CN207335513U - Parallel-flow heat exchanger inclining fin structure - Google Patents
Parallel-flow heat exchanger inclining fin structure Download PDFInfo
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- CN207335513U CN207335513U CN201721199630.1U CN201721199630U CN207335513U CN 207335513 U CN207335513 U CN 207335513U CN 201721199630 U CN201721199630 U CN 201721199630U CN 207335513 U CN207335513 U CN 207335513U
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Abstract
The utility model discloses a kind of parallel-flow heat exchanger inclining fin structure, includes several oblique substrates that spacing is set successively along the longitudinal direction, and the oblique substrate relative level, which tilts, to be extended;In addition to the oblique substrate of front and back ends, the left and right end of each oblique substrate is corresponding to the oblique substrate of adjacent forward and backward side respectively to be connected to form S-shaped structure;Formed with groove between extending obliquely out up and down between adjacent oblique substrate, it is described between groove there is upper and lower end opening, it is described between groove internal face vertically tilt it is extended;Thereby, by inclining fin structure design, air drag is reduced, is more easy to discharge quick smooth guide of condensed water, reduces icing phenomenon, thermal resistance reduces, and improves heat exchange efficiency, meanwhile, when being also applied for outdoor and dusty occasion, it is not easy dust stratification dirt.
Description
Technical field
Parallel-flow heat exchanger field technology is the utility model is related to, refers in particular to a kind of parallel-flow heat exchanger inclining fin
Structure.
Background technology
Parallel-flow heat exchanger has generally included header, flat tube, fin etc., and during work, refrigerant is along flat tube in afflux
Flowed between pipe along design direction, while flowing, the air with blowing over fin carries out heat exchange.In the prior art, fin
It is vertical design, fin surface condensate draining is not smooth, easily freezes, causes fin heat resistance to become larger, have impact on heat exchange efficiency.
Therefore, in present patent application, applicant has studied intensively a kind of new technical solution to solve the above problems.
Utility model content
In view of this, in view of the existing deficiencies of the prior art, its main purpose is to provide a kind of concurrent flow to the utility model
Heat exchanger inclining fin structure, which reduces air drag, is more easy to discharge quick smooth guide of condensed water, it is existing to reduce icing
As, fin heat resistance reduces, and improves heat exchange efficiency, meanwhile, when being also applied for outdoor and dusty occasion, it is not easy dust stratification dirt.
To achieve the above object, the utility model is using following technical solution:
A kind of parallel-flow heat exchanger inclining fin structure, include several along the longitudinal direction successively spacing set it is oblique
To substrate, the oblique substrate relative level, which tilts, to be extended;In addition to the oblique substrate of front and back ends, each oblique base
The left and right end of plate is corresponding to the oblique substrate of adjacent forward and backward side respectively to be connected to form S-shaped structure;Adjacent oblique substrate it
Between formed with groove between extending obliquely out up and down, it is described between groove there is upper and lower end opening, it is described between the internal face of groove vertically tilt
It is extended.
As a preferred embodiment, in main view angle, the opposite anteroposterior direction of two oblique substrates positioned at a groove both sides
Extend axis setting at an acute angle, two oblique substrates positioned at a groove both sides are set parallel to each other or are set each other in angle.
As a preferred embodiment, when two oblique substrates of groove both sides are set parallel to each other between main view angle is located at,
It is also parallel each other positioned at the top of two oblique substrates of a groove both sides in depression angle, the top of two oblique substrates herein
It is extended from left vertical-right or extends obliquely out setting from left to right.
As a preferred embodiment, between the number range of the acute angle is 25 degree to 35 degree.
As a preferred embodiment, some hollow out windows are further offered on the oblique substrate, the surface of hollow out window is set
It is equipped with welding coating.
As a preferred embodiment, the whole height 8 of the inclining fin is to 8.03mm, the overall width of inclining fin
12mm, the pitch of fins 1.7mm of adjacent oblique substrate, the thickness 0.08mm of oblique substrate.
The utility model has clear advantage and beneficial effect compared with prior art, specifically, by above-mentioned technology
Scheme understands that it mainly passes through inclining fin structure design, reduces air drag, is more easy to the quick smooth walking guide of condensed water
Discharge, reduces icing phenomenon, and fin heat resistance reduces, and improves heat exchange efficiency, more energy saving, advantageously reduces cost, meanwhile, also fit
During for outdoor and dusty occasion, dust stratification dirt is not easy.
More clearly to illustrate the architectural feature of the utility model and effect, come below in conjunction with the accompanying drawings with specific embodiment pair
The utility model is described in detail.
Brief description of the drawings
Fig. 1 is the substantially schematic perspective view of the embodiment of the utility model;
Fig. 2 is K1 direction views in Fig. 1;
Fig. 3 is the close-up schematic view of Fig. 2;
Fig. 4 is K2 direction views in Fig. 1;
Fig. 5 is the close-up schematic view of Fig. 4;
Fig. 6 is another embodiment situation schematic diagram of structure shown in Fig. 5;
Fig. 7 is the another embodiment situation schematic diagram of structure shown in Fig. 5.
Attached drawing identifier declaration:
10th, oblique substrate 20, a groove
30th, arc panel
10 ', oblique substrate 20 ', a groove
30 ', arc panel
10 〞, 20 〞 of oblique substrate, a groove
30 〞, arc panel.
Embodiment
It refer to shown in Fig. 1 to Fig. 7, that show the concrete structure of the embodiment of the utility model;The concurrent flow
Heat exchanger inclining fin structure, can be widely applied to the fields such as air-conditioning, refrigerator, its structure design is simple, ingenious reasonable, significantly
Heat exchange property is improved, there is larger application value.
Direction terms such as " up, down, left, right, before and afters " specifically described herein describes, and is explained exemplified by shown in attached drawing, not
Make unique limit to direction.
Specifically, in this present embodiment, whole inclining fin structure is in rectangular configuration;The inclining fin structure includes
There are several oblique substrates 10 that spacing is set successively along the longitudinal direction, oblique 10 relative level of substrate tilts extension and sets
Put;In addition to the oblique substrate 10 of front and back ends (the oblique substrate 10 of front and back ends only have left end, one end in right end with it is adjacent
Oblique substrate connection), the left and right end of each oblique substrate 10 is corresponding to the oblique substrate 10 of adjacent forward and backward side respectively to be connected
To form S-shaped structure, herein, the left and right end of each oblique substrate 10 phase with the oblique substrate 10 of adjacent forward and backward side respectively
Answer and connected by arc panel 30 between end, such as:Semi-circular shape arc panel 30;Formed with upper and lower between adjacent oblique substrate 10
Groove 20 between extending obliquely out, it is described between groove 20 there is upper and lower end opening, it is described between the internal face of groove 20 vertically tilt extension and set
Put, in this way, reducing air drag(Result of the test shows that it at least reduces windage more than 25%), can effectively force condensed water
Internal face along a groove 20 moves obliquely along air-flow direction, it is easy to is expelled directly out, draining is smooth, reduces and freezes now
As fin heat resistance reduces, and improves heat exchange efficiency, more energy saving, advantageously reduces cost.
It is at an acute angle in main view angle, the opposite anteroposterior direction extension axis of two oblique substrates 10 positioned at 20 both sides of a groove
Set, between the number range of preferably described acute angle is 25 degree to 35 degree, such as 30 degree.Two positioned at 20 both sides of a groove are oblique
Substrate 10 is set parallel to each other or is set each other in angle(With reference to shown in comparison diagram 5, Fig. 6 and Fig. 7).
When two of 20 both sides of groove oblique substrates 10 are set parallel to each other between main view angle is located at, in depression angle, position
Also parallel each other in the top of two oblique substrates 10 of 20 both sides of a groove, the top of two oblique substrates 10 is vertical from a left side herein
It is extended to the right(As shown in Figure 5)Or setting is extended obliquely out from left to right(As shown in Figure 6).
And applicant studies intensively the size characteristic of inclining fin, it is mainly from structural strength, easy processing
Property, the various aspects such as deformation resistance and product suitable dimensions parameter go to consider, obtain following reasonable ruler through multiple repetition test, analysis
Very little parameter designing:The whole height 8 of the inclining fin is to 8.03mm, the overall width 12mm of inclining fin, adjacent oblique base
The pitch of fins 1.7mm of plate, the thickness 0.08mm of oblique substrate.Some hollow out windows can be further offered on oblique substrate 10,
Certainly, hollow out window is that one is compressing on oblique substrate 10, and the design of hollow out window can play the role of increasing heat exchange area.
In general, the surface of hollow out window is provided with welding coating.
Next, substantially introduce the production process of foregoing inclining fin:After first carrying out right angle fin shaping, with inclination
The mould of fin carries out die mould shaping to former fin, reaches required fin shape;For fin caused by possibility after soldering
Deformation, can avoid deforming by way of increasing fin thickness and fin strength, therefore, the structural strength of inclining fin and
Anti-deformation performance etc. can be effectively ensured, and processing procedure is controllable reliable.
In conclusion the design focal point of the utility model is, it mainly passes through inclining fin structure design, reduces
Air drag, is more easy to discharge quick smooth guide of condensed water, reduces icing phenomenon, and fin heat resistance reduces, and improves heat exchange efficiency,
It is more energy saving, cost is advantageously reduced, meanwhile, when being also applied for outdoor and dusty occasion, it is not easy dust stratification dirt.
The above descriptions are merely preferred embodiments of the present invention, and not the technical scope of the utility model is made
Any restrictions, therefore every any trickle amendment made according to the technical essence of the utility model to above example, equivalent change
Change and modification, in the range of still falling within technical solutions of the utility model.
Claims (6)
- A kind of 1. parallel-flow heat exchanger inclining fin structure, it is characterised in that:Include several along the longitudinal direction successively between Oblique substrate away from setting, the oblique substrate relative level, which tilts, to be extended;In addition to the oblique substrate of front and back ends, The left and right end of each oblique substrate is corresponding to the oblique substrate of adjacent forward and backward side respectively to be connected to form S-shaped structure;It is adjacent Formed with groove between extending obliquely out up and down between oblique substrate, it is described between groove there is upper and lower end opening, it is described between groove internal face Vertically tilt and be extended.
- 2. parallel-flow heat exchanger according to claim 1 inclining fin structure, it is characterised in that:In main view angle, position The opposite anteroposterior direction extension axis setting at an acute angle of two oblique substrates in a groove both sides, two positioned at a groove both sides are oblique It is set parallel to each other to substrate or is set each other in angle.
- 3. parallel-flow heat exchanger according to claim 2 inclining fin structure, it is characterised in that:It is located in main view angle Between two oblique substrates of groove both sides when being set parallel to each other, in depression angle, two oblique substrates positioned at a groove both sides Top is also parallel each other, and the top of two oblique substrates is extended from left vertical-right or extends obliquely out from left to right herein Set.
- 4. parallel-flow heat exchanger according to claim 2 inclining fin structure, it is characterised in that:The numerical value of the acute angle Between scope is 25 degree to 35 degree.
- 5. parallel-flow heat exchanger according to claim 1 inclining fin structure, it is characterised in that:On the oblique substrate Some hollow out windows are further offered, the surface of hollow out window is provided with welding coating.
- 6. parallel-flow heat exchanger according to claim 1 inclining fin structure, it is characterised in that:The inclining fin Whole height 8 is to 8.03mm, the overall width 12mm of inclining fin, the pitch of fins 1.7mm of adjacent oblique substrate, the thickness of oblique substrate Spend 0.08mm.
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CN201721199630.1U CN207335513U (en) | 2017-09-19 | 2017-09-19 | Parallel-flow heat exchanger inclining fin structure |
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CN201721199630.1U CN207335513U (en) | 2017-09-19 | 2017-09-19 | Parallel-flow heat exchanger inclining fin structure |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110253131A (en) * | 2019-07-01 | 2019-09-20 | 中国科学院工程热物理研究所 | Capillary channel heat exchanger and preparation method thereof |
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2017
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110253131A (en) * | 2019-07-01 | 2019-09-20 | 中国科学院工程热物理研究所 | Capillary channel heat exchanger and preparation method thereof |
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