CN201764878U - Parallel flow type heat exchanger with novel equal allocation structure - Google Patents
Parallel flow type heat exchanger with novel equal allocation structure Download PDFInfo
- Publication number
- CN201764878U CN201764878U CN2010202835671U CN201020283567U CN201764878U CN 201764878 U CN201764878 U CN 201764878U CN 2010202835671 U CN2010202835671 U CN 2010202835671U CN 201020283567 U CN201020283567 U CN 201020283567U CN 201764878 U CN201764878 U CN 201764878U
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- tube
- pipe arrangement
- heat exchange
- heat exchanger
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Abstract
The utility model discloses a parallel flow type heat exchanger with a novel equal allocation structure, which comprises a plurality of micro channel heat exchange flat tubes. Side plates are arranged on the outer sides of the micro channel heat exchange flat tubes at upper and lower edges uniformly; one end of the micro channel heat exchange flat tube is connected on a liquid distribution tube, and the other end is connected on a liquid collecting tube; an equal allocation tube is longitudinally arranged in the liquid distribution tube; a plurality of baffles are laterally arranged in the liquid distribution tube to divide a cavity of the liquid distribution tube into a plurality of slow flow cavities; and a plurality of overflow holes are formed in the wall of the equal allocation tube in the slow flow cavity. The baffles are reasonably utilized for dividing the cavity of the liquid distribution tube into a plurality of slow flow cavities in different lengths according to the flow direction of medium, and different quantities of overflow holes are formed in the walls of the equal allocation tubes in all the slow flow cavities, therefore, the medium allocated to all the micro channel heat exchange flat tubes is equal, thus exerting the heat exchange effect of each micro channel heat exchange flat tube.
Description
Technical field
The utility model relates to a kind of parallel flow heat exchanger, specifically relates to a kind of parallel flow heat exchanger of novel uniform distribution structure.
Background technology
In the prior art, mostly parallel flow heat exchanger is vertically to be provided with equal pipe arrangement in separating tube, realizes the purpose of uniform distribution medium by the micropore on the equal pipe arrangement tube wall.Such structure, because still being communicated with up and down, the inner chamber of separating tube is integral, the medium that micropore on equal pipe arrangement tube walls overflows is easy to be subjected to gravity etc. to influence when flow slowly in the inner chamber of separating tube, cause medium pressure in equal pipe arrangement inconsistent, is difficult to realize the purpose of uniform distribution medium.
Summary of the invention
The utility model mainly is to solve above-mentioned existing in prior technology technical problem, and a kind of parallel flow heat exchanger of novel uniform distribution structure is provided.
Above-mentioned technical problem of the present utility model is mainly solved by following technical proposals: a kind of parallel flow heat exchanger of novel uniform distribution structure, comprise some Thermal Performance of Micro Channels flat tubes, the Thermal Performance of Micro Channels flat tube outside of last lower limb is equipped with side plate, one end of Thermal Performance of Micro Channels flat tube is connected on the separating tube, the other end is connected on the collector tube, described separating tube the inside vertically is provided with equal pipe arrangement, and the separating tube the inside laterally is provided with several dividing plates the inner chamber of separating tube is separated into several slow flow cavity; In the described slow flow cavity, all offer several spout holes on the tube wall of pipe arrangement.According to MEDIA FLOW to rationally utilizing dividing plate the inner chamber of separating tube to be separated into the slow flow cavity of several different lengths, on the tube wall of equal pipe arrangement, open the spout hole of different numbers in each slow flow cavity, be that the medium that every Thermal Performance of Micro Channels flat tube distributes can be comparatively even like this, give full play to the heat exchange effect of every Thermal Performance of Micro Channels flat tube.
As preferably, described equal pipe arrangement is arranged to the micropassage type flat tube configuration, and all the spout hole on the pipe arrangement sidewall is connected with hole, microchannel on the equal pipe arrangement; Be provided with buffer chamber between the upper end plug of described separating tube and equal pipe arrangement upper port at this moment.Equal pipe arrangement is arranged to the micropassage type flat tube configuration, medium before this in buffer chamber uniform distribution advance the micropassage type flat tube of equal pipe arrangement, each slow flow cavity is advanced in spout hole uniform distribution on equal pipe arrangement sidewall again, be that the medium that every Thermal Performance of Micro Channels flat tube distributes can be more even like this, give full play to the heat exchange effect of every Thermal Performance of Micro Channels flat tube.
As preferably; described equal pipe arrangement lower end sealing and the lower end that is fixed on separating tube are beyond the Great Wall; descend end plug no longer to stand the direct impact of high-pressure medium like this, help protecting down end plug and equal syndetons of pipe arrangement, also help protecting down the syndeton of side plate and equal pipe arrangement.
The utlity model has characteristics such as simple in structure, reasonable in design.
Description of drawings
Fig. 1 is a kind of structural representation of the present utility model;
Fig. 2 is an another kind of structural representation of the present utility model;
Fig. 3 is a kind of structural representation of the equal pipe arrangement of the utility model.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described in further detail.
Embodiment: referring to Fig. 1, the utility model comprises some Thermal Performance of Micro Channels flat tubes 3, Thermal Performance of Micro Channels flat tube 3 outsides of last lower limb are equipped with side plate 4, one end of Thermal Performance of Micro Channels flat tube 3 is connected on the separating tube 2, the other end is connected on the collector tube 1, separating tube 2 the insides vertically are provided with equal pipe arrangement 6, and separating tube 2 the insides laterally are provided with several dividing plates 24 inner chamber of separating tube 2 is separated into several slow flow cavity 23; In the slow flow cavity 23, all offer several spout holes 61 on the tube wall of pipe arrangement 6.According to MEDIA FLOW to rationally utilizing dividing plate the inner chamber of separating tube to be separated into the slow flow cavity of several different lengths, on the tube wall of equal pipe arrangement, open the spout hole of different numbers in each slow flow cavity, be that the medium that every Thermal Performance of Micro Channels flat tube distributes can be comparatively even like this, give full play to the heat exchange effect of every Thermal Performance of Micro Channels flat tube.
As improving further; all pipe arrangement 6 upper ends are fixed on the upper end plug 21 of separating tube 2; and be connected with external feed tube 5; all pipe arrangement 6 lower ends seal and are fixed on the following end plug 22 of separating tube 2; descend end plug no longer to stand the direct impact of high-pressure medium like this; help protecting down the syndeton of end plug and equal pipe arrangement, also help protecting down the syndeton of side plate and equal pipe arrangement.
Referring to Fig. 2 and Fig. 3, as improving further, the utility model is arranged to the micropassage type flat tube configuration with equal pipe arrangement 6, and all the spout hole 61 on pipe arrangement 6 sidewalls is connected with hole, microchannel 62 on the equal pipe arrangement 6; Be provided with buffer chamber 25 between the upper end plug 21 of separating tube 2 and equal pipe arrangement 6 upper port at this moment.Equal pipe arrangement is arranged to the micropassage type flat tube configuration, medium before this in buffer chamber uniform distribution advance the micropassage type flat tube of equal pipe arrangement, each slow flow cavity is advanced in spout hole uniform distribution on equal pipe arrangement sidewall again, be that the medium that every Thermal Performance of Micro Channels flat tube distributes can be more even like this, give full play to the heat exchange effect of every Thermal Performance of Micro Channels flat tube.
At last, should be pointed out that above embodiment only is the more representational example of the utility model.Obviously, the utility model is not limited to the foregoing description, and many distortion can also be arranged.Every foundation technical spirit of the present utility model all should be thought to belong to protection domain of the present utility model to any simple modification, equivalent variations and modification that above embodiment did.
Claims (3)
1. the parallel flow heat exchanger of a novel uniform distribution structure, comprise some Thermal Performance of Micro Channels flat tubes (3), Thermal Performance of Micro Channels flat tube (3) outside of last lower limb is equipped with side plate (4), one end of Thermal Performance of Micro Channels flat tube (3) is connected on the separating tube (2), the other end is connected on the collector tube (1), it is characterized in that described separating tube (2) the inside vertically is provided with equal pipe arrangement (6), separating tube (2) the inside laterally is provided with several dividing plates (24) inner chamber of separating tube (2) is separated into several slow flow cavity (23); In the described slow flow cavity (23), all offer several spout holes (61) on the tube wall of pipe arrangement (6).
2. the parallel flow heat exchanger of novel uniform distribution structure according to claim 1, it is characterized in that described equal pipe arrangement (6) is arranged to the micropassage type flat tube configuration, all the spout hole (61) on pipe arrangement (6) sidewall is connected with hole, microchannel (62) on the equal pipe arrangement (6); Be provided with buffer chamber (25) between the upper end plug (21) of described separating tube this moment (2) and equal pipe arrangement (6) upper port.
3. the parallel flow heat exchanger of novel uniform distribution structure according to claim 1 and 2 is characterized in that described equal pipe arrangement (6) lower end seals and is fixed on the following end plug (22) of separating tube (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202835671U CN201764878U (en) | 2010-08-05 | 2010-08-05 | Parallel flow type heat exchanger with novel equal allocation structure |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202835671U CN201764878U (en) | 2010-08-05 | 2010-08-05 | Parallel flow type heat exchanger with novel equal allocation structure |
Publications (1)
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CN201764878U true CN201764878U (en) | 2011-03-16 |
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CN2010202835671U Expired - Lifetime CN201764878U (en) | 2010-08-05 | 2010-08-05 | Parallel flow type heat exchanger with novel equal allocation structure |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101893403A (en) * | 2010-08-05 | 2010-11-24 | 浙江金宸三普换热器有限公司 | Novel parallel flow heat exchanger with uniform distribution structure |
CN102519181A (en) * | 2011-12-09 | 2012-06-27 | 广东美的电器股份有限公司 | Parallel flow heat exchanger |
CN103759569A (en) * | 2013-12-10 | 2014-04-30 | 柳州五菱宝马利汽车空调有限公司 | Distributing cavity embedded collecting and distributing tube for automotive parallel flow evaporator |
CN104937364A (en) * | 2013-01-28 | 2015-09-23 | 开利公司 | Multiple tube bank heat exchange unit with manifold assembly |
US10337799B2 (en) | 2013-11-25 | 2019-07-02 | Carrier Corporation | Dual duty microchannel heat exchanger |
-
2010
- 2010-08-05 CN CN2010202835671U patent/CN201764878U/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101893403A (en) * | 2010-08-05 | 2010-11-24 | 浙江金宸三普换热器有限公司 | Novel parallel flow heat exchanger with uniform distribution structure |
CN102519181A (en) * | 2011-12-09 | 2012-06-27 | 广东美的电器股份有限公司 | Parallel flow heat exchanger |
CN104937364A (en) * | 2013-01-28 | 2015-09-23 | 开利公司 | Multiple tube bank heat exchange unit with manifold assembly |
US10247481B2 (en) | 2013-01-28 | 2019-04-02 | Carrier Corporation | Multiple tube bank heat exchange unit with manifold assembly |
US10337799B2 (en) | 2013-11-25 | 2019-07-02 | Carrier Corporation | Dual duty microchannel heat exchanger |
CN103759569A (en) * | 2013-12-10 | 2014-04-30 | 柳州五菱宝马利汽车空调有限公司 | Distributing cavity embedded collecting and distributing tube for automotive parallel flow evaporator |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20110316 Effective date of abandoning: 20120307 |