CN204301586U - Porous ripple fin-type plate-fin heat exchanger - Google Patents

Porous ripple fin-type plate-fin heat exchanger Download PDF

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Publication number
CN204301586U
CN204301586U CN201420654356.2U CN201420654356U CN204301586U CN 204301586 U CN204301586 U CN 204301586U CN 201420654356 U CN201420654356 U CN 201420654356U CN 204301586 U CN204301586 U CN 204301586U
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China
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fin
heat exchange
plate
heat exchanger
heat
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CN201420654356.2U
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Chinese (zh)
Inventor
刘伟
李东明
李志奎
范柏
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Harbin broad power technology development Co., Ltd.
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703th Research Institute of CSIC
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Abstract

The utility model proposes porous ripple fin-type plate-fin heat exchanger.Existing plate-fin heat exchanger is made up of heat exchange fin, dividing plate, strip of paper used for sealing, flow deflector, end plate, end socket and fluid inlet and outlet adapter etc., when existing structure is constant, in conjunction with the feature of corrugated fin and perforated fin, the corrugation length direction of corrugated fin is beaten many densely covered keyhole formation porous ripple fins, when heat exchanging fluid flows in runner, porous makes thermal resistance boundary layer constantly break, serve the effect of enhanced heat exchange, the heat transfer efficiency of heat exchange fin is increased.Owing to adopting technique scheme, achieve and utilize porous ripple fin to form plate-fin heat exchanger, it is enhanced heat exchange effect not only, improves the heat transfer efficiency of heat exchange fin, and makes the structure of this plate-fin heat exchanger compacter.

Description

Porous ripple fin-type plate-fin heat exchanger
technical field:
The utility model relates to technical field of heat exchangers, specifically a kind of porous ripple fin-type plate-fin heat exchanger.
background technology:
Along with the development of modern science technology, all need heat exchanger from petro chemical industry to universe industry, of a great variety due to heat exchanger, carry out classification according to the shape of its heat-transfer surface and structure and can be divided into cast, template and other pattern heat exchangers.And tube type heat exchangers can be divided into coil heat exchanger, double pipe heat exchanger, shell-and-tube; Plate type regenerator can be divided into spiral heat exchanger, plate type heat exchanger, lamella heat exchanger and plate-fin heat exchanger.The heat transmission equipment of the advantage that plate-fin heat exchanger is a kind of compact conformation, quality is light, heat transfer efficiency is high and good economy performance etc. is given prominence to, be separated at the cryogenic separation of separation and liquefaction, the ethene of Aero-Space, refrigeration air-conditioner, air separation, oil gas field, synthetic ammonia tailgas, the field such as dynamic power machine, natural gas, atomic energy obtain applying more and more widely, and utilizing heat energy, recovery waste heat, economize in raw materials, to reduce costs etc. in achieve significant economic benefit.Plate-fin heat exchanger is by taking over, end socket, the compositions such as heat exchange core body, heat exchange core body is made up of some basic flow passage units and end plate, basic flow passage unit is by heat exchange fin, flow deflector, dividing plate and strip of paper used for sealing composition, several such flow passage units are integral according to the stacked soldering of fluid-flow mode, cold fluid and hot fluid flow in adjacent basic flow passage unit, heat exchange is carried out by heat exchange fin and with dividing plate, heat exchange fin is the minimum unit of plate-fin heat exchanger, heat exchange major part between cold fluid and hot fluid passes through heat exchange fin, fraction is directly undertaken by dividing plate.In normal design, heat exchange fin heat exchange area is approximately 67% ~ 88% of the total heat exchange area of heat exchanger, connection between heat exchange fin and dividing plate is perfect soldering, therefore most of heat passes to heat exchange fin, cold fluid is passed to by dividing plate by heat exchange fin, due to heat exchange direct heat transfer unlike dividing plate of heat exchange fin, therefore heat exchange fin has again the title on " secondary surface ", and secondary heat exchange face is generally low than the heat transfer efficiency of a heat-transfer surface.The type of heat exchange fin and physical dimension are the key factors affecting heat exchanger performance, conventional heat exchange fin has the structural shapes such as plain fin, saw tooth fin, perforated fin, corrugated fin, from heat transfer effect aspect, heat exchange fin is that enhanced heat exchange is carried out in the disturbance of the development and reinforcement fluid utilizing the discontinuity of geometry to destroy flow boundary layer air, is favourable to raising heat transfer effect.
summary of the invention:
The task of the utility model patent is to provide a kind of plate-fin heat exchanger, do not changing the physical dimension of the processing technology of existing heat exchange fin, process equipment and fin, adopt novel heat exchange fin, not only increase the heat transfer efficiency of heat exchange fin, and make the structure of plate-fin heat exchanger compacter.
The technical solution of the utility model is: existing plate-fin heat exchanger processing technology and structure constant when, in conjunction with the feature of corrugated fin and perforated fin, the surface of the corrugation length of corrugated fin is beaten many densely covered apertures, obtain a kind of porous ripple fin with loose structure feature, existing corrugated fin is replaced with this heat exchange fin, when heat exchanging fluid flows in runner, many densely covered apertures make thermal resistance boundary layer constantly break, serve the effect of enhanced heat exchange, the heat transfer efficiency of heat exchange fin is increased;
Porous ripple fin-type plate-fin heat exchanger, by heat exchange core body, end socket and fluid inlet and outlet adapter composition, heat exchange core body is made up of the end plate of some basic flow passage units and both sides, each basic flow passage unit is by heat exchange fin, flow deflector, dividing plate and strip of paper used for sealing composition, the surface of the corrugation length of corrugated fin is beaten many densely covered apertures and obtains a kind of novel porous corrugated fin with loose structure feature, stacked for several flow passage units soldering is become porous ripple fin-type plate-fin heat exchanger, cold fluid and hot fluid flow in adjacent basic flow passage unit, heat exchange is carried out by porous ripple fin and dividing plate.
The utility model has following beneficial effect: owing to adopting technique scheme, achieve and utilize novel porous corrugated fin composing plate fin heat exchanger, it is enhanced heat exchange effect not only, improves the heat transfer efficiency of heat exchange fin, and makes the structure of plate-fin heat exchanger compacter.
accompanying drawing illustrates:
Accompanying drawing 1 is contour structures schematic diagram of the present utility model;
Accompanying drawing 2 is profiles of accompanying drawing 1;
Accompanying drawing 3 ~ 4 is shape assumption diagrams of common porous and corrugated fin;
Accompanying drawing 5 is shape assumption diagrams of porous ripple fin in the utility model.
1. fluid inlet and outlet adapters in figure, 2. end socket, 3. flow deflector, 4. heat exchange fin, 5. dividing plate, 6. strip of paper used for sealing, 7. end plate, 8. cold fluid, 9. hot fluid, 12. perforated fins, 13. corrugated fins, 14. porous ripple fins.
detailed description of the invention:
Below in conjunction with accompanying drawing, the utility model is described in further detail:
Shown in Fig. 1 composition graphs 2 ~ Fig. 5, porous ripple fin-type plate-fin heat exchanger, by heat exchange core body, end socket 2 and fluid inlet and outlet adapter 1 form, heat exchange core body is made up of the end plate 7 of some basic flow passage units and both sides, each basic flow passage unit is by heat exchange fin 4, flow deflector 3, dividing plate 5 and strip of paper used for sealing 6 form, the surface of the corrugation length of corrugated fin is beaten many densely covered apertures and obtains a kind of novel porous corrugated fin 14 with loose structure feature, stacked for several flow passage units soldering is become porous ripple fin-type plate-fin heat exchanger, cold fluid 8 and hot fluid 9 flow in adjacent basic flow passage unit, heat exchange is carried out by porous ripple fin 14 and dividing plate 5.
In conjunction with the advantage of corrugated fin and perforated fin, obtain a kind of corrugated fin with perforated fin design feature, existing corrugated fin is replaced with this New type corrugated fin, when heat exchanging fluid flows in runner, porous makes thermal resistance boundary layer constantly break, serve the effect of enhanced heat exchange, improve the heat transfer efficiency of heat exchange fin, thus make the structure of plate-fin heat exchanger compacter.

Claims (1)

1. a porous ripple fin-type plate-fin heat exchanger, by heat exchange core body, end socket (2) and fluid inlet and outlet adapter (1) composition, it is characterized in that: heat exchange core body is made up of the end plate (7) of some basic flow passage units and both sides, each basic flow passage unit is by heat exchange fin (4), flow deflector (3), dividing plate (5) and strip of paper used for sealing (6) composition, the surface of the corrugation length of corrugated fin is beaten many densely covered apertures and obtains a kind of novel porous corrugated fin (14) with loose structure feature, stacked for several flow passage units soldering is become porous ripple fin-type plate-fin heat exchanger, cold fluid (8) and hot fluid (9) flow in adjacent basic flow passage unit, heat exchange is carried out by porous ripple fin (14) and dividing plate (5).
CN201420654356.2U 2014-11-05 2014-11-05 Porous ripple fin-type plate-fin heat exchanger Active CN204301586U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420654356.2U CN204301586U (en) 2014-11-05 2014-11-05 Porous ripple fin-type plate-fin heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420654356.2U CN204301586U (en) 2014-11-05 2014-11-05 Porous ripple fin-type plate-fin heat exchanger

Publications (1)

Publication Number Publication Date
CN204301586U true CN204301586U (en) 2015-04-29

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Country Status (1)

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CN (1) CN204301586U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104390508A (en) * 2014-11-05 2015-03-04 中国船舶重工集团公司第七�三研究所 Porous wavy fin template fin heat exchanger
CN105627808A (en) * 2015-12-31 2016-06-01 北京航空航天大学 Novel heat exchanger core and distribution structure
CN105854775A (en) * 2016-06-06 2016-08-17 徐州工程学院 Production device special for manganese slag light tile additive, working method and manufacturing method of key parts of production device
CN109883238A (en) * 2019-03-08 2019-06-14 西安交通大学 A kind of plate fin type heat exchanger core and its fin structure
CN110088455A (en) * 2016-12-26 2019-08-02 株式会社科伦斯 Cooler for recycled exhaust gas corrugated plate
CN112832988A (en) * 2021-01-13 2021-05-25 无锡宏盛换热器制造股份有限公司 Cooler of compressor

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104390508A (en) * 2014-11-05 2015-03-04 中国船舶重工集团公司第七�三研究所 Porous wavy fin template fin heat exchanger
CN105627808A (en) * 2015-12-31 2016-06-01 北京航空航天大学 Novel heat exchanger core and distribution structure
CN105854775A (en) * 2016-06-06 2016-08-17 徐州工程学院 Production device special for manganese slag light tile additive, working method and manufacturing method of key parts of production device
CN110088455A (en) * 2016-12-26 2019-08-02 株式会社科伦斯 Cooler for recycled exhaust gas corrugated plate
CN110088455B (en) * 2016-12-26 2020-11-13 株式会社科伦斯 Corrugated sheet for EGR cooler
CN109883238A (en) * 2019-03-08 2019-06-14 西安交通大学 A kind of plate fin type heat exchanger core and its fin structure
CN112832988A (en) * 2021-01-13 2021-05-25 无锡宏盛换热器制造股份有限公司 Cooler of compressor

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20151211

Address after: 150090 No. 35, Honghu Road, Yingbin Road, Harbin hi tech Development Zone, Heilongjiang, China

Patentee after: Harbin broad power technology development Co., Ltd.

Address before: 150000 Honghu Road, Daoli District, Heilongjiang, No. 35, Harbin

Patentee before: No.703 Inst. China Ship Heavy Industry Group Co.