CN111947490A - Liquid distribution structure with shielding prevention effect and heat exchanger - Google Patents
Liquid distribution structure with shielding prevention effect and heat exchanger Download PDFInfo
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- CN111947490A CN111947490A CN202010872528.3A CN202010872528A CN111947490A CN 111947490 A CN111947490 A CN 111947490A CN 202010872528 A CN202010872528 A CN 202010872528A CN 111947490 A CN111947490 A CN 111947490A
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- 239000007788 liquid Substances 0.000 title claims abstract description 136
- 230000000694 effects Effects 0.000 title abstract description 15
- 230000002265 prevention Effects 0.000 title 1
- 238000002347 injection Methods 0.000 claims abstract description 23
- 239000007924 injection Substances 0.000 claims abstract description 23
- 238000004891 communication Methods 0.000 claims description 28
- 239000007921 spray Substances 0.000 claims description 13
- 238000005452 bending Methods 0.000 claims description 8
- 239000004744 fabric Substances 0.000 claims 1
- 239000003507 refrigerant Substances 0.000 abstract description 17
- 230000008020 evaporation Effects 0.000 description 4
- 238000001704 evaporation Methods 0.000 description 4
- 238000005507 spraying Methods 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F25/00—Component parts of trickle coolers
- F28F25/02—Component parts of trickle coolers for distributing, circulating, and accumulating liquid
- F28F25/06—Spray nozzles or spray pipes
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- Engineering & Computer Science (AREA)
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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本发明提供一种具有避免遮挡效果的布液结构及换热器。布液结构包括:布液管;所述换热器内设置有换热管,所述布液管呈环形设置于所述换热管的上方。本发明提供的具有避免遮挡效果的布液结构及换热器,将现有技术中的布液盘结构替换为呈环形的布液管,从而在保证与布液盘结构相同的布液效果的情况下降低对气态冷媒的遮挡,从而保证换热器的换热性能,同时通过设置喷射孔,能够增加换热管的分布区域,有效的克服了现有技术中换热管分布区域小而存在多个换热死区的问题,减少布液器对换热管的遮挡,减少布液器对换热管布局的限制,简化布液器结构,使其占据空间小,布液无死角,换热无死角提高了换热器的空间利用率。
The invention provides a liquid distribution structure and a heat exchanger with the effect of avoiding shielding. The liquid distribution structure includes: a liquid distribution pipe; a heat exchange pipe is arranged in the heat exchanger, and the liquid distribution pipe is arranged above the heat exchange pipe in a ring shape. The liquid distribution structure and heat exchanger provided by the present invention have the effect of avoiding shielding, and the liquid distribution pan structure in the prior art is replaced by a ring-shaped liquid distribution pipe, so as to ensure the same liquid distribution effect as the liquid distribution pan structure. Under the circumstance, the shielding of the gaseous refrigerant is reduced, so as to ensure the heat exchange performance of the heat exchanger. At the same time, the distribution area of the heat exchange tubes can be increased by setting the injection holes, which effectively overcomes the existence of the small distribution area of the heat exchange tubes in the prior art. The problem of multiple heat exchange dead zones reduces the shielding of the heat exchange tubes by the liquid distributor, reduces the restrictions on the layout of the heat exchange tubes by the liquid distributor, and simplifies the structure of the liquid distributor, so that it occupies a small space, and the liquid distribution has no dead ends. There is no dead space in the heat, which improves the space utilization of the heat exchanger.
Description
技术领域technical field
本发明涉及空气处理设备技术领域,特别是一种具有避免遮挡效果的布液结构及换热器。The invention relates to the technical field of air treatment equipment, in particular to a liquid distribution structure and a heat exchanger with the effect of avoiding shielding.
背景技术Background technique
在热泵系统机组中,降膜式蒸发器需要具备兼顾蒸发、冷凝双工况功能,常规的布液器结构为整块矩形或其他形式的盒子形式,该结构只能满足蒸发工况时的布液效果及流体流动方式,在冷凝工况时,高温高压的气态冷媒通过原蒸发工况的出气口反向进入壳体顶部,中间布液器遮挡到绝大部分换热区域,气态冷媒无法充分与换热管接触,导致部分换热管换热较差,导致换热面积利用率不高,并且使换热管布局仅布置到壳体中部区域,布液器两侧无换热管布局,当转换为冷凝工况时,出现较多换热死区而导致气态冷媒虽然充满整个壳程,但减少了与换热管接触的面积,使整个空间利用率很低。In the heat pump system unit, the falling film evaporator needs to have the function of taking into account the dual working conditions of evaporation and condensation. The conventional liquid distributor structure is a whole rectangular or other form of box form, which can only meet the distribution of evaporation conditions. Liquid effect and fluid flow mode, in the condensing condition, the gaseous refrigerant with high temperature and high pressure enters the top of the shell through the outlet of the original evaporation condition, and the intermediate liquid distributor blocks most of the heat exchange area, and the gaseous refrigerant cannot fully Contact with the heat exchange tubes, resulting in poor heat exchange of some of the heat exchange tubes, resulting in a low utilization rate of the heat exchange area, and the layout of the heat exchange tubes is only arranged in the middle area of the shell, and there is no heat exchange tube layout on both sides of the liquid distributor. When it is converted to condensing condition, there are many dead zones of heat exchange, so that although the gaseous refrigerant fills the whole shell side, the area in contact with the heat exchange tube is reduced, so that the utilization rate of the whole space is very low.
发明内容SUMMARY OF THE INVENTION
为了解决现有技术中换热器内的布液器妨碍气态冷媒进入而造成换热器换热效率低的技术问题,而提供一种将布液管呈环形设置而避免对气态冷媒造成遮挡的具有避免遮挡效果的布液结构及换热器。In order to solve the technical problem of low heat exchange efficiency of the heat exchanger caused by the liquid distributor in the heat exchanger hindering the entry of gaseous refrigerant in the prior art, a liquid distribution pipe is provided in a ring shape to avoid blocking the gaseous refrigerant. The liquid distribution structure and heat exchanger have the effect of avoiding shading.
一种布液结构,应用于换热器,所述布液结构包括:A liquid distribution structure is applied to a heat exchanger, and the liquid distribution structure includes:
布液管,所述布液管设置于所述换热器内,且所述布液管上设置有喷射孔;a liquid distribution pipe, the liquid distribution pipe is arranged in the heat exchanger, and the liquid distribution pipe is provided with a spray hole;
所述换热器内设置有换热管,所述布液管呈环形设置于所述换热管的上方,且所述喷射孔的喷射方向朝向所述换热管和/或朝向所述换热管的上方。The heat exchanger is provided with a heat exchange tube, the liquid distribution tube is arranged above the heat exchange tube in a ring shape, and the spraying direction of the spray hole is towards the heat exchange tube and/or towards the heat exchange tube above the heat pipe.
所述换热器上设置有进液口,所述进液口与所述布液管连通。The heat exchanger is provided with a liquid inlet, and the liquid inlet communicates with the liquid distribution pipe.
所述布液管围成矩形框架,所述矩形框架的底面朝向所述换热管,且所述喷射孔处于所述矩形框架的内表面、底面或外表面上。The liquid distribution pipe is surrounded by a rectangular frame, the bottom surface of the rectangular frame faces the heat exchange tube, and the injection holes are located on the inner surface, the bottom surface or the outer surface of the rectangular frame.
所述布液结构还包括至少一根连通管路,所述连通管路设置于所述环形内部,且所述连通管路的两端均与所述布液管连通。The liquid distribution structure further includes at least one communication pipeline, the communication pipeline is arranged inside the annular shape, and both ends of the communication pipeline are communicated with the liquid distribution pipe.
所述连通管路的数量为至少两根,所有所述连通管路并列设置于所述环形内部;或所述连通管路的数量为至少两根,所有所述连通管路交叉设置于所述环形内部,且相互交叉的所述连通管路之间相互连通。The number of the communication pipelines is at least two, and all the communication pipelines are arranged side by side in the annular interior; or the number of the communication pipelines is at least two, and all the communication pipelines are arranged crosswise in the Inside the ring, the communicating pipes that cross each other communicate with each other.
所述连通管路上设置有喷射孔。The communication pipeline is provided with injection holes.
沿远离所述换热管的方向,所述喷射孔呈至少一个三角形分布于所述布液管上;或沿远离所述换热管的方向,所述喷射孔呈矩形分布于所述布液管上;或沿远离所述换热管的方向,所述喷射孔的流通面积逐渐减小。In the direction away from the heat exchange tube, the injection holes are distributed on the liquid distribution pipe in at least one triangle; or in the direction away from the heat exchange tube, the injection holes are distributed in the liquid distribution in a rectangular shape. On the tube; or along the direction away from the heat exchange tube, the flow area of the spray hole gradually decreases.
所述布液管的截面为梯形,所述梯形的底角角度范围为0°至90°;或所述布液管的截面为三角形,所述三角形的顶角的角度范围为0°至180°;或所述布液管的截面为圆形。The cross-section of the liquid distribution pipe is a trapezoid, and the bottom angle of the trapezoid is in the range of 0° to 90°; or the cross-section of the liquid distribution pipe is a triangle, and the angle of the top angle of the triangle is in the range of 0° to 180°. °; or the cross section of the liquid distribution pipe is circular.
所述布液管的截面为矩形,所述矩形的一个侧面向所述矩形的内部凹陷形成折弯结构,所述折弯结构上设置有喷射孔。The cross section of the liquid distribution pipe is a rectangle, one side of the rectangle is recessed toward the inside of the rectangle to form a bending structure, and the bending structure is provided with an injection hole.
所述折弯结构包括相互连接的第一平面和第二平面,所述第一平面和所述第二平面之间具有夹角。The bending structure includes a first plane and a second plane that are connected to each other, and there is an included angle between the first plane and the second plane.
所述第一平面上设置有喷射孔;或所述第二平面上设置有喷射孔;或所述第一平面和所述第二平面上均设置有喷射孔。The first plane is provided with injection holes; or the second plane is provided with injection holes; or both the first plane and the second plane are provided with injection holes.
所述夹角的角度范围为0°-180°。The angle range of the included angle is 0°-180°.
一种换热器,包括上述的布液结构。A heat exchanger includes the above-mentioned liquid distribution structure.
所述换热器还包括均气板,所述换热器上设置有通气孔,所述均气板设置于所述布液结构和所述通气孔之间。The heat exchanger further includes an air-distribution plate, the heat exchanger is provided with a ventilation hole, and the air-distribution plate is arranged between the liquid distribution structure and the ventilation hole.
本发明提供的具有避免遮挡效果的布液结构及换热器,将现有技术中的布液盘结构替换为呈环形的布液管,从而在保证与布液盘结构相同的布液效果的情况下降低对气态冷媒的遮挡,从而保证换热器的换热性能,同时通过设置喷射孔,能够增加换热管的分布区域,有效的克服了现有技术中换热管分布区域小而存在多个换热死区的问题,减少布液器对换热管的遮挡,减少布液器对换热管布局的限制,简化布液器结构,使其占据空间小,布液无死角,换热无死角提高了换热器的空间利用率。The liquid distribution structure and heat exchanger provided by the present invention have the effect of avoiding shielding, and the liquid distribution pan structure in the prior art is replaced by a ring-shaped liquid distribution pipe, so as to ensure the same liquid distribution effect as the liquid distribution pan structure. Under the circumstance, the shielding of the gaseous refrigerant is reduced, so as to ensure the heat exchange performance of the heat exchanger. At the same time, the distribution area of the heat exchange tubes can be increased by setting the injection holes, which effectively overcomes the existence of the small distribution area of the heat exchange tubes in the prior art. The problem of multiple heat exchange dead zones reduces the shielding of the heat exchange tubes by the liquid distributor, reduces the restrictions on the layout of the heat exchange tubes by the liquid distributor, and simplifies the structure of the liquid distributor, so that it occupies a small space, and the liquid distribution has no dead ends. There is no dead space in the heat, which improves the space utilization of the heat exchanger.
附图说明Description of drawings
图1为本发明提供的具有避免遮挡效果的布液结构及换热器的实施例的的换热器的侧剖示意图;FIG. 1 is a schematic side cross-sectional view of a heat exchanger according to an embodiment of a liquid distribution structure and a heat exchanger that avoids the blocking effect provided by the present invention;
图2为本发明提供的具有避免遮挡效果的布液结构及换热器的实施例的布液结构的结构示意图;2 is a schematic structural diagram of the liquid distribution structure of the embodiment of the liquid distribution structure and the heat exchanger with the avoidance of shading effect provided by the present invention;
图3为本发明提供的具有避免遮挡效果的布液结构及换热器的实施例的换热器的透视图;3 is a perspective view of a heat exchanger according to an embodiment of a liquid distribution structure and a heat exchanger that avoids shading effects provided by the present invention;
图4为本发明提供的具有避免遮挡效果的布液结构及换热器的实施例的布液管的截面为K形的结构示意图;4 is a schematic structural diagram of a liquid distribution pipe having a K-shaped cross-section according to an embodiment of the liquid distribution structure and heat exchanger provided by the present invention;
图5为本发明提供的具有避免遮挡效果的布液结构及换热器的实施例的布液管上设置有连通管路的结构示意图;5 is a schematic structural diagram of a liquid distribution pipe provided with a communication pipeline in an embodiment of a liquid distribution structure and a heat exchanger with a shielding effect provided by the present invention;
图中:In the picture:
1、换热器;2、布液管;21、喷射孔;3、换热管;11、进液口;4、连通管路。1. Heat exchanger; 2. Liquid distribution pipe; 21. Injection hole; 3. Heat exchange pipe; 11. Liquid inlet; 4. Connecting pipeline.
具体实施方式Detailed ways
为了使本发明的目的、技术方案及优点更加清楚明白,以下结合附图及实施例对本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅用于解释本发明,并不用于限定本发明。In order to make the objectives, technical solutions and advantages of the present invention clearer, the present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention, but not to limit the present invention.
如图1至图5所示的布液结构,应用于换热器1,特别是壳管式换热器1,所述布液结构包括:The liquid distribution structure shown in Figures 1 to 5 is applied to a
用于将液态冷媒分布至换热器1内部的布液管2,所述布液管2设置于所述换热器1内,且所述布液管2上设置有喷射孔21,液态冷媒进入布液管2后由喷射孔21喷射至换热器1内部;The
所述换热器1内设置有换热管3,所述布液管2呈环形设置于所述换热管3的上方,通过将布液管2环形设置,使布液管2能够与现有技术中的布液盘结构的尺寸相同,保证布液面积相同,且所述喷射孔21的喷射方向朝向所述换热管3和/或朝向所述换热管3的上方,使得喷射孔21喷射出的液态冷媒能够直接接触换热管3,保证液态冷媒的换热效率。The
所述换热器1上设置有进液口11,所述进液口11与所述布液管2连通,液态冷媒直接由进液口11进入布液管2中。The
所述布液管2围成矩形框架,所述矩形框架的底面朝向所述换热管3,且所述喷射孔21处于所述矩形框架的内表面、底面或外表面上,也即布液管2呈矩形方式设置,与现有技术中的布液盘结构的矩形布液盘的边沿位置相同,并且根据在不同侧面上设置喷射孔21控制液态冷媒的喷射方向,从而实现均匀布液的目的。The
所述布液结构还包括至少一根连通管路4,所述连通管路4设置于所述环形内部,且所述连通管路4的两端均与所述布液管2连通,利用连通管路4将所述布液管2的两个不同位置进行连通,增加液态冷媒的流动区域,使液态冷媒能够快速的到达布液管2的任意位置处,从而增加布液管2的布液效果。The liquid distribution structure also includes at least one communication pipeline 4, the communication pipeline 4 is arranged inside the ring, and both ends of the communication pipeline 4 are communicated with the
所述连通管路4的数量为至少两根,所有所述连通管路4并列设置于所述环形内部;或所述连通管路4的数量为至少两根,所有所述连通管路4交叉设置于所述环形内部,且相互交叉的所述连通管路4之间相互连通,具体连通管路4的数量和布置方式根据实际要求进行设置。The number of the communication pipelines 4 is at least two, and all the communication pipelines 4 are arranged in the annular interior side by side; or the number of the communication pipelines 4 is at least two, and all the communication pipelines 4 intersect The communication pipelines 4 that are arranged inside the ring and intersect with each other communicate with each other, and the specific number and arrangement of the communication pipelines 4 are set according to actual requirements.
所述连通管路4上设置有喷射孔21,尽可能的增加喷射孔21的数量,从而增加布液管2的布液效果。The communication pipeline 4 is provided with
沿远离所述换热管3的方向,所述喷射孔21呈至少一个三角形分布于所述布液管2上;或沿远离所述换热管3的方向,所述喷射孔21呈矩形分布于所述布液管2上;或沿远离所述换热管3的方向,所述喷射孔21的流通面积逐渐减小,上述方式均能够保证所有喷射孔21均能够实现均匀布液的目的。In the direction away from the
所述布液管2的截面为梯形,所述梯形的底角角度范围为0°至90°;或所述布液管2的截面为三角形,所述三角形的顶角的角度范围为0°至180°;或所述布液管2的截面为圆形。The cross-section of the
所述布液管2的截面为矩形,所述矩形的一个侧面向所述矩形的内部凹陷形成折弯结构,所述折弯结构上设置有喷射孔21,也即所述布液管2的截面为K形,并且在K形的两个斜面上均设置喷射孔21能够增加喷射的方向,从而增加布液效果。The cross section of the
所述折弯结构包括相互连接的第一平面和第二平面,所述第一平面和所述第二平面之间具有夹角,第一平面和第二平面构成K形的两个斜面。The bending structure includes a first plane and a second plane that are connected to each other, an included angle is formed between the first plane and the second plane, and the first plane and the second plane form two inclined planes of the K-shape.
所述第一平面上设置有喷射孔21;或所述第二平面上设置有喷射孔21;或所述第一平面和所述第二平面上均设置有喷射孔21。The first plane is provided with injection holes 21 ; or the second plane is provided with injection holes 21 ; or both the first plane and the second plane are provided with injection holes 21 .
所述夹角的角度范围为0°-180°。The angle range of the included angle is 0°-180°.
喷射孔21的数量按照冷媒灌注量进行流速计算确定,优选范围:1-10m/s。The number of injection holes 21 is determined by calculating the flow rate according to the amount of refrigerant injected, and the preferred range is 1-10 m/s.
一种换热器1,包括上述的布液结构。A
所述换热器1还包括均气板,所述换热器1上设置有通气孔,所述均气板设置于所述布液结构和所述通气孔之间,利用均气板将换热器1在蒸发过程中避免蒸发的气态冷媒产生带液的问题。The
以上所述实施例仅表达了本发明的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对本发明专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围。因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only represent several embodiments of the present invention, and the descriptions thereof are specific and detailed, but should not be construed as limiting the scope of the patent of the present invention. It should be noted that, for those skilled in the art, without departing from the concept of the present invention, several modifications and improvements can be made, which all belong to the protection scope of the present invention. Therefore, the protection scope of the patent of the present invention should be subject to the appended claims.
Claims (14)
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113865374A (en) * | 2021-10-22 | 2021-12-31 | 珠海格力电器股份有限公司 | Liquid distributor, heat exchanger and air conditioner |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201551964U (en) * | 2009-12-10 | 2010-08-18 | 庞金钊 | A liquid distributor for a flue gas biological desulfurization device |
JP2011027296A (en) * | 2009-07-23 | 2011-02-10 | Hitachi Appliances Inc | Liquid distributor, shell-type heat exchanger using this, and absorption refrigerator using these |
WO2013094206A1 (en) * | 2011-12-21 | 2013-06-27 | Sharp Kabushiki Kaisha | Heat and mass exchanger for liquid desiccant air conditioners |
CN104549057A (en) * | 2015-02-05 | 2015-04-29 | 青岛亿明翔精细化工科技有限公司 | Multipurpose tubular packed reactor |
CN104784949A (en) * | 2015-04-02 | 2015-07-22 | 沈阳航空航天大学 | Special-shaped falling-film evaporation tube |
CN210922264U (en) * | 2019-10-08 | 2020-07-03 | 沁阳市季晨化工有限公司 | Cooling tower for producing direct acid-resistant scarlet |
CN212362925U (en) * | 2020-08-26 | 2021-01-15 | 珠海格力电器股份有限公司 | Liquid distribution structure with shielding prevention effect and heat exchanger |
-
2020
- 2020-08-26 CN CN202010872528.3A patent/CN111947490A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011027296A (en) * | 2009-07-23 | 2011-02-10 | Hitachi Appliances Inc | Liquid distributor, shell-type heat exchanger using this, and absorption refrigerator using these |
CN201551964U (en) * | 2009-12-10 | 2010-08-18 | 庞金钊 | A liquid distributor for a flue gas biological desulfurization device |
WO2013094206A1 (en) * | 2011-12-21 | 2013-06-27 | Sharp Kabushiki Kaisha | Heat and mass exchanger for liquid desiccant air conditioners |
CN104549057A (en) * | 2015-02-05 | 2015-04-29 | 青岛亿明翔精细化工科技有限公司 | Multipurpose tubular packed reactor |
CN104784949A (en) * | 2015-04-02 | 2015-07-22 | 沈阳航空航天大学 | Special-shaped falling-film evaporation tube |
CN210922264U (en) * | 2019-10-08 | 2020-07-03 | 沁阳市季晨化工有限公司 | Cooling tower for producing direct acid-resistant scarlet |
CN212362925U (en) * | 2020-08-26 | 2021-01-15 | 珠海格力电器股份有限公司 | Liquid distribution structure with shielding prevention effect and heat exchanger |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113865374A (en) * | 2021-10-22 | 2021-12-31 | 珠海格力电器股份有限公司 | Liquid distributor, heat exchanger and air conditioner |
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