CN109084608A - A kind of heat exchanger fin - Google Patents
A kind of heat exchanger fin Download PDFInfo
- Publication number
- CN109084608A CN109084608A CN201710442737.2A CN201710442737A CN109084608A CN 109084608 A CN109084608 A CN 109084608A CN 201710442737 A CN201710442737 A CN 201710442737A CN 109084608 A CN109084608 A CN 109084608A
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- China
- Prior art keywords
- flow channel
- chute
- heat exchanger
- exchanger fin
- plate
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- 239000003507 refrigerant Substances 0.000 claims abstract description 81
- 230000005855 radiation Effects 0.000 claims abstract description 7
- 238000009423 ventilation Methods 0.000 claims description 34
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 238000009827 uniform distribution Methods 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000012530 fluid Substances 0.000 description 6
- 230000017525 heat dissipation Effects 0.000 description 5
- 238000003466 welding Methods 0.000 description 5
- 238000009792 diffusion process Methods 0.000 description 4
- 239000010410 layer Substances 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 235000012773 waffles Nutrition 0.000 description 4
- 230000009471 action Effects 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 241001075561 Fioria Species 0.000 description 1
- 241000883990 Flabellum Species 0.000 description 1
- 229910001069 Ti alloy Inorganic materials 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910000601 superalloy Inorganic materials 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2210/00—Heat exchange conduits
- F28F2210/08—Assemblies of conduits having different features
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2250/00—Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
- F28F2250/04—Communication passages between channels
Abstract
The present invention provides a kind of heat exchanger fin, is used for rotary heat radiation, including first runner, positioned at the front of direction of rotation, and radially extending along rotation, there is refrigerant inlet;Second flow channel, positioned at the rear of direction of rotation, and radially extending along rotation, there is refrigerant outlet;Third flow channel, have it is multiple, along rotation it is radially uniform being distributed between the first runner and the second flow channel, be separately connected to the first runner and the second flow channel;Heat exchanger fin of the invention, has the multiple third flow channels for independently connecting first runner and second flow channel, and third flow channel can guarantee that the refrigerant in runner is evenly distributed in cooling fin in rotation radiation processes along the radially uniform distribution of rotation.
Description
Technical field
The present invention relates to technical field of heat exchangers, and in particular to a kind of heat exchanger fin.
Background technique
It will be carried out in fields such as derived energy chemical, refrigeration air-conditioner, military project, electronic equipments, in equipment running process appropriate
Heat exchange, at present as electronic equipment is that the forced convertion formed by blower exchanges heat with heat transferring medium, the addition of blower is not
The load for increasing only whole system causes the loss and waste of energy, and heat exchange efficiency is lower.
Chinese patent literature CN101900407A discloses a kind of fan blade heat exchanger, including fan blade, fan leaf
On piece is equipped with refrigerant flow path, and fan shaft is interior equipped with liquid channel in gas channel in axis and axis, refrigerant flow path and gas channel in axis
It is communicated respectively with liquid channel in axis;Technical solution in the patent document, heat exchanger and fan are combined into one, and make electric fan
The speed that the existing air of relative velocity ratio between air flows through heat exchanger is much larger, has and improves unit area heat exchange efficiency
Effect;However, the refrigerant flow path being arranged in said fans blade is single circular tube structure, circle is set in fan blade
The refrigerant flow path of pipe structure has the drawback that 1, single round tube heat dissipation area is small, and heat transfer efficiency is low;2, fan blade is being revolved
Centrifugal force can be generated when turning, under the action of the centrifugal force, the refrigerant inside round tube can be flowed to top, and be assembled on top, this
It is uneven to will cause heat dissipation;Also due to the effect of centrifugal force, refrigerant speed when entering refrigerant flow path is fast, freezes in outflow
Speed is slow when agent runner, in order to enable the refrigerant to the smooth flow in runner, needs to improve refrigerant flow path import and export
Pressure difference, this be easy to cause refrigerant flow path to rupture.
Chinese patent literature CN101782346A discloses a kind of alternate intercommunicating microchannel net structure heat exchanger fin, in thin plate
Two sides is machined with microchannel, and two sides microchannel is mutually perpendicular to, and forms the reticular structure of intercommunication;Outside heat is passed by microchannel wall
It is directed in channel, the fluid for being then forced convection current is taken away, and since the size of microchannel is smaller, fluid can be dispersed in
In thin plate, increase the specific surface area of fluid, the bubble that the groove of reticular structure is conducive to fluid boiling overflows, and has excellent boiling
Reinforcing performance is risen, is made under same heat flow density, the reticular structure of heat exchanger fin is improved than the heat transfer efficiency of smooth surface texture;
However, the heat exchanger fin in above patent document is applied under stationary state, it is not applied to rotary type heat exchanger
Enlightenment, it is identical by diameter due to microchannel each in heat exchanger fin when applying in the blade with rotation, in centrifugal force
Effect, can equally prevent the fluid in heat exchanger from being uniformly distributed, cause the non-uniform defect that radiates.
Summary of the invention
Therefore, the technical problem to be solved in the present invention is that overcoming inside the heat exchanger fin rotatably to exchange heat in the prior art only
There is single round tube, when rotating heat dissipation, the technological deficiency that refrigerant can be unevenly distributed in round tube, to provide a kind of rotating
When heat dissipation, the equally distributed heat exchanger fin of refrigerant can be made.
In order to solve the above technical problems, the present invention provides a kind of heat exchanger fin, it to be used for rotary heat radiation, comprising: first runner,
Positioned at the front of direction of rotation, and radially extending along rotation, there is refrigerant inlet;Second flow channel, positioned at direction of rotation
Rear, and radially extending along rotation have refrigerant outlet;Third flow channel has multiple, the radially uniform distribution of edge rotation
Between the first runner and the second flow channel, it is separately connected to the first runner and the second flow channel.
Preferably, along the first runner to the second flow channel direction, the cross section of the third flow channel
Product is changed from small to big.
Preferably, the unhurried current structure for slowing down refrigerant flow rates is additionally provided with inside the third flow channel.
Preferably, the unhurried current structure includes: the first network, is distributed in inside the third flow channel, packet
Multiple first grids, one end sealing of first grid are included, the other end forms the first opening;Second network, is distributed in
Inside the third flow channel, including multiple second grids, one end sealing of second grid, the other end form the second opening;
First network is staggeredly superimposed with second network, first opening and at least two described second
It is open opposite, so that entering the refrigerant of the third flow channel staggeredly to enter first opening and second opening
Mode flows through the third flow channel.
Preferably, first grid and/or second grid are polygonized structure, circular configuration.
Preferably, further include ventilation hole, be arranged through heat exchanger fin, also, the ventilation hole is not with described first
Runner, the second flow channel and third flow channel connection.
Preferably, the ventilation hole has multiple, is distributed between two adjacent third flow channels.
The present invention also provides a kind of heat exchanger fins, are used for rotary heat radiation, comprising: the first plate;Second plate is located at described
Above first plate, have along the first chute of direction of rotation radially extended and the second chute;The first-class slot position is in rotation
Turn the front in direction, there is refrigerant inlet;The second slot position has refrigerant outlet in the rear of direction of rotation;Also
Including the first hole, have it is multiple, along direction of rotation it is radially uniform be distributed in first chute and second chute it
Between, be separately connected to first chute and second chute, first hole it is open at one end by described first
Plate seal forms third chute;Third plate is located above second plate, and there is the radial direction along direction of rotation to prolong
Stretch the 4th chute and the 5th chute;4th chute and the first chute face fasten to form first runner, and the described 5th
Chute and the second chute face fasten to form second flow channel;Further include the second hole, there is multiple, the diameter along direction of rotation
To being evenly distributed between the 4th chute and the 5th chute, it is separately connected to the 4th chute and described
Five chutes;Fourth panel is located above the third plate, seals the open at one end of second hole, forms the 6th chute;
The third chute and the 6th chute face fasten to form third flow channel.
Preferably, along the first runner to the second flow channel direction, the cross section of the third flow channel
Product is changed from small to big.
Preferably, first pore interior is equipped with the first grid of several both ends opens, first grid
One end by first plate seal, form the first network;Second pore interior is equipped with several both ends opens
One end of second grid, second grid is sealed by the fourth panel, forms the second network;The first grid knot
Structure is staggeredly superimposed with second network, an opening for first grid and opening at least two second grids
Mouth is opposite, so that entering the refrigerant of the third flow channel staggeredly to enter the side of first grid and second grid
Formula flows through the third flow channel.
Preferably, first grid and/or second grid are polygonized structure, circular configuration.
It preferably, further include through first plate, second plate, the third plate and described the
The ventilation hole of four plates, the ventilation hole are not connected to the first runner, the second flow channel and the third flow channel.
Preferably, second plate and/or the third plate are equipped with several entity protrusions, the entity
The middle part of protrusion is hollow, forms the part ventilation hole.
Preferably, further include heat sink, be mounted on outside first plate and/or the fourth panel.
Preferably, the heat sink includes: stripe board, has several, parallel between two neighboring stripe board
It arranges, is fixedly connected between adjacent three stripe boards by least one " people " font batten.
The present invention also provides a kind of heat exchanger fins, for rotatably exchanging heat, as described at least any one of two panels above scheme
Heat exchanger fin stack combinations constitute.
Technical solution of the present invention has the advantages that
1. heat exchanger fin of the invention has the multiple third flow channels for independently connecting first runner and second flow channel, the
Three runners can guarantee that the refrigerant in runner is evenly distributed in rotation radiation processes along the radially uniform distribution of rotation
In cooling fin.
2. heat exchanger fin of the invention, by third flow channel along the direction of first runner to second flow channel, be set as cross-sectional area by
The small structure to become larger functions as diffuser pipe, and the flow velocity that refrigerant flows through third flow channel becomes smaller but pressure becomes larger, refrigerant
Each layer of third flow channel is uniformly entered with divergent shape, and promotes refrigerant along first runner to second flow channel under pressure
Direction flowing, the refrigerant be conducive in heat exchanger fin is back to refrigerant outlet.
3. heat exchanger fin of the invention is equipped with unhurried current structure inside third flow channel, refrigerant is in third flow channel internal flow
Provisional blocking by unhurried current structure in the process, slows down the flow velocity of refrigerant, increase that refrigerant retains in heat exchanger fin when
Between, be conducive to the utilization rate for increasing refrigerant, achieve the effect that sufficiently to exchange heat.
4. heat exchanger fin of the invention, the unhurried current structure having is made of two interlaced intercommunications of waffle slab, refrigerant with
Staggeredly slow down flow velocity of the refrigerant in third flow channel in third flow channel internal flow into the mode of two waffle slabs, increases
The specific surface area of refrigerant improves the heat exchange efficiency of refrigerant.
5. heat exchanger fin of the invention, network includes polygon or round, facilitates processing and manufacturing.
6. heat exchanger fin of the invention has the ventilation hole of perforation heat exchanger fin, ventilation hole is isolated with heat exchanger fin inner flow passage,
Outside air, which passes through ventilation hole, can be improved the heat exchange efficiency of heat exchanger fin inner flow passage refrigerant, while reduce resistance when rotation
Power.
7. heat exchanger fin of the invention, the ventilation hole with multiple perforation heat exchanger fins, are distributed in two adjacent third flow channels
Between, improve the heat exchange efficiency of third flow channel inner refrigerant.
8. heat exchanger fin of the invention is assembled using four plates, wherein the first plate and the second plate form and freeze
Three chutes of agent circulation, third plate and fourth panel form the other three chute of refrigerant circulation, by four Flat buckles
Close formed refrigerant circulation three runners, wherein every plate can independent processing and fabricating, simplify manufacture craft, reduce production
Cost.
9. heat exchanger fin of the invention is all provided in the first hole and the second hole being located in the second plate and third plate
There is the grid of several both ends opens, two the wherein open at one end of grid are sealed by the first plate and fourth panel respectively, by four
When piece plate fastens, the first hole and the opposite grid of the second hole inner opening are staggeredly superimposed, and refrigerant is staggeredly to enter two
The mode of waffle slab slows down flow velocity of the refrigerant in third flow channel in third flow channel internal flow, increases the ratio table of refrigerant
Area improves the heat exchange efficiency of refrigerant, and the network of third flow channel is formed by the way of four plate simple superposition, letter
Change the manufacture craft of heat exchanger fin, reduces manufacturing cost.
10. heat exchanger fin of the invention is avoided in the ventilation hole setting on the second plate and third plate in entity protrusion
The connection of ventilation hole and heat exchanger fin inner flow passage effectively avoids the leakage of refrigerant, and protrusion can play the role of pressure-bearing, after being conducive to
Phase machine-shaping makes to combine by diffusion welding (DW) between each plate.
11. heat exchanger fin of the invention has heat sink, the heat exchange for increasing heat exchanger fin surface heat and outside air is imitated
Rate.
12. heat exchanger fin of the invention, the heat sink of outer layer covers has several stripe boards, between two neighboring stripe board
It is arranged in parallel, is fixedly connected between adjacent three stripe boards by least one " people " font batten, it is empty in heat exchanger fin and outside
When gas contacts, heat sink can make air uniform divided flows, disperse the air drag of heat exchanger fin each section, and having reduces noise of air
With reinforcing heat dissipation effect, " people " font batten has preferably support pressure-bearing effect simultaneously.
It, can be according to reality 13. combination heat exchanger fin of the invention is made of heat exchanger fin stack combinations described in any of the above embodiments
Need to be arranged reasonable heat exchanger fin quantity, combination simple and flexible.
14. heat exchanger fin of the invention, meshed raceway makes that heat transfer efficiency is high, refrigerant charge is few, compactness is high, clathrum
Flow-disturbing can not only be played and increase heat exchange area, enhancing refrigerant fluid interchange ability, can also be played in diffusion bond
Support the effect of pressure-bearing;It is combined between each plate using diffusion welding (DW) mode, contacts the holding between two layers of plate well, guaranteed
It is not leaked inside runner, eliminates the influence of thermal contact resistance exchange hot property, voltage endurance capability is higher;Using half-etching runner processing
Inlet and outlet have entity raised, play a supporting role;The inlet and outlet of refrigerant are designed in the same side, but its position does not exist
In approximately the same plane, internal heat is not influenced.
Detailed description of the invention
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art be briefly described, it should be apparent that, it is described below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the schematic perspective view of heat exchanger fin of the present invention.
Fig. 2 is the perspective structure schematic diagram of heat exchanger fin shown in FIG. 1.
Fig. 3 is the main view after the second plate and third plate fastening.
Fig. 4 is the schematic cross-sectional view of heat exchanger fin shown in Fig. 3.
Fig. 5 is the rearview after the first plate and the second plate fastening.
Fig. 6 is the main view after third plate and fourth panel fastening.
Fig. 7 is the main view of heat sink.
Fig. 8 is the explosive view of heat exchanger fin.
Fig. 9 is the schematic perspective view of present invention combination heat exchanger fin.
Figure 10 is the schematic view of the front view of grid.
Figure 11 is the schematic view of the front view of ventilation hole.
Figure 12 is the schematic view of the front view of heat sink.
Description of symbols:
1- first runner, 2- second flow channel, 3- third flow channel, 4- refrigerant inlet, 5- refrigerant outlet, the first grid of 6-
Structure, the second network of 7-, 8- first are open, and 9- second is open, 10- ventilation hole, the first plate of 11-, the second plate of 12-,
13- third plate, 14- fourth panel, the first chute of 15-, the second chute of 16-, 17- third chute, the 4th chute of 18-, 19-
Five chutes, the 6th chute of 20-, the first hole of 21-, the second hole of 22-, 23- entity protrusion, 24- heat sink, 25- stripe board,
The first grid of 61-, the second grid of 71-.
Specific embodiment
Technical solution of the present invention is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill
Personnel's every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the instructions such as term " on ", "lower", "vertical", "inner", "outside"
Orientation or positional relationship is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of the description present invention and simplification is retouched
It states, rather than the device or element of indication or suggestion meaning must have a particular orientation, be constructed and operated in a specific orientation,
Therefore it is not considered as limiting the invention.In addition, term " first ", " second ", " third ", " the 4th ", " the 5th ", "
Six " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected;It can
To be to be connected directly, the connection inside two elements can also be can be indirectly connected through an intermediary.For this field
For those of ordinary skill, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
As long as in addition, the non-structure each other of technical characteristic involved in invention described below different embodiments
It can be combined with each other at conflict.
Embodiment 1
As shown in Figure 1 and Figure 2, a kind of heat exchanger fin is used for rotary heat radiation, comprising: first runner 1, second flow channel 2, third
Runner 3 and multiple ventilation holes 10.
First runner 1 is located at the front of heat exchanger fin direction of rotation, and radially extending along rotation, has refrigerant inlet 4.
Second flow channel 2 is located at the rear of heat exchanger fin direction of rotation, and radially extending along rotation, has refrigerant outlet 5.
Third flow channel 3 have it is multiple, along heat exchanger fin rotation it is radially uniform be distributed in first runner 1 and second flow channel 2 it
Between, separately it is connected to first runner 1 and second flow channel 2;Third flow channel 3 is along first runner 1 to the side of second flow channel 2
To cross-sectional area changes from small to big.
Multiple ventilation holes 10 are distributed between two adjacent third flow channels 3 through heat exchanger fin, and ventilation hole 10 not with
First runner 1, second flow channel 2 and third flow channel 3 are connected to.
As shown in Figure 5, Figure 6, the unhurried current structure for slowing down refrigerant flow rates is additionally provided with inside third flow channel 3, flow slowly structure packet
It includes: the first network 6 and the second network 7.
First network 6 is distributed in inside third flow channel 3, including multiple first grids 61, one end of the first grid 61
Sealing, the other end form the first opening 8.
Second network 7 is distributed in inside third flow channel 3, including multiple second grids 71, one end of the second grid 71
Sealing, the other end form the second opening 9.
First network 6 is staggeredly superimposed with the second network 7, one first opening 8 and at least two second openings 9
Relatively, so that the refrigerant for entering third flow channel 3 flows through third in a manner of staggeredly entering the first opening 8 and the second opening 9
Runner 3;Wherein the first grid 61 is polygonized structure or circular configuration, and the second grid 71 is polygonized structure or circular configuration.
As the alternative of above-described embodiment, ventilation hole 10 can only have one, and need not necessarily need to be provided at adjacent two
Between third flow channel 3.
As the alternative of above-described embodiment, ventilation hole 10 be can be omitted.
As the alternative of above-described embodiment, the first grid 61 can also be that triangle, rectangle etc. have closing knot
The geometric figure of structure, the second grid 71 are also possible to the geometric figure that triangle, rectangle etc. have enclosed construction.
As the alternative of above-described embodiment, the structure that flows slowly can also be that throttle orifice, semi-closed plate etc. can be interrupted
Property reduce 3 aperture of third flow channel structure.
As the alternative of above-described embodiment, the structure that flows slowly be can be omitted.
As the alternative of above-described embodiment, the cross-sectional area of third flow channel 3, which can not be done, to be changed, can also basis
Each third flow channel 3 adjusts the size of each 3 cross-sectional area of third flow channel at a distance from heat exchanger fin rotation center.
Working principle
As shown in Figure 1 and Figure 2, refrigerant enters heat exchanger fin by refrigerant inlet 4, during heat exchanger fin rotary work, system
Cryogen quickly fills with first runner 1, then respectively enters third flow channel 3 and exchanges heat, and refrigeration is finally flowed in second flow channel 2
Agent outlet 5, completes heat transfer process of the refrigerant in heat exchanger fin, third flow channel 3 independently with first runner 1 and second
Road 2 is connected to, and is avoided refrigerant under the action of heat exchanger fin rotary centrifugal force and is assembled on top, refrigerant is evenly distributed on and is changed
In backing, heat exchange efficiency is improved.
After refrigerant is from first runner 1 into third flow channel 3, since the sectional area that third flow channel 3 starts is smaller, system
Flow velocity is all than very fast under the effect of the pressure cryogen, and when entering the bigger third flow channel 3 of sectional area, refrigerant is to send forth
Form projects, and increases specific surface area of the refrigerant in third flow channel 3, increases heat exchange efficiency.
In third flow channel 3, blocking of the refrigerant by unhurried current structure, flow path not instead of straight line will be bypassed
On the one hand several bendings can reduce the flow velocity of refrigerant during around bending, keep refrigerant more in third flow channel 3
A period of time is retained, increases the heat transfer rate of refrigerant, on the other hand can break up refrigerant, enabling the refrigerant to will be in runner
Wall is full of, and increases the heat exchange area of refrigerant, improves heat exchange efficiency.
In heat exchanger fin rotary course, outside air is passed through from ventilation hole, on the one hand can reduce the resistance of heat exchanger fin,
On the other hand the contact area for increasing heat exchanger fin and outside air, increases heat exchange efficiency.
Embodiment 2
As shown in figure 8, a kind of heat exchanger fin, for rotatably exchanging heat, comprising: the first plate 11, the second plate 12, third are flat
Plate 13, fourth panel 14, ventilation hole 10 and heat sink 24, wherein the first plate 11, the second plate 12, third plate 13 and
Four plates 14 are sequentially overlapped connection from bottom to up.
As shown in figure 3, figure 4 and figure 5, the second plate 12 is located at 11 top of the first plate, comprising: the first chute 15, second
Slot 16 and the first hole 21;First the radially extending along heat exchanger fin direction of rotation of chute 15, positioned at the front of direction of rotation, tool
There is refrigerant inlet 4;Second the radially extending along heat exchanger fin direction of rotation of chute 16 has system positioned at the rear of direction of rotation
Cryogen outlet 5;First hole 21 have it is multiple, radially uniform along heat exchanger fin direction of rotation is distributed in the first chute 15 and second
Between chute 16, it is separately connected to the first chute 15 and the second chute 16;Several both ends are equipped with inside first hole 21 to open
First grid 61 of mouth, the open at one end of the first grid 61 are sealed by the first plate 11, form the third stream of the first network 6
Slot 17.
As shown in Fig. 3, Fig. 4, Fig. 6, third plate 13 is located above the second plate 12, including the 4th chute 18, and the 5th
Chute 19 and the second hole 22;4th the radially extending along heat exchanger fin direction of rotation of chute 18 fastens with 15 face of the first chute
Form first runner 1;5th the radially extending along heat exchanger fin direction of rotation of chute 19 fastens to form with 16 face of the second chute
Two runners 2;Second hole 22 has multiple, and radially uniform along heat exchanger fin direction of rotation is distributed in the 4th chute 18 and the 5th stream
Between slot 19, it is separately connected to the 4th chute 18 and the 5th chute 19;Several both ends opens are equipped with inside second hole 22
The second grid 71, the open at one end of the second grid 71 sealed by fourth panel 14, forms the 6th stream of the second network 7
Slot 20.
Third chute 17 and 20 face of the 6th chute fasten, and form third flow channel 3;In third flow channel 3, the first grid
Structure 6 is staggeredly superimposed with the second network 7, the opening and the opening phase of at least two second grids 71 of first grid 61
It is right, so that the refrigerant for entering third flow channel 3 flows through third in a manner of staggeredly entering the first grid 61 and the second grid 71
Runner 3;Along first runner 1 to 2 direction of second flow channel, the cross-sectional area of third flow channel 3 changes from small to big;First grid 61 is
Polygonized structure or circular configuration;Second grid 71 is polygonized structure or circular configuration.
Ventilation hole 10 run through the first plate 11, the second plate 12, third plate 13 and fourth panel 14, and not with it is first-class
Road 1, second flow channel 2 and third flow channel 3 are connected to;Several entity protrusions 23 are equipped in the second plate 12, the setting of ventilation hole 10 exists
The middle part of entity protrusion 23;Several entity protrusions 23 are equipped on third plate 13, entity protrusion 23 is arranged in ventilation hole 10
Middle part.
As shown in Figure 7, Figure 8, heat sink 24 are mounted on outside 11 outside of the first plate or fourth panel 14, or pacify simultaneously
Outside the first plate 11 and fourth panel 14, single-layer or multi-layer can be used, comprising: several stripe boards 25, it is two neighboring
It is arranged in parallel between stripe board 25, is fixedly connected between adjacent three stripe boards 25 by least one " people " font batten.
As the alternative of above-described embodiment, heat sink 24, which can be, is covered on the outside of the first plate 11 and/or the
Orifice plate or fin outside four plates 14.
As the alternative of above-described embodiment, heat sink 24 be can be omitted.
As the alternative of above-described embodiment, entity protrusion 23 be can be omitted, and ventilation hole 10 can be using with wall
Hollow pipe passes through the second plate 12 and third plate 13.
As the alternative of above-described embodiment, ventilation hole 10 be can be omitted.
As the alternative of above-described embodiment, the first grid 61 can also be that triangle, rectangle etc. have closing knot
The geometric figure of structure, the second grid 71 are also possible to the geometric figure that triangle, rectangle etc. have enclosed construction.
As the alternative of above-described embodiment, the first network 6 and the second network 7 be can be omitted, or with
The replacement of the structures such as throttle orifice, semi-closed plate achievees the effect that discontinuity reduces 3 aperture of third flow channel.
As the alternative of above-described embodiment, the cross-sectional area of third flow channel 3, which can not be done, to be changed, can also basis
Each third flow channel 3 adjusts the size of each 3 cross-sectional area of third flow channel at a distance from heat exchanger fin rotation center.
In above-described embodiment, heat exchanger fin is formed by the way of plate superposition, after chute combination is arranged on each monolithic plate
Refrigerant flow path is formed, monolithic plate can distinguish processing and fabricating, simplify manufacture craft, and the material of plate uses stainless steel, titanium
Alloy, nickel base superalloy or the composite material with heat transmission function, after the completion of monolithic flat panel production, using diffusion welding (DW), one
Under the action of determining temperature and pressure, welding point is formed using the effect that atom is spread, two neighboring plate is fitted closely, is expanded
Scattered weldering does not need addition packing material, does not need to make welding in molten state.
Heat exchanger fin is under the shape for keeping flabellum, and there are equivalent diameters in the microchannel below 1mm, heat transfer efficiency for inside
Height, refrigerant charge is few, compactness is high.
The inlet and outlet of refrigerant are designed in the same side on heat exchanger fin, but the position where it is not in the same plane, has
Help evenly distributing and collecting for refrigerant.
As shown in Figure 10, in any of the above-described embodiment, the wide 0.1 < a1 < 1mm of waffle slab key dimension grid ribs is horizontal
Distance a1 < a2 < 2mm, vertical distance a1 < a3 < 2mm.
As shown in figure 11, in any of the above-described embodiment, ventilation hole is rectangular through-hole, 0 < L1 of rectangular ventilation holes key dimension
< 5mm, 0 < L2 < 15mm, 0.5 < d1 < 1mm, 1 < d2 < 2mm, can not only increase whole heat exchange efficiency, can also subtract
Resistance when small rotation.
As shown in figure 12, in any of the above-described embodiment, 0 < b1 < 1mm of heat sink key dimension, b1 < b2 < 1.5mm,
0 ° of 180 ° of < α <.
Embodiment 3
As shown in figure 9, a kind of combination heat exchanger fin, for rotatably exchanging heat, the heat exchanger fin as described in two panels above-described embodiment
Stack combinations are constituted.
As the alternative of above-described embodiment, the quantity of heat exchanger fin superposition can be set as multi-disc according to actual needs.
Obviously, the above embodiments are merely examples for clarifying the description, and does not limit the embodiments.It is right
For those of ordinary skill in the art, can also make on the basis of the above description it is other it is various forms of variation or
It changes.There is no necessity and possibility to exhaust all the enbodiments.And it is extended from this it is obvious variation or
It changes still within the protection scope of the invention.
Claims (16)
1. a kind of heat exchanger fin is used for rotary heat radiation, it is characterised in that: include:
First runner (1), positioned at the front of direction of rotation, and radially extending along rotation, have refrigerant inlet (4);
Second flow channel (2), positioned at the rear of direction of rotation, and radially extending along rotation, have refrigerant outlet (5);
Third flow channel (3), has multiple, radially uniform is distributed in the first runner (1) and the second flow channel along rotation
(2) between, the first runner (1) and the second flow channel (2) are separately connected to.
2. heat exchanger fin according to claim 1, it is characterised in that: along the first runner (1) to the second flow channel
(2) cross-sectional area in direction, the third flow channel (3) changes from small to big.
3. heat exchanger fin according to claim 1, it is characterised in that: be additionally provided with inside the third flow channel (3) and slow down refrigeration
The unhurried current structure of agent flow velocity.
4. heat exchanger fin according to claim 3, it is characterised in that: the unhurried current structure includes:
First network (6) is distributed in the third flow channel (3) inside, including multiple first grids (61), first net
One end of lattice (61) seals, and the other end forms the first opening (8);
Second network (7) is distributed in the third flow channel (3) inside, including multiple second grids (71), second net
One end of lattice (71) seals, and the other end forms the second opening (9);
First network (6) and second network (7) staggeredly be superimposeds, first opening (8) and extremely
Few two second openings (9) relatively, enter described first so that entering the refrigerant of the third flow channel (3) to interlock
The mode of opening (8) and second opening (9) flows through the third flow channel (3).
5. heat exchanger fin according to claim 4, it is characterised in that: first grid (61) and/or second grid
It (71) is polygonized structure, circular configuration.
6. heat exchanger fin according to any one of claims 1-5, it is characterised in that: further include ventilation hole (10), through changing
Backing setting, also, the ventilation hole (10) not with the first runner (1), the second flow channel (2) and the third stream
Road (3) connection.
7. heat exchanger fin according to claim 6, it is characterised in that: the ventilation hole (10) have it is multiple, be distributed in adjacent
Two third flow channels (3) between.
8. a kind of heat exchanger fin, for rotatably exchanging heat, it is characterised in that: include:
First plate (11);
Second plate (12) is located above first plate (11), has the first chute radially extended along direction of rotation
(15) and the second chute (16);First chute (15) is located at the front of direction of rotation, has refrigerant inlet (4);It is described
Second chute (16) is located at the rear of direction of rotation, has refrigerant outlet (5);Further include the first hole (21), have it is multiple,
Radially uniform along direction of rotation is distributed between first chute (15) and second chute (16), is separately connected
Lead to first chute (15) and second chute (16), first hole (21) it is open at one end by first plate
(11) it seals, is formed third chute (17);
Third plate (13) is located above second plate (12), has and radially extends the 4th chute along direction of rotation
(18) and the 5th chute (19);4th chute (18) and the first chute (15) face fasten to form first runner (1),
5th chute (19) and the second chute (16) face fasten to form second flow channel (2);It further include the second hole (22),
With multiple, radially uniform along direction of rotation is distributed between the 4th chute (18) and the 5th chute (19), point
It is not connected to the 4th chute (18) and the 5th chute (19) independently;
Fourth panel (14) is located above the third plate (13), seals the open at one end of second hole (22), is formed
6th chute (20);The third chute (17) and the 6th chute (20) face fasten to form third flow channel (3).
9. heat exchanger fin according to claim 8, it is characterised in that: along the first runner (1) to the second flow channel
(2) cross-sectional area in direction, the third flow channel (3) changes from small to big.
10. heat exchanger fin according to claim 8, it is characterised in that:
The first grid (61) of several both ends opens, one end of first grid (61) are equipped with inside first hole (21)
It is sealed, is formed the first network (6) by first plate (11);
The second grid (71) of several both ends opens, one end of second grid (71) are equipped with inside second hole (22)
It is sealed, is formed the second network (7) by the fourth panel (14);
First network (6) and second network (7) be staggeredly superimposed, and one the first grid (61) is opened
Mouth is opposite with the opening of at least two second grids (71), so that entering the refrigerant of the third flow channel (3) to hand over
Mistake enters first grid (61) and the mode of second grid (71) flows through the third flow channel (3).
11. heat exchanger fin according to claim 10, it is characterised in that: first grid (61) and/or second net
Lattice (71) are polygonized structure, circular configuration.
12. heat exchanger fin according to claim 8, it is characterised in that: further include through first plate (11), described the
The ventilation hole (10) of two plates (12), the third plate (13) and the fourth panel (14), the ventilation hole (10) not with
The first runner (1), the second flow channel (2) and the third flow channel (3) connection.
13. heat exchanger fin according to claim 12, it is characterised in that: second plate (12) and/or the third are flat
Plate (13) is equipped with several entities protrusions (23), and the middle part of the entity raised (23) is hollow, forms the part ventilation hole
(10)。
14. heat exchanger fin according to claim 8, it is characterised in that: further include heat sink (24), it is flat to be mounted on described first
Plate (11) and/or the fourth panel (14) are external.
15. heat exchanger fin according to claim 14, it is characterised in that: the heat sink (24) includes:
Stripe board (25), have several, be arranged in parallel between two neighboring stripe board (25), adjacent three stripe boards (25) it
Between be fixedly connected by least one " people " font batten.
16. a kind of combination heat exchanger fin, for rotatably exchanging heat, it is characterised in that: by any at least two panels claim 8~15
Heat exchanger fin stack combinations described in are constituted.
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CN201710442737.2A CN109084608A (en) | 2017-06-13 | 2017-06-13 | A kind of heat exchanger fin |
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CN201710442737.2A CN109084608A (en) | 2017-06-13 | 2017-06-13 | A kind of heat exchanger fin |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110398166A (en) * | 2019-08-28 | 2019-11-01 | 浙江工业大学 | A kind of Fumigator heat recoverer |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102230692A (en) * | 2010-06-29 | 2011-11-02 | 三花丹佛斯(杭州)微通道换热器有限公司 | Heat exchanger with improved heat exchange performance |
CN103776285A (en) * | 2014-02-20 | 2014-05-07 | 杭州沈氏换热器有限公司 | Micro-channel heat exchanger |
CN105526813A (en) * | 2015-12-10 | 2016-04-27 | 上海理工大学 | Microchannel heat radiator |
CN106288526A (en) * | 2016-08-31 | 2017-01-04 | 合肥美的电冰箱有限公司 | Micro-channel heat exchanger and refrigerator, wind cooling refrigerator |
CN206832110U (en) * | 2017-06-13 | 2018-01-02 | 杭州沈氏节能科技股份有限公司 | A kind of heat exchanger fin |
-
2017
- 2017-06-13 CN CN201710442737.2A patent/CN109084608A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102230692A (en) * | 2010-06-29 | 2011-11-02 | 三花丹佛斯(杭州)微通道换热器有限公司 | Heat exchanger with improved heat exchange performance |
CN103776285A (en) * | 2014-02-20 | 2014-05-07 | 杭州沈氏换热器有限公司 | Micro-channel heat exchanger |
CN105526813A (en) * | 2015-12-10 | 2016-04-27 | 上海理工大学 | Microchannel heat radiator |
CN106288526A (en) * | 2016-08-31 | 2017-01-04 | 合肥美的电冰箱有限公司 | Micro-channel heat exchanger and refrigerator, wind cooling refrigerator |
CN206832110U (en) * | 2017-06-13 | 2018-01-02 | 杭州沈氏节能科技股份有限公司 | A kind of heat exchanger fin |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110398166A (en) * | 2019-08-28 | 2019-11-01 | 浙江工业大学 | A kind of Fumigator heat recoverer |
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