CN204227763U - Air-conditioner and parallel-flow evaporator thereof - Google Patents
Air-conditioner and parallel-flow evaporator thereof Download PDFInfo
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- CN204227763U CN204227763U CN201420607887.6U CN201420607887U CN204227763U CN 204227763 U CN204227763 U CN 204227763U CN 201420607887 U CN201420607887 U CN 201420607887U CN 204227763 U CN204227763 U CN 204227763U
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Abstract
The utility model relates to air-conditioner technical field, air-conditioner and parallel-flow evaporator thereof are provided, parallel-flow evaporator comprises that gas-liquid two-phase is all equipped to be put, it comprises separator and air and liquid mixer, gas-liquid separator is provided with gas-liquid input port, gas phase delivery outlet and liquid phase delivery outlet, air and liquid mixer comprises gas phase collector, isocon in gas phase external shunt pipe and liquid phase, gas phase delivery outlet and gas phase header in communication, in liquid phase isocon to be located in lower header and with lower header conducting, liquid phase delivery outlet is communicated with isocon in liquid phase, gas phase collector is communicated with by some equally distributed gas phase external shunt pipes with between lower header.In the utility model, gas phase refrigerant after dividing equally mixes in lower header again with liquid phase refrigerant, and final uniform distribution enters in the micro-channel flat of parallel-flow evaporator each road, this gas phase is all equipped puts that uniformity is good, easy to operate and reliability is high, and the gas-liquid two-phase distribution greatly improved in evaporimeter, improve the heat exchange efficiency of evaporimeter.
Description
Technical field
The utility model relates to air-conditioner technical field, more particularly, relates to a kind of air-conditioner and parallel-flow evaporator thereof.
Background technology
Parallel-flow heat exchanger is made up of heat exchange fin, parallel microchannels flat tube, the isocon being connected to each flat tube end and manifold trunk.Compared with the fin-tube type heat exchanger in conventional air conditioner, advantage that parallel-flow heat exchanger has compact conformation, heat transfer efficiency is high, refrigerant demand is few and cost is low etc., has therefore been widely used in domestic air conditioning and business air conditioner at present.
When parallel-flow heat exchanger is as evaporimeter, in it, point pairing its heat transfer property impact of gas-liquid two-phase between each flat tube is comparatively large, will decline significantly if gas-liquid distributes its heat transfer property uneven.And due to the derivation of parallel-flow evaporator conveniently condensed water, adopt the design of level header, flat tube is vertically placed, after gas-liquid two-phase refrigerant enters level header, because gas phase refrigerant volume flow comparatively large and gas phase refrigerant and liquid phase refrigerant exist alternate speed difference to a certain degree, in collector, flow pattern is mainly based on stratified flow and annular flow, causes two-phase refrigerant divided fluid stream in level header very uneven to the coolant quantity of each micro-channel flat, thus has had a strong impact on the heat exchange efficiency of evaporimeter.
For above-mentioned situation, existing patent document proposes the measure improving parallel-flow evaporator gas-liquid two-phase and distribute at present.Concrete grammar is in collector, arrange interior isocon or flow distribution plate, and gas-liquid refrigerant realizes shunting by the uniform aperture on interior isocon or flow distribution plate; Outside heat exchanger, arrange distributor, and adopt dividing plate that exchanger header is divided into several chamber, several roads gas-liquid refrigerant through distributor shunting flow to corresponding chamber respectively and realizes shunting.Above-mentioned inside and outside shunt method, although improve the gas-liquid two-phase distribution situation in parallel-flow evaporator to a certain extent, but due to the gas-liquid two-phase flow pattern (stratified flow and annular flow) in collector cannot be changed, thus fundamentally cannot solve the uneven problem of parallel-flow evaporator gas-liquid refrigerant distribution.
Utility model content
The purpose of this utility model is to provide a kind of air-conditioner and parallel-flow evaporator thereof, is intended to there is gas-liquid refrigerant in the parallel-flow evaporator existed in solution prior art and distributes uneven problem.
For solving the problems of the technologies described above, the technical solution of the utility model is: provide parallel-flow evaporator, comprise vertically disposed multichannel microchannel flat tube, be located at the fin in micro-channel flat described in each road, be connected to upper header and the lower header at micro-channel flat two ends described in each road, also comprise that gas-liquid two-phase is all equipped to be put, described gas-liquid two-phase all equipped putting comprises gas-liquid separator and air and liquid mixer, described gas-liquid separator is provided with gas-liquid input port, gas phase delivery outlet and liquid phase delivery outlet, described air and liquid mixer comprises gas phase collector, isocon in gas phase external shunt pipe and liquid phase, described gas-liquid input port is communicated with outside segments fluid element, described gas phase delivery outlet and described gas phase header in communication, in described liquid phase isocon to be located in described lower header and with described lower header conducting, described liquid phase delivery outlet is communicated with isocon in described liquid phase, described gas phase collector is communicated with by some equally distributed described gas phase external shunt pipes with between described lower header.
Particularly, described gas-liquid separator comprises the tank body of reverse taper shape, and the middle part of described tank body is located in described gas-liquid input port, and described gas phase delivery outlet is located at the top of described tank body, and described liquid phase delivery outlet is located at the bottom of described tank body.
Particularly, described gas-liquid input port place connects an input pipe, and described input pipe is arranged along the tangential direction of described tank wall.
Particularly, in described liquid phase, isocon is uniformly distributed some points of fluid apertures, the opening of each point of fluid apertures is towards described gas phase external shunt pipe.
Further, described point of fluid apertures and described gas phase external shunt pipe one_to_one corresponding.
Further, micro-channel flat described in described gas phase external shunt Guan Yuge road is corresponding.
Particularly, described gas phase delivery outlet is by a conduit and described gas phase header in communication, and described tubes connection, in the middle part of described gas phase collector, is also provided with gas phase baffle plate in described gas phase collector, described gas phase baffle plate be provided with some can the airflow hole that flows through of air feed.
Particularly, the aperture in described gas phase baffle plate overdraught hole is different, becomes large along the middle part of described gas phase baffle plate gradually to aperture, both ends; The density of setting in described gas phase baffle plate overdraught hole is different, and diminishes gradually along the middle part of described gas phase baffle plate to both ends density.
Further, described gas phase delivery outlet is by some equally distributed gas-distributing pipes and described gas phase header in communication.
The utility model additionally provides air-conditioner, includes parallel-flow evaporator, and described parallel-flow evaporator has above-mentioned structure.
In the utility model, during air-conditioner work, the gas-liquid refrigerant flowed out by restricting element is separated through gas-liquid separator, wherein, gas phase refrigerant is exported by gas phase delivery outlet and enters gas phase collector, and is evenly entered in lower header by the gas phase external shunt pipe of gas phase collector; Simultaneously, liquid phase refrigerant to enter in liquid phase in isocon by liquid phase delivery outlet, and enter in lower header after isocon in liquid phase is divided equally, like this, gas phase refrigerant after dividing equally mixes in lower header again with liquid phase refrigerant, and final uniform distribution enters in the micro-channel flat of parallel-flow evaporator each road, this gas phase is all equipped puts that uniformity is good, easy to operate and reliability is high; The stratified flow simultaneously avoiding conventional shunt method to be formed or annular flow, thus greatly improve the gas-liquid two-phase distribution in evaporimeter, and finally improve the heat exchange efficiency of evaporimeter.
Accompanying drawing explanation
Fig. 1 is all equipped structural representation put when being applied to parallel-flow evaporator of gas-liquid two-phase that the utility model embodiment provides;
Fig. 2 is A place enlarged drawing in Fig. 1;
Fig. 3 is the structural representation of the gas-liquid separator that the utility model embodiment provides;
Fig. 4 is B-B sectional view in Fig. 1;
Fig. 5 is C-C sectional view in Fig. 1;
Fig. 6 is the structural representation of gas phase baffle plate in the utility model embodiment;
100-parallel-flow evaporator; 110-micro-channel flat; The upper header of 120-;
130-lower header; 200-gas-liquid separator; 210-gas-liquid input port;
220-gas phase delivery outlet; 230-liquid phase delivery outlet; 240-tank body;
250-input pipe; 300-gas and liquid mixture; 310-gas phase collector;
320-gas phase external shunt pipe; Isocon in 330-liquid phase; 331-divides fluid apertures;
340-gas phase baffle plate; 341-airflow hole; 400-conduit.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
It should be noted that, when element is called as " being fixed on " or " being arranged at " another element, it can directly on another element or may there is centering elements simultaneously.When an element is called as " being connected to " another element, it can be directly connected to another element or may there is centering elements simultaneously.
Also it should be noted that, the orientation term such as left and right, upper and lower in the present embodiment, is only relative concept or be reference with the normal operating condition of product each other, and should not be regarded as have restrictive.
With reference to Fig. 1, Fig. 2, the utility model embodiment provides the parallel-flow evaporator 100 that a kind of distributing uniformity is good, easy to operate and reliability is high.Parallel-flow evaporator 100 comprises vertically disposed multichannel microchannel flat tube 110, the fin (not shown) be located in each road micro-channel flat 110, the upper header 120 being connected to micro-channel flat 110 two ends, each road and lower header 130.Parallel-flow evaporator 100 also comprises that gas-liquid two-phase is all equipped to be put, gas-liquid two-phase all equipped putting comprises gas-liquid separator 200 and air and liquid mixer 300, gas-liquid separator 200 is provided with gas-liquid input port 210, gas phase delivery outlet 220 and liquid phase delivery outlet 230, air and liquid mixer 300 comprises gas phase collector 310, isocon 330 in gas phase external shunt pipe 320 and liquid phase, gas-liquid input port 210 is communicated with the restricting element (not shown) in outside air-conditioning system, gas phase delivery outlet 220 is communicated with gas phase collector 310, gas phase collector 310 level is located at below lower header 130, and in liquid phase isocon 330 to be located in lower header 130 and with lower header 130 conducting, liquid phase delivery outlet 230 is communicated with isocon in liquid phase 330, be communicated with by some equally distributed gas phase external shunt pipes 320 between gas phase collector 310 with lower header 130.Like this, during air-conditioner work, the gas-liquid refrigerant flowed out by restricting element is separated through gas-liquid separator 200, wherein, gas phase refrigerant is exported by gas phase delivery outlet 220 and enters gas phase collector 310, and evenly enters in lower header 130 by the gas phase external shunt pipe 320 of gas phase collector 310; Simultaneously, liquid phase refrigerant to enter in liquid phase in isocon 330 by liquid phase delivery outlet 230, and enter after isocon in liquid phase 330 is divided equally in lower header 130, like this, gas phase refrigerant after dividing equally mixes in lower header 130 again with liquid phase refrigerant, and final uniform distribution enters in parallel-flow evaporator 100 each road micro-channel flat 110.
Particularly, with reference to Fig. 3, Fig. 4, gas-liquid separator 200 comprises the tank body 240 of reverse taper shape, and the middle part of tank body 240 is located in gas-liquid input port 210, and gas phase delivery outlet 220 is located at the top of tank body 240, and liquid phase delivery outlet 230 is located at the bottom of tank body 240.Meanwhile, gas-liquid input port 210 place connects an input pipe 250, and input pipe 250 is arranged along the tangential direction of tank body 240 outer wall.Because the middle part of tank body 240 is located at by input pipe 250, like this, gas-liquid refrigerant is positioned at after entering tank body 240 in the middle part of tank body 240, and on the top of tank body 240 and bottom, all reserved activity space is convenient to be separated.When gas-liquid refrigerant enters tank body 240 by input pipe 250, vortex movement can be carried out along tank body 240 inwall, and be automatically separated under self gravitation and whirlpool centrifugal action, wherein lighter gas phase refrigerant moves upward from gas phase delivery outlet 220 and exports, and heavier liquid phase refrigerant moves downward and exports from liquid phase delivery outlet 230.
In the present embodiment, in liquid phase, isocon 330 is sheathed on the body in lower header 130 for level, it is uniformly distributed some points of fluid apertures 331, each point of fluid apertures 331 opening down namely towards gas phase external shunt pipe 320.The pore size of point fluid apertures 331 depends on liquid phase cold medium flux.And point fluid apertures 331 is identical with gas phase external shunt pipe 320 quantity, and in one-to-one relationship.Composition graphs 5, in lower header 130, gas phase refrigerant enters in lower header 130 by gas phase external shunt pipe 320, and liquid phase refrigerant enters in lower collector pipe by point fluid apertures 331, to divide fluid apertures 331 and gas phase external shunt pipe 320 one_to_one corresponding like this, namely ensure that gas phase refrigerant with liquid phase refrigerant evenly mix, form gas-liquid mixed refrigerant.
And further, gas phase external shunt Guan320Yu Ge road micro-channel flat 110 one_to_one corresponding.Like this, mixed uniformly gas-liquid mixed refrigerant in lower header 130 is made can again to branch to uniformly in each road micro-channel flat 110.
In the present embodiment, gas phase delivery outlet 220 is communicated with gas phase collector 310 by a conduit 400, because conduit 400 is connected to the middle part of gas phase collector 310, like this, cause the air-flow in the middle part of gas phase collector 310 comparatively large, the air-flow at two ends is little, and it is uneven in order to alleviate this air-flow, in the present embodiment, a gas phase baffle plate 340 is set in gas phase collector 310, gas phase baffle plate 340 be provided with some can the airflow hole 341 that flows through of air feed.With reference to Fig. 6, the aperture in gas phase baffle plate 340 overdraught hole 341 is different, becomes large along the middle part of gas phase baffle plate 340 gradually to aperture, both ends; The density of setting in gas phase baffle plate 340 overdraught hole 341 is different, and diminishes gradually along the middle part of gas phase baffle plate 340 to both ends density.Like this, because the aperture of the airflow hole 341 at middle part is little, and density is large, like this, with regard to large to the resistance of air-flow generation in the middle part of gas phase baffle plate 340, force the air-flow at middle part to move to the both ends of gas phase baffle plate 340, thus the original uniform stream too concentrated is distributed in gas phase collector 310, and then ensure that gas phase refrigerant evenly enters in gas phase external shunt pipe 320.
Here adopt gas phase baffle plate 340, be a preferred version, it realizes the uniform distribution of the gas phase refrigerant in gas phase collector 310 when structure simplifies most.Certainly, also gas phase baffle plate 340 can not be set herein.As an alternative, in gas phase collector 310 bottom, some equally distributed gas-distributing pipe (not shown)s are set, the other end of each gas-distributing pipe is connected to gas phase delivery outlet 220, like this, also can ensure that the gas phase refrigerant in gas phase collector 310 is uniformly distributed, just this alternative complex structure.
Referring again to Fig. 1, Fig. 2, in the utility model embodiment, the all equipped operation principle of putting of gas-liquid two-phase is: the gas-liquid refrigerant flowed out through restricting element enters gas-liquid separator 200 by input pipe 250, the separation of gas-liquid refrigerant is realized under deadweight and whirlpool centrifugal action, the gas phase refrigerant be separated exports from the gas phase delivery outlet 220 at gas-liquid separator 200 top, and input in the middle part of gas phase collector 310, with after through gas phase baffle plate 340 uniform divided flows to gas phase external shunt pipe 320, and enter in lower header 130 through gas phase external shunt pipe 320; Another road liquid phase refrigerant then exports from the liquid phase delivery outlet 230 bottom gas-liquid separator 200, and from isocon 330 end input in the liquid phase in lower header 130, exported by point fluid apertures 331 on isocon in liquid phase 330 subsequently, and be broken into graininess in lower header 130; Broken liquid phase refrigerant particle fully mixes in lower header 130 with gas phase refrigerant, and form gas phase mixed flow, finally under the carrying of gas phase refrigerant, uniform divided flows is in each road micro-channel flat 110 of parallel-flow evaporator 100.
The utility model embodiment still provides a kind of air-conditioner (not shown) adopting above-mentioned parallel-flow evaporator, because the gas-liquid two-phase in above-mentioned parallel-flow evaporator 100 is evenly distributed, evaporator heat exchange efficiency is high, thus improve the heat exchange property of air-conditioner, use more comfortable.
These are only preferred embodiment of the present utility model, not in order to limit the utility model, all do within spirit of the present utility model and principle any amendment, equivalent to replace and improvement etc., all should be included within protection domain of the present utility model.
Claims (10)
1. parallel-flow evaporator, comprise vertically disposed multichannel microchannel flat tube, be located at the fin in micro-channel flat described in each road, be connected to upper header and the lower header at micro-channel flat two ends described in each road, it is characterized in that: also comprise that gas-liquid two-phase is all equipped to be put, described gas-liquid two-phase all equipped putting comprises gas-liquid separator and air and liquid mixer, described gas-liquid separator is provided with gas-liquid input port, gas phase delivery outlet and liquid phase delivery outlet, described air and liquid mixer comprises gas phase collector, isocon in gas phase external shunt pipe and liquid phase, described gas-liquid input port is communicated with outside segments fluid element, described gas phase delivery outlet and described gas phase header in communication, in described liquid phase isocon to be located in described lower header and with described lower header conducting, described liquid phase delivery outlet is communicated with isocon in described liquid phase, described gas phase collector is communicated with by some equally distributed described gas phase external shunt pipes with between described lower header.
2. parallel-flow evaporator as claimed in claim 1, it is characterized in that: described gas-liquid separator comprises the tank body of reverse taper shape, the middle part of described tank body is located in described gas-liquid input port, and described gas phase delivery outlet is located at the top of described tank body, and described liquid phase delivery outlet is located at the bottom of described tank body.
3. parallel-flow evaporator as claimed in claim 2, it is characterized in that: described gas-liquid input port place connects an input pipe, described input pipe is arranged along the tangential direction of described tank wall.
4. parallel-flow evaporator as claimed in claim 1, it is characterized in that: in described liquid phase, isocon is uniformly distributed some points of fluid apertures, the opening of each point of fluid apertures is towards described gas phase external shunt pipe.
5. parallel-flow evaporator as claimed in claim 4, is characterized in that: described point of fluid apertures and described gas phase external shunt pipe one_to_one corresponding.
6. parallel-flow evaporator as claimed in claim 1, is characterized in that: micro-channel flat described in described gas phase external shunt Guan Yuge road is corresponding.
7. the parallel-flow evaporator according to any one of claim 1 to 6, it is characterized in that: described gas phase delivery outlet is by a conduit and described gas phase header in communication, described tubes connection is in the middle part of described gas phase collector, also be provided with gas phase baffle plate in described gas phase collector, described gas phase baffle plate be provided with some can the airflow hole that flows through of air feed.
8. parallel-flow evaporator as claimed in claim 7, is characterized in that: the aperture in described gas phase baffle plate overdraught hole is different, becomes large along the middle part of described gas phase baffle plate gradually to aperture, both ends; The density of setting in described gas phase baffle plate overdraught hole is different, and diminishes gradually along the middle part of described gas phase baffle plate to both ends density.
9. the parallel-flow evaporator according to any one of claim 1 to 6, is characterized in that: described gas phase delivery outlet is by some equally distributed gas-distributing pipes and described gas phase header in communication.
10. air-conditioner, includes parallel-flow evaporator, it is characterized in that: described parallel-flow evaporator has structure as claimed in any one of claims 1-9 wherein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420607887.6U CN204227763U (en) | 2014-10-20 | 2014-10-20 | Air-conditioner and parallel-flow evaporator thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420607887.6U CN204227763U (en) | 2014-10-20 | 2014-10-20 | Air-conditioner and parallel-flow evaporator thereof |
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| Publication Number | Publication Date |
|---|---|
| CN204227763U true CN204227763U (en) | 2015-03-25 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420607887.6U Withdrawn - After Issue CN204227763U (en) | 2014-10-20 | 2014-10-20 | Air-conditioner and parallel-flow evaporator thereof |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104315758A (en) * | 2014-10-20 | 2015-01-28 | 广东美的制冷设备有限公司 | Air conditioner and parallel flow evaporator thereof |
| CN105996899A (en) * | 2016-07-11 | 2016-10-12 | 江苏美的清洁电器股份有限公司 | Ground brush assembly and dust collector |
| CN106016841A (en) * | 2016-05-12 | 2016-10-12 | 南京师范大学 | Microchannel heat pipe evaporator |
| CN106813425A (en) * | 2015-11-30 | 2017-06-09 | 青岛海尔空调器有限总公司 | For the combined micro-channel heat exchanger of radiation refrigeration |
| CN111055861A (en) * | 2018-10-16 | 2020-04-24 | 中车青岛四方机车车辆股份有限公司 | Vehicle air conditioning system and control method |
-
2014
- 2014-10-20 CN CN201420607887.6U patent/CN204227763U/en not_active Withdrawn - After Issue
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104315758A (en) * | 2014-10-20 | 2015-01-28 | 广东美的制冷设备有限公司 | Air conditioner and parallel flow evaporator thereof |
| CN106813425A (en) * | 2015-11-30 | 2017-06-09 | 青岛海尔空调器有限总公司 | For the combined micro-channel heat exchanger of radiation refrigeration |
| CN106813425B (en) * | 2015-11-30 | 2019-10-01 | 青岛海尔空调器有限总公司 | Combined micro-channel heat exchanger for radiation refrigeration |
| CN106016841A (en) * | 2016-05-12 | 2016-10-12 | 南京师范大学 | Microchannel heat pipe evaporator |
| CN106016841B (en) * | 2016-05-12 | 2018-05-15 | 南京师范大学 | A kind of micro channel heat pipe evaporator |
| CN105996899A (en) * | 2016-07-11 | 2016-10-12 | 江苏美的清洁电器股份有限公司 | Ground brush assembly and dust collector |
| CN105996899B (en) * | 2016-07-11 | 2019-03-08 | 江苏美的清洁电器股份有限公司 | Ground brush assemblies and dust catcher |
| CN111055861A (en) * | 2018-10-16 | 2020-04-24 | 中车青岛四方机车车辆股份有限公司 | Vehicle air conditioning system and control method |
| CN111055861B (en) * | 2018-10-16 | 2021-07-23 | 中车青岛四方机车车辆股份有限公司 | Vehicle air conditioning system and control method |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150325 Effective date of abandoning: 20160907 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |