CN204665988U - Multipaths micropore heat exchanger - Google Patents

Multipaths micropore heat exchanger Download PDF

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Publication number
CN204665988U
CN204665988U CN201520334488.1U CN201520334488U CN204665988U CN 204665988 U CN204665988 U CN 204665988U CN 201520334488 U CN201520334488 U CN 201520334488U CN 204665988 U CN204665988 U CN 204665988U
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China
Prior art keywords
flow channel
cold
collector
medium
multipaths
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CN201520334488.1U
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Chinese (zh)
Inventor
吴维武
袁振钦
王东宝
陈伟
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SHANGHAI RICHTECH CO Ltd
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SHANGHAI RICHTECH CO Ltd
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Abstract

The utility model provides a kind of multipaths micropore heat exchanger, its thermal medium inlet collector, thermal medium outlet collector lays respectively at the relative both sides of main part, heat medium flow channel linearly extends, cold medium inlet collector, cold media outlet collector lays respectively at two relative diagonal positions of main part, cold media flow channel is first from collector place, cold medium inlet, the edge of cold medium plate is extended to along the direction perpendicular with heat medium flow channel, revolution extends to another edge of cold medium plate along the direction perpendicular with heat medium flow channel again, the roundabout advance of cold media flow channel is until be connected with cold media outlet collector.This multipaths micropore heat exchanger, has larger heat exchange area, adopts multipaths runner and the mode that single process runner is combined simultaneously, ensure that efficient exchange capability of heat; Structurally adopt Optical Electro-Chemistry etching technics and atoms permeating processes to manufacture, ensure that the ability of the high temperature high voltage resistant of heat exchange core body, version is simple.

Description

Multipaths micropore heat exchanger
Technical field
The utility model relates to a kind of multipaths micropore heat exchanger.
Background technology
Heat exchanger has various ways, and as finned heat exchanger, plate type heat exchanger, double pipe heat exchanger, shell-and-tube heat exchanger etc., different heat exchangers is for different use occasions.
Along with the development of the industry such as Aero-Space, petrochemical industry, the demand for heat exchanger is also more and more extensive, and the requirement of heat exchanger is also more and more higher simultaneously.If Aerospace Engineering equipment is because of limited space, often need to adopt the compact heat exchanger that size is little, lightweight, heat transfer efficiency is high; Petroleum chemical industry due to traditional heat exchangers bulky, install complicated, the low inferior shortcoming of heat exchange efficiency, also need to adopt lightweight, compact, the new type heat exchanger easily installed.
The company producing micropore heat exchanger in the world at present only has Heatric company of Britain, defines the situation of dominance.Exploitation has the micropore heat exchanger of independent intellectual property right, all significant for China's oil chemical industry, aerospace industries.Traditional micropore heat exchanger adopts single process liquid form, and heat exchange efficiency has certain limitation.The utility model is based on traditional single process runner, carries out technological improvement, adopts multipaths runner and single process runner combination, realizes high efficient heat exchanging.
Utility model content
The shortcoming of prior art in view of the above, the purpose of this utility model is to provide a kind of multipaths micropore heat exchanger, adopts single process liquid form, heat exchange efficiency has the problem of certain limitation for solving heat exchanger traditional in prior art.
For achieving the above object and other relevant objects, the utility model provides a kind of multipaths micropore heat exchanger, it comprises main part, main part is fixed with at least one heat exchange core body, heat exchange core body comprises base plate, top board and is clipped in the cold medium plate of at least one deck, at least one deck thermal medium plate between base plate, top board, cold medium plate, thermal medium plate are alternately stacked, cold medium plate is etched with many cold media flow channels be parallel to each other, thermal medium plate is etched with many heat medium flow channels be parallel to each other, main part is also provided with thermal medium inlet collector, thermal medium outlet collector, cold medium inlet collector and cold media outlet collector, thermal medium inlet collector, thermal medium outlet collector are communicated with the two ends of heat medium flow channel respectively, and cold medium inlet collector, cold media outlet collector are communicated with the two ends of cold media flow channel respectively, thermal medium inlet collector, thermal medium outlet collector lays respectively at the relative both sides of main part, heat medium flow channel linearly extends, cold medium inlet collector, cold media outlet collector lays respectively at two relative diagonal positions of main part, cold media flow channel is first from collector place, cold medium inlet, the edge of cold medium plate is extended to along the direction perpendicular with heat medium flow channel, revolution extends to another edge of cold medium plate along the direction perpendicular with heat medium flow channel again, the roundabout advance of cold media flow channel is until be connected with cold media outlet collector.
Preferably, cold media flow channel is covered with cold medium plate.
Preferably, heat medium flow channel is provided with multiple bend along flowing to, along flowing to complications forward.
Preferably, the cross section of heat medium flow channel is semicircle.
Preferably, heat medium flow channel is formed by Optical Electro-Chemistry etching technics etching.
Preferably, cold media flow channel is provided with multiple bend along flowing to, along flowing to complications forward.
Preferably, the cross section of cold media flow channel is semicircle.
Preferably, cold media flow channel is formed by Optical Electro-Chemistry etching technics etching.
Preferably, the cold medium plate of multilayer, thermal medium plate form integral structure by atoms permeating mode is molten mutually.
Preferably, thermal medium inlet collector, thermal medium outlet collector, cold medium inlet collector and cold media outlet collector are connected as a single entity by welding manner and main part.
As mentioned above, the utility model multipaths micropore heat exchanger, has following beneficial effect:
1, heat transfer area density is high, and heat exchange efficiency is high;
2, in manufacturing process, adopt Optical Electro-Chemistry etching and atoms permeating adhering technique, the channel design of various shape can be formed, its heat exchange core body is made up of unique fertile material, without the need to pad and welding, effectively can reduce leakage and vibration loss, improve service life;
3, from a structural point, this kind of micropore heat exchanger runner effectively can reduce pressure drop, reduces the impact blocking and bring;
4, adopt integral structure, this kind of micropore heat exchanger can anti-high and low-temp and high pressure requirement, and reduce the application of pipeline and valve, Stability Analysis of Structures, security is good, and size is little, lightweight, easy for installation, Maintenance free simultaneously.
Accompanying drawing explanation
Fig. 1 is shown as the structural representation of the utility model multipaths micropore heat exchanger.
Fig. 2 is shown as the left view of the multipaths micropore heat exchanger shown in Fig. 1.
Fig. 3 is shown as the sectional view of the heat exchange core body of the multipaths micropore heat exchanger shown in Fig. 1.
Fig. 4 is shown as the partial enlarged drawing of the heat exchange core body of the multipaths micropore heat exchanger shown in Fig. 3.
Fig. 5 is shown as the structural representation of the thermal medium plate of the multipaths micropore heat exchanger shown in Fig. 1.
Fig. 6 is shown as the structural representation of the cold medium plate of the multipaths micropore heat exchanger shown in Fig. 1.
Fig. 7 a is shown as the cold medium inlet collector of the multipaths micropore heat exchanger shown in Fig. 1, the structural representation of cold media outlet collector.
Fig. 7 b be shown as the cold medium inlet collector of the multipaths micropore heat exchanger shown in Fig. 7 a, cold media outlet collector A-A to schematic diagram.
Fig. 7 c be shown as the cold medium inlet collector of the multipaths micropore heat exchanger shown in Fig. 7 a, cold media outlet collector B-B to schematic diagram.
Fig. 8 a is shown as the thermal medium inlet collector of multipaths micropore heat exchanger shown in Fig. 1, the structural representation of thermal medium outlet collector.
Fig. 8 b be shown as the thermal medium inlet collector of the multipaths micropore heat exchanger shown in Fig. 8 a, thermal medium outlet collector A-A to schematic diagram.
Fig. 8 c be shown as the thermal medium inlet collector of the multipaths micropore heat exchanger shown in Fig. 8 a, thermal medium outlet collector B-B to schematic diagram.
Element numbers explanation
1 main part
2 heat exchange core bodies
21 base plates
22 top boards
23 cold medium plates
24 thermal medium plates
25 cold media flow channels
26 heat medium flow channels
3 thermal medium inlet collector
4 thermal medium outlet collectors
5 cold medium inlet collectors
6 cold media outlet collectors
Detailed description of the invention
By particular specific embodiment, embodiment of the present utility model is described below, person skilled in the art scholar the content disclosed by this description can understand other advantages of the present utility model and effect easily.
Refer to Fig. 1 to Fig. 8 c.Notice, structure, ratio, size etc. that this description institute accompanying drawings illustrates, content all only in order to coordinate description to disclose, understand for person skilled in the art scholar and read, and be not used to limit the enforceable qualifications of the utility model, therefore the not technical essential meaning of tool, the adjustment of the modification of any structure, the change of proportionate relationship or size, do not affecting under effect that the utility model can produce and the object that can reach, all should still drop in scope that technology contents that the utility model discloses can contain.Simultaneously, quote in this description as " on ", D score, "left", "right", " centre " and " one " etc. term, also only for ease of understanding of describing, and be not used to limit the enforceable scope of the utility model, the change of its relativeness or adjustment, under changing technology contents without essence, when being also considered as the enforceable category of the utility model.
As shown in Fig. 1 to Fig. 8 c, the utility model provides a kind of multipaths micropore heat exchanger, it comprises main part 1, main part 1 is fixed with at least one heat exchange core body 2, heat exchange core body 2 comprises base plate 21, top board 22 and is clipped in the cold medium plate 23 of at least one deck, at least one deck thermal medium plate 24 between base plate 21, top board 22, cold medium plate 23, thermal medium plate 24 are alternately stacked, cold medium plate 23 is etched with many cold media flow channels be parallel to each other 25, thermal medium plate 24 is etched with many heat medium flow channels be parallel to each other 26, main part 1 is also provided with thermal medium inlet collector 3, thermal medium outlet collector 4, cold medium inlet collector 5 and cold media outlet collector 6, thermal medium inlet collector 3, thermal medium outlet collector 4 are communicated with the two ends of heat medium flow channel 26 respectively, and cold medium inlet collector 5, cold media outlet collector 6 are communicated with the two ends of cold media flow channel 25 respectively, thermal medium inlet collector 3, thermal medium outlet collector 4 lays respectively at the relative both sides of main part 1, heat medium flow channel 26 linearly extends, cold medium inlet collector 5, cold media outlet collector 6 lays respectively at two relative diagonal positions of main part 1, cold media flow channel 25 is first from collector 5 place, cold medium inlet, the edge of cold medium plate 23 is extended to along the direction perpendicular with heat medium flow channel 26, revolution extends to another edge of cold medium plate 23 along the direction perpendicular with heat medium flow channel 26 again, the roundabout advance of cold media flow channel 25 is until be connected with cold media outlet collector 6.
The effect of thermal medium inlet collector 3 thermal medium is entered and is diverted to each heat medium flow channel 26, and the effect of thermal medium outlet collector 4 is to thermal medium afflux and discharges; The effect of cold medium inlet collector 5 cold medium is entered and is diverted to each cold media flow channel 25, and the effect of cold media outlet collector 6 is to cold medium afflux and discharges.
Cold medium plate 23, thermal medium plate 24 are alternately stacked, make thermal medium, cold medium carry out heat exchange in by the process in heat medium flow channel 26, cold media flow channel 25.Cold medium is entered by cold medium inlet collector 5, and shunting enters each cold media flow channel 25, after heat exchange heating, converges to cold media outlet collector 6 and discharges; Thermal medium is entered by thermal medium inlet collector 3, and shunting enters each heat medium flow channel 26, after heat exchange cooling, converges to thermal medium outlet collector 4 and discharges.
The flow direction of heat medium flow channel 26 adopts the mode of the roundabout advance of S type, can improve the length of heat medium flow channel 26, thus improve the heat exchange efficiency of this heat exchanger; Solid matter many cold media flow channels 25 also keeping parallelism on every layer of cold medium plate 23, heat medium flow channel 26 is covered with every layer of thermal medium plate 24, adds the space availability ratio of cold medium plate 23, thermal medium plate 24.
As shown in Figure 5 to Figure 6, cold media flow channel 25, heat medium flow channel 26 are provided with multiple bend along the flow direction, in Z-shaped along flowing to complications forward.This design adds the entire length of cold media flow channel 25, heat medium flow channel 26, adds the heat exchange area of cold medium plate 23, thermal medium plate 24.
As shown in Figure 4, the cross section of cold media flow channel 25, heat medium flow channel 26 is semicircle, is formed by Optical Electro-Chemistry etching technics etching.
As shown in Figure 3, the cold medium plate 23 of above-mentioned multilayer, thermal medium plate 24 form integral structure by atoms permeating mode is molten mutually, and at two sides welding upper plate 21, top board 22, ensure that independence and the closure of every bar cold media flow channel 25, heat medium flow channel 26.
Thermal medium inlet collector 3, thermal medium outlet collector 4, cold medium inlet collector 5 and cold media outlet collector 6 are connected as a single entity by welding manner and main part 1, form a complete heat exchanger, whole heat exchanger is integral structure, cannot dismantle, indivisible.
The utility model multipaths micropore heat exchanger has the following advantages:
1, heat transfer area density is high, and heat exchange efficiency is high;
2, in manufacturing process, adopt Optical Electro-Chemistry etching and atoms permeating adhering technique, the channel design of various shape can be formed, its heat exchange core body is made up of unique fertile material, without the need to pad and welding, effectively can reduce leakage and vibration loss, improve service life;
3, from a structural point, this kind of micropore heat exchanger runner effectively can reduce pressure drop, reduces the impact blocking and bring;
4, adopt integral structure, this kind of micropore heat exchanger can anti-high and low-temp and high pressure requirement, and reduce the application of pipeline and valve, Stability Analysis of Structures, security is good, and size is little, lightweight, easy for installation, Maintenance free simultaneously.
In sum, the utility model multipaths micropore heat exchanger, has larger heat exchange area, adopts multipaths runner and the mode that single process runner is combined simultaneously, ensure that efficient exchange capability of heat; Structurally adopt the manufacture of atoms permeating processes, ensure that the ability of the high temperature high voltage resistant of heat exchange core body, stability is high, and version is simple.So the utility model effectively overcomes various shortcoming of the prior art and tool high industrial utilization.
Above-described embodiment is illustrative principle of the present utility model and effect thereof only, but not for limiting the utility model.Any person skilled in the art scholar all without prejudice under spirit of the present utility model and category, can modify above-described embodiment or changes.Therefore, such as have in art and usually know that the knowledgeable modifies or changes not departing from all equivalences completed under the spirit and technological thought that the utility model discloses, must be contained by claim of the present utility model.

Claims (10)

1. a multipaths micropore heat exchanger, it is characterized in that: it comprises main part (1), described main part (1) is fixed with at least one heat exchange core body (2), described heat exchange core body (2) comprises base plate (21), top board (22) and be clipped in described base plate (21), the cold medium plate (23) of at least one deck between top board (22), at least one deck thermal medium plate (24), described cold medium plate (23), thermal medium plate (24) is alternately stacked, described cold medium plate (23) is etched with many cold media flow channels be parallel to each other (25), described thermal medium plate (24) is etched with many heat medium flow channels be parallel to each other (26), described main part (1) is also provided with thermal medium inlet collector (3), thermal medium outlet collector (4), cold medium inlet collector (5) and cold media outlet collector (6), described thermal medium inlet collector (3), thermal medium outlet collector (4) are communicated with the two ends of described heat medium flow channel (26) respectively, and described cold medium inlet collector (5), cold media outlet collector (6) are communicated with the two ends of described cold media flow channel (25) respectively, described thermal medium inlet collector (3), thermal medium outlet collector (4) lays respectively at the relative both sides of described main part (1), described heat medium flow channel (26) linearly extends, described cold medium inlet collector (5), cold media outlet collector (6) lays respectively at two relative diagonal positions of described main part (1), described cold media flow channel (25) is first from collector (5) place, described cold medium inlet, the edge of cold medium plate (23) is extended to along the direction perpendicular with described heat medium flow channel (26), revolution extends to another edge of cold medium plate (23) along the direction perpendicular with heat medium flow channel (26) again, described cold media flow channel (25) roundabout advance is until be connected with cold media outlet collector (6).
2. multipaths micropore heat exchanger according to claim 1, is characterized in that: described cold media flow channel (25) is covered with described cold medium plate (23).
3. multipaths micropore heat exchanger according to claim 1, is characterized in that: described heat medium flow channel (26) is provided with multiple bend along flowing to, along flowing to complications forward.
4. multipaths micropore heat exchanger according to claim 1, is characterized in that: the cross section of described heat medium flow channel (26) is for semicircle.
5. multipaths micropore heat exchanger according to claim 1, is characterized in that: described heat medium flow channel (26) is formed by Optical Electro-Chemistry etching technics etching.
6. multipaths micropore heat exchanger according to claim 1, is characterized in that: described cold media flow channel (25) is provided with multiple bend along flowing to, along flowing to complications forward.
7. multipaths micropore heat exchanger according to claim 1, is characterized in that: the cross section of described cold media flow channel (25) is for semicircle.
8. multipaths micropore heat exchanger according to claim 1, is characterized in that: described cold media flow channel (25) is formed by Optical Electro-Chemistry etching technics etching.
9. multipaths micropore heat exchanger according to claim 1, is characterized in that: described cold medium plate (23), thermal medium plate (24) form integral structure by atoms permeating mode is molten mutually.
10. multipaths micropore heat exchanger according to claim 1, is characterized in that: described thermal medium inlet collector (3), thermal medium outlet collector (4), cold medium inlet collector (5) and cold media outlet collector (6) are connected as a single entity by welding manner and main part (1).
CN201520334488.1U 2015-05-21 2015-05-21 Multipaths micropore heat exchanger Active CN204665988U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520334488.1U CN204665988U (en) 2015-05-21 2015-05-21 Multipaths micropore heat exchanger

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Application Number Priority Date Filing Date Title
CN201520334488.1U CN204665988U (en) 2015-05-21 2015-05-21 Multipaths micropore heat exchanger

Publications (1)

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CN204665988U true CN204665988U (en) 2015-09-23

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104833245A (en) * 2015-05-21 2015-08-12 上海利策科技股份有限公司 Multi-path micro-hole heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104833245A (en) * 2015-05-21 2015-08-12 上海利策科技股份有限公司 Multi-path micro-hole heat exchanger

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