Method for controlling operation of a vapour compression system in a subcritical and a supercritical mode
A method for controlling operation of a vapor compression system ( 1 ), and a vapor compression system ( 1 ) are disclosed. The vapor compression system ( 1 ) comprises a compressor ( 2 ), a heat rejecting heat exchanger ( 3 ), a controllable valve ( 4 ), a receiver ( 5 ), at least one expansion device and at least one evaporator arranged along a refrigerant path having refrigerant flowing therein. The vapor compression system ( 1 ) is capable of being operated in a subcritical control regime as well as in a supercritical control regime. The method comprises the steps of measuring a temperature, T GC , of refrigerant leaving the heat rejecting heat exchanger; calculating a pressure reference, P GC, Ref , based on the measured temperature, T GC , and using a calculation formula being applicable to the subcritical control regime as well as to the supercritical control regime; and controlling an opening degree of the controllable valve in order to obtain a pressure of refrigerant leaving the heat rejecting heat exchanger which is equal to the calculated pressure reference, P GC, Ref . Since the calculation formula is applicable to the subcritical control regime as well as to the supercritical control regime, only one calculation formula is necessary, and the vapor compression system ( 1 ) can thereby be controlled in a very easy manner.
1. A method for controlling operation of a vapour compression system, the vapour compression system comprising a compressor, a heat rejecting heat exchanger, a controllable valve, a receiver, at least one expansion device and at least one evaporator arranged along a refrigerant path having refrigerant flowing therein, the vapour compression system being capable of being operated in a subcritical control regime as well as in a supercritical control regime, the method comprising the steps of:
measuring a temperature, T GC , of refrigerant leaving the heat rejecting heat exchanger,
calculating a pressure reference, P GC, Ref , based on the measured temperature, T GC , and using a calculation formula being applicable to the subcritical control regime as well as to the supercritical control regime, and
controlling an opening degree of the controllable valve and obtaining a pressure of refrigerant leaving the heat rejecting heat exchanger which is equal to the calculated pressure reference, P GC, Ref ,
wherein the step of calculating is performed using the calculation formula:
wherein P sat represents a saturation pressure in the subcritical control regime, extrapolated into the supercritical control regime, ΔT is a desired subcooling of refrigerant leaving the heat rejecting heat exchanger in the subcritical control regime, T* is a transition temperature indicating a transition between a subcritical control regime and a supercritical control regime, and α and β are constants.
2. The method according to claim 1 , further comprising the step of measuring a pressure, P GC , of refrigerant leaving the heat rejecting heat exchanger, and wherein the step of controlling an opening degree of the controllable valve comprises comparing the measured pressure, P GC , to the calculated pressure reference, P GC,Ref .
3. The method according to claim 1 , wherein the step of calculating further comprises the step of deriving the transition temperature, T*, on the basis of a preselected transition pressure, P*, and said desired sub-cooling value, ΔT.
4. A control system for controlling operation of a vapour compression system, the control system being capable of performing the method steps of the method according to claim 1 .
5. A vapour compression system comprising a compressor, a heat rejecting heat exchanger, a controllable valve , a receiver, at least one expansion device and at least one evaporator arranged along a refrigerant path having refrigerant flowing therein, the vapour compression system further comprising a control system according to claim 4 .
6. The vapour compression system according to claim 5 , wherein the heat rejecting heat exchanger is arranged to operate as a condenser when the vapour compression system is operated in a subcritical control regime, and the heat rejecting heat exchanger is arranged to operate as a gas cooler when the vapour compression system is operated in a supercritical control regime.
7. The vapour compression system according to claim 5 , wherein the controllable valve is an expansion valve.
8. The vapour compression system according to claim 5 , wherein the vapour compression system is a refrigeration system.
9. The vapour compression system according to claim 5 , wherein the refrigerant flowing in the refrigerant path is CO 2 .
10. A control system for controlling operation of a vapour compression system, the control system being capable of performing the method steps of the method according to claim 2 .
11. A control system for controlling operation of a vapour compression system, the control system being capable of performing the method steps of the method according to claim 1 .
12. A control system for controlling operation of a vapour compression system, the control system being capable of performing the method steps of the method according to claim 3 .
13. The vapour compression system according to claim 6 , wherein the controllable valve is an expansion valve.
14. The vapour compression system according to claim 6 , wherein the vapour compression system is a refrigeration system.
15. The vapour compression system according to claim 7 , wherein the vapour compression system is a refrigeration system.
16. The vapour compression system according to claim 6 , wherein the refrigerant flowing in the refrigerant path is CO 2 .
17. The vapour compression system according to claim 7 , wherein the refrigerant flowing in the refrigerant path is CO 2 .
18. The vapour compression system according to claim 8 , wherein the refrigerant flowing in the refrigerant path is CO 2 .