I think the problem is the relationship among the three loops:
- - Chilled water loop
- - Hot water loop
- -- Aquifer loop
In all those loops the CentralHeatPumpSystem is present.
In the aquifer loop Iâ??m using PlantComponent:TemperatureSource (constant and equal to 13°C)
Iâ??ve found no example file where both PlantComponent:TemperatureSource and CentralHeatPumpSystem are present.
Some doubts:
-1. - For the aquifer loop is PlantLoop or the CondenserLoop object the best solution?
2. - Which kind of setpoint manager (scheduled?) shall be used? With which value (the same temperature of the temperaturesource, i.e. 13°C?)?
-3. - Which kind of Plant Equipment Operation scheme shall be used? PlantEquipmentOperation:Uncontrolled?
4. - Other input data to which I should pay attention?
Now I have replaced the PlantLoop with the CondenserLoop and the system works also in chiller mode, but only in winter... When I used the PlantLoop it was never working in chiller mode.
Here some parts of the model now:
CentralHeatPumpSystem,
ChillerBank, !- Name
SmartMixing, !- Control Method
Raffreddamento Pompa di Calore CHW Inlet Node, !- Cooling Loop Inlet Node Name
Raffreddamento Pompa di Calore CHW Outlet Node, !- Cooling Loop Outlet Node Name
Pompa di Calore Condenser Inlet Node, !- Source Loop Inlet Node Name
Pompa di Calore Condenser Outlet Node, !- Source Loop Outlet Node Name
Riscaldamento Pompa di Calore HW Inlet Node, !- Heating Loop Inlet Node Name
Riscaldamento Pompa di Calore HW Outlet Node, !- Heating Loop Outlet Node Name
460, !- Ancillary Power {W}
, !- Ancillary Operation Schedule Name
ChillerHeaterPerformance:Electric:EIR, !- Chiller Heater Modules Performance Component Object Type 1
ChillerHeaterModule 1, !- Chiller Heater Modules Performance Component Name 1
ON, !- Chiller Heater Modules Control Schedule Name 1
4; !- Number of Chiller Heater Modules 1
PlantLoop,
aquifer loop, !- Name
Water, !- Fluid Type
, !- User Defined Fluid Type
Circuito di Condensazione Funzionamento, !- Plant Equipment Operation Scheme Name
Circuito di Condensazione Supply Side Outlet, !- Loop Temperature Setpoint Node Name
50, !- Maximum Loop Temperature {C}
5, !- Minimum Loop Temperature {C}
autosize, !- Maximum Loop Flow Rate {m3/s}
0.001, !- Minimum Loop Flow Rate {m3/s}
autocalculate, !- Plant Loop Volume {m3}
Circuito di Condensazione Supply Side Inlet, !- Plant Side Inlet Node Name
Circuito di Condensazione Supply Side Outlet, !- Plant Side Outlet Node Name
Circuito di Condensazione Rami del lato di Alimentazione, !- Plant Side Branch List Name
Circuito di Condensazione Connessioni del lato di Alimentazione, !- Plant Side Connector List Name
Circuito di Condensazione Demand Side Inlet, !- Demand Side Inlet Node Name
Circuito di Condensazione Demand Side Outlet, !- Demand Side Outlet Node Name
Circuito di Condensazione Rami del Lato della Domanda, !- Demand Side Branch List Name
Circuito di Condensazione Connessioni del Lato della Domanda, !- Demand Side Connector List Name
Optimal, !- Load Distribution Scheme
Circuito di Condensazione Lista dei Manager di Disponibilitଠ!- Availability Manager List Name
, !- Plant Loop Demand Calculation Scheme
None, !- Common Pipe Simulation
None; !- Pressure Simulation Type
PlantEquipmentOperationSchemes,
Circuito di Condensazione Funzionamento, !- Name
PlantEquipmentOperation:Uncontrolled, !- Control Scheme 1 Object Type
Circuito di Condensazione Scheme 1, !- Control Scheme 1 Name
On 24/7; !- Control Scheme 1 Schedule Name
PlantEquipmentOperation:Uncontrolled,
Circuito di Condensazione Scheme 1, !- Name
Circuito di Condensazione Scheme 1 Equipment List; !- Equipment List Name
PlantEquipmentList,
Circuito di Condensazione Scheme 1 Equipment List, !- Name
PlantComponent:TemperatureSource, !- Equipment 1 Object Type
FluidSource; !- Equipment 1 Name
NodeList,
Circuito di Condensazione Setpoint Manager Node List, !- Name
Circuito di Condensazione Supply Side Outlet; !- Node 1 Name
SetpointManager:Scheduled,
Circuito di Condensazione Setpoint Manager, !- Name
Temperature, !- Control Variable
15C, !- Schedule Name
Circuito di Condensazione Setpoint Manager Node List; !- Setpoint Node or NodeList Name
PlantComponent:TemperatureSource,
FluidSource, !- Name
Scambiatore di Calore Geotermico Water Inlet Node, !- Inlet Node
Scambiatore di Calore Geotermico Water Outlet Node, !- Outlet Node
0.0045, !- Design Volume Flow Rate {m3/s}
Constant, !- Temperature Specification Type
13; !- Source Temperature {C}
A strange result (actually, I get many strange results): as you can see in the attached images, in the results the â??Chiller Heater System Source Mass Flow Rateâ?? is different from the water flow rate through the condenser (the second one is constantly equal to 0!). I thought they were the same.
Thanks
Best Regards
Francesco
On Mon, Jul 3, 2017 at 8:46 AM, fpasserini.tn@... [EnergyPlus_Support] <EnergyPlus_Support@xxxxxxxxxxxxxxx> wrote:Hello, JimThe source/condenser temperature is constant because the PlantComponent: TemperatureSource object is used.The calculated output is constant. I have recalculate the output in excel, considering the parameters used for the curve, and the polynomial formula is calculated by EnergyPlus properly.â??"Properly" should mean that E+ is using the â??actual chilled water temp and actual condenser water temp. Is that the case?The strange issue is that the leaving chilled water temperature used in the calculation is not taken from the dynamic simulation but it is the â??Reference Cooling Mode Leaving Chilled Water Temperatureâ??.â?? Is the setpoint manager value different than the "reference" temperature?â??I have plotted the â??Cooling Mode Electric Input to Cooling Output Ratio Function of Temperatureâ?? (CHILLERHEATERCLGEIRFT) too and Iâ??m attaching it now. As for that curve, the temperature 6°C, which is the setpoint manager temperature, is considered as leaving chilled water temperature!?As you can see in the second picture, the chiller-heater is working in cooling mode only one hour. Therefore the setpoint manager temperature is not met.â?? You'll need to determine why the chiller does not operate for more than one hour. That may â??be part of the reason for the curve output problem.Best Regards--James V Dirkes II, CEO / President
The Building Performance Team Inc.
1631 Acacia Dr, GR, MI 49504