High efficiency refrigeration system

Patent metadata

Field	Value
Publication number	US-10935286-B2
Application number	US-201214348531-A
Country	US
Kind code	B2
Filing date	Sep 27, 2012
Priority date	Sep 30, 2011
Publication date	Mar 2, 2021
Grant date	Mar 2, 2021

Abstract

A refrigerant system includes a first, substantially outdoor, two phase heat transfer fluid vapor compression circulation loop including a compressor, a heat exchanger condenser, an expansion device, and the heat absorption side of a heat exchanger evaporator condenser, connected by conduit in a closed loop and having disposed therein a first heat transfer fluid having a critical temperature of greater than or equal to 31.2° C. The system also includes a second, at least partially indoor, two phase heat transfer fluid circulation loop that transfers heat to the first loop through the heat exchanger evaporator condenser. The second loop includes the heat rejection side of the heat exchanger evaporator condenser, a liquid pump, and a heat exchanger evaporator, connected by conduit in a closed loop and having disposed therein a second heat transfer fluid that has an ASHRAE Class A toxicity rating and an ASHRAE Class 1 or 2L flammability rating.

First claim

The invention claimed is:

1. A heat transfer system, comprising:
a first two-phase vapor/compression fluid circulation loop, disposed outdoor, comprising a compressor, a heat exchanger condenser, an expansion device, and a heat absorption side of a heat exchanger evaporator/condenser, connected by conduit in a closed fluid circulation loop and having disposed therein a first heat transfer fluid having a critical temperature of greater than or equal to 31.2° C. selected from the group consisting of saturated hydrocarbons, unsaturated hydrocarbons, R32, R152a, an R1234 isomer, R410A, and mixtures of the foregoing; and
a second two-phase fluid circulation loop, disposed indoor, that transfers heat to the first two-phase vapor/compression fluid circulation loop through the heat exchanger evaporator/condenser, said second two-phase fluid circulation loop comprising a heat rejection side of the heat exchanger evaporator/condenser, a liquid pump, and a heat exchanger evaporator, connected by conduit in a closed fluid circulation loop and having disposed therein a second heat transfer fluid selected from the group consisting of sub-critical fluid CO 2 , an R1234 isomer, a mixture of an R1234 isomer and an R134 isomer, 2-phase water, sub-critical fluid CO 2 in combination with nanoparticles, an R1234 isomer in combination with nanoparticles, a mixture of an R1234 isomer and an R134 isomer in combination with nanoparticles, 2-phase water in combination with nanoparticles and mixtures of the foregoing, wherein the second fluid circulation loop includes liquid second heat transfer fluid flowing in the conduit between the heat rejection side of the heat exchanger evaporator/condenser and the liquid pump and flowing in the conduit between the liquid pump and the heat exchanger evaporator, and gaseous second heat transfer fluid flowing in the conduit between the heat exchanger evaporator and the heat absorption side of the heat exchanger evaporator/condenser, and further wherein the liquid pump is a variable speed pump or the second fluid circulation loop includes an expansion device between the liquid pump and the heat exchanger evaporator.

2. The heat transfer system of claim 1 , wherein the compressor in the first two-phase vapor/compression fluid circulation loop is a variable speed compressor.

3. The heat transfer system of claim 1 , wherein the liquid pump in the second two-phase fluid circulation loop is said variable speed pump.

4. The heat transfer system of claim 1 , wherein the second two-phase fluid circulation loop further comprises said expansion device between the liquid pump and the heat exchanger evaporator.

5. The heat transfer system of claim 1 , wherein the first heat transfer fluid is a saturated hydrocarbon or unsaturated hydrocarbon.

6. The heat transfer system of claim 1 , wherein the first heat transfer fluid is R32, R152a, an R1234 isomer, or R410a.

7. The heat transfer system of claim 1 , wherein the second heat transfer fluid is selected from the group consisting of sub-critical fluid CO 2 , a mixture of an R1234 isomer and an R134 isomer or R32, and 2-phase water.

8. The heat transfer system of claim 1 , wherein the second heat transfer fluid has nanoparticles having a specific heat and a thermal conductivity that is greater than either or both of the specific heat and thermal conductivity of the second heat transfer fluid.

9. The heat transfer system of claim 1 , wherein the expansion device in the first two-phase vapor compression fluid circulation loop is a two-phase ejector.

10. The heat transfer system of claim 9 wherein the ejector includes an electronically controlled expansion valve.

11. The heat transfer system of claim 1 , wherein one or more of the heat exchanger condenser in the first two-phase vapor compression fluid circulation loop, the heat exchanger evaporator in the second two-phase fluid circulation loop, and the heat exchanger evaporator/condenser bridging the first two-phase vapor compression fluid circulation loop and the second two-phase fluid circulation loop is a microchannel heat exchanger.

12. The heat transfer system of claim 1 , wherein one or more of the heat exchanger condenser in the first two-phase vapor compression fluid circulation loop, the heat exchanger evaporator in the second two-phase fluid circulation loop, and the heat exchanger evaporator/condenser bridging the first two-phase vapor compression fluid circulation loop and the second two-phase fluid circulation loop, comprises heat transfer plates or fins bonded by brazing or welding to the exterior of one or more tubes.

13. The heat transfer system of claim 1 , comprising a plurality of heat exchanger evaporators disposed in parallel in the second two-phase fluid circulation loop, and optionally a plurality of heat exchanger condensers disposed in parallel in the first two-phase vapor compression fluid circulation loop provided that the number of heat exchanger condensers disposed in the first two-phase vapor compression fluid circulation loop is fewer than the number of heat exchanger evaporators disposed in the second two-phase fluid circulation loop.

14. A heat transfer system, comprising:
a first two-phase vapor/compression fluid circulation loop, disposed outdoors, comprising a compressor, a heat exchanger condenser, an expansion device, and a heat absorption side of a heat exchanger evaporator/condenser, connected by conduit in a closed fluid circulation loop and having disposed therein a first heat transfer fluid having a critical temperature of greater than or equal to 31.2° C. selected from the group consisting of saturated hydrocarbons, unsaturated hydrocarbons, R32, R152a, an R1234 isomer, R410A, and mixtures of the foregoing; and
a second two-phase fluid circulation loop, disposed indoors, that transfers heat to the first two-phase vapor/compression fluid circulation loop through the heat exchanger evaporator/condenser, said second two-phase fluid circulation loop comprising a heat rejection side of the heat exchanger evaporator/condenser, a liquid pump, and a heat exchanger evaporator, connected by conduit in a closed fluid circulation loop and having disposed therein a second heat transfer fluid selected from the group consisting of sub-critical fluid CO 2 , an R1234 isomer, a mixture of an R1234 isomer and an R134 isomer, 2-phase water, sub-critical fluid CO 2 in combination with nanoparticles, an R1234 isomer in combination with nanoparticles, a mixture of an R1234 isomer and an R134 isomer in combination with nanoparticles, 2-phase water in combination with nanoparticles, and mixtures of the foregoing, wherein the second fluid circulation loop includes liquid second heat transfer fluid flowing in the conduit between the heat rejection side of the heat exchanger evaporator/condenser and the liquid pump and flowing in the conduit between the liquid pump and the heat exchanger evaporator, and gaseous second heat transfer fluid flowing in the conduit between the heat exchanger evaporator and the heat absorption side of the heat exchanger evaporator/condenser, and further wherein the liquid pump is a variable speed pump or the second fluid circulation loop includes an expansion device between the liquid pump and the heat exchanger evaporator.

15. The heat transfer system of claim 14 , wherein the second heat transfer fluid is sub-critical fluid CO 2 or 2-phase water.

16. The heat transfer system of claim 15 , wherein the first heat transfer fluid is a saturated hydrocarbon or unsaturated hydrocarbon, and the second heat transfer fluid is sub-critical fluid CO 2 or 2-phase water.

Assignees

• Carrier Corp

Inventors

• Verma Parmesh
• Cogswell Frederick J
• Radcliff Thomas D
• Farzad Mohsen
• Blasko Vladimir
• Munoz Jules R
• Sivakumar Seshadri

Classifications

• F25B2309/06

  Compression machines, plants or systems characterised by the refrigerant being carbon dioxide · CPC title

• F25B2600/0253

  with variable speed · CPC title

• F25B2400/12

  Inflammable refrigerants · CPC title

• F25B2341/0012

  Ejectors with the cooled primary flow at high pressure · CPC title

• F25B41/00

  Fluid-circulation arrangements · CPC title