Refrigeration storage in a refrigerant vapor compression system
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
F25B-001/00
F25B-001/10
F25B-009/00
출원번호
US-0517136
(2011-01-19)
등록번호
US-9068765
(2015-06-30)
국제출원번호
PCT/US2011/021685
(2011-01-19)
§371/§102 date
20120619
(20120619)
국제공개번호
WO2011/091014
(2011-07-28)
발명자
/ 주소
Huff, Hans-Joachim
출원인 / 주소
CARRIER CORPORATION
대리인 / 주소
Cantor Colburn LLP
인용정보
피인용 횟수 :
0인용 특허 :
20
초록▼
A refrigerant vapor compression system (10) includes a plurality of components, including a flash tank (70), connected in a refrigerant flow circuit by a plurality of refrigerant lines (2, 4, 6, 8). The system internal volume equals to the sum of the internal volumes of the plurality of components a
A refrigerant vapor compression system (10) includes a plurality of components, including a flash tank (70), connected in a refrigerant flow circuit by a plurality of refrigerant lines (2, 4, 6, 8). The system internal volume equals to the sum of the internal volumes of the plurality of components and the internal volume of the plurality of refrigerant lines. The internal volume of the flash tank ranges from at least 10% to about 30% of the total system internal volume.
대표청구항▼
1. A refrigerant vapor compression system comprising a plurality of components connected in a refrigerant flow circuit by a plurality of refrigerant lines, said components including at least a compression device, a refrigerant heat rejection heat exchanger, a primary expansion device, a refrigerant
1. A refrigerant vapor compression system comprising a plurality of components connected in a refrigerant flow circuit by a plurality of refrigerant lines, said components including at least a compression device, a refrigerant heat rejection heat exchanger, a primary expansion device, a refrigerant heat absorption heat exchanger, and a flash tank; each of said components defining an internal volume and the plurality of refrigerant lines defining an internal volume, the system volume equal to the sum of the internal volumes of said component volumes and the internal volume of the plurality of refrigerant lines, and the internal volume of the flash tank ranging from at least 10% to about 30% of the system volume;wherein the flash tank is disposed in the refrigerant flow circuit between the refrigerant heat rejection heat exchanger and the refrigerant heat absorption heat exchanger. 2. The refrigerant vapor compression system as recited in claim 1 wherein the internal volume of the flash tank ranges from at about least 20% to about 30% of the system volume. 3. The refrigerant vapor compression system as recited in claim 1 wherein the internal volume of the flash tank ranges from at least 0.1 cubic feet up to about 0.2 cubic feet. 4. The refrigerant vapor compression system as recited in claim 3 wherein the internal volume of the flash tank is about 0.15 cubic feet. 5. The refrigerant vapor compression system as recited in claim 1 further comprising an economizer circuit operatively associated with the refrigerant flow circuit, the economizer including a refrigerant vapor injection line connecting the chamber of the flash tank in refrigerant vapor flow communication with an intermediate pressure stage of the compression device. 6. The refrigerant vapor compression system as recited in claim 1 wherein said refrigerant is carbon dioxide. 7. A refrigerant vapor compression system for a transport refrigeration unit for conditioning a cargo space, comprising: a compression device;a refrigerant heat rejection heat exchanger;at least one expansion device;a refrigerant heat absorption heat exchanger;a flash tank defining a chamber having an internal volume; anda plurality of refrigerant lines connecting the compression device, the refrigerant heat rejection heat exchanger, the at least one expansion device, the refrigerant heat absorption heat exchanger and the flash tank in a refrigerant flow circuit;the internal volume of the flash tank having a volume between at least 10% up to 30% of a total system internal volume. 8. The refrigerant vapor compression system as recited in claim 7 wherein the internal volume of the flash tank ranges from at about least 20% to about 30% of the system volume. 9. The refrigerant vapor compression system as recited in claim 7 wherein the internal volume of the flash tank ranges from at least 0.1 cubic feet up to about 0.2 cubic feet. 10. The refrigerant vapor compression system as recited in claim 9 wherein the internal volume of the charge storage device is about 0.15 cubic feet. 11. The refrigerant vapor compression system as recited in claim 7 wherein said refrigerant is carbon dioxide. 12. The refrigerant vapor compression system as recited in claim 7 wherein the total system internal volume includes an internal volume of the compression device, an internal volume of the refrigerant heat rejection heat exchanger, an internal volume of the at least one expansion device, an internal volume of the refrigerant heat absorption heat exchanger, a total internal volume of the plurality of refrigerant lines and the internal volume of the flash tank. 13. The refrigerant vapor compression system as recited in claim 7 wherein the flash tank is disposed in the refrigerant flow circuit between the refrigerant heat rejection heat exchanger and the refrigerant heat absorption heat exchanger, and the at least one expansion device includes a primary expansion device disposed in the refrigerant flow circuit between the flash tank and the refrigerant heat absorption heat exchanger and a secondary expansion device disposed in the refrigerant flow circuit between the refrigerant heat rejection heat exchanger and the flash tank. 14. The refrigerant vapor compression system as recited in claim 13 wherein the plurality of refrigerant lines includes a refrigerant vapor injection line connecting the chamber of the flash tank to refrigerant vapor flow communication with an intermediate pressure stage of the compression device. 15. The refrigerant vapor compression system as recited in claim 14 further comprising a suction line accumulator interdisposed in the refrigerant flow circuit intermediate the refrigerant heat absorption heat exchanger and a suction inlet to the compression device, the suction line accumulator defining an internal volume, the sum of the internal volume of the flash tank and the internal volume of the suction line accumulator being up to 30% of the total system internal volume. 16. The refrigerant vapor compression system as recited in claim 7 wherein the refrigeration is carbon dioxide and the refrigerant vapor compression system is operable in a transcritical cycle. 17. A method for designing a refrigerant vapor compression system for operation in a transcritical cycle, the refrigerant vapor compression system having a plurality of components including at least a compression device, a refrigerant heat rejection heat exchanger, at least one expansion device, and a refrigerant heat absorption heat exchanger connected in a refrigerant flow circuit by a plurality of refrigerant lines, comprising: providing a flash tank interdisposed in the refrigerant flow circuit intermediate the refrigerant heat rejection heat exchanger and the refrigerant heat absorption heat exchanger; andsizing an internal volume of the flash tank to provide sufficient volume that at the maximum volume of liquid refrigerant collecting within the flash tank during operation, adequate volume is provided above the maximum liquid level within the flash tank to ensure that the process of separation of the refrigerant vapor and refrigerant liquid will still occur unimpeded. 18. The method as recited in claim 17 further comprising: sizing the internal volume of the flash tank to have a volume between 10% up to 30% of the total internal volume of the refrigerant vapor compression system. 19. The method as recited in claim 18 further comprising determining the total system internal volume by summing the respective internal volume of each of said plurality of components in the refrigerant flow circuit in which refrigerant may reside and the total internal volume of the refrigerant lines in the refrigerant flow circuit.
연구과제 타임라인
LOADING...
LOADING...
LOADING...
LOADING...
LOADING...
이 특허에 인용된 특허 (20)
Stierlin Hans (Schlieren CHX) Ferguson John R. (Grove Hill GB2), Absorption refrigerating unit.
Norberto Lemcoff ; Shuguang Deng ; Michael Ernest Garrett GB; Michael John Heywood GB; Ralph John Whiteman GB, Atmosphere control for perishable produce.
Vander Woude, David J.; Viegas, Herman H.; Seshadri, Jayaram; Glentz, Joseph Louis; Schwichtenberg, Bryan Edward; Stuart, William Ehrich, Control method for a self-powered cryogen based refrigeration system.
Miller Jeremy P. (Mortimer GBX) Monroe Charles M. (High Wycombe GBX) Williams Mark S. (Kingston-Upon-Thames PA GBX) Drake Miles P. (Allentown PA), Refrigeration apparatus and method of refrigeration.
※ AI-Helper는 부적절한 답변을 할 수 있습니다.