CO2 refrigeration system with supercritical subcooling control

1. A refrigeration system comprising:

a gas cooler/condenser configured to remove heat from a refrigerant and discharge the refrigerant into a high pressure conduit;

a temperature sensor located along the high pressure conduit and configured to measure a temperature of the refrigerant leaving the gas cooler/condenser;

a pressure sensor located along the high pressure conduit and configured to measure a pressure of the refrigerant leaving the gas cooler/condenser;

a pressure control valve located along the high pressure conduit and operable to regulate the pressure of the refrigerant leaving the gas cooler/condenser; and

a controller configured to determine whether the refrigerant leaving the gas cooler/condenser is in a subcritical region based on at least one of the measured temperature of the refrigerant or the measured pressure of the refrigerant and, in response to determining that the refrigerant leaving the gas cooler/condenser is not in the subcritical region:

add a pseudo-subcooling temperature value to the measured temperature of the refrigerant to calculate a summed temperature;

calculate a supercritical pseudo-saturated pressure as a function of the summed temperature; and

operate the pressure control valve to drive the pressure of the refrigerant leaving the gas cooler/condenser to the supercritical pseudo-saturated pressure corresponding to the summed temperature.

2. The refrigeration system of claim 1 , wherein the controller is configured to:

generate a supercritical pseudo-saturation function for the refrigerant using supercritical pressure (P), enthalpy (H), and temperature (T) data for the refrigerant; and

calculate the supercritical pseudo-saturated pressure using the supercritical pseudo-saturation function.

3. The refrigeration system of claim 2 , wherein the controller is configured to generate the supercritical pseudo-saturation function by:

identifying inflection points of supercritical P-H isotherms for the refrigerant using the supercritical P-H-T data for the refrigerant; and

deriving the supercritical pseudo-saturation function from the inflection points of the supercritical isotherms.

4. The refrigeration system of claim 3 , wherein deriving the supercritical pseudo-saturation function from the inflection points of the supercritical isotherms comprises fitting a supercritical pseudo-saturated line to the inflection points of the supercritical isotherms.

5. The refrigeration system of claim 1 , wherein:

the pseudo-subcooling temperature value is a dynamic value; and

the controller is configured to calculate the dynamic pseudo-subcooling temperature value as a function of the measured temperature of the refrigerant leaving the gas cooler/condenser.

6. The refrigeration system of claim 1 , wherein:

the pseudo-subcooling temperature value is one of a plurality of pseudo-subcooling temperature values, each of which applies to a corresponding temperature of the refrigerant leaving the gas cooler/condenser; and

default values of the plurality of pseudo-subcooling temperature values are adjustable by a user to control the pressure of the refrigerant leaving the gas cooler/condenser to higher or lower pressures at any measured temperature of the refrigerant leaving the gas cooler/condenser.

7. The refrigeration system of claim 1 , wherein the controller is configured to, in response to determining that the refrigerant leaving the gas cooler/condenser is in the subcritical region:

add a fixed temperature value to the measured temperature of the refrigerant to calculate a second summed temperature;

calculate a subcritical saturated pressure as a function of the second summed temperature; and

operate the pressure control valve to drive the pressure of the refrigerant leaving the gas cooler/condenser to the subcritical saturated pressure corresponding to the second summed temperature.