Method for controlling a vapour compression system

Patent metadata

Field	Value
Publication number	US-9303901-B2
Application number	US-66305308-A
Country	US
Kind code	B2
Filing date	Jun 11, 2008
Priority date	Jun 12, 2007
Publication date	Apr 5, 2016
Grant date	Apr 5, 2016

Abstract

A method for controlling a vapor compression system, such as a refrigeration system, preferably an air condition system, comprising at least two evaporators. While monitoring a superheat (SH) at a common outlet for the evaporators, the amount of available refrigerant is controlled in response to the SH and in order to obtain an optimum SH value. The available refrigerant is distributed among the evaporators in accordance with a distribution key. The distribution key is preferably obtained while taking individual consideration to operating conditions for each of the evaporators into account. Thereby the vapor compression system can be operated in such a way that each of the evaporators is operated in an optimal manner, and in such a way that the system in general is operated in an optimal manner.

First claim

What is claimed is:

1. A method for controlling a vapor compression system, the vapor compression system comprising a compressor, a condenser, at least two evaporators fluidly connected in parallel between the compressor and an expansion device comprising a multi-valve connected to each of the evaporators for controlling a flow of refrigerant across each of the evaporators, the at least two evaporators sharing a common outlet fluidly connected to the compressor, the method comprising the steps of:
monitoring a superheat, SH, only at the common outlet of the at least two evaporators;
controlling an amount of available refrigerant in response to the monitored superheat, SH, at the common outlet of the at least two evaporators; and
operating the expansion device to provide a superheat, SH, level which is sufficiently high to prevent liquid refrigerant from passing through the evaporators;
obtaining a first distribution key determining the relative allocation of available refrigerant among each of the evaporators, while the superheat, SH, level is sufficiently high to prevent liquid refrigerant from passing through the evaporators;
adjusting the relative allocation of available refrigerant through each of the evaporators to be in accordance with the first distribution key;
operating the expansion device to lower the superheat, SH, level, by increasing opening time of the expansion device or by decreasing the refrigeration load on the vapor compression system;
obtaining a second distribution key at the lowered SH level obtained by said operation of the expansion device, the second distribution key modifying the first distribution key's relative allocation of available refrigerant among each of the evaporators for the lowered SH level; and
distributing the available refrigerant among each of the evaporators in accordance with the second distribution key's relative allocation of available refrigerant by using the expansion device.

2. The method according to claim 1 , wherein the expansion device comprises at least one valve.

3. The method according to claim 1 , wherein for each evaporator, a time interval during which the multi-valve supplies refrigerant to the evaporator can be adjusted, and wherein the step of controlling an amount of available refrigerant comprises adjusting said time interval for each of the evaporators in such a manner that the mutual distribution of refrigerant among the evaporators is maintained.

4. The method according to claim 3 , wherein the step of controlling an amount of available refrigerant comprises adjusting the length of a combined time interval during which refrigerant is supplied to one of the evaporators relatively to the length of a combined time interval during which no refrigerant is supplied to the evaporators.

5. The method according to claim 1 , wherein the step of obtaining a first distribution key comprises the steps of:
a) modifying the distribution of refrigerant through the evaporators in such a manner that a mass flow of refrigerant through a first evaporator is altered while keeping the total mass flow of refrigerant through all the evaporators substantially constant;
b) when a significant change in superheat, SH, occurs, detecting a control parameter based on the change in mass flow of refrigerant through the first evaporator obtained during step b), the significant change in SH being either one of: 1) a mass flow through an evaporator being increased, the SH then decreasing significantly when the mass flow is sufficiently large to allow liquid refrigerant to pass all the way through the evaporator, or 2) a mass flow through an evaporator being decreased, the SH then increasing significantly when the mass flow is sufficiently small to prevent liquid refrigerant to pass all the way through the evaporator; and
c) repeating steps a) to c) for each of the remaining evaporator(s),
wherein the step of adjusting the distribution of refrigerant through each of the evaporators to be in accordance with the first distribution key is performed on the basis of the detected control parameters.

6. The method according to claim 1 , wherein the step of obtaining a second distribution key comprises the steps of:
a) modifying the distribution of refrigerant through the evaporators in such a manner that a mass flow of refrigerant through a first evaporator is altered while keeping the total mass flow of refrigerant through all the evaporators substantially constant,
b) when a significant change in superheat, SH, occurs, detecting a control parameter based on the change in mass flow of refrigerant through the first evaporator obtained during step b), the significant change in SH being either one of: 1) a mass flow through an evaporator being increased, the SH then decreasing significantly when the mass flow is sufficiently large to allow liquid refrigerant to pass all the way through the evaporator, or 2) a mass flow through an evaporator being decreased, the SH then increasing significantly when the mass flow is sufficiently small to prevent liquid refrigerant to pass all the way through the evaporator, and
c) repeating steps a) to c) for each of the remaining evaporator(s).

7. The method according to claim 1 wherein the step of obtaining a first distribution key comprises the steps of:
a) modifying the distribution of refrigerant through the evaporators in such a manner that a mass flow of refrigerant through a first evaporator is altered by a predefined amount while keeping the total mass flow of refrigerant through all the evaporators substantially constant,
b) detecting a control parameter based on the change in mass flow of refrigerant through the first evaporator obtained during step b), said control parameter reflecting a change in superheat, SH, occurring as a result of the modification of the distribution of refrigerant, and
c) repeating steps a) to c) for each of the remaining evaporator(s), and
wherein the step of adjusting the distribution of refrigerant through each of the evaporators to be in accordance with the first distribution key is performed on the basis of the detected control parameters.

8. The method according to claim 1 , wherein the step of obtaining a second distribution key comprises the steps of:
a) modifying the distribution of refrigerant through the evaporators in such a manner that a mass flow of refrigerant through a first evaporator is altered by a predefined amount while keeping the total mass flow of refrigerant through all the evaporators substantially constant,
b) detecting a control parameter based on the change in mass flow of refrigerant through the first evaporator obtained during step b), said control parameter reflecting a change in superheat, SH, occurring as a result of the modification of the distribution of refrigerant, and
c) repeating steps a) to c) for each of the remaining evaporator(s).

9. The method according to claim 5 , further comprising the steps of:
comparing the detected control parameters for each of the evaporators, and
in the case that the detected control parameter of an evaporator is significantly different from the detected control parameters of the remaining evaporators, generating a failure warning signal to an operator.

10. The method according to claim 9 , further comprising the step of initiating defrost of the evaporator having a significantly different control parameter upon generation of a failure warning signal.

11. The method according to claim 1 , further comprising repeating the step of obtaining a second distribution key.

12. The method according to claim 1 , further comprising the steps of:
obtaining information relating to at least one disturbance o

Assignees

• Thybo Claus
• Wisniewski Rafael
• Danfoss As

Inventors

• Thybo Claus
• Wisniewski Rafael

Classifications

• F25B49/02

  for compression type machines, plants or systems · CPC title

• F25B2600/2511

  Evaporator distribution valves · CPC title

• F25B2600/21

  Refrigerant outlet evaporator temperature · CPC title

• F25B5/02 Primary

  arranged in parallel · CPC title