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CN102012175A - Novel gas-liquid heat-exchange device - Google Patents

Novel gas-liquid heat-exchange device Download PDF

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Publication number
CN102012175A
CN102012175A CN 201010570361 CN201010570361A CN102012175A CN 102012175 A CN102012175 A CN 102012175A CN 201010570361 CN201010570361 CN 201010570361 CN 201010570361 A CN201010570361 A CN 201010570361A CN 102012175 A CN102012175 A CN 102012175A
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China
Prior art keywords
heat exchange
liquid
outlet
liquid inlet
runner
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CN 201010570361
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Chinese (zh)
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CN102012175B (en
Inventor
刘明国
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Intercooler High Tech Beijing Environmental Technology Co ltd
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Suzhou Qutu Thermal Control System Co Ltd
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Priority to CN2010105703611A priority Critical patent/CN102012175B/en
Publication of CN102012175A publication Critical patent/CN102012175A/en
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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention discloses a novel gas-liquid heat-exchange device, comprising a main heat exchange plate and a plurality of auxiliary heat exchange fins. The device is characterized in that a liquid inlet and a liquid outlet are formed on the main heat exchange plate; a main liquid inlet channel and a main liquid outlet channel connected with the liquid inlet and the liquid outlet respectively are arranged inside the main heat exchange plate; the auxiliary heat exchange fins are vertically and alternately distributed on the main heat exchange plate in parallel, a liquid inlet subchannel and a liquid outlet subchannel which are respectively connected with the main liquid inlet channel and the main liquid outlet channel are arranged in each auxiliary heat exchange fin, and a plurality of secondary subchannels which are in vertical through connection with the liquid inlet subchannel and the liquid outlet subchannel are arranged in each auxiliary heat exchange fin. The novel gas-liquid heat-exchange device achieves the aim of heat exchange just by own structure and natural convection of air, reduces the volume, saves the cost, and prolongs the service life.

Description

The novel gas-liquid heat-exchanger rig
Technical field
The present invention relates to a kind of refrigeration technology field that belongs to, be specifically related to a kind of novel gas-liquid heat-exchanger rig.
Background technology
Heat exchanger is the vitals of temperature controlling instruments such as air-conditioning, heat exchanger, and the power of its performance and function directly has influence on the operating efficiency and the service life of temperature controlling instruments.Use form to be mainly pipe type heat exchanger and parallel-flow heat exchanger at present at the gas-liquid heat-exchange aspect cabinet air conditioner and the heat exchanger, basically combine by piping and sheet system, because this type of heat exchanger self structure limits, when heat exchange, need reach final heat exchange purpose by the convection current that fan is strengthened air.Plant maintenance and operation cost height also are subjected to the influence of fan life the service life of complete equipment.Improve heat exchange efficiency, the reduction equipment volume prolongs service life of equipment, reduces the equipment cost expense, is the important proposition that improves the heat exchanger quality, also is simultaneously one of main contents of temperature controlling instruments refrigeration system development.
Summary of the invention
The present invention seeks to: a kind of novel gas-liquid heat-exchanger rig that only depends on self structure and can reach the heat exchange purpose by the free convection of air is provided, must carry out the fluid media (medium) heat exchange and cause volume big by auxiliary equipment such as fan and heat exchange pipings, the problem that cost is high in order to solve current heat exchanger.
Technical scheme of the present invention is: a kind of novel gas-liquid heat-exchanger rig comprises main heat exchange plate and some auxiliary heat exchange fins; It is characterized in that: described main heat exchange plate is provided with liquid inlet and outlet, inner then be provided with the liquid inlet and outlet sprue that links to each other with liquid inlet and outlet respectively, and the vertical parallel interval of described auxiliary heat exchange fin is arranged on the main heat exchange plate, be provided with the liquid inlet and outlet runner that links to each other with the liquid inlet and outlet sprue respectively in the every auxiliary heat exchange fin, in every auxiliary heat exchange fin, also be provided with the inferior runner that some vertical perforations connect aforementioned liquid inlet and outlet runner simultaneously.
Further, the sprue of liquid inlet and outlet described in the present invention be arranged in parallel up and down in the main heat exchange intralamellar part, and described liquid inlet and outlet runner also be arranged in parallel up and down in every auxiliary heat exchange fin inside.
Further, liquid inlet and outlet described in the present invention is located at the side of main heat exchange plate.
Preferably, liquid inlet and outlet described in the present invention is located at the homonymy of main heat exchange plate.
Preferably, every auxiliary heat exchange fin is provided with the main heat exchange plate is vertical described in the present invention, and the feed liquor runner in the described every auxiliary heat exchange fin is vertical with the feed liquor sprue, and the fluid runner is vertical with the fluid sprue.
Preferably, the surface of auxiliary heat exchange fin is corrugated described in the present invention, with further increase heat exchange area, improves radiating effect.
The sprue of liquid inlet and outlet described in the present invention, the cross section of liquid inlet and outlet runner and time runner can be circle, and is perhaps oval, perhaps rectangle, perhaps triangle.
Liquid inlet and outlet runner in liquid inlet and outlet sprue in the main heat exchange plate of the present invention and the every auxiliary heat exchange fin and time runner be common to constitute a circuitous parallel flow passages of connect, supplies the fluid media (medium) circulation.When the present invention specifically works, liquid inlet and outlet links to each other with the pipeline of conventional cooling cycle system respectively, fluid media (medium) is flowed into by the inlet of main heat exchange plate one side, after in the feed liquor sprue, compiling, in the feed liquor runner in every auxiliary heat exchange fin of parallel again inflow, and then flow in the fluid runner through some vertical inferior runners, be collected to the fluid sprue again, flow out by liquid outlet at last.When fluid media (medium) flows, carry out heat exchange by the surface and the outside air of assisting the heat exchange fin in auxiliary heat exchange fin.
Advantage of the present invention is:
1. this novel gas-liquid heat-exchanger rig provided by the invention, it comes the water conservancy diversion heat exchange by the multi-channel structure of specialized designs in main heat exchange plate and auxiliary heat exchange fin, and need not heat exchange piping in the routine techniques, also need not to be aided with fan, so not only dwindled volume, save cost, also prolonged service life.And, reduce the cost of temperature controlling instruments when integral installation of the present invention can significantly have been dwindled the temperature controlling instruments volume inside to temperature controlling instruments inside.
2. this novel gas-liquid heat-exchanger rig provided by the invention, liquid inlet and outlet runner in liquid inlet and outlet sprue in its main heat exchange plate and the every auxiliary heat exchange fin and time runner be common to constitute a circuitous parallel flow passages of connecting, for the fluid media (medium) circulation, and by the surface of a plurality of auxiliary heat exchange fins and the free convection enforcement heat exchange of outside air, heat exchange area is big, the heat exchange efficiency height.Especially when auxiliary heat exchange fin surface design became corrugated, heat exchange area was bigger, and heat exchange efficiency is higher.
Description of drawings
Below in conjunction with drawings and Examples the present invention is further described:
Fig. 1 is the perspective view of a kind of specific embodiment of the present invention;
Fig. 2 is another visual angle view of Fig. 1;
Fig. 3 is the rearview of the embodiment of Fig. 1;
Fig. 4 is the A-A profile of Fig. 3;
Fig. 5 is the B-B profile of Fig. 3;
Fig. 6 is the vertical view of Fig. 3;
Fig. 7 is the partial sectional perspective view of Fig. 2.
Wherein: 1, main heat exchange plate; 2, auxiliary heat exchange fin; 3, inlet; 4, liquid outlet; 5, feed liquor sprue; 6, fluid sprue; 7, feed liquor runner; 8, fluid runner; 9, inferior runner.
The specific embodiment
Embodiment: in conjunction with Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5, Fig. 6 and shown in Figure 7, this novel gas-liquid heat-exchanger rig that present embodiment provides, it together is made of main heat exchange plate 1 and 10 auxiliary heat exchange fins 2 being fixed on the main heat exchange plate 1, the side homonymy of described main heat exchange plate 1 is provided with liquid inlet and outlet 3,4, inner then be provided with the liquid inlet and outlet sprue 5,6 that links to each other with liquid inlet and outlet 3,4 respectively, and liquid inlet and outlet sprue 5,6 be arranged in parallel up and down in main heat exchange plate 1 inside in the present embodiment.Described 10 auxiliary heat exchange fin 2 vertical parallel interval are arranged on the main heat exchange plate 1, be provided with the liquid inlet and outlet runner 7,8 that links to each other with liquid inlet and outlet sprue 5,6 respectively in the every auxiliary heat exchange fin 2, and the runner of liquid inlet and outlet described in the present embodiment 7,8 be arranged up and down in every auxiliary heat exchange fin 2 inside also in parallel.Simultaneously in every auxiliary heat exchange fin 2, also be provided with the inferior runner 9 that some vertical perforations connect aforementioned liquid inlet and outlet runner 7,8.And the feed liquor runner 7 in the every auxiliary heat exchange fin 2 and the 1 vertical setting of main heat exchange plate in the present embodiment, every auxiliary heat exchange fin 2 is vertical with feed liquor sprue 5, and fluid runner 8 is vertical with fluid sprue 6.The surface of described every auxiliary heat exchange fin 2 is corrugated.Described liquid inlet and outlet sprue 5,6, the cross section of liquid inlet and outlet runner 7,8 and time runner 9 is circular.
Liquid inlet and outlet runner 7,8 in liquid inlet and outlet sprue 5,6 in the main heat exchange plate 1 of present embodiment and the every auxiliary heat exchange fin 2 and inferior runner 9 be common to constitute a circuitous parallel flow passages of connect, confession fluid media (medium) circulation.When present embodiment is specifically worked, liquid inlet and outlet 3,4 links to each other with the pipeline of conventional cooling cycle system respectively, fluid media (medium) is flowed into by the inlet 3 of main heat exchange plate 1 one sides, after in feed liquor sprue 5, compiling, in the feed liquor runner 7 in every auxiliary heat exchange fin 2 of parallel again inflow, and then flow in the fluid runner 8 through some vertical inferior runners 9, be collected to fluid sprue 6 again, at last by liquid outlet 4 outflows.When fluid media (medium) flows, carry out heat exchange by the surface and the outside air of assisting heat exchange fin 2 in auxiliary heat exchange fin 2.
Certainly, more than only be concrete exemplary applications of the present invention, protection scope of the present invention is not constituted any limitation.In addition to the implementation, the present invention can also have other embodiment.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop within the present invention's scope required for protection.

Claims (7)

1. a novel gas-liquid heat-exchanger rig comprises main heat exchange plate (1) and some auxiliary heat exchange fins (2); It is characterized in that: described main heat exchange plate (1) is provided with into, liquid outlet (3,4), inside then is provided with respectively and advances, liquid outlet (3, what 4) link to each other advances, fluid sprue (5,6), and the vertical parallel interval of described auxiliary heat exchange fin (2) is arranged on the main heat exchange plate (1), be provided with in the every auxiliary heat exchange fin (2) respectively and advance, fluid sprue (5, what 6) link to each other advances, fluid runner (7,8), also being provided with simultaneously some vertical perforations in every auxiliary heat exchange fin (2) connects aforementionedly to advance, fluid runner (7,8) inferior runner (9).
2. novel gas-liquid heat-exchanger rig according to claim 1, it is characterized in that described liquid inlet and outlet sprue (5,6) be arranged in parallel up and down in main heat exchange plate (1) inside, and described liquid inlet and outlet runner (7,8) be arranged up and down in every auxiliary heat exchange fin (2) inside also in parallel.
3. novel gas-liquid heat-exchanger rig according to claim 2 is characterized in that described liquid inlet and outlet (3,4) is located at the side of main heat exchange plate (1).
4. novel gas-liquid heat-exchanger rig according to claim 3 is characterized in that described liquid inlet and outlet (3,4) is located at the homonymy of main heat exchange plate (1).
5. according to claim 1 or 2 or 3 or 4 described novel gas-liquid heat-exchanger rigs, it is characterized in that described every auxiliary heat exchange fin (2) and the vertical setting of main heat exchange plate (1), and the feed liquor runner (7) in the described every auxiliary heat exchange fin (2) is vertical with feed liquor sprue (5), and fluid runner (8) is vertical with fluid sprue (6).
6. novel gas-liquid heat-exchanger rig according to claim 1 is characterized in that the surface of described auxiliary heat exchange fin (2) is corrugated.
7. novel gas-liquid heat-exchanger rig according to claim 1 is characterized in that described liquid inlet and outlet sprue (5,6), and the cross section of liquid inlet and outlet runner (7,8) and time runner (9) is circular, or oval, or rectangle, or triangle.
CN2010105703611A 2010-12-02 2010-12-02 Novel gas-liquid heat-exchange device Active CN102012175B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010105703611A CN102012175B (en) 2010-12-02 2010-12-02 Novel gas-liquid heat-exchange device

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Application Number Priority Date Filing Date Title
CN2010105703611A CN102012175B (en) 2010-12-02 2010-12-02 Novel gas-liquid heat-exchange device

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CN102012175A true CN102012175A (en) 2011-04-13
CN102012175B CN102012175B (en) 2012-01-25

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102506601A (en) * 2011-10-20 2012-06-20 胡芸雪 Temperature-difference-drive-type self-adapting heat transfer pipe
CN104033966A (en) * 2013-03-06 2014-09-10 苏州昆拓热控系统股份有限公司 Equipment cabinet air conditioner
CN104669984A (en) * 2015-02-13 2015-06-03 陈春平 Vehicle-mounted LNG (liquefied natural gas) heat exchanger and refrigeration transport vehicle provided with heat exchanger
CN107726674A (en) * 2017-07-27 2018-02-23 杭州三花家电热管理系统有限公司 Heat exchanger and heat pump

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3114560A1 (en) * 1981-04-10 1982-11-11 Fa. J. Eberspächer, 7300 Esslingen Location-independent air heating device
SU1206582A1 (en) * 1984-05-04 1986-01-23 .JC.O. Филин, Н.С. Кирпач Refrigerating chamber
JPS63182844A (en) * 1987-01-23 1988-07-28 Nec Corp Semiconductor device
US20020021556A1 (en) * 1999-07-15 2002-02-21 Dibene Joseph T. Vapor chamber with integrated pin array
US20020056908A1 (en) * 1999-11-12 2002-05-16 Michael Philip Brownell Heatpipesink having integrated heat pipe and heat sink
US20020118511A1 (en) * 2001-02-28 2002-08-29 Dujari Prateek J. Heat dissipation device
CN1869574A (en) * 2006-06-23 2006-11-29 石桂菊 Radiation core and radiator
US20080264611A1 (en) * 2007-04-30 2008-10-30 Kun-Jung Chang Heat plate
CN201892440U (en) * 2010-12-02 2011-07-06 苏州昆拓热控系统股份有限公司 Novel gas-liquid heat exchange device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU676297B2 (en) * 1993-03-29 1997-03-06 Milne Jurisich Heat exchanger assembly

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3114560A1 (en) * 1981-04-10 1982-11-11 Fa. J. Eberspächer, 7300 Esslingen Location-independent air heating device
SU1206582A1 (en) * 1984-05-04 1986-01-23 .JC.O. Филин, Н.С. Кирпач Refrigerating chamber
JPS63182844A (en) * 1987-01-23 1988-07-28 Nec Corp Semiconductor device
US20020021556A1 (en) * 1999-07-15 2002-02-21 Dibene Joseph T. Vapor chamber with integrated pin array
US20020056908A1 (en) * 1999-11-12 2002-05-16 Michael Philip Brownell Heatpipesink having integrated heat pipe and heat sink
US20020118511A1 (en) * 2001-02-28 2002-08-29 Dujari Prateek J. Heat dissipation device
CN1869574A (en) * 2006-06-23 2006-11-29 石桂菊 Radiation core and radiator
US20080264611A1 (en) * 2007-04-30 2008-10-30 Kun-Jung Chang Heat plate
CN201892440U (en) * 2010-12-02 2011-07-06 苏州昆拓热控系统股份有限公司 Novel gas-liquid heat exchange device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102506601A (en) * 2011-10-20 2012-06-20 胡芸雪 Temperature-difference-drive-type self-adapting heat transfer pipe
CN104033966A (en) * 2013-03-06 2014-09-10 苏州昆拓热控系统股份有限公司 Equipment cabinet air conditioner
CN104033966B (en) * 2013-03-06 2017-04-12 苏州昆拓热控系统股份有限公司 Equipment cabinet air conditioner
CN104669984A (en) * 2015-02-13 2015-06-03 陈春平 Vehicle-mounted LNG (liquefied natural gas) heat exchanger and refrigeration transport vehicle provided with heat exchanger
CN104669984B (en) * 2015-02-13 2017-12-01 陈春平 Vehicle-mounted LNG heat exchangers and the refrigerating transport vehicle for installing the heat exchanger
CN107726674A (en) * 2017-07-27 2018-02-23 杭州三花家电热管理系统有限公司 Heat exchanger and heat pump

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Effective date of registration: 20161214

Address after: 225800 Jiangsu city of Yangzhou province Baoying Beiyuan Road Economic Development Zone No. 1

Patentee after: BAOYING QUTU THERMAL CONTROL SYSTEM CO.,LTD.

Address before: Suzhou City, Jiangsu province 215126 Industrial Park Sheng Pu Zhen Min Sheng Road No. 61

Patentee before: SUZHOU QUTU THERMAL CONTROL SYSTEM Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20231201

Address after: 100176 1204a, building 6, yard 2, Ronghua South Road, Beijing Economic and Technological Development Zone, Daxing District, Beijing

Patentee after: Intercooler high tech (Beijing) Environmental Technology Co.,Ltd.

Address before: 225800 1 Beiyuan Road, Baoying Economic Development Zone, Yangzhou, Jiangsu

Patentee before: BAOYING QUTU THERMAL CONTROL SYSTEM CO.,LTD.