CN205642108U - Heat exchanger of porous microchannel section bar - Google Patents
Heat exchanger of porous microchannel section bar Download PDFInfo
- Publication number
- CN205642108U CN205642108U CN201620051442.3U CN201620051442U CN205642108U CN 205642108 U CN205642108 U CN 205642108U CN 201620051442 U CN201620051442 U CN 201620051442U CN 205642108 U CN205642108 U CN 205642108U
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- section bar
- heat exchanger
- heat
- microchannel
- refrigerant
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Abstract
The utility model discloses a heat exchanger of porous microchannel section bar, it relates to a heat transfer device who uses in heat exchange system, including section bar, pipe, inlayer collector, outer collector, refrigerant entry, refrigerant export, heat transferring medium entry, heat exchange medium outlet. Its characterized in that: the section bar circumferencial direction is refrigerant circulation passageway, and the section bar inner chamber is heat exchange media channel, heat exchanger uses a section bar at least, both ends and two refrigerant collectors of section bar directly link to each other, and section bar inner chamber heat exchange media channel passes through pipe and two outer collector intercommunications, the refrigerant is imported and exported and is offered on the inlayer collector, and the exit of heat transferring medium are offered on outer collector, heat exchanger outside bearer bar is used for increasing the structural stiffness of a heat exchanger. Section bar and heat exchanger simple structure, high -efficient heat exchange is realized with the heat transferring medium in the inner chamber passageway to the refrigerant in the section bar microchannel that enables to flow through.
Description
Technical field
This utility model patent relates to heat-exchange system field, particularly to a kind of that do not rely on external environment condition, uses closed dielectric to complete the heat exchanger of heat exchanging process.
Background technology
In existing heat exchanger system, when cold-producing medium flows through condenser or vaporizer, cold-producing medium is by producing heat exchange between copper pipe (or aluminum pipe) and external agency.Copper pipe (or aluminum pipe) surface attachment has fin, to improve heat exchanger effectiveness.After completing heat exchanging process, generally external agency is discharged in open environment.
The heat-exchange system of prior art has following defect: external environment condition is complicated and changeable so that the heat exchanging process between cold-producing medium and air is difficult to be effectively controlled.Owing to extraneous air generally comprises, air-conditioning duct is had corrosive composition, during long-time use, expose aerial heat exchanger and be susceptible to lose efficacy.Narrow space or there is no air occasion in, traditional heat-exchange system is restricted.Meanwhile, because the use of fin, its manufacturing cost is considerably increased.Factors above, increases the difficulty that heat exchanger designs manufactures, adds production cost, reduce the service life of heat exchanger, limit the application scenario of heat exchanger.
Utility model content
The purpose of this utility model patent is to provide between a kind of two media that can make isolation in different channels generation High Efficiency Thermal exchange;For reaching above-mentioned purpose, this utility model patent discloses the heat exchanger of a kind of porous microchannel section bar.
The heat exchanger of a kind of porous microchannel described in the utility model section bar, including section bar (1), conduit (2), internal layer collector (3,4), outer layer collector (5,6), refrigerant inlet (7) and outlet (8), heat transferring medium entrance (9) and outlet (10);Every root type material circumferentially has multiple cold-producing medium microchannel (11~18) and heat exchanging medium passage (19), the described passage on section bar (1) circumference is cold-producing medium microchannel (11~18), section bar bore passages is heat exchanging medium passage (19), cold-producing medium and heat transferring medium are via being located at different collector (3,5) entrance (7 on, 9) input heat exchanger, by different collectors (4,6) outlet (8,10) on is flowed out from heat exchanger.
Further, on every root type material (1) circumference, the quantity of described cold-producing medium microchannel (11~18) is 2 to 26.
Further, in every root type material (1) inner chamber, the quantity of heat exchanging medium passage (19) is 1.
Further, internal at section bar (1), described cold-producing medium microchannel (11~18) do not produce with heat exchanging medium passage (19) and connect.
Further, described cold-producing medium microchannel (11~18) two ends and internal layer collector (3,4) directly connect, and refrigerant inlet (7) and outlet (8) are opened on two internal layer collectors (3,4) respectively;Heat exchanging medium passage (19) is connected with outer layer collector (5,6) at two ends by conduit (2),
Further, in described heat exchanger manufacture process, at least use 1 described section bar (1).
Further, at least one fender bracket (20,21) increasing structural stability it is provided with outside described heat exchanger.
Accompanying drawing explanation
The present invention is further described with embodiment below in conjunction with the accompanying drawings.
Fig. 1 is this utility model patent heat exchanger schematic cross-section.
Fig. 2 is this utility model patent heat exchanger perspective view.
Fig. 3 is this utility model patent system coolant channel and the cross section view of heat exchanging medium passage.
In Fig. 1,2,3,1 is section bar, and 2 is conduit, and 3,4 is internal layer collector; 5,6 is outer layer collector, and 7 is refrigerant inlet, and 8 is refrigerant outlet, and 9 is heat transferring medium entrance; 10 export for heat transferring medium, and 11~18 is cold-producing medium microchannel, and 19 is heat exchanging medium passage, and 20,21 is fender bracket.
Detailed description of the invention
This utility model patent is further described by the example shown in below in conjunction with the accompanying drawings.
Such as Fig. 1, shown in 2, this utility model patent provides the heat exchanger of a kind of porous microchannel section bar.Mainly include section bar (1), conduit (2), internal layer collector (3,4), outer layer collector (5,6), refrigerant inlet (7), refrigerant outlet (8), heat transferring medium entrance (9), heat transferring medium outlet (10).For every root type material, on circumference, cold-producing medium microchannel (11~18) number is 8, and internal heat medium channel (19) number is 1.2 fender brackets (20,21) it are provided with outside heat exchanger.
As shown in Figure 3, in the present embodiment, cold-producing medium is conveyed into heat exchanger by the entrance (7) on internal layer collector (3), the chamber of collector (3) directly connects with the cold-producing medium microchannel (11~18) of many root type material (1), and the heat exchanging medium passage (19) internal with section bar (1) does not connects.Heat transferring medium entrance (9) inflow heat exchanger on collector (5), the chamber of collector (5) is connected with the heat exchanging medium passage of section bar (1) by conduit (2), and does not connects with the cold-producing medium microchannel (11~18) of section bar (1).Conduit (2) plays the effect that the heat exchanging medium passage (19) making section bar (1) connects with outer layer collector (5,6).
Cold-producing medium enters internal layer collector (4) through the cold-producing medium microchannel (11~18) of section bar (1);Meanwhile, heat transferring medium flows into outer layer collector (6) through the heat exchanging medium passage (19) of section bar (1).High Efficiency Thermal exchange between cold-producing medium and heat transferring medium occurs during two kinds of fluids flow in section bar (1) inner passage simultaneously, and two media flow direction in section bar (1) is contrary.After completing heat exchange, cold-producing medium is via outlet (8) outflow heat exchanger of collector (4);Heat transferring medium is via outlet (10) outflow heat exchanger of collector (6).
Owing to heat exchanging medium passage is closed in heat exchanger, heat exchanger can select fluid that thermal capacitance is high as heat transferring medium, and is not limited to air and aqueous water, is conducive to expanding the range of choice of heat transferring medium, improves heat exchange efficiency.The heat transferring medium of inflow heat exchanger is in stable condition controlled, and the design for heat exchange control system is provided convenience.Heat transferring medium is in use closed in pipe-line system, will not be polluted by impurity.Heat exchanger pipeline system itself will not be conducive to improving the service life of heat exchanger because heat transferring medium is by corrosion failure.Owing to profile design make use of microchannel enhanced heat exchange mechanism, whole heat exchanger size is little, lightweight, compact conformation, can be applicable to narrow space and the occasion of environmental condition harshness.
The purpose of above-described embodiment is to illustrate design and the feature of this utility model patent, is to allow professional will appreciate that the content of this utility model patent and to implement according to this, without limiting the protection domain of this utility model patent.All equivalence changes done according to this utility model patent statement essence, within all should being included in the protection domain of this utility model patent.
Claims (6)
1. the heat exchanger of a porous microchannel section bar, including section bar (1), conduit (2), internal layer collector (3,4), outer layer collector (5,6), refrigerant inlet (7) and outlet (8), heat transferring medium entrance (9) and outlet (10);Every root type material circumferentially has multiple cold-producing medium microchannel (11~18) and heat exchanging medium passage (19);It is characterized in that: section bar (1) is internal comprises two kinds of fluid passages, wherein on circumference for cold-producing medium microchannel (11~18), section bar inner chamber is heat exchanging medium passage (19);Cold-producing medium microchannel (11~18) two ends and internal layer collector (3,4) directly connect, and refrigerant inlet (7) and refrigerant outlet (8) are opened on two internal layer collectors (3,4) respectively;The heat exchanging medium passage (19) of section bar (1) passes through conduit (2) at two ends and outer layer collector (5,6) connection, outer layer collector (5,6) is provided with heat transferring medium entrance (9) and outlet (10).
The heat exchanger of a kind of porous microchannel the most according to claim 1 section bar, it is characterised in that: the quantity of the cold-producing medium microchannel (11~18) that described section bar (1) has is 2 to 26.
The heat exchanger of a kind of porous microchannel the most according to claim 2 section bar, it is characterised in that: the quantity of the heat exchanging medium passage (19) that described section bar (1) has is 1.
The heat exchanger of a kind of porous microchannel the most according to claim 3 section bar, it is characterised in that: described section bar (1) is internal, and cold-producing medium microchannel (11~18) do not produce with heat exchanging medium passage (19) and connect.
The heat exchanger of a kind of porous microchannel the most according to claim 4 section bar, it is characterised in that: described section bar (1) at least uses 1.
The heat exchanger of a kind of porous microchannel the most according to claim 5 section bar, it is characterised in that: have at least one fender bracket (20,21) outside the heat exchanger of described a kind of porous microchannel section bar.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620051442.3U CN205642108U (en) | 2016-01-19 | 2016-01-19 | Heat exchanger of porous microchannel section bar |
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CN201620051442.3U CN205642108U (en) | 2016-01-19 | 2016-01-19 | Heat exchanger of porous microchannel section bar |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108106174A (en) * | 2017-12-08 | 2018-06-01 | 广东纽恩泰新能源科技发展有限公司 | Microchannel tubing heat exchanger |
CN111721147A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Heat exchange unit and heat exchange reactor |
-
2016
- 2016-01-19 CN CN201620051442.3U patent/CN205642108U/en active Active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108106174A (en) * | 2017-12-08 | 2018-06-01 | 广东纽恩泰新能源科技发展有限公司 | Microchannel tubing heat exchanger |
CN111721147A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Heat exchange unit and heat exchange reactor |
CN111721147B (en) * | 2019-03-22 | 2022-02-25 | 中国石油化工股份有限公司 | Heat exchange unit and heat exchange reactor |
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CP01 | Change in the name or title of a patent holder |
Address after: 213300 No. 5 Feiyue Road, Shanghuang Town Industrial Concentration Zone, Liyang City, Changzhou City, Jiangsu Province Patentee after: Jiangsu Gongchang Precision Aluminum Industry Co., Ltd. Address before: 213300 No. 5 Feiyue Road, Shanghuang Town Industrial Concentration Zone, Liyang City, Changzhou City, Jiangsu Province Patentee before: JIANGSU HANGGANG PRECISION ALUMINUM CO., LTD. |