This is model of a heat pump whose coefficient of performance COP changes with temperatures in the same way as the Carnot efficiency changes. The input signal y is the control signal for the compressor.
The model allows to either specify the Carnot effectivness ηCarnot,0, or a COP0 at the nominal conditions, together with the evaporator temperature Teva,0 and the condenser temperature Tcon,0, in which case the model computes the Carnot effectivness as
ηCarnot,0 = COP0 ⁄ (Tcon,0 ⁄ (Tcon,0-Teva,0)).
The heat pump COP is computed as the product
COP = ηCarnot,0 COPCarnot ηPL,
where COPCarnot is the Carnot efficiency and ηPL is a polynomial in the heating part load ratio yPL that can be used to take into account a change in COP at part load conditions. This polynomial has the form
ηPL = a1 + a2 yPL + a3 yPL2 + ...
where the coefficients ai are declared by the parameter a
.
On the Dynamics
tag, the model can be parametrized to compute a transient
or steady-state response.
The transient response of the model is computed using a first
order differential equation for the evaporator and condenser fluid volumes.
The heat pump outlet temperatures are equal to the temperatures of these lumped volumes.
When using this component, make sure that the evaporator and the condenser have sufficient mass flow rate. Based on the mass flow rates, the compressor power, temperature difference and the efficiencies, the model computes how much heat will be added to the condenser and removed at the evaporator. If the mass flow rates are too small, very high temperature differences can result.
The condenser heat flow rate QCon_flow_nominal
is used to assign
the default value for the mass flow rates, which are used for the pressure drop
calculations.
It is also used to compute the part load efficiency.
Hence, make sure that QCon_flow_nominal
is set to a reasonable value.
The maximum heating capacity is set by the parameter QCon_flow_max
,
which is by default set to infinity.
The coefficient of performance depends on the evaporator and condenser leaving temperature since otherwise the second law of thermodynamics may be violated.
For a similar model that can be used as a chiller, see IBPSA.Fluid.Chillers.Carnot_y.
effInpEva
and effInpCon
and updated documentation.
This is for
issue 497.
staA1
, staB1
, staA2
and staB2
as the
efficiency of the Carnot machine should only be computed in the design flow direction.staB1
and staB2
which mistakenly used the inStream
operator
for the configuration without flow reversal.
This is for
issue 476.
dTEva_nominal
to be consistent with
other models.
The model will still work with the old values for dTEva_nominal
,
but it will write a warning so that users can transition their models.
assert
statement for the efficiency curve.
This is for
issue 468.
prescribedHeatFlowRate=true
for vol2
.
sta_a1
,
sta_a2
, sta_b1
and sta_b2
.
P
as an output signal.