CN206037814U - Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage - Google Patents

Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage Download PDF

Info

Publication number
CN206037814U
CN206037814U CN201620895476.0U CN201620895476U CN206037814U CN 206037814 U CN206037814 U CN 206037814U CN 201620895476 U CN201620895476 U CN 201620895476U CN 206037814 U CN206037814 U CN 206037814U
Authority
CN
China
Prior art keywords
inclined plane
flat tube
thermal performance
cavity
micro channels
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.)
Active
Application number
CN201620895476.0U
Other languages
Chinese (zh)
Inventor
赵永芹
穆景阳
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.)
Air International Thermal Systems (shanghai) Co Ltd
Original Assignee
Air International Thermal Systems (shanghai) 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 Air International Thermal Systems (shanghai) Co Ltd filed Critical Air International Thermal Systems (shanghai) Co Ltd
Priority to CN201620895476.0U priority Critical patent/CN206037814U/en
Application granted granted Critical
Publication of CN206037814U publication Critical patent/CN206037814U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model provides an air conditioner heat exchanger technical field's flat pipe of microchannel heat transfer and evaporimeter with optimize drainage, includes: up end, lower terminal surface and evagination tip, wherein: upper and lower terminal surface parallel arrangement, simultaneously the left and right sides of upper and lower terminal surface is connected with the evagination tip respectively and forms the cavity, the cavity is inside be equipped with with a plurality of runner division boards of upper and lower terminal surface vertically, to be located the evagination tip structure of the cavity left and right sides the same, include first inclined plane and the second inclined plane be connected respectively with upper and lower terminal surface, first inclined plane and second inclined plane link to each other, the contained angle is alpha, 30 <= alpha < 85, contained angle alpha's angular bisector is parallel with upper and lower terminal surface. The utility model discloses a set up the slope structure at flat tub of both ends, improve drainage efficiency, guarantee the heat exchange efficiency of the flat pipe of microchannel heat transfer.

Description

Thermal Performance of Micro Channels flat tube with optimization draining and its vaporizer
Technical field
The utility model relates to a kind of technology of air-conditioning field of heat exchangers, specifically a kind of with the micro- of optimization draining Channel for heat exchange flat tube and its vaporizer.
Background technology
The heat-exchanger rig that existing concurrent flow micro-channel heat exchanger is domestic, commercialization, commonly used in automotive air-conditioning system, wherein The two ends of Thermal Performance of Micro Channels flat tube used be circular shape, this structure be used for condenser in, when sewage cannot be discharged in time, hold Corrosion is also easy to produce, accelerated ageing reduces its life-span;In for vaporizer, the vaporizer particularly on air conditioning for automobiles, impeded drainage When, can usually cause the problems such as frosting, leaving air temp are uneven, water is spilt from air-conditioning box shell topic gap, so as to cause passenger's Complaint.
Utility model content
This utility model is directed to deficiencies of the prior art, it is proposed that a kind of microchannel with optimization draining is changed Hot flat tube and its vaporizer, by arranging incline structure at flat tube two ends, improve drainage efficiency, it is ensured that Thermal Performance of Micro Channels flat tube Heat exchange efficiency.
This utility model is achieved through the following technical solutions,
This utility model is related to a kind of Thermal Performance of Micro Channels flat tube with optimization draining, including:Upper surface, lower surface and outer Nose portion, wherein:Upper and lower end face be arranged in parallel, while the left and right sides of upper and lower end face is connected to evagination end and is formed Cavity, inside cavity are provided with some runner demarcation strips vertical with upper and lower end face;
The described evagination end construction positioned at the cavity left and right sides is identical, including for being connected with upper and lower end face respectively One inclined plane and the second inclined plane;
The first described inclined plane is connected with the second inclined plane, and angle is α, 85 ° of 30 °≤α <;Put down at the angle of the angle α Separated time is parallel with upper and lower end face.
Preferably, the first described inclined plane and the second inclined plane are seamlessly transitted by fillet.
Preferably, the first described inclined plane is seamlessly transitted by fillet with upper surface, and the second described inclined plane is with End face is seamlessly transitted by fillet.
Preferably, first inclined plane and the second inclined plane respectively with cavity in one piece of runner demarcation strip up and down two End is connected, and is seamlessly transitted by fillet.
The cross-sectional length of the cavity is L, 13mm≤L < 22mm;The transverse section width of the cavity be W, 2.4mm≤ W < 2.9mm.
This utility model is related to a kind of vaporizer based on above-mentioned Thermal Performance of Micro Channels flat tube, including:First collecting tank and Two collecting tanks, are provided with multiple rows of described Thermal Performance of Micro Channels flat tube, adjacent microchannel between the first and second described collecting tanks Be provided with fin between flat heat exchange pipe, fin be adjacent between the upper surface or lower surface of Thermal Performance of Micro Channels flat tube at least provided with One windowing angle.
Described windowing angle angle is 27~33 °.
Technique effect
Compared with prior art, in this utility model Thermal Performance of Micro Channels flat tube both sides evagination end in isosceles triangle simultaneously Seamlessly transitted by fillet so that the condensed water from fin can be flowed down along the hypotenuse of evagination end, increase catchment The scope in domain, can guarantee that heat exchanger effectiveness while Quick drainage is realized again.By taking the vaporizer of fin width 38mm as an example, In the case that fin height and the pitch of waves are constant, using vaporizer of the present utility model and using common flat tube, fin width 45mm Vaporizer compare, performance quite, while cold-producing medium flow resistance reduces 50%, weight saving 26%.
Description of the drawings
Fig. 1 is cross-sectional configuration schematic diagram of the present utility model;
Fig. 2 is the structural representation of the vaporizer assembled using this utility model;
In figure:A () is overall structure diagram, (b) be partial enlarged drawing;
In figure:Upper surface 1, lower surface 2, evagination end 3, runner demarcation strip 4, the first inclined plane 5, the second inclined plane 6, One collecting tank 7, the second collecting tank 8, Thermal Performance of Micro Channels flat tube 9, fin 10.
Specific embodiment
Below embodiment of the present utility model is elaborated, the present embodiment is with technical solutions of the utility model as front Put and implemented, give detailed embodiment and specific operating process, but protection domain of the present utility model is not limited In following embodiments.
Embodiment 1
As shown in figure 1, the present embodiment includes:Upper surface 1, lower surface 2 and evagination end 3, wherein:Upper surface 1 and lower end Face 2 be arranged in parallel, while upper surface 1, the left and right sides of lower surface 2 are connected to evagination end 3 and form cavity;Described Inside cavity is provided with some runner demarcation strips 4 vertical with upper surface 1, lower surface 2;
Described 3 structure of evagination end positioned at the cavity left and right sides is identical, including connecting with upper surface 1, lower surface 2 respectively The first inclined plane 5 for connecing and the second inclined plane 6;
The first described inclined plane 5 is connected with the second inclined plane 6, and angle is α, 85 ° of 30 °≤α <, it is ensured that at least Individual fin opens a window angle on 5/ second inclined-plane 6 of the first inclined-plane, as shown in Figure 2;The angular bisector of the angle α and upper surface 1, under End face 2 is parallel.
Preferably, the first described inclined plane 5 and the second inclined plane 6 are seamlessly transitted by fillet.
Preferably, the first described inclined plane 5 is seamlessly transitted by fillet with upper surface 1, described second inclined plane 6 with Lower surface 2 is seamlessly transitted by fillet.
Preferably, first inclined plane 5 and the second inclined plane 6 respectively with cavity in one piece of runner demarcation strip 4 it is upper Lower two ends are connected, and are seamlessly transitted by fillet.
The cross-sectional length of the cavity is L, 13mm≤L < 22mm;The transverse section width of the cavity be W, 2.4mm≤ W < 2.9mm.
As shown in Fig. 2 the present embodiment is related to a kind of vaporizer based on above-mentioned Thermal Performance of Micro Channels flat tube, including the first liquid collecting Groove 7 and the second collecting tank 8, are provided with multiple rows of above-mentioned Thermal Performance of Micro Channels between the first described collecting tank 7 and the second collecting tank 8 flat Pipe 9, is provided with fin 10 between adjacent microchannel flat heat exchange pipe 9, fin 10 is adjacent the upper surface of Thermal Performance of Micro Channels flat tube 9 At least provided with a windowing angle between 1 or lower surface 2.
Described windowing angle beta is 27~33 °, preferably 30 °.
In this utility model, the size of angle α determines the size of drainage, has important work to heat exchanger effectiveness With.If angle α is too little, internal circulation area diminishes, and can reduce heat exchange efficiency;If angle α is too big, it is impossible to ensure at least one wing Piece opens a window angle in flat tube end chamfer, and water easily can not spill out, and easily cause condensed water spattering problem.

Claims (7)

1. it is a kind of with the Thermal Performance of Micro Channels flat tube for optimizing draining, it is characterised in that to include:Upper surface, lower surface and male end Portion, wherein:Upper and lower end face be arranged in parallel, while the left and right sides of upper and lower end face is connected to evagination end and forms chamber Body, inside cavity are provided with some runner demarcation strips vertical with upper and lower end face;
The described evagination end construction positioned at the cavity left and right sides is identical, including inclining with first that upper and lower end face is connected respectively Inclined-plane and the second inclined plane;
The first described inclined plane is connected with the second inclined plane, and angle is α, 85 ° of 30 °≤α <;The angular bisector of the angle α It is parallel with upper and lower end face.
2. the Thermal Performance of Micro Channels flat tube with optimization draining according to claim 1, is characterized in that, the first described inclination Face and the second inclined plane are seamlessly transitted by fillet.
3. the Thermal Performance of Micro Channels flat tube with optimization draining according to claim 1 and 2, is characterized in that, described first Inclined plane is seamlessly transitted by fillet with upper surface, and the second described inclined plane is seamlessly transitted by fillet with lower surface.
4. the Thermal Performance of Micro Channels flat tube with optimization draining according to claim 1 and 2, is characterized in that, described first inclines Inclined-plane is connected with the upper and lower ends of one piece of runner demarcation strip in cavity respectively with the second inclined plane, and smoothed by fillet Cross.
5. it is according to claim 1 with optimization draining Thermal Performance of Micro Channels flat tube, it is characterized in that, the cavity it is cross-section Face length is L, 13mm≤L < 22mm;The transverse section width of the cavity is W, 2.4mm≤W < 2.9mm.
6. a kind of vaporizer, it is characterised in that include:Arbitrary described Thermal Performance of Micro Channels flat tube and the in Claims 1 to 5 One collecting tank, the second collecting tank;Multiple rows of Thermal Performance of Micro Channels flat tube is provided between the first and second described collecting tanks, it is adjacent micro- Fin is provided between channel for heat exchange flat tube, and fin is adjacent between the upper surface or lower surface of Thermal Performance of Micro Channels flat tube at least It is provided with a windowing angle.
7. vaporizer according to claim 6, is characterized in that, described windowing angle size is 27~33 °.
CN201620895476.0U 2016-08-17 2016-08-17 Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage Active CN206037814U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620895476.0U CN206037814U (en) 2016-08-17 2016-08-17 Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620895476.0U CN206037814U (en) 2016-08-17 2016-08-17 Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage

Publications (1)

Publication Number Publication Date
CN206037814U true CN206037814U (en) 2017-03-22

Family

ID=58306873

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620895476.0U Active CN206037814U (en) 2016-08-17 2016-08-17 Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage

Country Status (1)

Country Link
CN (1) CN206037814U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109945721A (en) * 2019-03-28 2019-06-28 揭阳市美度实业有限公司 A kind of automobile radiators six terrace with edge end structure flat tube design method of fillet
CN110243222A (en) * 2019-07-03 2019-09-17 张家港市宏基精密铝材科技有限公司 A kind of angular aluminium flat conduit, production technology and purposes

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109945721A (en) * 2019-03-28 2019-06-28 揭阳市美度实业有限公司 A kind of automobile radiators six terrace with edge end structure flat tube design method of fillet
CN109945721B (en) * 2019-03-28 2020-06-30 揭阳市美度实业有限公司 Method for designing rounded-corner hexagonal frustum end structure flat tube for automobile radiator
CN110243222A (en) * 2019-07-03 2019-09-17 张家港市宏基精密铝材科技有限公司 A kind of angular aluminium flat conduit, production technology and purposes

Similar Documents

Publication Publication Date Title
CN108917174B (en) Gas-electricity coupling limit condensation cast aluminum silicon magnesium gas water heater
CN101995172B (en) Micro-channel heat exchanger and equipment using same
CN204177261U (en) A kind of flat pipes of heat exchanger and micro-channel heat exchanger
CN206037814U (en) Flat pipe of microchannel heat transfer and evaporimeter with optimize drainage
CN202793131U (en) Parallel flow heat exchanger and flat tube section bars thereof
CN205784786U (en) A kind of flat tube and fin type heat exchanger
CN107702382A (en) micro-channel evaporator
CN206310797U (en) The micro-channel heat exchanger of non-finned
CN206281394U (en) The improved micro-channel flat of drainage structure
CN105547014B (en) A kind of heat exchanger
CN218723446U (en) Fin structure and heat exchanger thereof
CN116294703A (en) Fin tube type heat exchanger
CN202757493U (en) Parallel flow heat exchanger and parallel flow heat exchanging device
CN214039043U (en) Micro-channel heat exchanger and air conditioning system
WO2017020666A1 (en) Heat exchanger
CN203501559U (en) Fin-type evaporator for refrigerator of large heat exchange area
CN205014692U (en) Microchannel heat exchanger and have its heat pump water heater
CN212620242U (en) Radiating tube structure with wavy flying wings
CN211626225U (en) Heat-transfer pipe heat radiation structure
CN210463271U (en) Annular C-shaped opening micro-channel parallel flow heat exchanger
CN105928258A (en) Heat exchanger and air conditioner
CN205690750U (en) Heat exchanger and air-conditioning
CN105757923B (en) Environmental protection and energy saving heat dump
CN203501848U (en) Fin type heat exchanger
CN210922315U (en) Fin for heat exchange of air conditioning system

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant