CN104154802A - Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner - Google Patents
Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner Download PDFInfo
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- CN104154802A CN104154802A CN201410410165.6A CN201410410165A CN104154802A CN 104154802 A CN104154802 A CN 104154802A CN 201410410165 A CN201410410165 A CN 201410410165A CN 104154802 A CN104154802 A CN 104154802A
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- flow dividing
- flute profile
- refrigerant flow
- dividing structure
- refrigerant
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- 239000003507 refrigerant Substances 0.000 title claims abstract description 93
- 239000012530 fluid Substances 0.000 claims description 16
- 230000008676 import Effects 0.000 claims description 9
- 238000009736 wetting Methods 0.000 claims description 4
- 238000009826 distribution Methods 0.000 abstract description 5
- 230000001276 controlling effect Effects 0.000 description 5
- 230000005484 gravity Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000005219 brazing Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention relates to a refrigerant flow distribution structure, a micro-channel flow distribution assembly, a heat exchanger and an air conditioner. The invention can control the amount of the refrigerant entering the shunting cavity, provides conditions for accurately controlling the distribution amount of the refrigerant, has no influence on the height of the whole structure shunting structure and has wider application range.
Description
Technical field
The present invention relates to air-conditioner technical field, particularly relate to a kind of refrigerant flow dividing structure, microchannel shunt assembly, heat exchanger and air-conditioner.
Background technology
Micro-channel heat exchanger progressively obtains applying more and more widely because of its heat exchange efficiency height in air-conditioning system, and its version is: two, both sides collector parallel to each other, the flat tube of the porous by many heat exchange between two collectors connects.Micro-channel heat exchanger, as heat exchanger, while carrying out work, need to be assigned to by distribution structure (i.e. " distributor ") many flat tubes that are connected with collector from the inner chamber of collector for the cold-producing medium that conducts heat or cold such as condenser.But above-mentioned assigning process often there will be cold-producing medium to distribute difficult problem, it easily causes micro-channel heat exchanger to be subject to restriction to a certain extent in heat exchange application.For this problem, current existing solution has:
1) continue to use the shunting mode of traditional finned tube exchanger, be divided into multiple branch roads, adopt shunting capillary to shunt.But, tens easily of the flat tubes that this scheme is used, even up to a hundred, this shunting mode makes distributor volume too large, and so shunts multiple branch circuit and cause complicated integral structure.
2) when micro-channel heat exchanger is installed and used, make each flat tube be vertical direction and arrange, now isocon is in same level, thereby can shunt in same level, and then makes shunting more even.But, when cold-producing medium flows in the vertical flat tube of placing, its gravity can increase the resistance of fluid in pipe, if distribute from bottom to top, highly too large, need to overcome larger gravitional force, cause system pressure ratio large, cause upstream and downstream distribution of refrigerant inequality, heat exchange efficiency is low, therefore micro-channel heat exchanger is unsuitable too high, is only only applicable to undersized plate shaped heat exchanger.In addition, while vertically arranging flat tube, if bending design easily causes fin to depart from flat tube, so generally do not adopt bendable heat exchanger.
Prior art exists the improved demand of above-mentioned technical problem.
Summary of the invention
The object of the invention is to propose a kind of improved refrigerant flow dividing structure, microchannel shunt assembly, heat exchanger and air-conditioner, the cold-producing medium while having solved micro-channel heat exchanger heat exchange distributes difficult problem.
For achieving the above object, the invention provides following technical scheme:
A kind of refrigerant flow dividing structure, it comprises cylinder, on described cylinder, be provided with shunting chamber, refrigerant inlet and runner, wherein: described runner is the flute profile runner arranging along the outer surface of described cylinder, described in described refrigerant inlet and each, shunting chamber is communicated with via described flute profile runner fluid.
Further, described flute profile runner around described refrigerant inlet radially.
Further, described refrigerant inlet directly by described flute profile runner with described in each, shunt chamber fluid and be communicated with.
Further, described flute profile runner is bifurcation structure, has import and at least two outlets, and described import is communicated with described refrigerant inlet fluid, exports corresponding fluid described in each and shunts chamber described in being communicated with one.
Further, described flute profile runner is straight line or curve.
Further, the cross section of described flute profile runner be shaped as circle, ellipse, rectangle or D shape.
Further, D=4S/C, wherein: described D, described S and described C are respectively the wetting girth of hydraulic diameter, cross-sectional area and cross section of described flute profile runner.
Further, the height on the lower edge of the outlet of described flute profile runner is higher than the height on the lower edge in described shunting chamber.
Further, each described shunting chamber extends to described column body from the outer surface of described cylinder, forms comb teeth-shaped.
The present invention also provides a kind of microchannel shunt assembly, comprises collector, and described collector is provided with refrigerant inlet and flat pipe hole; It comprises the refrigerant flow dividing structure in the various embodiments described above, described collector is set in outside the cylinder in described refrigerant flow dividing structure and is connected, the center line of the refrigerant inlet of described collector overlaps substantially with the center line of the refrigerant inlet on described cylinder, and the center line of described flat pipe hole is substantially concordant with the center line in the shunting chamber on described cylinder.
The present invention also provides a kind of micro-channel heat exchanger, and it comprises the refrigerant flow dividing structure in the various embodiments described above.
Further, also comprise collector and flat tube, wherein: described collector is provided with refrigerant inlet and flat pipe hole, described collector is set in outside the cylinder in described refrigerant flow dividing structure and is connected, the center line of the refrigerant inlet of described collector overlaps substantially with the center line of the refrigerant inlet on described cylinder, and the center line of described flat pipe hole is substantially concordant with the center line in the shunting chamber on described cylinder; Described flat tube is arranged in described shunting chamber by described flat pipe hole.
The present invention also provides a kind of air-conditioner, and it comprises the refrigerant flow dividing structure in the various embodiments described above.
Based on technique scheme, advantage of the present invention is:
Because the present invention is provided with cylinder, on cylinder, be provided with shunting chamber, refrigerant inlet and runner, runner is the flute profile runner that is arranged on body surfaces, between refrigerant inlet and each shunting chamber, be connected by flute profile runner, by one or more parameters in track curvature, path length, cross-sectional area and the shape of cross section of control flute profile runner, thereby can control the amount that enters the cold-producing medium in shunting chamber, for the sendout of accurately controlling cold-producing medium provides condition; In addition, can be by flat tube horizontal positioned when the present invention installs and uses, therefore cold-producing medium flowing in flat tube can not be subject to the impact of gravity, thus the height of total flow dividing structure can not be affected, and then the scope of application is wider.
Brief description of the drawings
Accompanying drawing described herein is used to provide a further understanding of the present invention, forms the application's a part, and schematic description and description of the present invention is used for explaining the present invention, does not form inappropriate limitation of the present invention.In the accompanying drawings:
Fig. 1 is the structural representation of an embodiment of micro-channel heat exchanger provided by the present invention;
Fig. 2 is the general assembly exploded view of Fig. 1;
Fig. 3~6 are the structural representation of the refrigerant flow dividing structure in Fig. 1;
Fig. 7~10 are the structural representation of the collector in Fig. 1.
Detailed description of the invention
For making object of the invention process, technical scheme and advantage clearer, below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is further described in more detail.In the accompanying drawings, same or similar label represents same or similar element or has the element of identical or similar functions from start to finish.Described embodiment is the present invention's part embodiment, instead of whole embodiment.Be exemplary below by the embodiment being described with reference to the drawings, be intended to for explaining the present invention, and can not be interpreted as limitation of the present invention.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtaining under creative work prerequisite, belong to the scope of protection of the invention.Below in conjunction with accompanying drawing, embodiments of the invention are elaborated.
In description of the invention, it will be appreciated that, term " " center ", " longitudinally ", " laterally ", " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end ", " interior ", orientation or the position relationship of instructions such as " outward " are based on orientation shown in the drawings or position relationship, only the present invention for convenience of description and simplified characterization, instead of device or the element of instruction or hint indication must have specific orientation, with specific orientation structure and operation, therefore can not be interpreted as limiting the scope of the invention.
As shown in Fig. 1~10, refrigerant flow dividing structure provided by the present invention comprises cylinder 1, is provided with shunting chamber 2, refrigerant inlet 4 and runner on cylinder 1.Wherein: described runner is the flute profile runner 5 arranging along the outer surface of cylinder 1, refrigerant inlet 4 and each shunting chamber 2 are communicated with via flute profile runner 5 fluids.Being not intended is herein confined to refrigerant inlet 4 and is directly communicated with each shunting chamber 2 fluid by flute profile runner 5, and refrigerant inlet 4 can also be shunted chamber 2 via flute profile runner 5 and the parts except flute profile runner 5 and each and carry out fluid and be communicated with.The present invention can be by one or more parameters in track curvature, path length, cross-sectional area and the shape of cross section of control flute profile runner, thereby can control the amount that enters the cold-producing medium in shunting chamber, for the sendout of accurately controlling cold-producing medium provides condition.
In above-described embodiment, several shuntings chamber 2 is all opened in cylinder 1 surface and distributes along the axially spaced-apart of cylinder 1, such as: respectively shunt chamber 2 and all can extend to cylinder 1 inside from the outer surface of cylinder 1, form comb teeth-shaped.Each shunting chamber 2 is for placing flat tube 3, the number of the flat tube 3 that it holds can be one, can be also multiple, that is to say, can several flat tubes 3 by same shunting chamber 2 the supply system cryogens, can on the comparatively limited cylinder 1 of volume, realize more flow manifold like this.Certainly, the thickness sum of each flat tube 3 and the height in this shunting chamber 2 in each shunting chamber 2 is suitable.
Refrigerant inlet 4 is opened on cylinder 1 and shunts the part outside chamber 2, between refrigerant inlet 4 and each shunting chamber 2, is connected by flute profile runner 5, and each flute profile runner 5 is offered along the surface of cylinder 1.As can be seen from the figure: flute profile runner 5 around refrigerant inlet 4 radially.Flute profile runner 5 has import 51 and outlet 52, and import 51 is connected with refrigerant inlet 4, and outlet 52 connects shunting chamber 2.Therefore, cold-producing medium enters the import 51 of flute profile runner 5 from refrigerant inlet 4, arrives outlet 52, then entered in coupled logical shunting chamber 2 by outlet 52 via flute profile runner 5, is finally entered in flat tube 3 by shunting chamber 2.
Certainly, refrigerant inlet 4 can directly be communicated with each shunting chamber 2 fluid by flute profile runner 5.Also flute profile runner 5 can be set to bifurcation structure, make flute profile runner 5 have import and at least two outlets, this import is communicated with refrigerant inlet 4 fluids, and each exports corresponding fluid and is communicated with a shunting chamber 2.In the present embodiment, the flute profile runner 5 of bifurcation structure can spread shunting to cold-producing medium step by step, this simple in structure, has solved cold-producing medium and has distributed difficult problem, for the sendout of accurately controlling cold-producing medium provides condition.
For relative altitude lower than for the shunting chamber 2 of refrigerant inlet 4, the cold-producing medium of carrying from refrigerant inlet 4 is because Action of Gravity Field must have certain gravitional force, this gravitional force can change into the kinetic energy of cold-producing medium, so relative altitude is more easily assigned to cold-producing medium than relative altitude higher than the shunting chamber 2 of refrigerant inlet 4 lower than the shunting chamber 2 of refrigerant inlet 4, therefore, the intermediate altitude that refrigerant inlet 4 is arranged on cylinder 1 by the present invention is comparatively suitable, to ensure that distributed uniform is as principle as far as possible.
As can be seen from the above analysis: by controlling flute profile runner 5, can distribute equably the amount that enters the cold-producing medium in shunting chamber 2, and the structure of refrigerant flow dividing structure provided by the present invention is more simple with respect to traditional finned tube exchanger in prior art, and can be by flat tube 3 horizontal positioned while installing and using, therefore cold-producing medium flowing in flat tube 3 can not be subject to the impact of gravity, thereby the height of total flow dividing structure can not be affected, and then the scope of application is wider.
In above-described embodiment, at least one parameter in track curvature, path length, cross-sectional area and the shape of cross section of flute profile runner 5 is adjustable.The pressure of the refrigerant fluid of refrigerant inlet 4 is identical, by regulating one or more in track curvature, path length, cross-sectional area and the shape of cross section of flute profile runner 5, cold-producing medium can be accurately controlled from refrigerant inlet 4 to the pressure drop shunting chamber 2, thereby the refrigerant flow that enters shunting chamber 2 can be controlled.Refrigerant inlet 4 is less to the pressure drop between shunting chamber 2, less along resistance and the pressure loss of flute profile runner 5, and flow velocity is also just faster, and unit interval flow is also just larger.Below by parameters, the impact of the refrigerant flow that enters shunting chamber 2 is described.
1,, about track curvature, it refers to route that flute profile runner 5 will be walked or the radius of track, such as being straight path, and also can curvilinear path.Straight path wherein and curvilinear path are compared known: under the identical situation of path length, cross-sectional area and shape of cross section, the radius of curvature of straight path is less, cold-producing medium is after the flute profile runner 5 of straight path, the pressure loss is less, pressure drop is also just less, thereby it is relatively larger to distribute to the flow in shunting chamber 2.
2,, about path length, it refers to the distance that flute profile runner 5 will be walked.Under the identical situation of track curvature, cross-sectional area and shape of cross section, the shorter pressure loss of path length is less, and pressure drop is also just less, thereby it is relatively larger to distribute to the flow in shunting chamber 2.
3,, about shape of cross section, it can be the regular shapes such as circle, ellipse, rectangle or D shape, can also be the irregularly shaped of other.Under the identical situation of track curvature, path length and cross-sectional area, circular circulating resistance is less, and the pressure loss is less, and pressure drop is also just less, thereby it is relatively larger to distribute to the flow in shunting chamber 2.
4, about cross-sectional area, under the identical situation of track curvature, path length and shape of cross section, cross-sectional area is larger, and circulating resistance is less, and the pressure loss is less, and pressure drop is also just less, thereby it is relatively larger to distribute to the flow in shunting chamber 2.Given this, for the flute profile runner 5 of on-circular cross-section characteristic size, D=4S/C, wherein: D is the hydraulic diameter of flute profile runner 5, S is the cross-sectional area of flute profile runner 5, C is the wetting girth of the cross section of flute profile runner 5.By controlling cross-sectional area and the wetting girth of cross section of flute profile runner 5, can control the hydraulic diameter of flute profile runner 5, and then control the flow of distributing to shunting chamber 2.
According to the actual requirements, can control separately track curvature, path length, cross-sectional area and the shape of cross section of above flute profile runner 5, also can even multiplely to wherein two jointly control, to reach the object of refrigerant flow in accurate control shunting chamber 2.
In actual manufacture process, when micro-channel heat exchanger is designed, the heat exchange amount of micro-channel heat exchanger is known, according to design conditions, refrigerant flow is measured to determine by known heat exchange, when after the basic length and width of micro-channel heat exchanger and high size restrictions, the number of branches of flute profile runner 5 is also corresponding to be determined; Then, according to the difference of the heat transfer effect of each flute profile runner 5, by adjusting track curvature, path length, cross-sectional area and the shape of cross section etc. of flute profile runner 5, the sendout of the refrigerant flow to each flute profile runner 5 is controlled, thereby realize, the refrigerant flow in each shunting chamber 2 is accurately controlled.Wherein, the long-pending size of flow channel cross-section is more remarkable on the impact of refrigerant flow, controls the large I of sectional area with respect to more conveniently carrying out flow coarse adjustment; Different shape of cross sections is except the resistance of controllable flow body circulation and adjusting refrigerant flow rate, be also convenient to according to processing regulate, processing mode selects applicable flow channel cross-section flexibly; By adjusting track curvature, path length, can do meticulous adjusting to refrigerant flow.
In above-described embodiment, the height on the lower edge of the outlet 52 of flute profile runner 5, higher than the height in shunting chamber 2, like this, can ensure that cold-producing medium flow into voluntarily in shunting chamber 2 under Action of Gravity Field on the one hand; After can making on the other hand cold-producing medium chamber 2 flowing into flat tube 3 from shunting, then it is more even to flow into the flow of porous channel wherein by flat tube 3.
Cylinder 1 can adopt the aluminium manufacture of solid or hollow cylinder to obtain, and no matter is to adopt real stem stem body, still adopts hollow cylinder, as long as ensure that it has adequate thickness and conveniently cuts grooved runner 5.The manufacturing process of refrigerant flow dividing structure is: first, according to the heat exchange amount of known micro-channel heat exchanger, determine refrigerant flow; Then,, according to basic length and width and the height of micro-channel heat exchanger, determine the number of branches of flute profile runner 5; According to the difference of the heat transfer effect of each flute profile runner 5, by adjusting track curvature, path length, cross-sectional area and the shape of cross section etc. of flute profile runner 5, form grooved runner 5 in outer surface cutting or the milling of cylinder 1 again; Moreover, cut shunting chamber 2.
The present invention also provides a kind of microchannel shunt assembly, comprises the refrigerant flow dividing structure in collector 8 and the various embodiments described above.Collector 8 is with refrigerant inlet 6 and flat pipe hole 7, collector 8 is set in outside the cylinder 1 in described refrigerant flow dividing structure, and, the inner surface of collector 8 is connected with the outer surface of cylinder 1, the center line of the refrigerant inlet 6 of collector 8 overlaps substantially with the center line of the refrigerant inlet 4 on cylinder 1, and the center line of flat pipe hole 7 is substantially concordant with the center line in the shunting chamber 2 on cylinder 1.
When microchannel shunt assembly is assembled, first, avoid grooved runner 5 regions and be coated with pricker material loading and brazing flux at the outer surface (non-) of cylinder 1, stand-by; Then, be coated with and be covered with solder at the inner surface of collector 8; Finally, collector 8 is set in to the outer surface of cylinder 1, assembles complete.Almost consistent with original collector 8 requisite spaces after micro-channel heat exchanger assembles, take up room little, simple in structure.
The present invention also provides a kind of micro-channel heat exchanger, comprises the refrigerant flow dividing structure in flat tube 3, collector 8 and the various embodiments described above.The height of the flat pipe hole 7 on collector 8 is greater than the 2-6mm of the height of flat tube 3 wherein, thereby can ensure that flat tube 3 can stretch into collector 8 completely, and flat tube 3 is specifically arranged in shunting chamber 2 by flat pipe hole 7.The material of collector 8 can be selected Al material.
The present invention also provides a kind of air-conditioner, and it comprises the refrigerant flow dividing structure in the various embodiments described above, and the other parts of described air-conditioner are prior art, do not repeat them here.
Finally should be noted that: above embodiment is only in order to illustrate that technical scheme of the present invention is not intended to limit; Although the present invention is had been described in detail with reference to preferred embodiment, those of ordinary skill in the field are to be understood that: still can modify or part technical characterictic is equal to replacement the specific embodiment of the present invention; And not departing from the spirit of technical solution of the present invention, it all should be encompassed in the middle of the technical scheme scope of request protection of the present invention.
Claims (13)
1. a refrigerant flow dividing structure, it is characterized in that: comprise cylinder, on described cylinder, be provided with shunting chamber, refrigerant inlet and runner, wherein: described runner is the flute profile runner arranging along the outer surface of described cylinder, described in described refrigerant inlet and each, shunting chamber is communicated with via described flute profile runner fluid.
2. refrigerant flow dividing structure as claimed in claim 1, is characterized in that: described flute profile runner around described refrigerant inlet radially.
3. refrigerant flow dividing structure as claimed in claim 1 or 2, is characterized in that: described refrigerant inlet directly by described flute profile runner with described in each, shunt chamber fluid and be communicated with.
4. refrigerant flow dividing structure as claimed in claim 1 or 2, it is characterized in that: described flute profile runner is bifurcation structure, have import and at least two outlets, described import is communicated with described refrigerant inlet fluid, exports corresponding fluid described in each and shunts chamber described in being communicated with one.
5. the refrigerant flow dividing structure as described in claim 1 or 2 or 3, is characterized in that: described flute profile runner is straight line or curve.
6. refrigerant flow dividing structure as claimed in claim 1 or 2 or 3 or 4, is characterized in that: the cross section of described flute profile runner be shaped as circle, ellipse, rectangle or D shape.
7. refrigerant flow dividing structure as claimed in claim 1 or 2 or 3 or 4, is characterized in that: D=4S/C, wherein: described D, described S and described C are respectively the wetting girth of hydraulic diameter, cross-sectional area and cross section of described flute profile runner.
8. refrigerant flow dividing structure as claimed in claim 1 or 2, is characterized in that: the height on the lower edge of the outlet of described flute profile runner is higher than the height on the lower edge in described shunting chamber.
9. the refrigerant flow dividing structure as described in any one in claim 1~8, is characterized in that: each described shunting chamber extends to described column body from the outer surface of described cylinder, forms comb teeth-shaped.
10. a microchannel shunt assembly, comprises collector, and described collector is provided with refrigerant inlet and flat pipe hole; It is characterized in that: also comprise the refrigerant flow dividing structure as described in any one in claim 1~9, described collector is set in outside the cylinder in described refrigerant flow dividing structure and is connected, the center line of the refrigerant inlet of described collector overlaps substantially with the center line of the refrigerant inlet on described cylinder, and the center line of described flat pipe hole is substantially concordant with the center line in the shunting chamber on described cylinder.
11. 1 kinds of micro-channel heat exchangers, is characterized in that: also comprise the refrigerant flow dividing structure as described in any one in claim 1~9.
12. micro-channel heat exchangers as claimed in claim 11, it is characterized in that: also comprise collector and flat tube, wherein: described collector is provided with refrigerant inlet and flat pipe hole, described collector is set in outside the cylinder in described refrigerant flow dividing structure and is connected, the center line of the refrigerant inlet of described collector overlaps substantially with the center line of the refrigerant inlet on described cylinder, and the center line of described flat pipe hole is substantially concordant with the center line in the shunting chamber on described cylinder; Described flat tube is arranged in described shunting chamber by described flat pipe hole.
13. 1 kinds of air-conditioners, is characterized in that: comprise the refrigerant flow dividing structure as described in any one in claim 1~9.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201410410165.6A CN104154802B (en) | 2014-08-19 | 2014-08-19 | Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner |
Applications Claiming Priority (1)
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CN201410410165.6A CN104154802B (en) | 2014-08-19 | 2014-08-19 | Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner |
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CN104154802A true CN104154802A (en) | 2014-11-19 |
CN104154802B CN104154802B (en) | 2016-08-17 |
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CN201410410165.6A Expired - Fee Related CN104154802B (en) | 2014-08-19 | 2014-08-19 | Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner |
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Cited By (3)
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US10941955B2 (en) | 2017-10-27 | 2021-03-09 | Dometic Sweden Ab | Systems, methods, and apparatuses for providing communications between climate control devices in a recreational vehicle |
CN112944951A (en) * | 2021-04-01 | 2021-06-11 | 哈尔滨理工大学 | Microchannel heat exchanger and shunting structure |
US11254183B2 (en) | 2017-08-25 | 2022-02-22 | Dometic Sweden Ab | Recreational vehicle, cooling device, controlling system and method for controlling the cooling device |
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US20110061845A1 (en) * | 2009-01-25 | 2011-03-17 | Alcoil, Inc. | Heat exchanger |
CN202137017U (en) * | 2011-06-11 | 2012-02-08 | 广州金南磁塑有限公司 | Low-noise dry powder ball mill |
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CN103217052A (en) * | 2013-04-22 | 2013-07-24 | 陆群英 | Fluid distributor |
CN103256757A (en) * | 2013-03-28 | 2013-08-21 | 广东美的电器股份有限公司 | Heat exchanger and air conditioner |
CN204115554U (en) * | 2014-08-19 | 2015-01-21 | 珠海格力电器股份有限公司 | Refrigerant shunting structure, microchannel shunting assembly, heat exchanger and air conditioner |
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JPH09217968A (en) * | 1996-02-09 | 1997-08-19 | Hitachi Ltd | Plate type refrigerant flow divider |
US20110061845A1 (en) * | 2009-01-25 | 2011-03-17 | Alcoil, Inc. | Heat exchanger |
CN202137017U (en) * | 2011-06-11 | 2012-02-08 | 广州金南磁塑有限公司 | Low-noise dry powder ball mill |
CN202902977U (en) * | 2012-11-28 | 2013-04-24 | 无锡鸿声铝业有限公司 | Heat exchanger unit with diverting grooves |
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Publication number | Priority date | Publication date | Assignee | Title |
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US11254183B2 (en) | 2017-08-25 | 2022-02-22 | Dometic Sweden Ab | Recreational vehicle, cooling device, controlling system and method for controlling the cooling device |
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CN112944951A (en) * | 2021-04-01 | 2021-06-11 | 哈尔滨理工大学 | Microchannel heat exchanger and shunting structure |
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CN104154802B (en) | 2016-08-17 |
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