Method for operating a vapour compression system with heat recovery

Patent metadata

Field	Value
Publication number	US-10928107-B2
Application number	US-201615577916-A
Country	US
Kind code	B2
Filing date	May 25, 2016
Priority date	Jun 8, 2015
Publication date	Feb 23, 2021
Grant date	Feb 23, 2021

Abstract

A method for operating a vapour compression system ( 1 ) comprising a heat recovery heat exchanger ( 4 ) is disclosed. The heat recovery system requests a required level of recovered heat to be provided by the heat recovery heat exchanger ( 4 ) to the heat recovery system, generates a signal indicating the required level of recovered heat, and supplies the generated signal to a control unit of the vapour compression system ( 1 ). A setpoint value for at least one control parameter of the vapour compression system ( 1 ) is calculated, based on the generated signal, and the vapour compression system ( 1 ) is operated in accordance with the calculated setpoint value(s).

First claim

What is claimed is:

1. A method for operating a vapour compression system, the vapour compression system comprising a compressor unit comprising one or more compressors, a heat recovery heat exchanger, a heat rejecting heat exchanger, an expansion device and an evaporator arranged along a refrigerant path, the heat recovery heat exchanger being arranged to recover heat from refrigerant flowing in the refrigerant path and to provide the recovered heat to a heat recovery system, the method comprising the steps of:
the heat recovery system requesting a required level of recovered heat to be provided by the heat recovery heat exchanger to the heat recovery system, generating a signal indicating the required level of recovered heat, and supplying the generated signal to a control unit of the vapour compression system,
calculating a setpoint value for at least one control parameter of the vapour compression system, based on the generated signal, and
operating the vapour compression system in accordance with the calculated setpoint value(s),
wherein the required level of recovered heat includes a value indicating an amount of heat.

2. The method according to claim 1 , wherein one of the control parameter(s) is a pressure prevailing inside the heat rejecting heat exchanger, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the pressure prevailing inside the heat rejecting heat exchanger to reach a pressure which is equal to the calculated setpoint value for the pressure prevailing inside the heat rejecting heat exchanger.

3. The method according to claim 2 , wherein one of the control parameter(s) is a temperature of refrigerant leaving the heat rejecting heat exchanger, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the temperature of refrigerant leaving the heat rejecting heat exchanger to reach a temperature which is equal to the calculated setpoint value for the temperature of refrigerant leaving the heat rejecting heat exchanger.

4. The method according to claim 2 , wherein one of the control parameter(s) is a superheat of refrigerant entering the compressor unit, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the superheat of refrigerant entering the compressor unit to reach a superheat value which is equal to the calculated setpoint value for the superheat of refrigerant entering the compressor unit.

5. The method according to claim 2 , wherein the step of the heat recovery system requesting the required level of recovered heat comprises generating a signal indicating a fraction of a maximum available recoverable heat under maximum refrigeration load conditions, corresponding to the required level of recovered heat.

6. The method according to claim 2 , wherein the step of calculating the setpoint value comprises establishing a model of a part of the vapour compression system which is related to the at least one control parameter, and calculating the setpoint value using the established model, and wherein the model reflects a relationship between the at least one control parameter and a level of recovered heat.

7. The method according to claim 1 , wherein one of the control parameter(s) is a temperature of refrigerant leaving the heat rejecting heat exchanger, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the temperature of refrigerant leaving the heat rejecting heat exchanger to reach a temperature which is equal to the calculated setpoint value for the temperature of refrigerant leaving the heat rejecting heat exchanger.

8. The method according to claim 7 , wherein one of the control parameter(s) is a superheat of refrigerant entering the compressor unit, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the superheat of refrigerant entering the compressor unit to reach a superheat value which is equal to the calculated setpoint value for the superheat of refrigerant entering the compressor unit.

9. The method according to claim 7 , wherein the step of the heat recovery system requesting a required level of recovered heat comprises generating a signal indicating a fraction of a maximum available recoverable heat under maximum refrigeration load conditions, corresponding to the required level of recovered heat.

10. The method according to claim 7 , wherein the step of calculating the setpoint value comprises establishing a model of a part of the vapour compression system which is related to the control parameter(s), and calculating the setpoint value using the established model.

11. The method according to claim 1 , wherein one of the control parameter(s) is a superheat of refrigerant entering the compressor unit, and wherein the step of operating the vapour compression system comprises operating the vapour compression system in order to adjust the superheat of refrigerant entering the compressor unit to reach a superheat value which is equal to the calculated setpoint value for the superheat of refrigerant entering the compressor unit.

12. The method according to claim 11 , wherein the step of the heat recovery system requesting a required level of recovered heat comprises generating a signal indicating a fraction of a maximum available recoverable heat under maximum refrigeration load conditions, corresponding to the required level of recovered heat.

13. The method according to claim 11 , wherein the step of calculating the setpoint value comprises establishing a model of a part of the vapour compression system which is related to the control parameter(s), and calculating the setpoint value using the established model.

14. The method according to claim 1 , wherein the step of the heat recovery system requesting the required level of recovered heat comprises generating a signal indicating a fraction of a maximum available recoverable heat under maximum refrigeration load conditions, corresponding to the required level of recovered heat.

15. The method according to claim 1 , wherein the step of calculating the setpoint value comprises establishing a model of a part of the vapour compression system which is related to the at least one control parameter, and calculating the setpoint value using the established model, and wherein the model reflects a relationship between the at least one control parameter and a level of recovered heat.

16. The method according to claim 1 , wherein the step of calculating the setpoint value comprises the steps of:
calculating a mass flow rate through the compressor unit,
calculating an enthalpy per unit mass required in order to provide the requested level of recovered heat, at the calculated mass flow rate through the compressor unit, and calculating the setpoint value for at least one control parameter which provides the calculated enthalpy per unit mass.

17. The method according to claim 1 , the vapour compression system further comprising a receiver having an inlet connected to an outlet of the heat rejecting heat exchanger, a gaseous outlet and a liquid outlet, and wherein the compressor unit comprises one or more compressors having an inlet connected to an outlet of the evaporator and one or more compressors having an inlet connected to the gaseous outlet of the receiver, the gaseous outlet of the receiver further being connectable to a par

Assignees

• Danfoss As

Inventors

• Schmidt Frede
• Fredslund Kristian
• Prins Jan

Classifications

• Y02B30/52

  Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency · CPC title

• F25B2400/13

  Economisers · CPC title

• F25B49/022

  Compressor control arrangements · CPC title

• F25B1/00 Primary

  Compression machines, plants or systems with non-reversible cycle (F25B3/00, F25B5/00, F25B6/00, F25B7/00, F25B9/00 take precedence) · CPC title

• F25B2400/23

  Separators · CPC title