Method for controlling a vapour compression system in ejector mode for a prolonged time

Patent metadata

Field	Value
Publication number	US-10775086-B2
Application number	US-201615763918-A
Country	US
Kind code	B2
Filing date	Oct 14, 2016
Priority date	Oct 20, 2015
Publication date	Sep 15, 2020
Grant date	Sep 15, 2020

Abstract

A method for controlling a vapour compression system having an ejector includes, in the case that a pressure difference between a pressure prevailing in the receiver and a pressure of refrigerant leaving the evaporator decreases below a first lower threshold value, the pressure of refrigerant leaving the heat rejecting heat exchanger is kept at a level which is slightly higher than the pressure level providing optimal coefficient of performance.

First claim

What is claimed is:

1. A method for controlling a vapor compression system, the vapor compression system comprising a compressor unit, a heat rejecting heat exchanger, an ejector comprising a primary inlet, a secondary inlet and an outlet, a receiver, at least one expansion device and at least one evaporator, arranged in a refrigerant path, the method comprising the steps of:
obtaining a temperature of refrigerant leaving the heat rejecting heat exchanger,
deriving a reference pressure value of refrigerant leaving the heat rejecting heat exchanger, based on the obtained temperature of refrigerant leaving the heat rejecting heat exchanger,
obtaining a pressure difference between a pressure prevailing in the receiver and a pressure of refrigerant leaving the evaporator,
comparing the pressure difference to a predefined first lower threshold value,
in the case that the pressure difference is higher than the first lower threshold value, controlling the vapor compression system on the basis of the derived reference pressure value, and in order to obtain a pressure of refrigerant leaving the heat rejecting heat exchanger which is equal to the derived reference pressure value, and
in the case that the pressure difference is lower than the first lower threshold value, selecting a fixed reference pressure value corresponding to a derived reference pressure value when the pressure difference is at a predefined level which is equal to the first lower threshold value, and controlling the vapor compression system on the basis of the selected fixed reference pressure value, and in order to obtain a pressure of refrigerant leaving the heat rejecting heat exchanger which is equal to the selected fixed reference pressure value.

2. The method according to claim 1 , further comprising the steps of, in the case that the pressure difference is lower than the first lower threshold value:
obtaining a difference between the derived reference pressure value and the selected fixed reference pressure value,
comparing the obtained difference to a second upper threshold value, and
in the case that the obtained difference is higher than the second upper threshold value, selecting the derived reference pressure value, and controlling the vapor compression system according to the derived reference pressure value, and in order to obtain a pressure of refrigerant leaving the heat rejecting heat exchanger which is equal to the derived reference pressure value.

3. The method according to claim 2 , wherein the step of obtaining a pressure difference between a pressure prevailing in the receiver and a pressure of refrigerant leaving the evaporator comprises the step of measuring the pressure in the receiver and/or the pressure of refrigerant leaving the evaporator.

4. The method according to claim 2 , wherein the step of deriving a reference pressure comprises using a look-up table providing corresponding values of temperature of refrigerant leaving the heat rejecting heat exchanger, pressure of refrigerant leaving the heat rejecting heat exchanger, and optimal coefficient of performance (COP) for the vapor compression system.

5. The method according to claim 2 , wherein the step of deriving a reference pressure value comprises calculating the reference pressure value based on the temperature of refrigerant leaving the heat rejecting heat exchanger.

6. The method according to claim 2 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a secondary fluid flow across the heat rejecting heat exchanger.

7. The method according to claim 2 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a compressor capacity of the compressor unit.

8. The method according to claim 1 , wherein the step of obtaining a pressure difference between a pressure prevailing in the receiver and a pressure of refrigerant leaving the evaporator comprises the step of measuring the pressure in the receiver and/or the pressure of refrigerant leaving the evaporator.

9. The method according to claim 8 , wherein the step of deriving a reference pressure comprises using a look-up table providing corresponding values of temperature of refrigerant leaving the heat rejecting heat exchanger, pressure of refrigerant leaving the heat rejecting heat exchanger, and optimal coefficient of performance (COP) for the vapor compression system.

10. The method according to claim 8 , wherein the step of deriving a reference pressure value comprises calculating the reference pressure value based on the temperature of refrigerant leaving the heat rejecting heat exchanger.

11. The method according to claim 8 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a secondary fluid flow across the heat rejecting heat exchanger.

12. The method according to claim 8 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a compressor capacity of the compressor unit.

13. The method according to claim 1 , wherein the step of deriving a reference pressure comprises using a look-up table providing corresponding values of temperature of refrigerant leaving the heat rejecting heat exchanger, pressure of refrigerant leaving the heat rejecting heat exchanger, and optimal coefficient of performance (COP) for the vapor compression system.

14. The method according to claim 13 , wherein the step of deriving a reference pressure value comprises calculating the reference pressure value based on the temperature of refrigerant leaving the heat rejecting heat exchanger.

15. The method according to claim 13 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a secondary fluid flow across the heat rejecting heat exchanger.

16. The method according to claim 1 , wherein the step of deriving a reference pressure value comprises calculating the reference pressure value based on the temperature of refrigerant leaving the heat rejecting heat exchanger.

17. The method according to claim 16 , wherein the steps of controlling the compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a secondary fluid flow across the heat rejecting heat exchanger.

18. The method according to claim 1 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a secondary fluid flow across the heat rejecting heat exchanger.

19. The method according to claim 1 , wherein the steps of controlling the vapor compression system on the basis of the derived reference pressure value or on the basis of the selected fixed reference pressure value comprises adjusting a compressor capacity of the compressor unit.

20. The method according to claim 1 , wherein the steps of controlling the vapor compression system on the basis of

Assignees

• Danfoss As

Inventors

• Prins Jan
• Schmidt Frede
• Madsen Kenneth Bank
• Fredslund Kristian

Classifications

• F25B41/385

  Dispositions with two or more expansion means arranged in parallel on a refrigerant line leading to the same evaporator · CPC title

• F25B2500/29

  High ambient temperatures · CPC title

• F25B2400/16

  Receivers · CPC title

• F25B2500/31

  Low ambient temperatures · CPC title

• F25B2700/21163

  of the refrigerant at the outlet of the condenser · CPC title