Method for controlling a vapour compression system during gas bypass valve malfunction

Patent metadata

Field	Value
Publication number	US-12097451-B2
Application number	US-201716461938-A
Country	US
Kind code	B2
Filing date	Nov 15, 2017
Priority date	Nov 22, 2016
Publication date	Sep 24, 2024
Grant date	Sep 24, 2024

Abstract

A method for controlling a vapour compression system ( 1 ) is disclosed. Malfunctioning of a gas bypass valve ( 8 ) is registered. An actual opening degree of the gas bypass valve ( 8 ) is derived, and a target opening degree of the gas bypass valve ( 8 ) is derived, based on one or more control parameters of the vapour compression system ( 1 ). The actual opening degree is compared to the target opening degree, and the vapour compression system ( 1 ) is controlled based on the comparison, and in order to match a mass flow of gaseous refrigerant through the gas bypass valve ( 8 ) to the actual opening degree of the gas bypass valve ( 8 ).

First claim

What is claimed is:

1. A method for controlling a vapour compression system, the vapour compression system comprising at least one compressor, a heat rejecting heat exchanger, a high pressure expansion device, a receiver, an evaporator expansion device, an evaporator and a gas bypass valve, arranged in a refrigerant path, the method comprising the steps of:
registering that the gas bypass valve is malfunctioning,
deriving an actual opening degree of the malfunctioning gas bypass valve,
deriving a target opening degree of the malfunctioning gas bypass valve, based on one or more control parameters of the vapour compression system,
comparing the actual opening degree of the malfunctioning gas bypass valve to the target opening degree of the malfunctioning gas bypass valve, and
controlling the vapour compression system based on the comparison, and in order to match a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve to the actual opening degree of the malfunctioning gas bypass valve;

wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the step of:
obtaining one or more refrigerant pressure values and one or more refrigerant temperature values at selected positions along the refrigerant path.

2. The method according to claim 1 , wherein the step of controlling the vapour compression system based on the comparison comprises the steps of:
in the case that the comparison reveals that the actual opening degree of the malfunctioning gas bypass valve is larger than the target opening degree of the malfunctioning gas bypass valve, controlling the vapour compression system to increase the mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, and
in the case that the comparison reveals that the actual opening degree of the malfunctioning gas bypass valve is smaller than the target opening degree of the malfunctioning gas bypass valve, controlling the vapour compression system to decrease the mass flow of gaseous refrigerant through the malfunctioning gas bypass valve.

3. The method according to claim 2 , wherein the step of increasing the mass flow of gaseous refrigerant through the malfunctioning gas bypass valve comprises decreasing a pressure of refrigerant leaving the heat rejecting heat exchanger and/or increasing a temperature of refrigerant leaving the heat rejecting heat exchanger.

4. The method according to claim 2 , wherein the step of decreasing the mass flow of gaseous refrigerant through the malfunctioning gas bypass valve comprises increasing a pressure of refrigerant leaving the heat rejecting heat exchanger and/or decreasing a temperature of refrigerant leaving the heat rejecting heat exchanger.

5. The method according to claim 1 , wherein the step of controlling the vapour compression system based on the comparison step comprises adjusting an opening degree of the high pressure expansion device, adjusting a secondary fluid flow across the heat rejecting heat exchanger and/or adjusting a compressor capacity of the compressor(s).

6. The method according to claim 1 , wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the steps of:
estimating a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, based on the obtained refrigerant pressure value(s) and refrigerant temperature value(s), and
deriving the actual opening degree of the malfunctioning gas bypass valve based on the estimated mass flow of gaseous refrigerant through the malfunctioning gas bypass valve.

7. The method according to claim 1 , wherein the step of deriving a target opening degree of the malfunctioning gas bypass valve is based on at least an obtained value of a pressure prevailing inside the receiver.

8. The method according to claim 1 , wherein the step of controlling the vapour compression system is performed in such a manner that a compressor capacity of the compressor(s) is not allowed to decrease below a minimum compressor capacity level.

9. The method according to claim 1 , further comprising a step of forcing the compressor(s) to start at predefined time intervals.

10. The method according to claim 3 , wherein the step of decreasing the mass flow of gaseous refrigerant through the malfunctioning gas bypass valve comprises increasing a pressure of refrigerant leaving the heat rejecting heat exchanger and/or decreasing a temperature of refrigerant leaving the heat rejecting heat exchanger.

11. The method according to claim 2 , wherein the step of controlling the vapour compression system based on the comparison step comprises adjusting an opening degree of the high pressure expansion device, adjusting a secondary fluid flow across the heat rejecting heat exchanger and/or adjusting a compressor capacity of the compressor(s).

12. The method according to claim 3 , wherein the step of controlling the vapour compression system based on the comparison step comprises adjusting an opening degree of the high pressure expansion device, adjusting a secondary fluid flow across the heat rejecting heat exchanger and/or adjusting a compressor capacity of the compressor(s).

13. The method according to claim 4 , wherein the step of controlling the vapour compression system based on the comparison step comprises adjusting an opening degree of the high pressure expansion device, adjusting a secondary fluid flow across the heat rejecting heat exchanger and/or adjusting a compressor capacity of the compressor(s).

14. The method according to claim 2 , wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the steps of:
estimating a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, based on the obtained refrigerant pressure value(s) and refrigerant temperature value(s), and
deriving the actual opening degree of the malfunctioning gas bypass valve based on the estimated mass flow of gaseous refrigerant through the malfunctioning gas bypass valve.

15. The method according to claim 3 , wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the steps of:
estimating a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, based on the obtained refrigerant pressure value(s) and refrigerant temperature value(s), and
deriving the actual opening degree of the malfunctioning gas bypass valve based on the estimated mass flow of gaseous refrigerant through the malfunctioning gas bypass valve.

16. The method according to claim 4 , wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the steps of:
estimating a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, based on the obtained refrigerant pressure value(s) and refrigerant temperature value(s), and
deriving the actual opening degree of the malfunctioning gas bypass valve based on the estimated mass flow of gaseous refrigerant through the malfunctioning gas bypass valve.

17. The method according to claim 5 , wherein the step of deriving an actual opening degree of the malfunctioning gas bypass valve comprises the steps of:
estimating a mass flow of gaseous refrigerant through the malfunctioning gas bypass valve, based on the obtained refrigerant pressure value(s) and refrigerant temperature value(s), and
deriving the actual opening degree of the malfunctioning gas bypass valve based on the estimated mass flow of gaseous refrigerant through the malfunctioning gas bypass v

Assignees

• Danfoss As

Inventors

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

Classifications

• F25B41/39

  Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator · CPC title

• Y02B30/70

  Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating · CPC title

• F25B2700/21163

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

• F25B2500/19

  Calculation of parameters · CPC title

• F25B2400/23

  Separators · CPC title