CN108240719A - Net formula heat exchanger - Google Patents
Net formula heat exchanger Download PDFInfo
- Publication number
- CN108240719A CN108240719A CN201611227752.7A CN201611227752A CN108240719A CN 108240719 A CN108240719 A CN 108240719A CN 201611227752 A CN201611227752 A CN 201611227752A CN 108240719 A CN108240719 A CN 108240719A
- Authority
- CN
- China
- Prior art keywords
- radiating subassembly
- refrigerant
- heat exchanger
- refrigerant flow
- net formula
- Prior art date
- 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.)
- Pending
Links
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
- F25B39/00—Evaporators; Condensers
-
- 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
- F25B2339/00—Details of evaporators; Details of condensers
-
- 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
- F25B2500/00—Problems to be solved
- F25B2500/09—Improving heat transfers
Abstract
The invention discloses a kind of net formula heat exchangers.Net formula heat exchanger, including isocon, collecting pipe and radiating subassembly, the radiating subassembly is in integrally hollow type network, is formed with several interconnected refrigerant flow paths in the radiating subassembly, the radiating subassembly is connected between the isocon and the collecting pipe.Concentrated supply refrigerant and unified collection refrigerant are realized by isocon and collecting pipe, and the radiating subassembly between isocon and collecting pipe is in integrally hollow type network, several interconnected refrigerant flow paths are formed inside radiating subassembly, refrigerant refrigerant flow path flowing different in radiating subassembly, refrigerant will be shunted repeatedly, collaborate cross flow one, external air, which is formed from radiating subassembly in engraved structure, to be flowed through, the flow disturbance of refrigerant and outer air in radiating subassembly is very big, enhance the heat exchange of refrigerant with extraneous air progress rapidly and efficiently, improve heat transfer coefficient, realize the heat exchange efficiency for improving net formula heat exchanger.
Description
Technical field
The present invention relates to air-conditioning equipment more particularly to a kind of net formula heat exchangers.
Background technology
At present, heat exchanger is common heat-exchanger rig, is widely used in air-conditioning equipment.Heat exchanger of the prior art
Two kinds of structural formulas of plate heat exchanger or pipe heat exchanger are generally divided into, and fin-tube heat exchanger is widely used in air-conditioning and sets
In standby.But in actual use, it is influenced by heat exchange area and heat conduction efficiency, the heat exchange of fin-tube heat exchanger
It is less efficient.How to design a kind of high heat exchanger of heat exchange efficiency is the technical problems to be solved by the invention.
Invention content
The present invention provides a kind of net formula heat exchangers, realize the heat exchange efficiency for improving net formula heat exchanger.
To reach above-mentioned technical purpose, the present invention is realized using following technical scheme:
A kind of net formula heat exchanger, including isocon, collecting pipe and radiating subassembly, the radiating subassembly is in integrally hollow type grid knot
Structure is formed with several interconnected refrigerant flow paths in the radiating subassembly, and the radiating subassembly is connected to the shunting
Between pipe and the collecting pipe.
Further, the radiating subassembly includes more heat-dissipating pipes, and the Single port of the heat-dissipating pipe connects the isocon,
The another port of the heat-dissipating pipe connects the collecting pipe, and many places connecting portion is formed between adjacent two heat-dissipating pipes, adjacent
Two heat-dissipating pipes are interconnected at the position of the connecting portion, and the refrigerant flow path is formed in the heat-dissipating pipe.
Further, the radiating subassembly includes two panels heat sink, and multiple cut-out openings, institute are formed on the heat sink
It states and interconnected groove structure is formed on heat sink, heat sink described in two panels stacks, described in two panels on heat sink
The groove structure is tightly connected to form the refrigerant flow path.
Further, the radiating subassembly include several three-way pipes and several connecting tubes, the two neighboring three-way pipe it
Between pass through the corresponding connecting tube and connect.
Further, the inside caliber of the refrigerant flow path is 0.5~3mm.
Further, the external wall thickness of the refrigerant flow path is 0.15~0.3mm.
Further, the hollow type network is hexagonal honeycomb structure.
Further, the refrigerant flow path length for forming the vertical section of the hexagonal honeycomb structure is L1, is formed
The refrigerant flow path length of the tilting section of the hexagonal honeycomb structure is L2;L1:L2=1:(1~1.5).
Further, the refrigerant flow path length for forming the vertical section of the hexagonal honeycomb structure is D1, is formed
The refrigerant flow path length of the tilting section of the hexagonal honeycomb structure is D2;D1:D2=1:(0.7~1.5).
Compared with prior art, the advantages and positive effects of the present invention are:It realizes to concentrate by isocon and collecting pipe and supply
To refrigerant and unified collection refrigerant, and the radiating subassembly between isocon and collecting pipe is in integrally hollow type network,
Also, several interconnected refrigerant flow paths are formed inside radiating subassembly, the refrigerant of isocon output enters heat dissipation
Component, refrigerant refrigerant flow path flowing different in radiating subassembly, refrigerant will be shunted repeatedly, collaborate cross flow one, outside
The air in portion, which is formed from radiating subassembly in engraved structure, to be flowed through, and the flow disturbance of refrigerant and outer air in radiating subassembly is very
Greatly, the heat exchange of refrigerant with extraneous air progress rapidly and efficiently is also significantly enhanced, heat transfer coefficient is substantially increased, realizes and improve
The heat exchange efficiency of net formula heat exchanger.
Description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, to embodiment or will show below
There is attached drawing needed in technology description to be briefly described, it should be apparent that, the accompanying drawings in the following description is this hair
Some bright embodiments, for those of ordinary skill in the art, without having to pay creative labor, can be with
Other attached drawings are obtained according to these attached drawings.
Fig. 1 is the structure principle chart one of net formula heat exchanger embodiments of the present invention;
Fig. 2 is the structure principle chart two of net formula heat exchanger embodiments of the present invention.
Specific embodiment
Purpose, technical scheme and advantage to make the embodiment of the present invention are clearer, below in conjunction with the embodiment of the present invention
In attached drawing, the technical solution in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
Part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art
All other embodiments obtained without making creative work shall fall within the protection scope of the present invention.
As shown in Figure 1, the present embodiment net formula heat exchanger, including isocon 1, collecting pipe 2 and radiating subassembly 3, the heat dissipation
Whole component 3 is in hollow type network, and several interconnected refrigerant flow paths 31 are formed in the radiating subassembly 3,
The radiating subassembly 3 is connected between the isocon 1 and the collecting pipe 2.
Specifically, refrigerant is input to the refrigeration in radiating subassembly 3 by isocon 1 by the present embodiment net formula heat exchanger
Agent runner 31, and since 3 inside of radiating subassembly forms several interconnected refrigerant flow paths 31, different refrigerant flow paths
31 junctions will form refrigerant distributary division or refrigerant merging part, and refrigerant is in 31 flow process of refrigerant flow path, refrigeration
Agent will pass through multiple shunting, interflow cross flow one, be in hollow type network since radiating subassembly 3 is whole, outside at the same time
Portion's air passes through the engraved structure that radiating subassembly 3 is formed, and air can be caused more efficiently to be changed with radiating subassembly 3
Heat, compared to finned heat exchanger, the coefficient of heat transfer between improving inside and outside heat exchanger eliminates the exchanges such as thermal contact resistance, dust stratification
The adverse effect of heat greatly improves the heat transfer coefficient of heat exchanger.The refrigerant flow path 31 of radiating subassembly 3 is without swollen after aluminum fin-stock flange
Copper pipe outer surface is connected on, eliminates the thermal contact resistance that existing finned heat exchanger is generated by copper pipe outer surface expanded joint aluminum fin-stock, separately
Outside, it is no rib structure outside the pipe of refrigerant flow path 31, it is 100% to be equivalent to fin efficiency.Due to outside pipe without arranging close fin
Structure, heat exchange pipe external surface are not easy to accumulate dust, and substantially reduce adverse effect of the dust stratification to heat transfer.In summary factor, this
The heat transfer coefficient of the cellular heat exchanger heat exchanger of kind can reach 600W/m2 DEG C or so, and nearly one is improved than finned heat exchanger
A order of magnitude.
In actual use, net formula heat exchanger can be used as evaporator, can also be used as condenser.Such as:Refrigeration
When net formula heat exchanger as evaporator, refrigerant side:The refrigerant of gas-liquid two-phase enters isocon 1, along what is connect with isocon 1
It is flowed up in refrigerant flow path 31, during flowing up, refrigerant is in different refrigerant flow paths 31 by multiple
Shunting, interflow cross flow one, while exchange heat with the air outside pipe, and refrigerant is evaporated to gaseous state, into collecting pipe 2 after flow
Go out;Air side:The direction of air along vertical paper is flowed vertically through in the engraved structure and refrigerant flow path 31 of the formation of radiating subassembly 3
The quick heat exchange of refrigerant.Net formula heat exchanger is as condenser, refrigerant side during heating:The refrigerant of gas phase enters collecting pipe
2, it flows downward along each branched pipe pipe being connect with collecting pipe 2, during flowing downward, refrigerant is in different refrigerants
By repeatedly shunting, interflow cross flow one in runner 31, meanwhile, it exchanging heat with the air outside pipe, refrigerant is condensed into liquid,
It is flowed out after into isocon 1;Air side:The direction of air along vertical paper flows vertically through the engraved structure of the formation of radiating subassembly 3
With the quick heat exchange of refrigerant in refrigerant flow path 31.
Wherein, in order to more effectively improve heat exchange efficiency, the inside caliber of refrigerant flow path 31 is 0.5~3mm, the system
The external wall thickness of refrigerant flow conduit 31 is 0.15~0.3mm.The coefficient of heat transfer of net formula heat exchanger uses more than 7 copper of Φ compared to existing
The fin-tube heat exchanger of pipe is much greater, in addition, due to 31 interlaced connection of refrigerant flow path, refrigerant is multiple in pipe
Cross flow one is collaborated in shunting, very big to tube refrigerant and the flow disturbance for managing outer air, is also significantly enhanced in pipe, outside pipe
Heat exchange.And the hollow type network that radiating subassembly 3 shows can be polygonized structure, it is preferred that hollow type grid knot
Structure is hexagonal honeycomb structure, forms the refrigerant flow path length of vertical section of the hexagonal honeycomb structure as L1, shape
The refrigerant flow path length into the tilting section of the hexagonal honeycomb structure is L2;L1:L2=1:(1~1.5), form institute
The refrigerant flow path length for stating the vertical section of hexagonal honeycomb structure is D1, forms the inclination of the hexagonal honeycomb structure
The refrigerant flow path length of section is D2;D1:D2=1:(0.7~1.5).
In addition, diversified forms may be used in the processing method of the 3 specific entity of radiating subassembly in the present embodiment:Such as:It dissipates
Hot component 3 is integral structure, and 3D printing technique acquisition may be used;Alternatively, radiating subassembly 3 includes more heat-dissipating pipes, it is described
The Single port of heat-dissipating pipe connects the isocon 1, and the another port of the heat-dissipating pipe connects the collecting pipe 2, adjacent two institutes
It states and many places connecting portion 301 is formed between heat-dissipating pipe, adjacent two heat-dissipating pipes are interconnected at the position of the connecting portion,
The refrigerant flow path 31 is formed in the heat-dissipating pipe;Alternatively, radiating subassembly 3 includes two panels heat sink, shape on the heat sink
Into there are multiple cut-out openings, interconnected groove structure is formed on the heat sink, heat sink described in two panels stacks,
The groove structure described in two panels on heat sink is tightly connected to form the refrigerant flow path 31;Alternatively, as shown in Fig. 2, institute
It states radiating subassembly 3 and includes several three-way pipes 301 and several connecting tubes 302, pass through correspondence between the two neighboring three-way pipe 301
The connecting tube 302 connect.
Compared with prior art, the advantages and positive effects of the present invention are:It realizes to concentrate by isocon and collecting pipe and supply
To refrigerant and unified collection refrigerant, and the radiating subassembly between isocon and collecting pipe is in integrally hollow type network,
Also, several interconnected refrigerant flow paths are formed inside radiating subassembly, the refrigerant of isocon output enters heat dissipation
Component, refrigerant refrigerant flow path flowing different in radiating subassembly, refrigerant will be shunted repeatedly, collaborate cross flow one, outside
The air in portion, which is formed from radiating subassembly in engraved structure, to be flowed through, and the flow disturbance of refrigerant and outer air in radiating subassembly is very
Greatly, the heat exchange of refrigerant with extraneous air progress rapidly and efficiently is also significantly enhanced, heat transfer coefficient is substantially increased, realizes and improve
The heat exchange efficiency of net formula heat exchanger.
Finally it should be noted that:The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Although
The present invention is described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that:It still may be used
To modify to the technical solution recorded in foregoing embodiments or carry out equivalent replacement to which part technical characteristic;
And these modifications or replace, the spirit for the present invention embodiment technical solution that it does not separate the essence of the corresponding technical solution and
Range.
Claims (9)
1. a kind of net formula heat exchanger, which is characterized in that including isocon, collecting pipe and radiating subassembly, the radiating subassembly is whole
In hollow type network, several interconnected refrigerant flow paths, the radiating subassembly are formed in the radiating subassembly
It is connected between the isocon and the collecting pipe.
2. net formula heat exchanger according to claim 1, which is characterized in that the radiating subassembly includes more heat-dissipating pipes, institute
The Single port for stating heat-dissipating pipe connects the isocon, and the another port of the heat-dissipating pipe connects the collecting pipe, adjacent two institutes
It states and many places connecting portion is formed between heat-dissipating pipe, adjacent two heat-dissipating pipes are interconnected at the position of the connecting portion, institute
It states and the refrigerant flow path is formed in heat-dissipating pipe.
3. net formula heat exchanger according to claim 1, which is characterized in that the radiating subassembly includes two panels heat sink, institute
It states and multiple cut-out openings is formed on heat sink, interconnected groove structure is formed on the heat sink, is dissipated described in two panels
Hot plate stacks, and the groove structure described in two panels on heat sink is tightly connected to form the refrigerant flow path.
4. net formula heat exchanger according to claim 1, which is characterized in that if the radiating subassembly include several three-way pipes and
Involvement is taken over, and is connected between the two neighboring three-way pipe by the corresponding connecting tube.
5. net formula heat exchanger according to claim 1, which is characterized in that the inside caliber of the refrigerant flow path is 0.5
~3mm.
6. net formula heat exchanger according to claim 5, which is characterized in that the external wall thickness of the refrigerant flow path is 0.15
~0.3mm.
7. net formula heat exchanger according to claim 1, which is characterized in that the hollow type network is hexagonal honeycomb
Structure.
8. net formula heat exchanger according to claim 7, which is characterized in that form the vertical section of the hexagonal honeycomb structure
The refrigerant flow path length for L1, the refrigerant flow path length for forming the tilting section of the hexagonal honeycomb structure is
L2;L1:L2=1:(1~1.5).
9. net formula heat exchanger according to claim 7, which is characterized in that form the vertical section of the hexagonal honeycomb structure
The refrigerant flow path length for D1, the refrigerant flow path length for forming the tilting section of the hexagonal honeycomb structure is
D2;D1:D2=1:(0.7~1.5).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201611227752.7A CN108240719A (en) | 2016-12-27 | 2016-12-27 | Net formula heat exchanger |
Applications Claiming Priority (1)
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---|---|---|---|
CN201611227752.7A CN108240719A (en) | 2016-12-27 | 2016-12-27 | Net formula heat exchanger |
Publications (1)
Publication Number | Publication Date |
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CN108240719A true CN108240719A (en) | 2018-07-03 |
Family
ID=62701817
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CN201611227752.7A Pending CN108240719A (en) | 2016-12-27 | 2016-12-27 | Net formula heat exchanger |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111780608A (en) * | 2020-07-14 | 2020-10-16 | 北京石油化工学院 | Dividing wall type heat exchanger based on hollow ball complex channel |
CN112460856A (en) * | 2019-09-09 | 2021-03-09 | 青岛海尔电冰箱有限公司 | Condenser |
CN112595145A (en) * | 2020-12-24 | 2021-04-02 | 季华实验室 | Unsupported honeycomb type heat exchange unit based on 3D printing and heat exchanger |
CN112902324A (en) * | 2021-02-08 | 2021-06-04 | 珠海格力电器股份有限公司 | Air conditioning system |
CN117249503A (en) * | 2023-10-10 | 2023-12-19 | 南京御风环境技术有限公司 | Energy-saving dehumidifier with multi-stage heating of regenerated wind |
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US20140251585A1 (en) * | 2013-03-05 | 2014-09-11 | The Boeing Company | Micro-lattice Cross-flow Heat Exchangers for Aircraft |
CN106091733A (en) * | 2016-08-04 | 2016-11-09 | 唐玉敏 | A kind of dual-purpose heat exchanger plates |
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DE102008007608A1 (en) * | 2008-02-04 | 2009-08-06 | Behr Gmbh & Co. Kg | Heat exchanger for motor vehicle, has pipes with maeander-shaped moldings and connected directly to block, where pipes are soldered with one another at contact points and are shifted against each other |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112460856A (en) * | 2019-09-09 | 2021-03-09 | 青岛海尔电冰箱有限公司 | Condenser |
CN111780608A (en) * | 2020-07-14 | 2020-10-16 | 北京石油化工学院 | Dividing wall type heat exchanger based on hollow ball complex channel |
CN112595145A (en) * | 2020-12-24 | 2021-04-02 | 季华实验室 | Unsupported honeycomb type heat exchange unit based on 3D printing and heat exchanger |
CN112902324A (en) * | 2021-02-08 | 2021-06-04 | 珠海格力电器股份有限公司 | Air conditioning system |
CN112902324B (en) * | 2021-02-08 | 2022-05-27 | 珠海格力电器股份有限公司 | Air conditioning system |
CN117249503A (en) * | 2023-10-10 | 2023-12-19 | 南京御风环境技术有限公司 | Energy-saving dehumidifier with multi-stage heating of regenerated wind |
CN117249503B (en) * | 2023-10-10 | 2024-02-09 | 南京御风环境技术有限公司 | Energy-saving dehumidifier with multi-stage heating of regenerated wind |
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