High efficiency ejector cycle

Patent metadata

Field	Value
Publication number	US-11149989-B2
Application number	US-201916565995-A
Country	US
Kind code	B2
Filing date	Sep 10, 2019
Priority date	Jul 23, 2010
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

A system has a compressor, a heat rejection heat exchanger, first and second ejectors, first and second heat absorption heat exchangers, and first and second separators. The heat rejection heat exchanger is coupled to the compressor to receive refrigerant compressed by the compressor. The first ejector has a primary inlet coupled to the heat rejection exchanger to receive refrigerant, a secondary inlet, and an outlet. The first separator has an inlet coupled to the outlet of the first ejector to receive refrigerant from the first ejector. The first separator has a gas outlet coupled to the compressor to return refrigerant to the compressor. The first separator has a liquid outlet coupled to the secondary inlet of the ejector to deliver refrigerant to the first ejector. The first heat absorption heat exchanger is coupled to the liquid outlet of the first separator to receive refrigerant and to the secondary inlet of the first ejector to deliver refrigerant to the first ejector. The second ejector has a primary inlet coupled to the liquid outlet of the first separator to receive refrigerant, a secondary inlet, and an outlet. The second separator has an inlet coupled to an outlet of the second ejector to receive refrigerant from the second ejector, a gas outlet coupled to the compressor to return refrigerant to the compressor, and a liquid outlet. The second heat absorption heat exchanger is coupled to the liquid outlet of the second separator to receive refrigerant and to the secondary inlet of the second ejector to deliver refrigerant to the second ejector.

First claim

What is claimed is:

1. A system ( 200 ) comprising:
a compressor ( 22 );
a heat rejection heat exchanger ( 30 ) coupled to the compressor to receive refrigerant compressed by the compressor;
a first ejector ( 38 ) having:
a primary inlet ( 40 ) coupled to the heat rejection heat exchanger to receive refrigerant;
a secondary inlet ( 42 ); and
an outlet ( 44 );

a first separator ( 48 ) having:
an inlet ( 50 ) coupled to the outlet of the first ejector to receive refrigerant from the first ejector;
a gas outlet ( 54 ) coupled to the compressor to return refrigerant to the compressor; and
a liquid outlet ( 52 );

a first heat absorption heat exchanger ( 64 ) coupled to the liquid outlet of the first separator to receive refrigerant and coupled to the secondary inlet of the first ejector to deliver refrigerant to the first ejector, wherein the only flowpath to the first ejector secondary inlet passes through the first heat absorption heat exchanger;
a second ejector ( 202 ) having:
a primary inlet ( 204 ) coupled to the liquid outlet of the first separator to receive refrigerant;
a secondary inlet ( 206 ); and
an outlet ( 208 );

a second separator ( 210 ) having:
an inlet ( 212 ) coupled to the outlet of the second ejector to receive refrigerant from the second ejector;
a gas outlet ( 216 ) coupled to the compressor to return refrigerant to the compressor; and
a liquid outlet ( 214 ); and

a second heat absorption heat exchanger ( 220 ) coupled to the liquid outlet of the second separator to receive refrigerant and to the secondary inlet of the second ejector to deliver refrigerant.

2. The system of claim 1 further comprising:
a first expansion device ( 70 ) between the first separator liquid outlet ( 52 ) and the first heat absorption heat exchanger ( 64 ) inlet ( 66 ); and
a second expansion device ( 226 ) between the second separator ( 210 ) liquid outlet ( 214 ) and the second heat absorption heat exchanger ( 220 ) inlet ( 222 ).

3. The system of claim 1 wherein:
the first and second separators are gravity separators.

4. The system of claim 1 wherein:
the system has no other separator.

5. The system of claim 1 wherein:
the system has no other ejector.

6. The system of claim 1 wherein:
the system has no other compressor.

7. The system of claim 1 wherein:
the gas outlet ( 54 ) of the first separator feeds an economizer port of the compressor; and
the gas outlet ( 216 ) of the second separator feeds a suction port of the compressor.

8. The system of claim 1 wherein:
the first heat absorption heat exchanger is in a first refrigerated space; and
the second heat absorption heat exchanger is in a second refrigerated space.

9. The system of claim 1 wherein:
the refrigerant comprises at least 50% carbon dioxide, by weight.

10. A method for operating the system of claim 1 comprising running the compressor in a first mode wherein:
the refrigerant is compressed in the compressor;
refrigerant received from the compressor by the heat rejection heat exchanger rejects heat in the heat rejection heat exchanger to produce initially cooled refrigerant;
the initially cooled refrigerant passes through the first ejector; and
a liquid discharge of the first separator is split into a first portion passing to the first ejector secondary inlet ( 42 ) and a second portion passing to the primary inlet ( 204 ) of the second ejector.

11. The method of claim 10 wherein:
the first portion of the liquid discharge of the first separator passes to the first ejector secondary inlet through an expansion device ( 70 ) followed by the first heat absorption heat exchanger ( 64 ); and
the second portion of the liquid discharge of the first separator passes directly to the primary inlet of the second ejector.

12. The method of claim 10 wherein:
an entire gas discharge of the first separator passes to an economizer port of the compressor; and
an entire gas discharge of the second separator passes to a suction port of the compressor.

13. The method of claim 10 further comprising:
driving a first airflow across the first heat absorption heat exchanger via a first fan to cool a frozen food storage area; and
driving a second airflow across the second heat absorption heat exchanger via a second fan to cool a refrigerated perishables storage area.

14. The method of claim 10 further comprising:
driving an airflow across the second heat absorption heat exchanger and therefrom across the first heat absorption heat exchanger.

15. The system of claim 1 further comprising:
a fan positioned to drive an airflow sequentially across the second heat absorption heat exchanger and therefrom across the first heat absorption heat exchanger.

16. A method for running a system ( 200 ), the system comprising:
a compressor ( 22 );
a heat rejection heat exchanger ( 30 ) coupled to the compressor to receive refrigerant compressed by the compressor;
a first ejector ( 38 ) having:
a primary inlet ( 40 ) coupled to the heat rejection heat exchanger to receive refrigerant;
a secondary inlet ( 42 ); and
an outlet ( 44 );

a first separator ( 48 ) having:
an inlet ( 50 ) coupled to the outlet of the first ejector to receive refrigerant from the first ejector;
a gas outlet ( 54 ) coupled to the compressor to return refrigerant to the compressor; and
a liquid outlet ( 52 );

a first heat absorption heat exchanger ( 64 ) coupled to the liquid outlet of the first separator to receive refrigerant and coupled to the secondary inlet of the first ejector to deliver refrigerant to the first ejector;
a second ejector ( 202 ) having:
a primary inlet ( 204 ) coupled to the liquid outlet of the first separator to receive refrigerant;
a secondary inlet ( 206 ); and
an outlet ( 208 );

a second separator ( 210 ) having:
an inlet ( 212 ) coupled to the outlet of the second ejector to receive refrigerant from the second ejector;
a gas outlet ( 216 ) coupled to the compressor to return refrigerant to the compressor; and
a liquid outlet ( 214 ); and

a second heat absorption heat exchanger ( 220 ) coupled to the liquid outlet of the second separator to receive refrigerant and to the secondary inlet of the second ejector to deliver refrigerant, the method comprising running the compressor in a first mode wherein:
the refrigerant is compressed in the compressor;
refrigerant received from the compressor by the heat rejection heat exchanger rejects heat in the heat rejection heat exchanger to produce initially cooled refrigerant;
the initially cooled refrigerant passes through the first ejector;
a liquid discharge of the first separator is split into a first portion passing to the first ejector secondary inlet ( 42 ) and a second portion passing to the primary inlet ( 204 ) of the second ejector;
an entire gas discharge of the first separator passes to an economizer port of the compressor; and
an entire gas discharge of the second separator passes to a suction port of the compressor.

17. The method of claim 16 wherein:
the first portion of the liquid discharge of the first separator passes to the first ejector secondary inlet through an expansion device ( 70 ) followed by the first heat absorption heat exchanger ( 64 ); and
the second portion of the liquid discharge of the first separator passes directly to the primary inlet of the second ejector.

18. The method of claim 16 wherein:
the first heat absorption heat exchanger is in a first refrigerated space; and
the second heat absorption heat exchanger is in

Assignees

• Carrier Corp

Inventors

• Wang Jinliang
• Verma Parmesh

Classifications

• F25B41/00 Primary

  Fluid-circulation arrangements · CPC title

• F25B1/06 Primary

  with compressor of jet type, e.g. using liquid under pressure ({F25B1/005,} F25B1/10 take precedence) · CPC title

• F25B43/006

  Accumulators · CPC title

• F25B2341/0015

  using two or more ejectors · CPC title

• F25B2309/061

  with cycle highest pressure above the supercritical pressure · CPC title