CN108759202B - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- CN108759202B CN108759202B CN201810851912.8A CN201810851912A CN108759202B CN 108759202 B CN108759202 B CN 108759202B CN 201810851912 A CN201810851912 A CN 201810851912A CN 108759202 B CN108759202 B CN 108759202B
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- Prior art keywords
- low
- pipe
- heat conducting
- temperature
- heat
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 239000007788 liquid Substances 0.000 title claims abstract description 32
- 239000003507 refrigerant Substances 0.000 claims abstract description 23
- 238000007789 sealing Methods 0.000 claims abstract description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 6
- 229910052802 copper Inorganic materials 0.000 claims description 6
- 239000010949 copper Substances 0.000 claims description 6
- 238000005057 refrigeration Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
Abstract
The invention provides a gas-liquid separator which comprises a body, a heat exchange assembly, a low-temperature low-pressure input pipe, a low-temperature low-pressure output pipe and a high-temperature high-pressure pipeline for performing heat exchange with a gas-liquid two-phase refrigerant output by the low-temperature low-pressure input pipe, wherein the body comprises an upper cylinder body with a closed upper end face and an open lower end face, and a lower cylinder body with a closed lower end face and an open upper end face, the lower end of the upper cylinder body is connected with the upper end of the lower cylinder body in a sealing manner, an inlet pipe orifice of the low-temperature low-pressure input pipe is arranged outside the body, an outlet pipe orifice of the low-temperature low-pressure input pipe is arranged inside the body, and an inlet pipe orifice of the low-temperature low-pressure output pipe is arranged inside the body, and the heat exchange assembly comprises a closed shell, a first connecting pipe, a second connecting pipe, a heat conducting pipe and a heat conducting plate. The invention carries out the second heat exchange on the low-temperature low-pressure gaseous refrigerant from the evaporator through the heat exchange component, thereby improving the heat exchange efficiency.
Description
Technical Field
The invention relates to the technical field of air conditioner refrigeration, in particular to a gas-liquid separator.
Background
In an air conditioning system, a compressor compresses only gaseous refrigerant, which can cause damage to the compressor and system rejection if liquid refrigerant is drawn into the compressor in large quantities. Therefore, in the prior art, a gas-liquid separator is often installed between the evaporator and the compressor. The working principle of the gas-liquid separator is as follows: the gas-liquid two-phase refrigerant from the evaporator enters the gas-liquid separator, the liquid refrigerant sinks under the action of gravity, and the gaseous refrigerant rises; the gas-liquid separator is internally provided with a low-temperature low-pressure pipeline, the outlet end of the low-temperature low-pressure pipeline is communicated to the outside of the gas-liquid separator, the opening of the inlet end of the low-temperature low-pressure pipeline is exposed to the inner cavity at the upper part of the gas-liquid separator, and rising gaseous refrigerant flows to the outlet end through the inlet end and then enters the compressor. The prior gas-liquid separator comprises a body, a low-temperature low-pressure input pipe, a low-temperature low-pressure output pipe and a high-temperature high-pressure pipeline which exchanges heat with the refrigerant input by the low-temperature low-pressure input pipe. The low-temperature low-pressure gaseous refrigerant from the evaporator is subjected to heat exchange through the high-temperature high-pressure pipe, so that the gaseous refrigerant in a subcritical state at the inlet of the compressor is overheated, and the liquid refrigerant in a supercritical state before throttling is supercooled, thereby obviously improving the efficiency of a transcritical refrigerant refrigeration cycle system, reducing the exhaust pressure required by the optimal performance of the system, avoiding the occurrence of liquid impact of the compressor and the like. The defects are that: the high-temperature high-pressure pipe of the gas-liquid separator has low heat exchange efficiency on the low-temperature low-pressure gaseous refrigerant coming out of the evaporator.
Disclosure of Invention
The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a gas-liquid separator.
The above object is achieved by the following technical scheme:
the invention provides a gas-liquid separator, which comprises a body, a heat exchange component, a low-temperature low-pressure input pipe, a low-temperature low-pressure output pipe and a high-temperature high-pressure pipeline for carrying out heat exchange with a gas-liquid two-phase refrigerant output by the low-temperature low-pressure input pipe, wherein the body comprises an upper cylinder body with a closed upper end face and an open lower end face and a lower cylinder body with a closed lower end face and an open upper end face, the lower end of the upper cylinder body is connected with the upper end of the lower cylinder body in a sealing way, the inlet opening of the low-temperature low-pressure input pipe is arranged outside the body, the outlet opening of the low-temperature low-pressure input pipe is arranged inside the body, the inlet opening of the low-temperature low-pressure output pipe is arranged inside the body, the heat exchange component comprises a closed shell, a first connecting pipe, a second connecting pipe, a heat conducting pipe and a heat conducting plate, the heat pipe and the heat conducting plate are located in the shell, the inlet of the heat pipe is located outside the shell, the outlet of the heat pipe is located outside the shell, the inlet of the first connecting pipe is located outside the body, the outlet of the first connecting pipe is communicated with the inlet of the heat pipe, the outlet of the heat pipe is communicated with the inlet of the high-temperature high-pressure pipeline, the outlet of the high-temperature high-pressure pipeline is arranged outside the body, the heat conducting plate is in contact with the heat pipe, the shell is provided with an air inlet and an air outlet, the air inlet of the shell is communicated with the outlet of the low-temperature low-pressure output pipe, the air outlet of the shell is communicated with the inlet of the second connecting pipe, and the outlet of the second connecting pipe is arranged outside the body.
Further, the heat exchange assembly further comprises a heat conducting screen, wherein the heat conducting screen is arranged in the shell, and the heat conducting screen is in contact with the heat conducting plate.
Further, the high-temperature high-pressure pipeline is a spiral high-temperature high-pressure pipeline.
Further, the heat conducting pipe and the heat conducting plate are made of copper.
Further, the heat conducting screen is made of copper.
Further, the number of the heat conducting plates is four.
The beneficial effects of the invention are as follows: the low-temperature low-pressure gaseous refrigerant from the evaporator is subjected to secondary heat exchange through the heat exchange component, so that the heat exchange efficiency is improved; the second heat exchange process is as follows: after the first heat exchange, the low-temperature low-pressure gaseous refrigerant flows into the shell of the heat exchange assembly from the low-temperature low-pressure output pipe, and exchanges heat with the heat conducting screen, the heat conducting plate and the heat conducting pipe, so that the second heat exchange is realized. The heat of the heat conducting pipe is transferred by the high-temperature high-pressure liquid refrigerant entering the heat conducting pipe from the first connecting pipe, the heat conducting pipe transfers heat to the heat conducting plate, and the heat conducting plate transfers heat to the heat conducting screen, so that the contact area of the low-temperature low-pressure gaseous refrigerant is increased, and the heat exchange efficiency is improved.
Drawings
FIG. 1 is a schematic cross-sectional view of the present invention;
fig. 2 is a schematic cross-sectional view of a heat exchange assembly according to the present invention.
Detailed Description
The invention is described in further detail below with reference to the attached drawings and detailed description:
as shown in fig. 1 to 2, the present invention provides a gas-liquid separator, comprising a body 1, a heat exchange assembly 2, a low temperature low pressure input pipe 3, a low temperature low pressure output pipe 4, and a high temperature high pressure pipeline 5 for performing heat exchange with a gas-liquid two-phase refrigerant output from the low temperature low pressure input pipe 3, wherein the body 1 comprises an upper cylinder 11 with a closed upper end surface and an open lower end surface, and a lower cylinder 12 with a closed lower end surface and an open upper end surface, the lower end of the upper cylinder 11 is welded with the upper end of the lower cylinder 12 in a sealing manner, an inlet pipe orifice 31 of the low temperature low pressure input pipe 3 is arranged outside the body 1, an outlet pipe orifice 32 of the low temperature low pressure input pipe 3 is arranged inside the body 1, an inlet pipe orifice 41 of the low temperature low pressure output pipe 4 is arranged inside the body 1, the heat exchange assembly 2 comprises a sealed shell 21, a first connecting pipe 22, a second connecting pipe 23, a heat conducting pipe 24, and a heat conducting plate 25, the heat conducting pipe 24 and the heat conducting plate 25 are positioned in the shell 21, the inlet opening 241 of the heat conducting pipe 24 is positioned outside the shell 21, the outlet opening 242 of the heat conducting pipe 24 is positioned outside the shell 21, the inlet opening 221 of the first connecting pipe 22 is positioned outside the body 1, the outlet opening of the first connecting pipe 22 is communicated with the inlet opening 241 of the heat conducting pipe 24, the outlet opening 242 of the heat conducting pipe 24 is communicated with the inlet opening 51 of the high-temperature and high-pressure pipeline 5, the outlet opening 52 of the high-temperature and high-pressure pipeline 5 is arranged outside the body 1, the heat conducting plate 25 is contacted with the heat conducting pipe 24, the shell 21 is provided with an air inlet 211 and an air outlet 212, the air inlet 211 of the shell 21 is communicated with the outlet opening 42 of the low-temperature and low-pressure output pipe 4, the air outlet 212 of the housing 21 is communicated with the air inlet of the second connecting pipe 23, the air outlet 231 of the second connecting pipe 23 is arranged outside the body 1, the heat conducting pipe 24 and the heat conducting plate 25 are made of copper, and the heat conducting plate 25 is four.
The heat exchange assembly 2 further comprises a heat conducting screen 26, the heat conducting screen 26 is arranged inside the shell 21, the heat conducting screen 26 is in contact with the heat conducting plate 25, and the heat conducting screen 26 is made of copper. The heat conductive plate 25 transfers heat to the heat conductive screen 26, which increases the contact area of the low-temperature low-pressure gaseous refrigerant, thereby improving heat exchange efficiency.
The high-temperature high-pressure pipeline 5 is a spiral high-temperature high-pressure pipeline 5. The spiral high temperature and high pressure pipeline 5 increases the contact area with the gas-liquid two-phase refrigerant exiting from the evaporator, thereby increasing the first heat exchange efficiency.
The above is only a preferred embodiment of the present invention, and the scope of the present invention is not limited to the above examples, and all technical solutions belonging to the inventive concept belong to the scope of the present invention.
Claims (6)
1. A gas-liquid separator, characterized in that: comprises a body, a heat exchange component, a low-temperature low-pressure input pipe, a low-temperature low-pressure output pipe and a high-temperature high-pressure pipeline for carrying out heat exchange with a gas-liquid two-phase refrigerant output by the low-temperature low-pressure input pipe, wherein the body comprises an upper cylinder body with a closed upper end face and an open lower end face and a lower cylinder body with a closed lower end face and an open upper end face, the lower end of the upper cylinder body is connected with the upper end of the lower cylinder body in a sealing way, the inlet opening of the low-temperature low-pressure input pipe is arranged outside the body, the outlet opening of the low-temperature low-pressure input pipe is arranged inside the body, the inlet opening of the low-temperature low-pressure output pipe is arranged inside the body, the heat exchange component comprises a closed shell, a first connecting pipe, a second connecting pipe, a heat conducting pipe and a heat conducting plate, the heat pipe and the heat conducting plate are located in the shell, the inlet of the heat pipe is located outside the shell, the outlet of the heat pipe is located outside the shell, the inlet of the first connecting pipe is located outside the body, the outlet of the first connecting pipe is communicated with the inlet of the heat pipe, the outlet of the heat pipe is communicated with the inlet of the high-temperature high-pressure pipeline, the outlet of the high-temperature high-pressure pipeline is arranged outside the body, the heat conducting plate is in contact with the heat pipe, the shell is provided with an air inlet and an air outlet, the air inlet of the shell is communicated with the outlet of the low-temperature low-pressure output pipe, the air outlet of the shell is communicated with the inlet of the second connecting pipe, and the outlet of the second connecting pipe is arranged outside the body.
2. A gas-liquid separator according to claim 1, wherein: the heat exchange assembly further comprises a heat conducting screen, wherein the heat conducting screen is arranged inside the shell, and the heat conducting screen is in contact with the heat conducting plate.
3. A gas-liquid separator according to claim 1, wherein: the high-temperature high-pressure pipeline is a spiral high-temperature high-pressure pipeline.
4. A gas-liquid separator according to claim 1, wherein: the heat conducting pipe and the heat conducting plate are made of copper.
5. A gas-liquid separator according to claim 2, characterized in that: the heat conducting screen is made of copper.
6. A gas-liquid separator according to claim 1, wherein: the number of the heat conducting plates is four.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201810851912.8A CN108759202B (en) | 2018-07-30 | 2018-07-30 | Gas-liquid separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810851912.8A CN108759202B (en) | 2018-07-30 | 2018-07-30 | Gas-liquid separator |
Publications (2)
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CN108759202A CN108759202A (en) | 2018-11-06 |
CN108759202B true CN108759202B (en) | 2023-10-27 |
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CN201810851912.8A Active CN108759202B (en) | 2018-07-30 | 2018-07-30 | Gas-liquid separator |
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Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN113739457A (en) * | 2020-05-29 | 2021-12-03 | 绍兴三花新能源汽车部件有限公司 | Heat exchanger and gas-liquid separator |
WO2021238649A1 (en) * | 2020-05-29 | 2021-12-02 | 绍兴三花新能源汽车部件有限公司 | Heat exchanger and gas-liquid separator |
Citations (12)
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JPH11190573A (en) * | 1997-10-20 | 1999-07-13 | Calsonic Corp | Gas-liquid separator |
KR100784610B1 (en) * | 2006-08-17 | 2007-12-11 | 주식회사 두원공조 | Accumulator combined with internal heat exchanger of air conditioner |
CN201973964U (en) * | 2011-02-16 | 2011-09-14 | 陈卫华 | Vertical evaporator with gas-liquid separation function |
CN202562148U (en) * | 2012-04-12 | 2012-11-28 | 广州金抡电器有限公司 | Undercooling and overheating type reservoir |
CN202692564U (en) * | 2012-07-06 | 2013-01-23 | 青岛开拓隆海制冷配件有限公司 | Built-in heat exchange gas-liquid separator |
CN203837333U (en) * | 2014-03-04 | 2014-09-17 | 广东美的暖通设备有限公司 | Cylindrical heat exchanger |
CN105805990A (en) * | 2014-12-29 | 2016-07-27 | 浙江三花汽车零部件有限公司 | Carbon dioxide air-conditioning system and gas-liquid separator thereof |
CN205481968U (en) * | 2016-03-24 | 2016-08-17 | 青岛海尔空调电子有限公司 | Air conditioner removes liquid heat transfer device and air conditioner circulation system |
WO2017063613A1 (en) * | 2015-10-16 | 2017-04-20 | 珠海格力电器股份有限公司 | Gas liquid separator, air conditioning system, and air conditioning system operation method |
EP3173714A1 (en) * | 2015-11-25 | 2017-05-31 | Mitsubishi Heavy Industries, Ltd. | Refrigerating cycle system and liquid flow-back prevention method |
JP2018076993A (en) * | 2016-11-08 | 2018-05-17 | サンデンホールディングス株式会社 | Accumulator integrated with internal heat exchanger, and refrigeration cycle using the same |
CN208536462U (en) * | 2018-07-30 | 2019-02-22 | 东莞市艾瑞科热能设备有限公司 | A kind of gas-liquid separator |
-
2018
- 2018-07-30 CN CN201810851912.8A patent/CN108759202B/en active Active
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11190573A (en) * | 1997-10-20 | 1999-07-13 | Calsonic Corp | Gas-liquid separator |
KR100784610B1 (en) * | 2006-08-17 | 2007-12-11 | 주식회사 두원공조 | Accumulator combined with internal heat exchanger of air conditioner |
CN201973964U (en) * | 2011-02-16 | 2011-09-14 | 陈卫华 | Vertical evaporator with gas-liquid separation function |
CN202562148U (en) * | 2012-04-12 | 2012-11-28 | 广州金抡电器有限公司 | Undercooling and overheating type reservoir |
CN202692564U (en) * | 2012-07-06 | 2013-01-23 | 青岛开拓隆海制冷配件有限公司 | Built-in heat exchange gas-liquid separator |
CN203837333U (en) * | 2014-03-04 | 2014-09-17 | 广东美的暖通设备有限公司 | Cylindrical heat exchanger |
CN105805990A (en) * | 2014-12-29 | 2016-07-27 | 浙江三花汽车零部件有限公司 | Carbon dioxide air-conditioning system and gas-liquid separator thereof |
WO2017063613A1 (en) * | 2015-10-16 | 2017-04-20 | 珠海格力电器股份有限公司 | Gas liquid separator, air conditioning system, and air conditioning system operation method |
EP3173714A1 (en) * | 2015-11-25 | 2017-05-31 | Mitsubishi Heavy Industries, Ltd. | Refrigerating cycle system and liquid flow-back prevention method |
CN205481968U (en) * | 2016-03-24 | 2016-08-17 | 青岛海尔空调电子有限公司 | Air conditioner removes liquid heat transfer device and air conditioner circulation system |
JP2018076993A (en) * | 2016-11-08 | 2018-05-17 | サンデンホールディングス株式会社 | Accumulator integrated with internal heat exchanger, and refrigeration cycle using the same |
CN208536462U (en) * | 2018-07-30 | 2019-02-22 | 东莞市艾瑞科热能设备有限公司 | A kind of gas-liquid separator |
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CN108759202A (en) | 2018-11-06 |
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Address after: 523000 No. 3, Fengtian Road, Tangxia Town, Dongguan City, Guangdong Province Applicant after: DONGGUAN ARCIO HEAT ENERGY EQUIPMENT CO.,LTD. Address before: Block 117, new sun industrial city, No.20, Xinhong Road, Lin village, Tangxia Town, Dongguan City, Guangdong Province, 523000 Applicant before: DONGGUAN ARCIO HEAT ENERGY EQUIPMENT CO.,LTD. |
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