[특허]Refrigeration cycle device and method of controlling the same

Mitsubishi Electric Corporation

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Refrigeration cycle device and method of controlling the same

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	G05D-015/00 F25B-041/04 F25B-041/00 F25B-040/06 F24F-011/00 F25B-040/02
출원번호	US-0995343 (2008-11-11)
등록번호	US-9163865 (2015-10-20)
우선권정보	JP-2008-155520 (2008-06-13)
국제출원번호	PCT/JP2008/070445 (2008-11-11)
§371/§102 date	20101130 (20101130)
국제공개번호	WO2009/150761 (2009-12-17)
발명자 / 주소	Wakamoto, Shinichi Unezaki, Fumitake Kuramochi, Takeshi Iijima, Hitoshi
출원인 / 주소	Mitsubishi Electric Corporation
대리인 / 주소	Oblon, McClelland, Maier & Neustadt, L.L.P.
인용정보	피인용 횟수 : 1 인용 특허 : 5

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A refrigeration cycle device 100 where a combustible refrigerant circulates includes a bypass pipe 5 that is connected so that part of the refrigerant that flows through a circulation pipe extending from a condenser 2 to a flow control valve 3 bypasses the flow control valve 3 and an evaporator 4; a bypass flow control valve 6 that controls the amount of the refrigerant flowing through the bypass pipe 5; a heat exchanger 7 that allows heat exchange between the refrigerant that flows through the bypass pipe 5 after flowing out of the bypass flow control valve 6 and the refrigerant that flows through the circulation pipe after flowing out of the condenser 2; and a subcooling degree sensor T73 that detects the subcooling degree of the refrigerant at the inlet of the flow control valve 3. At least either the flow control valve 3 or the bypass flow control valve 6 is controlled so that the subcooling degree of the refrigerant at the inlet of the flow control valve 3 is equal to or greater than or a predetermined value.

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1. A refrigeration cycle device comprising: a compressor that compresses a combustible refrigerant; a condenser that condenses the combustible refrigerant compressed by the compressor;a heat exchanger that subcools the combustible refrigerant discharged from the condenser; an expansion valve that expands the combustible refrigerant subcooled by the heat exchanger;an evaporator that evaporates the combustible refrigerant expanded by the expansion valve;an evaporator upstream pressure sensor that detects a pressure of the combustible refrigerant in a pipe between an upstream side of the evaporator and a downstream side of the expansion valve;an evaporator downstream pressure sensor that detects a pressure of the combustible refrigerant in a pipe between a downstream side of the evaporator and an upstream side of the compressor;a bypass pipe that connects an upstream pipe of the compressor and a downstream pipe of the heat exchanger;a bypass expansion valve provided on the bypass pipe to expand a secondary stream that diverges from a primary stream of the combustible refrigerant flowing through the downstream pipe; anda controller configured to: acquire a detected pressure value from the evaporator upstream pressure sensor and a detected pressure value from the evaporator downstream pressure sensor;calculate an evaporator pressure difference wherein the evaporator pressure difference is the difference between the detected pressure value from the evaporator upstream pressure sensor and the detected pressure value from the evaporator downstream pressure sensor;increase the opening of the bypass expansion valve when the evaporator pressure difference is greater than a control target value; anddecrease the opening of the bypass expansion valve when the evaporator pressure difference is less than a control target value. 2. The refrigeration cycle device of claim 1, comprising a combustible refrigerant whose quantity is less than or equal to the permissible quantity of refrigerant of an air-conditioned space determined by a lean flammability limit of the combustible refrigerant. 3. The refrigeration cycle device of claim 1, comprising a combustible refrigerant whose quantity is less than or equal to the permissible quantity of refrigerant of a cooled space of the refrigeration cycle device specified by a lean flammability limit of the combustible refrigerant. 4. The refrigeration cycle device of claim 1, further comprising: a subcooling degree detection section that detects the subcooling degree of the primary stream of the combustible refrigerant at the inlet side of the expansion valve, whereinthe heat exchanger is thermally connected to the downstream side of the bypass expansion valve of the bypass pipe, andthe controller controls the opening of at least either the expansion valve or the bypass expansion valve on the basis of the detection result by the subcooling degree detection section so that the subcooling degree of the primary stream is greater than or equal to a predetermined value. 5. The refrigeration cycle device of claim 1, wherein the heat exchanger is thermally connected to the downstream side of the bypass expansion valve of the bypass pipe, andthe controller controls the subcooling degree of the primary stream and the superheat degree of the secondary stream. 6. The refrigeration cycle device of claim 5, wherein the controller controls the opening of the expansion valve on the basis of the temperature of the primary stream and the opening of the bypass expansion valve on the basis of the temperature of the secondary stream. 7. The refrigeration cycle device of claim 5, wherein the controller controls the opening of the expansion valve on the basis of the subcooling degree of the primary stream and the opening of the bypass expansion valve on the basis of the superheating degree of the secondary stream. 8. The refrigeration cycle device of claim 5, wherein the controller increases the amount of the combustible refrigerant flowing through the bypass pipe and raises the subcooling degree of the combustible refrigerant between an outlet of the heat exchanger and the expansion valve. 9. The refrigeration cycle device of claim 4, further comprising: a superheat degree detection section that detects the superheat degree of the combustible refrigerant at the downstream side of the heat exchanger in the bypass pipe, whereinthe controller includes a superheat degree control section that sets a control target value of the superheat degree of the combustible refrigerant in the bypass pipe, and the controller controls the bypass expansion valve so that the superheat degree detected by the superheat degree detection section becomes the control target value set by the superheat degree control section. 10. The refrigeration cycle device of claim 1, further comprising a subcooling degree control section that changes a control target value of the subcooling degree of the combustible refrigerant at an inlet of the expansion valve in accordance with either the type of the combustible refrigerant or the length of an extension pipe, or both. 11. The refrigeration cycle device of claim 4, wherein when either the difference in pressure between the combustible refrigerant at an inlet of the bypass pipe and the combustible refrigerant at an outlet of the bypass pipe or the difference in pressure between the combustible refrigerant at an inlet of the evaporator and the combustible refrigerant at an outlet of the evaporator, or both, increases, the controller controls the opening of the bypass expansion valve such that the quantity of the combustible refrigerant flowing through the bypass pipe is increased. 12. The refrigeration cycle device of claim 4, wherein the secondary and primary streams flow directions in the heat exchanger are opposed. 13. The refrigeration cycle device of claim 4, wherein: a capillary tube that expands the combustible refrigerant is disposed at the downstream of the bypass expansion valve of the bypass pipe, and the heat exchanger is formed by the capillary tube and part of a connection pipe that connects the condenser and the expansion valve; andthe direction in which the combustible refrigerant in the capillary tube flows is parallel to the direction in which the combustible refrigerant in the connection pipe flows. 14. The refrigeration cycle device of claim 4, wherein: part of the bypass pipe is separated into a plurality of heat conduction tubes at an inlet of the heat exchanger;a plurality of the heat conduction tubes are put together at an outlet of the heat exchanger; anda number-of-diverging-points variable section that changes the heat conduction tubes through which the combustible refrigerant flows out of a plurality of the heat conduction tubes is included. 15. The refrigeration cycle device of claim 4, further comprising a gas-liquid separator provided between the expansion valve and the evaporator; a gas pipe that allows the combustible refrigerant in the state of vapor separated by the gas-liquid separator to flow into the compressor; and a gas flow control valve provided on the gas pipe to control the flow quantity of the combustible refrigerant. 16. The refrigeration cycle device of claim 15, further comprising: a gas flow control valve upstream pressure sensor that detects the pressure of the combustible refrigerant at the upstream side of the gas flow control valve of the gas pipe; anda gas flow control valve downstream pressure sensor that detects the pressure of the combustible refrigerant at the downstream side of the gas flow control valve of the gas pipe, whereinthe gas flow control valve is controlled in accordance with a pressure value detected by the gas flow control valve upstream pressure sensor and a pressure value detected by the gas flow control valve downstream pressure sensor. 17. A refrigeration cycle device comprising: a compressor that compresses a combustible refrigerant; a condenser that condenses the combustible refrigerant compressed by the compressor; a heat exchanger that subcools the combustible refrigerant discharged from the condenser; an expansion valve that expands the combustible refrigerant subcooled by the heat exchanger; an evaporator that evaporates the combustible refrigerant expanded by the expansion valve; a bypass pipe that connects an upstream pipe of the compressor to an downstream pipe of the heat exchanger; a bypass expansion valve provided on the bypass pipe to expand a secondary stream that diverges from a primary stream of the combustible refrigerant flowing through the downstream pipe; a controller that controls an amount of heat exchange of the heat exchanger in accordance with a temperature or pressure of the combustible refrigerant between the condenser and the expansion valve; an evaporator upstream pressure sensor that detects a pressure of a refrigerant in a pipe between an upstream side of the evaporator and a downstream side of the expansion valve; an evaporator downstream pressure sensor that detects a pressure of a refrigerant in a pipe between a downstream side of the evaporator and an upstream side of the compressor; and a superheat degree detection section that detects a superheat degree of the combustible refrigerant at a downstream side of the heat exchanger in the bypass pipe,wherein the controller includes a superheat degree control section and is configured to: acquire a detected pressure value from the evaporator upstream pressure sensor and a detected pressure value from the evaporator downstream pressure sensor;calculate an evaporator pressure difference wherein the evaporator pressure difference is the difference between the detected pressure value from the evaporator upstream pressure sensor and the detected pressure value from the evaporator downstream pressure sensor;set a superheat control target value based on the calculated evaporator pressure difference; andcontrol the opening of the bypass expansion valve such that the superheat degree detected by the superheat degree detection section becomes the superheat control target value. 18. The refrigeration cycle device of claim 17, further comprising: a subcooling degree detection section that detects the subcooling degree of the primary stream of the combustible refrigerant at the inlet side of the expansion valve,wherein the heat exchanger is thermally connected to the downstream side of the bypass expansion valve of the bypass pipe, andwherein the controller controls the opening of at least either the expansion valve or the bypass expansion valve on the basis of the detection result by the subcooling degree detection section so that the subcooling degree of the primary stream is greater than or equal to a predetermined value. 19. The refrigeration cycle device of claim 17, wherein the heat exchanger is thermally connected to the downstream side of the bypass expansion valve of the bypass pipe, andwherein the controller controls the subcooling degree of the primary stream and the superheat degree of the secondary stream. 20. The refrigeration cycle device of claim 1, wherein the controller increases the opening of the bypass expansion valve when the evaporator pressure difference is at least 0.01 Mpa greater than the control target value. 21. The refrigeration cycle device of claim 17, wherein the superheat degree control selection decreases the superheat control target value when the calculated evaporator pressure difference is at least 0.01 Mpa greater than a pressure control target value.

이 특허에 인용된 특허 (5)

이 특허를 인용한 특허 피인용횟수: 1

Furui, Shuji; Furusho, Kazuhiro; Fujino, Hirokazu; Yoh, Hiroshi. Refrigerating apparatus. USP2017029581365.

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