Absorption subcooler for a refrigeration system

Patent metadata

Field	Value
Publication number	US-10458685-B2
Application number	US-201615346329-A
Country	US
Kind code	B2
Filing date	Nov 8, 2016
Priority date	Nov 8, 2016
Publication date	Oct 29, 2019
Grant date	Oct 29, 2019

Abstract

An absorption subcooler comprises a first heat exchanger operable to receive refrigerant from a compressor of a refrigeration system and apply a first cooling stage to the refrigerant. The absorption subcooler is further operable to discharge the refrigerant to a gas cooler operable to apply a second cooling stage to the refrigerant.

First claim

The invention claimed is:

1. A refrigeration system operable to circulate refrigerant through the refrigeration system in order to cool a refrigeration load, the refrigeration system comprising:
a compressor operable to receive the refrigerant from the refrigeration load and compress the refrigerant;
an absorption subcooler comprising a first heat exchanger, a second heat exchanger, a condenser, and an absorption chamber, wherein the first heat exchanger is operable to:
receive the compressed refrigerant from the compressor;
apply a first cooling stage to the compressed refrigerant;
receive a solution comprising a first liquid and an absorption subcooler refrigerant;
discharge the first liquid from the solution to the absorption chamber; and
discharge the absorption subcooler refrigerant from the solution to the condenser; and

a third heat exchanger external from the absorption subcooler, the third heat exchanger operable to receive the refrigerant that has been cooled by the first heat exchanger and apply a second cooling stage to the refrigerant;
wherein the second heat exchanger of the absorption subcooler is operable to receive the cooled refrigerant from the third heat exchanger, apply a third cooling stage to the refrigerant, and discharge the refrigerant to an expansion valve operable to supply the refrigerant to the refrigeration load.

2. The refrigeration system of claim 1 , wherein the absorption subcooler is powered by heat absorbed by the first heat exchanger.

3. The refrigeration system of claim 1 , wherein the third heat exchanger is a gas cooler and the refrigerant is a natural refrigerant.

4. The refrigeration system of claim 1 , wherein the third heat exchanger is a condenser and the refrigerant is a synthetic refrigerant.

5. The refrigeration system of claim 1 , wherein the absorption subcooler refrigerant is one of:
ammonia; and
lithium bromide.

6. The refrigeration system of claim 1 , wherein:
the condenser is operable to receive the absorption subcooler refrigerant in a gaseous state and condense the absorption subcooler refrigerant into a liquid state; and
the absorption chamber is operable to receive the absorption subcooler refrigerant and mix the absorption subcooler refrigerant with the first liquid.

7. The refrigeration system of claim 1 , wherein cooling the refrigerant with the absorption subcooler corresponds to one or more of:
a reduction in power consumed by the refrigeration system relative to the power consumed by a refrigeration system without the absorption subcooler; and
a reduction in a mass flow rate of flash gas discharged from a flash tank of the refrigeration system relative to a mass flow rate of flash gas discharged from the flash tank in the refrigeration system without the absorption subcooler.

8. The refrigeration system of claim 1 , wherein the first cooling stage is configured to cool the refrigerant by at least 15° C., the second cooling stage is configured to cool the refrigerant by at least 50° C., and the third cooling stage is configured to cool the refrigerant by at least 2° C.

9. An absorption subcooler comprising a first heat exchanger, an absorption chamber, and a condenser, the first heat exchanger operable to:
receive refrigerant from a compressor of a refrigeration system;
apply a first cooling stage to the refrigerant;
discharge the refrigerant to a gas cooler operable to apply a second cooling stage to the refrigerant;
receive a solution comprising a first liquid and an absorption subcooler refrigerant;
discharge the first liquid from the solution to the absorption chamber; and
discharge the absorption subcooler refrigerant from the solution to the condenser.

10. The absorption subcooler of claim 9 , wherein the absorption subcooler is powered by heat absorbed by the first heat exchanger.

11. The absorption subcooler of claim 9 , wherein the refrigerant is one of:
carbon dioxide;
ammonia; and
hydrofluorocarbons.

12. The absorption subcooler of claim 9 , wherein the absorption subcooler refrigerant is one of:
ammonia; and
lithium bromide.

13. The absorption subcooler of claim 9 , wherein:
the condenser is operable to receive the absorption subcooler refrigerant in a gaseous state and condense the absorption subcooler refrigerant into a liquid state; and
absorption chamber is operable to receive the absorption subcooler refrigerant and mix the absorption subcooler refrigerant with the first liquid.

14. The absorption subcooler of claim 9 , further comprising a second heat exchanger operable to:
receive the refrigerant from the gas cooler;
apply a third cooling stage to the refrigerant; and
discharge the refrigerant to an expansion valve operable to supply the refrigerant to a refrigeration load.

15. The absorption subcooler of claim 9 , wherein the first cooling stage is configured to cool the refrigerant by at least 15 degrees, the second cooling stage is configured to cool the refrigerant by at least 50 degrees.

16. A method in an absorption subcooler comprising:
receiving refrigerant from a compressor of a refrigeration system;
applying a first cooling stage to the refrigerant;
discharging the refrigerant to a gas cooler operable to apply a second cooling stage to the refrigerant;
receiving a solution comprising a first liquid and an absorption subcooler refrigerant;
discharging the first liquid from the solution to the absorption chamber; and
discharging the absorption subcooler refrigerant from the solution to the condenser.

17. The method of claim 16 , wherein the refrigerant is one of:
carbon dioxide;
ammonia; and
hydrofluorocarbons.

18. The method of claim 16 , wherein the absorption subcooler refrigerant comprising is one of:
ammonia; and
lithium bromide.

19. The method of claim 18 , further comprising:
condensing the absorption subcooler refrigerant from a gaseous state into a liquid state using a condenser; and
mixing the absorption subcooler refrigerant with the first liquid.

20. The method of claim 16 , further comprising:
receiving the refrigerant from the gas cooler;
applying a third cooling stage to the refrigerant; and
discharging the refrigerant to an expansion valve operable to supply the refrigerant to a refrigeration load.

Assignees

• Heatcraft Refrigeration Products Llc

Inventors

• Wilkerson Carlton
• Edwards Bucky William
• Ali Masood

Classifications

• F25B2400/13

  Economisers · CPC title

• F25B27/007

  in sorption type systems · CPC title

• F25B15/06

  the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide {(F25B15/025 takes precedence)} · CPC title

• F25B5/02

  arranged in parallel · CPC title

• F25B29/006

  of the sorption type system · CPC title