CN108240719A - Net formula heat exchanger - Google Patents

Net formula heat exchanger Download PDF

Info

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
Application number
CN201611227752.7A
Other languages
Chinese (zh)
Inventor
谢涛
路则锋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao Haier Smart Technology R&D Co Ltd
Original Assignee
Qingdao Haier Smart Technology R&D Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Qingdao Haier Smart Technology R&D Co Ltd filed Critical Qingdao Haier Smart Technology R&D Co Ltd
Priority to CN201611227752.7A priority Critical patent/CN108240719A/en
Publication of CN108240719A publication Critical patent/CN108240719A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2500/00Problems to be solved
    • F25B2500/09Improving 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

Net formula heat exchanger
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).
CN201611227752.7A 2016-12-27 2016-12-27 Net formula heat exchanger Pending CN108240719A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611227752.7A CN108240719A (en) 2016-12-27 2016-12-27 Net formula heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611227752.7A CN108240719A (en) 2016-12-27 2016-12-27 Net formula heat exchanger

Publications (1)

Publication Number Publication Date
CN108240719A true CN108240719A (en) 2018-07-03

Family

ID=62701817

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611227752.7A Pending CN108240719A (en) 2016-12-27 2016-12-27 Net formula heat exchanger

Country Status (1)

Country Link
CN (1) CN108240719A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
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

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000329485A (en) * 1999-05-18 2000-11-30 Central Res Inst Of Electric Power Ind Heat exchanger
CN101261094A (en) * 2008-04-24 2008-09-10 丁宏广 Plate heat exchanger
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
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
CN206440035U (en) * 2016-12-27 2017-08-25 青岛海尔智能技术研发有限公司 Net formula heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000329485A (en) * 1999-05-18 2000-11-30 Central Res Inst Of Electric Power Ind Heat exchanger
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
CN101261094A (en) * 2008-04-24 2008-09-10 丁宏广 Plate heat exchanger
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
CN206440035U (en) * 2016-12-27 2017-08-25 青岛海尔智能技术研发有限公司 Net formula heat exchanger

Cited By (7)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
CN108240719A (en) Net formula heat exchanger
JP6011009B2 (en) Heat exchanger and air conditioner
WO2017020834A1 (en) Integral heat superconducting plate heat exchanger and fabrication method therefor
US10619951B2 (en) Phase transition suppression heat transfer plate-based heat exchanger
CN206440153U (en) A kind of pipe wing micro-channel heat exchanger
WO2017113571A1 (en) Integrated phase-change inhibition heat transfer and heat exchange plate structure and manufacturing method thereof
JP2012163328A5 (en)
JP5312413B2 (en) Finned tube heat exchanger and refrigeration cycle apparatus using the same
JP5517801B2 (en) Heat exchanger and heat pump system equipped with this heat exchanger
CN106642826B (en) Heat exchanger
CN107990758A (en) Heat exchanger and heat pump system
JP2011106738A (en) Heat exchanger and heat pump system
EP3062037B1 (en) Heat exchanger and refrigeration cycle device using said heat exchanger
CN206440035U (en) Net formula heat exchanger
CN207247967U (en) Thermosyphon heat dissipation device
JP6383942B2 (en) Heat exchanger
JP5744316B2 (en) Heat exchanger and heat pump system equipped with the heat exchanger
JP6016935B2 (en) Plate heat exchanger and refrigeration cycle apparatus equipped with the plate heat exchanger
JP2016050718A (en) Air conditioner
JP5404571B2 (en) Heat exchanger and equipment
JP6987227B2 (en) Heat exchanger and refrigeration cycle equipment
CN209165620U (en) A kind of hot pipe cooling dehumidification device of cross arrangement formula
CN203731744U (en) Stable parallel flow heat exchanger
CN108344210B (en) Parallel flow heat exchange system for improving heat exchange efficiency
CN207280034U (en) Using the air conditioner of multi-path microcapillary parallel split-flow heat exchanger

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination