
288.15; 1200,288.15; 1800,288.15; 2400,295.15; 2400,295.15])
"Setpoint temperature";
Buildings.Fluid.HeatExchangers.WetCoilDiscretized hex(
redeclare package Medium1 = Medium1,
redeclare package Medium2 = Medium2,
show_T=true,
nPipPar=1,
nPipSeg=3,
nReg=4,
m1_flow_nominal=m1_flow_nominal,
m2_flow_nominal=m2_flow_nominal,
UA_nominal=m1_flow_nominal*4200*(T_a1_nominal-T_b1_nominal)/
Buildings.Fluid.HeatExchangers.BaseClasses.lmtd(
T_a1_nominal,
T_b1_nominal,
T_a2_nominal,
T_b2_nominal),
dp2_nominal(displayUnit="Pa") = 200,
dp1_nominal(displayUnit="Pa") = 0,
energyDynamics=Modelica.Fluid.Types.Dynamics.FixedInitial);
Modelica.Blocks.Sources.Step TSou_2(
startTime=3000,
offset=T_a2_nominal,
height=-3);
Modelica.Blocks.Sources.Step TSou_1(
startTime=3000,
height=10,
offset=T_a1_nominal);
Buildings.Controls.Continuous.LimPID con(
k=1,
Ti=60,
controllerType=Modelica.Blocks.Types.SimpleController.P,
Td=60,
reverseAction=true)
"Controller";
Buildings.Fluid.Actuators.Motors.IdealMotor mot(tOpe=60)
"Motor model";
equation
connect(PSin.y, sin_1.p_in);
connect(sou_2.ports[1], hex.port_a2);
connect(hex.port_b2, temSen.port_a);
connect(val.port_b, hex.port_a1);
connect(sou_1.ports[1], val.port_a);
connect(TSou_2.y, sou_2.T_in);
connect(TSou_1.y, sou_1.T_in);
connect(TSet.y, con.u_s);
connect(temSen.T, con.u_m);
connect(con.y, mot.u);
connect(mot.y, val.y);
connect(sin_2.ports[1], temSen.port_b);
connect(hex.port_b1, sin_1.ports[1]);
end WetCoilDiscretizedPControl;
Automatically generated Mon May 4 10:21:45 2015.
Buildings.Fluid.HeatExchangers.Examples.DryCoilCounterFlowMassFlow