WO2024066212A1 - Gas-liquid separation device and new energy vehicle air-conditioning system - Google Patents

Gas-liquid separation device and new energy vehicle air-conditioning system Download PDF

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Publication number
WO2024066212A1
WO2024066212A1 PCT/CN2023/080684 CN2023080684W WO2024066212A1 WO 2024066212 A1 WO2024066212 A1 WO 2024066212A1 CN 2023080684 W CN2023080684 W CN 2023080684W WO 2024066212 A1 WO2024066212 A1 WO 2024066212A1
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WIPO (PCT)
Prior art keywords
gas
reflux
liquid separation
side wall
flow hole
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PCT/CN2023/080684
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French (fr)
Chinese (zh)
Inventor
余挺
覃小军
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浙江银轮机械股份有限公司
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Publication of WO2024066212A1 publication Critical patent/WO2024066212A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/006Accumulators

Definitions

  • the present application relates to the technical field of gas-liquid separation of refrigerant media, and in particular to a gas-liquid separation device and a new energy vehicle air-conditioning system.
  • the gas-liquid separation device is generally set between the evaporator and the compressor, that is, the refrigerant enters the gas-liquid separation device from the evaporator and then enters the compressor.
  • An important function of the gas-liquid separation device is to separate the gas-liquid two-phase refrigerant flowing out of the evaporator, thereby minimizing the probability of liquid refrigerant being sucked into the compressor to prevent liquid refrigerant from causing liquid hammer on the compressor.
  • the gas-liquid separation device needs to separate the liquid refrigerant from the gas-liquid two-phase refrigerant as much as possible.
  • the gas-liquid separation device in the related technology usually designs a U-shaped tube to realize the gas-liquid separation of the refrigerant.
  • the residence time of the gas-liquid mixed refrigerant in the U-shaped tube is relatively short, which leads to incomplete gas-liquid separation of the refrigerant, thereby reducing the effect of gas-liquid separation of the refrigerant.
  • a gas-liquid separation device and a new energy vehicle air conditioning system are provided. System.
  • the gas-liquid separation device provided in the present application is provided with an inlet, a diverter chamber, a first gas-liquid separation channel and a second gas-liquid separation channel.
  • the diverter chamber is provided with a bottom wall, a first side wall and a second side wall.
  • the first side wall and the second side wall are arranged at a conical angle to enclose a diverter chamber with a conical cross-section; an end of the first side wall away from the second side wall is connected to the first gas-liquid separation channel, and an end of the second side wall away from the first side wall is connected to the second gas-liquid separation channel.
  • the flow direction of the inlet is perpendicular to the bottom wall of the diverter chamber.
  • the refrigerant can enter the diverter chamber through the inlet, and the refrigerant in the diverter chamber can enter the first gas-liquid separation channel along the first side wall, and enter the second gas-liquid separation channel along the second side wall.
  • the angle between the first side wall and the second side wall is greater than or equal to 45° and less than or equal to 135°.
  • an arc-shaped transition section is provided between the first side wall and the second side wall, and a portion of the outer contour of the orthographic projection of the inlet on the bottom wall of the diversion cavity coincides with the arc-shaped transition section.
  • the gas-liquid separation device includes an outer shell, a partition, an inlet pipe and an outlet pipe.
  • the outer shell is provided with a accommodating chamber and an inlet port and an outlet port respectively connected to the accommodating chamber.
  • the inlet pipe is inserted into the inlet port and connected to the inlet port.
  • One end of the outlet pipe is inserted into the accommodating chamber, and the other end extends out of the accommodating chamber and is inserted into the outlet port.
  • One end of the partition is directly or indirectly connected to the outer wall of the outlet pipe, and the other end extends toward a direction close to the side wall of the accommodating chamber to separate the accommodating chamber into a first chamber and a second chamber, and the partition is provided with a connecting port connecting the first chamber and the second chamber.
  • the shell includes a cylinder and a sealing cover, the sealing cover is sealingly arranged at the opening of the cylinder, and the inlet and the outlet are arranged on the sealing cover.
  • a liquid outlet gap connecting the first cavity and the second cavity is provided between the partition and the inner wall of the accommodating cavity.
  • one of the first gas-liquid separation channel and the second gas-liquid separation channel Or one or more reflux structures are provided in both, and the reflux structure includes a first reflux plate and a second reflux plate distributed in sequence along a first direction, wherein the first direction is the extension direction of the first gas-liquid separation channel or the first direction is the extension direction of the second gas-liquid separation channel, the first reflux plate is provided with a first through-flow hole and a first reflux surface, the second reflux plate is provided with a second through-flow hole and a second reflux surface, the first through-flow hole and the second reflux surface are correspondingly distributed along the first direction, and the second through-flow hole and the first reflux surface are correspondingly distributed along the first direction, the second reflux surface can reflux the refrigerant entering through the first through-flow hole to the first reflux surface, and the first reflux surface can reflux the refrigerant refluxed from the second reflux surface to the second through-flow hole.
  • the reflux structure also includes a third reflux plate, the first reflux plate, the second reflux plate and the third reflux plate are sequentially distributed along the first direction, the third reflux plate is provided with a third through-hole and a third reflux surface, the second reflux plate is provided with a back reflux surface at one end away from the second reflux surface, the third through-hole and the back reflux surface are correspondingly distributed along the first direction, and the third reflux surface and the second through-hole are correspondingly distributed along the first direction, the third reflux surface can return the refrigerant entering through the second through-hole to the back reflux surface, and the back reflux surface can return the refrigerant returning from the third reflux surface to the third through-hole.
  • a first guide plate extending toward the second return surface is provided at an edge of the first flow hole.
  • a second guide plate extending toward the third return surface is provided at an edge of the second flow hole.
  • a third guide plate extending toward the reverse flow surface is provided at the edge of the third through-flow hole.
  • a vertically arranged first liquid baffle is provided at the bottom of the first through-hole.
  • a second liquid baffle plate is vertically arranged at the bottom of the second through-flow hole.
  • a third liquid baffle plate is vertically arranged at the bottom of the third through-flow hole.
  • the present application also provides a new energy vehicle air conditioning system, including an evaporator, a compressor and the above
  • the gas-liquid separation device is arranged between the evaporator and the compressor, and the refrigerant enters the gas-liquid separation device from the evaporator and then enters the compressor.
  • FIG1 is a schematic diagram of the structure of a gas-liquid separation device according to one or more embodiments provided in the present application.
  • FIG2 is a cross-sectional view of a gas-liquid separation device according to one or more embodiments provided in the present application.
  • FIG. 3 is an exploded view of a gas-liquid separation device according to one or more embodiments provided in the present application.
  • FIG. 4 is a schematic diagram of a partial structure of a gas-liquid separation device according to one or more embodiments provided in the present application.
  • FIG5 is a schematic diagram of the structure of a new energy vehicle air-conditioning system according to one or more embodiments provided in the present application.
  • first and second are used for descriptive purposes only and should not be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features defined as “first” and “second” may explicitly or implicitly include at least one of the features. In the description of this application, the meaning of "plurality” is at least two, such as two, three, etc., unless otherwise clearly and specifically defined.
  • the terms “installed”, “connected”, “connected”, “fixed” and the like should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements, unless otherwise clearly defined.
  • installed can be a fixed connection, a detachable connection, or an integral connection
  • it can be a mechanical connection or an electrical connection
  • it can be a direct connection or an indirect connection through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements, unless otherwise clearly defined.
  • the specific meanings of the above terms in this application can be understood according to specific circumstances.
  • a first feature is “on” or “on” a second feature.
  • “Under” means that the first and second features are in direct contact, or the first and second features are in indirect contact through an intermediate medium.
  • the first feature “above”, “above” and “above” the second feature may mean that the first feature is directly above or obliquely above the second feature, or simply means that the first feature is higher in level than the second feature.
  • the first feature “under”, “below” and “below” the second feature may mean that the first feature is directly below or obliquely below the second feature, or simply means that the first feature is lower in level than the second feature.
  • the gas-liquid separation device 100 is generally arranged between the evaporator 901 and the compressor 902, that is, the refrigerant enters the gas-liquid separation device from the evaporator 901 and then enters the compressor 902.
  • An important function of the gas-liquid separation device is to separate the gas-liquid two-phase refrigerant flowing out of the evaporator 901 into gas and liquid, thereby minimizing the probability of the liquid refrigerant being sucked into the compressor 902, so as to prevent the liquid refrigerant from causing liquid hammer to the compressor 902.
  • the gas-liquid separation device needs to separate the liquid refrigerant from the gas-liquid two-phase refrigerant as much as possible.
  • the gas-liquid separation device in the related technology usually designs a U-shaped tube to realize the gas-liquid separation of the refrigerant.
  • the residence time of the gas-liquid mixed refrigerant in the U-shaped tube is relatively short, which leads to incomplete gas-liquid separation of the refrigerant, thereby reducing the effect of gas-liquid separation of the refrigerant.
  • the present application provides a gas-liquid separation device 100.
  • the gas-liquid separation device 100 is provided with an inlet 313, a diverter cavity 700, a first gas-liquid separation channel 110 and a second gas-liquid separation channel 120.
  • the diverter cavity 700 is provided with a bottom wall 710, a first side wall 720 and a second side wall 730.
  • the first side wall 720 and the second side wall 730 are arranged at a conical angle to enclose the diverter cavity 700 with a conical cross section.
  • first side wall 720 away from the second side wall 730 is connected to the first gas-liquid separation channel 110, and one end of the second side wall 730 away from the first side wall 720 is connected to the second gas-liquid separation channel 120.
  • the flow direction of the inlet port 313 is perpendicular to the bottom wall 710 of the diversion chamber 700.
  • the refrigerant can enter the diversion chamber 700 through the inlet port 313, and the refrigerant in the diversion chamber 700 can enter the first gas-liquid separation channel 110 along the first side wall 720, and enter the second gas-liquid separation channel 120 along the second side wall 730.
  • the conical angle setting refers to that the first side wall 720 and the second side wall 730 are arranged to form a conical angle, and the angle is greater than 0° and less than 180°.
  • the inflow direction refers to the flow direction of the gas-liquid two-phase refrigerant.
  • the refrigerant will fully contact the bottom wall 710, the first side wall 720 and the second side wall 730 of the flow diversion chamber 700 during the diffusion process in the flow diversion chamber 700, so that the liquid refrigerant condenses on the bottom wall 710, the first side wall 720 and the second side wall 730 of the flow diversion chamber 700.
  • the gas-liquid two-phase refrigerant can enter the first gas-liquid separation channel along the first side wall 720 under the promotion of the gas pressure difference. 110, and enter the second gas-liquid separation channel 120 along the second side wall 730, so that the condensation effect of the liquid refrigerant on the first side wall 720 and the second side wall 730 is further enhanced, thereby improving the gas-liquid separation effect of the refrigerant.
  • first side wall 720 and the second side wall 730 have a certain flow-guiding effect on the refrigerant, avoiding turbulence of the refrigerant in the diversion cavity 700, so that the separation efficiency of the gas-liquid separation device 100 is improved.
  • the angle between the first side wall 720 and the second side wall 730 is greater than or equal to 45° and less than or equal to 135°.
  • the angle between the first side wall 720 and the second side wall 730 is greater than or equal to 45°, which is conducive to expanding the volume of the diversion chamber 700 so that the diversion chamber 700 can accommodate more gas-liquid two-phase refrigerant.
  • the angle between the first side wall 720 and the second side wall 730 is less than or equal to 135°, which can avoid the angle between the first side wall 720 and the second side wall 730 being too large and affecting the refrigerant entering the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120.
  • the included angle between the first side wall 720 and the second side wall 730 is 90°.
  • an arcuate transition section 740 is provided between the first side wall 720 and the second side wall 730 , and a portion of the outer contour of the inlet 313 projected onto the bottom wall 710 of the diversion cavity 700 coincides with the arcuate transition section 740 .
  • the refrigerant can smoothly enter the first side wall 720 and the second side wall 730 along the arc transition section 740, avoiding turbulence of the gas-liquid two-phase refrigerant in the diversion chamber 700, thereby improving the diversion efficiency of the gas-liquid separation device 100.
  • one or both of the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 are provided with one or more reflux structures 200
  • the reflux structure 200 includes a first reflux plate 210 and a second reflux plate 220 sequentially distributed along a first direction, wherein the first direction is an extension direction of the first gas-liquid separation channel 110 or a direction of the second gas-liquid separation channel 120.
  • the first return plate 210 is provided with a first through-hole 211 and a first return surface 212
  • the second return plate 220 is provided with a second through-hole 221 and a second return surface 222.
  • the first through-hole 211 and the second return surface 222 are correspondingly distributed along the first direction, and the second through-hole 221 and the first return surface 212 are correspondingly distributed along the first direction, and the second return surface 222 can return the refrigerant entering through the first through-hole 211 to the first return surface 212, and the first return surface 212 can return the refrigerant returned by the second return surface 222 to the second through-hole 221.
  • the first direction is not a fixed direction.
  • the first direction is the extension direction of the first gas-liquid separation channel 110.
  • the first direction is the extension direction of the second gas-liquid separation channel 120.
  • the first direction may be a direction along a straight line, a direction along a curve, or a specific direction extending along an arbitrary shape, which is not limited here.
  • first side wall 720 and the second side wall 730 are side walls of different first reflow plates 210 .
  • the refrigerant will pass through one or more reflux structures 200 when flowing in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 .
  • the reflux structure 200 includes a first reflux plate 210 and a second reflux plate 220 sequentially distributed along the first direction, the first reflux plate 210 is provided with a first through-hole 211 and a first reflux surface 212, and correspondingly, the second reflux plate 220 is provided with a second through-hole 221 and a second reflux surface 222.
  • first through-hole 211 and the second reflux surface 222 are correspondingly distributed along the first direction
  • the second through-hole 221 and the first reflux surface 212 are correspondingly distributed along the first direction
  • the second reflux surface 222 can reflux the refrigerant entering through the first through-hole 211 to the second reflux surface 222
  • the second reflux surface 222 can The refrigerant returning from the first return surface 212 is returned to the second flow hole 221 .
  • the second return surface 222 of the second return plate 220 returns the refrigerant to the first return surface 212 of the first return plate 210, and then the first return surface 212 returns the refrigerant to the second flow hole 221 of the second return plate 220, and finally, the refrigerant leaves the return structure 200 from the second flow hole 221.
  • the contact area and contact time of the gas-liquid two-phase refrigerant with the first reflux plate 210 and the second reflux plate 220 are significantly increased, that is, the residence time of the refrigerant in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 is significantly increased, and the contact area between the refrigerant and the gas-liquid separation device 100 is significantly increased, which is conducive to the adsorption of liquid refrigerant on the inner walls of the first reflux plate 210, the second reflux plate 220 and the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120, thereby significantly improving the gas-liquid separation effect of the gas-liquid separation device 100.
  • one or more reflux structures 200 are arranged in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 to achieve a better gas-liquid separation effect, without the need to lengthen the traditional gas-liquid separation channel to achieve a better gas-liquid separation effect. Therefore, the gas-liquid separation device 100 provided in the present application is smaller in size, and it is easier to install the gas-liquid separation device 100.
  • the reflux structure 200 further includes a third reflux plate 230, the first reflux plate 210, the second reflux plate 220 and the third reflux plate 230 are sequentially distributed along the first direction, the third reflux plate 230 is provided with a third through-flow hole 231 and a third reflux surface 232, the second reflux plate 220 is provided with a back reflux surface 223 at one end away from the second reflux surface 222, the third through-flow hole 231 and the back reflux surface 223 are correspondingly distributed along the first direction, and the third reflux surface 232 and the second through-flow hole 221 are arranged along the first direction.
  • the third return surface 232 can return the refrigerant entering through the second through-flow hole 221 to the back return surface 223 , and the back return surface 223 can return the refrigerant returning from the third return surface 232 to the third through-flow hole 231 .
  • the third return surface 232 of the third return plate 230 can return the refrigerant to the back return surface 223 of the second return plate 220, and then the back return surface 223 returns the refrigerant to the third flow hole 231 of the third return plate 230, and finally, the refrigerant leaves the return structure 200 from the third flow hole 231.
  • the contact area and contact time of the gas-liquid two-phase refrigerant with the first reflux plate 210, the second reflux plate 220 and the third reflux plate 230 are significantly increased, that is, the residence time of the refrigerant in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 is significantly increased, and the contact area between the refrigerant and the gas-liquid separation device 100 is significantly increased, which is conducive to the adsorption of liquid refrigerant on the inner walls of the first reflux plate 210, the second reflux plate 220, the third reflux plate 230 and the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120, thereby significantly improving the gas-liquid separation effect of the gas-liquid separation device 100.
  • a first guide plate 240 extending toward the second return surface 222 is disposed at an edge of the first through hole 211 .
  • the refrigerant is facilitated to flow toward the second return surface 222 through the first guide plate 240 .
  • a second guide plate 250 extending toward the third return surface 232 is disposed at an edge of the second through-hole 221 .
  • the refrigerant is facilitated to flow to the third return surface 232 through the second guide plate 250 .
  • one end of the second guide plate 250 away from the third return plate 230 extends toward a direction close to the first return surface 212 .
  • the refrigerant is facilitated to enter the second flow path from the first return surface 212 through the second guide plate 250.
  • the hole 221 further enhances the flow guiding effect of the second guide plate 250.
  • a third guide plate 290 extending toward the back-flow surface 223 is disposed at the edge of the third through-hole 231 .
  • a vertically disposed first liquid baffle plate 260 is disposed at the bottom of the first flow hole 211 .
  • the liquid refrigerant is usually concentrated at the bottom of the refrigerant due to its higher density. Therefore, by providing a vertically arranged first liquid baffle plate 260 at the bottom of the first flow hole 211, it is beneficial to increase the contact time between the liquid refrigerant and the first liquid baffle plate 260, thereby helping to improve the separation effect of the liquid refrigerant.
  • a second liquid baffle plate 270 is vertically disposed at the bottom of the second through-hole 221 .
  • a third liquid baffle plate 280 is vertically disposed at the bottom of the third through-hole 231 .
  • the gas-liquid separation device 100 includes a housing 300, a partition 400, an inlet pipe 800, and an outlet pipe 600.
  • the housing 300 is provided with a receiving chamber 310 and an inlet port 313 and an outlet port 315 respectively connected to the receiving chamber 310.
  • the inlet pipe 800 is inserted into the inlet port 313 and connected to the outlet port 315.
  • one end of the air outlet pipe 600 is inserted into the accommodating chamber 310, and the other end extends out of the accommodating chamber 310 and is inserted into the air outlet 315, one end of the partition 400 is directly or indirectly connected to the outer wall of the air outlet pipe 600, and the other end extends toward the direction close to the side wall of the accommodating chamber 310 to separate the accommodating chamber 310 into a first chamber 311 and a second chamber 312, and the partition 400 is provided with a connecting port 500 connecting the first chamber 311 and the second chamber 312.
  • the reflux structure 200 is disposed in the first cavity 311 .
  • the gas-liquid two-phase refrigerant enters the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 from the inlet pipe 800 through the inlet port 313. After that, the refrigerant undergoes gas-liquid separation under the action of the reflux structure 200. Then, the refrigerant enters the second cavity 312 through the connecting port 500, and the liquid refrigerant is deposited at the bottom of the second cavity 312. The gaseous refrigerant leaves the second cavity 312 through the outlet pipe 600, thereby realizing the gas-liquid separation of the gas-liquid two-phase refrigerant.
  • the housing 300 includes a cylinder 320 and a sealing cover 330 , the sealing cover 330 is sealingly disposed at the opening of the cylinder 320 , the inlet 313 and the outlet 315 are disposed at the sealing cover 330 , and the reflux structure 200 and the partition 400 are both disposed in the cylinder 320 .
  • the inlet 313 and the outlet 315 are arranged on the sealing cover 330 , which greatly reduces the difficulty of connecting the inlet pipe 800 and the housing 300 , and reduces the difficulty of connecting the outlet pipe 600 and the housing 300 .
  • a liquid outlet gap 314 communicating with the first cavity 311 and the second cavity 312 is provided between the partition plate 400 and the inner wall of the accommodating cavity 310 .
  • the liquid refrigerant can enter the second chamber 312 from the first chamber 311 through the liquid outlet gap 314 .
  • the end surface of one side of the partition 400 close to the first cavity 311 is inclined from an end away from the liquid outlet gap 314 to an end close to the liquid outlet gap 314 toward a direction away from the first cavity 311 .

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Air-Conditioning For Vehicles (AREA)
  • Separating Particles In Gases By Inertia (AREA)

Abstract

A gas-liquid separation device (100) and a new energy vehicle air-conditioning system (1000). The gas-liquid separation device (100) is provided with a flow inlet (313), a flow dividing cavity (700), a first gas-liquid separation channel (110) and a second gas-liquid separation channel (120), wherein the flow dividing cavity (700) is provided with a bottom wall (710), a first side wall (720) and a second side wall (730); the first side wall (720) is in communication with the first gas-liquid separation channel (110); the second side wall (730) is in communication with the second gas-liquid separation channel (120); the flow intake direction of the flow inlet (313) is perpendicular to the bottom wall (710) of the flow dividing cavity (700); and a refrigerant can enter the flow dividing cavity (700) through the flow inlet (313), enter the first gas-liquid separation channel (110) along the first side wall (720), and enter the second gas-liquid separation channel (120) along the second side wall (730).

Description

气液分离装置及新能源汽车空调系统Gas-liquid separation device and new energy vehicle air conditioning system
相关申请Related Applications
本申请要求2022年9月28日申请的,申请号为202211189937.9,发明名称为“气液分离装置”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims priority to the Chinese patent application filed on September 28, 2022, with application number 202211189937.9 and invention name “Gas-Liquid Separation Device”, the entire contents of which are incorporated by reference into this application.
技术领域Technical Field
本申请涉及冷媒介质气液分离技术领域,特别是涉及一种气液分离装置及新能源汽车空调系统。The present application relates to the technical field of gas-liquid separation of refrigerant media, and in particular to a gas-liquid separation device and a new energy vehicle air-conditioning system.
背景技术Background technique
在新能源汽车空调系统中,气液分离装置一般设置于蒸发器和压缩机之间,也即,冷媒从蒸发器进入气液分离装置之后再进入压缩机。气液分离装置的一个重要的功能便是对从蒸发器流出的气液两相的冷媒进行气液分离,从而最大限度地降低液态冷媒被吸入压缩机的概率,以防止液态冷媒对压缩机造成液击。In the air conditioning system of new energy vehicles, the gas-liquid separation device is generally set between the evaporator and the compressor, that is, the refrigerant enters the gas-liquid separation device from the evaporator and then enters the compressor. An important function of the gas-liquid separation device is to separate the gas-liquid two-phase refrigerant flowing out of the evaporator, thereby minimizing the probability of liquid refrigerant being sucked into the compressor to prevent liquid refrigerant from causing liquid hammer on the compressor.
因此,气液分离装置需要尽可能地将液态冷媒从气液两相的冷媒中的分离开来,为了实现上述目的,相关技术中的气液分离装置通常会设计U型管实现冷媒的气液分离,但是,气液混合的冷媒在U型管内的停留时间较短,如此,导致冷媒的气液分离不彻底,进而降低冷媒气液分离的效果。Therefore, the gas-liquid separation device needs to separate the liquid refrigerant from the gas-liquid two-phase refrigerant as much as possible. In order to achieve the above purpose, the gas-liquid separation device in the related technology usually designs a U-shaped tube to realize the gas-liquid separation of the refrigerant. However, the residence time of the gas-liquid mixed refrigerant in the U-shaped tube is relatively short, which leads to incomplete gas-liquid separation of the refrigerant, thereby reducing the effect of gas-liquid separation of the refrigerant.
发明内容Summary of the invention
根据本申请的各种实施例,提供一种气液分离装置及新能源汽车空调系 统。According to various embodiments of the present application, a gas-liquid separation device and a new energy vehicle air conditioning system are provided. System.
本申请提供的气液分离装置设有进流口、分流腔、第一气液分离通道和第二气液分离通道,分流腔设有底壁、第一侧壁和第二侧壁,第一侧壁和第二侧壁呈锥形夹角设置,以围设形成横截面呈锥形的分流腔;第一侧壁远离第二侧壁的一端连通第一气液分离通道,第二侧壁远离第一侧壁的一端连通第二气液分离通道,进流口的进流方向垂直于分流腔的底壁,冷媒能够通过进流口进入分流腔,且分流腔内的冷媒能够沿着第一侧壁进入第一气液分离通道,以及沿着第二侧壁进入第二气液分离通道。The gas-liquid separation device provided in the present application is provided with an inlet, a diverter chamber, a first gas-liquid separation channel and a second gas-liquid separation channel. The diverter chamber is provided with a bottom wall, a first side wall and a second side wall. The first side wall and the second side wall are arranged at a conical angle to enclose a diverter chamber with a conical cross-section; an end of the first side wall away from the second side wall is connected to the first gas-liquid separation channel, and an end of the second side wall away from the first side wall is connected to the second gas-liquid separation channel. The flow direction of the inlet is perpendicular to the bottom wall of the diverter chamber. The refrigerant can enter the diverter chamber through the inlet, and the refrigerant in the diverter chamber can enter the first gas-liquid separation channel along the first side wall, and enter the second gas-liquid separation channel along the second side wall.
在其中一个实施例中,第一侧壁和第二侧壁之间的夹角大于或等于45°且小于或等于135°。In one embodiment, the angle between the first side wall and the second side wall is greater than or equal to 45° and less than or equal to 135°.
在其中一个实施例中,第一侧壁和第二侧壁之间设有弧形过渡段,且进流口在分流腔底壁上的正投影的部分外轮廓与弧形过渡段重合。In one of the embodiments, an arc-shaped transition section is provided between the first side wall and the second side wall, and a portion of the outer contour of the orthographic projection of the inlet on the bottom wall of the diversion cavity coincides with the arc-shaped transition section.
在其中一个实施例中,气液分离装置包括外壳、隔板、进流管以及出气管,外壳设有容纳腔以及分别连通容纳腔的进流口和出气口,进流管插置于进流口并连通进流口,出气管一端插置于容纳腔内,另一端伸出容纳腔并插置于出气口,隔板一端直接或间接连接出气管的外壁,另一端朝向靠近容纳腔侧壁的方向延伸,以将容纳腔分隔成第一腔和第二腔,并且,隔板设有连通第一腔和第二腔的连通口。In one embodiment, the gas-liquid separation device includes an outer shell, a partition, an inlet pipe and an outlet pipe. The outer shell is provided with a accommodating chamber and an inlet port and an outlet port respectively connected to the accommodating chamber. The inlet pipe is inserted into the inlet port and connected to the inlet port. One end of the outlet pipe is inserted into the accommodating chamber, and the other end extends out of the accommodating chamber and is inserted into the outlet port. One end of the partition is directly or indirectly connected to the outer wall of the outlet pipe, and the other end extends toward a direction close to the side wall of the accommodating chamber to separate the accommodating chamber into a first chamber and a second chamber, and the partition is provided with a connecting port connecting the first chamber and the second chamber.
在其中一个实施例中,外壳包括筒体和密封盖,密封盖密封设置于筒体的开口处,进流口和出气口设于密封盖。In one embodiment, the shell includes a cylinder and a sealing cover, the sealing cover is sealingly arranged at the opening of the cylinder, and the inlet and the outlet are arranged on the sealing cover.
在其中一个实施例中,隔板与容纳腔内壁之间设有连通第一腔和第二腔的出液间隙。In one of the embodiments, a liquid outlet gap connecting the first cavity and the second cavity is provided between the partition and the inner wall of the accommodating cavity.
在其中一个实施例中,第一气液分离通道和第二气液分离通道中的一者 或者两者内设有一个或多个回流结构,回流结构包括沿着第一方向依次分布的第一回流板和第二回流板,其中,第一方向为第一气液分离通道的延伸方向或者第一方向为第二气液分离通道的延伸方向,第一回流板设有第一通流孔和第一回流面,第二回流板设有第二通流孔和第二回流面,第一通流孔和第二回流面沿着第一方向对应分布,且第二通流孔和第一回流面沿着第一方向对应分布,第二回流面能够将通过第一通流孔进入的冷媒回流至第一回流面,且第一回流面能够将第二回流面回流的冷媒回流至第二通流孔。In one embodiment, one of the first gas-liquid separation channel and the second gas-liquid separation channel Or one or more reflux structures are provided in both, and the reflux structure includes a first reflux plate and a second reflux plate distributed in sequence along a first direction, wherein the first direction is the extension direction of the first gas-liquid separation channel or the first direction is the extension direction of the second gas-liquid separation channel, the first reflux plate is provided with a first through-flow hole and a first reflux surface, the second reflux plate is provided with a second through-flow hole and a second reflux surface, the first through-flow hole and the second reflux surface are correspondingly distributed along the first direction, and the second through-flow hole and the first reflux surface are correspondingly distributed along the first direction, the second reflux surface can reflux the refrigerant entering through the first through-flow hole to the first reflux surface, and the first reflux surface can reflux the refrigerant refluxed from the second reflux surface to the second through-flow hole.
在其中一个实施例中,回流结构还包括第三回流板,第一回流板、第二回流板和第三回流板沿着第一方向依次分布,第三回流板设有第三通流孔和第三回流面,第二回流板背离第二回流面的一端设有背向回流面,第三通流孔和背向回流面沿着第一方向对应分布,且第三回流面和第二通流孔沿着第一方向对应分布,第三回流面能够将通过第二通流孔进入的冷媒回流至背向回流面,且背向回流面能够将第三回流面回流的冷媒回流至第三通流孔。In one embodiment, the reflux structure also includes a third reflux plate, the first reflux plate, the second reflux plate and the third reflux plate are sequentially distributed along the first direction, the third reflux plate is provided with a third through-hole and a third reflux surface, the second reflux plate is provided with a back reflux surface at one end away from the second reflux surface, the third through-hole and the back reflux surface are correspondingly distributed along the first direction, and the third reflux surface and the second through-hole are correspondingly distributed along the first direction, the third reflux surface can return the refrigerant entering through the second through-hole to the back reflux surface, and the back reflux surface can return the refrigerant returning from the third reflux surface to the third through-hole.
在其中一个实施例中,第一通流孔的边缘设有朝向第二回流面延伸的第一导流板。In one of the embodiments, a first guide plate extending toward the second return surface is provided at an edge of the first flow hole.
在其中一个实施例中,第二通流孔的边缘设有朝向第三回流面延伸的第二导流板。In one of the embodiments, a second guide plate extending toward the third return surface is provided at an edge of the second flow hole.
在其中一个实施例中,第三通流孔的边缘设有朝向背向回流面延伸的第三导流板。In one of the embodiments, a third guide plate extending toward the reverse flow surface is provided at the edge of the third through-flow hole.
在其中一个实施例中,第一通流孔的底部设有竖直设置的第一挡液板。In one of the embodiments, a vertically arranged first liquid baffle is provided at the bottom of the first through-hole.
在其中一个实施例中,第二通流孔的底部设有竖直设置的第二挡液板。In one embodiment, a second liquid baffle plate is vertically arranged at the bottom of the second through-flow hole.
在其中一个实施例中,第三通流孔的底部设有竖直设置的第三挡液板。In one of the embodiments, a third liquid baffle plate is vertically arranged at the bottom of the third through-flow hole.
本申请还提供了一种新能源汽车空调系统,包括蒸发器、压缩机和如上 所述的气液分离装置,所述气液分离装置设置于所述蒸发器和所述压缩机之间,冷媒从所述蒸发器进入所述气液分离装置之后再进入所述压缩机。The present application also provides a new energy vehicle air conditioning system, including an evaporator, a compressor and the above The gas-liquid separation device is arranged between the evaporator and the compressor, and the refrigerant enters the gas-liquid separation device from the evaporator and then enters the compressor.
本申请的一个或多个实施例的细节在下面的附图和描述中提出。本申请的其它特征、目的和优点将从说明书、附图以及权利要求书变得明显。The details of one or more embodiments of the present application are set forth in the following drawings and description. Other features, objects, and advantages of the present application will become apparent from the description, drawings, and claims.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
为了更好地描述和说明这里公开的那些发明的实施例和/或示例,可以参考一幅或多幅附图。用于描述附图的附加细节或示例不应当被认为是对所公开的发明、目前描述的实施例和/或示例以及目前理解的这些发明的最佳模式中的任何一者的范围的限制。In order to better describe and illustrate the embodiments and/or examples of the inventions disclosed herein, reference may be made to one or more drawings. The additional details or examples used to describe the drawings should not be considered as limiting the scope of the disclosed inventions, the embodiments and/or examples currently described, and any of the best modes of these inventions currently understood.
图1为本申请提供的一个或多个实施例的气液分离装置的结构示意图。FIG1 is a schematic diagram of the structure of a gas-liquid separation device according to one or more embodiments provided in the present application.
图2为本申请提供的一个或多个实施例的气液分离装置的剖视图。FIG2 is a cross-sectional view of a gas-liquid separation device according to one or more embodiments provided in the present application.
图3为本申请提供的一个或多个实施例的气液分离装置的分解图。FIG. 3 is an exploded view of a gas-liquid separation device according to one or more embodiments provided in the present application.
图4为本申请提供的一个或多个实施例的气液分离装置的局部结构示意图。FIG. 4 is a schematic diagram of a partial structure of a gas-liquid separation device according to one or more embodiments provided in the present application.
图5为本申请提供的一个或多个实施例的新能源汽车空调系统的结构示意图。FIG5 is a schematic diagram of the structure of a new energy vehicle air-conditioning system according to one or more embodiments provided in the present application.
附图标记:100、气液分离装置;110、第一气液分离通道;120、第二气液分离通道;200、回流结构;210、第一回流板;211、第一通流孔;212、第一回流面;220、第二回流板;221、第二通流孔;222、第二回流面;223、背向回流面;230、第三回流板;231、第三通流孔;232、第三回流面;240、第一导流板;250、第二导流板;260、第一挡液板;270、第二挡液板;280、第三挡液板;290、第三导流板;300、外壳;310、容纳腔;311、第一腔; 312、第二腔;313、进流口;314、出液间隙;315、出气口;320、筒体;330、密封盖;400、隔板;500、连通口;600、出气管;700、分流腔;710、底壁;720、第一侧壁;730、第二侧壁;740、弧形过渡段;800、进流管;901、蒸发器;902、压缩机;1000、新能源汽车空调系统。Figure numerals: 100, gas-liquid separation device; 110, first gas-liquid separation channel; 120, second gas-liquid separation channel; 200, reflux structure; 210, first reflux plate; 211, first through-flow hole; 212, first reflux surface; 220, second reflux plate; 221, second through-flow hole; 222, second reflux surface; 223, back reflux surface; 230, third reflux plate; 231, third through-flow hole; 232, third reflux surface; 240, first guide plate; 250, second guide plate; 260, first liquid baffle plate; 270, second liquid baffle plate; 280, third liquid baffle plate; 290, third guide plate; 300, housing; 310, accommodating cavity; 311, first cavity; 312, second cavity; 313, inlet; 314, liquid outlet gap; 315, air outlet; 320, cylinder; 330, sealing cover; 400, partition; 500, connecting port; 600, air outlet pipe; 700, diversion cavity; 710, bottom wall; 720, first side wall; 730, second side wall; 740, arc-shaped transition section; 800, inlet pipe; 901, evaporator; 902, compressor; 1000, new energy vehicle air-conditioning system.
具体实施方式Detailed ways
在本申请的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”、“轴向”、“径向”、“周向”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。In the description of the present application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise", "axial", "radial", "circumferential" and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present application and simplifying the description, and do not indicate or imply that the referred device or element must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be understood as a limitation on the present application.
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。在本申请的描述中,“多个”的含义是至少两个,例如两个,三个等,除非另有明确具体的限定。In addition, the terms "first" and "second" are used for descriptive purposes only and should not be understood as indicating or implying relative importance or implicitly indicating the number of the indicated technical features. Therefore, the features defined as "first" and "second" may explicitly or implicitly include at least one of the features. In the description of this application, the meaning of "plurality" is at least two, such as two, three, etc., unless otherwise clearly and specifically defined.
在本申请中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或成一体;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通或两个元件的相互作用关系,除非另有明确的限定。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本申请中的具体含义。In this application, unless otherwise clearly specified and limited, the terms "installed", "connected", "connected", "fixed" and the like should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, it can be the internal connection of two elements or the interaction relationship between two elements, unless otherwise clearly defined. For ordinary technicians in this field, the specific meanings of the above terms in this application can be understood according to specific circumstances.
在本申请中,除非另有明确的规定和限定,第一特征在第二特征“上”或 “下”可以是第一和第二特征直接接触,或第一和第二特征通过中间媒介间接接触。而且,第一特征在第二特征“之上”、“上方”和“上面”可是第一特征在第二特征正上方或斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”可以是第一特征在第二特征正下方或斜下方,或仅仅表示第一特征水平高度小于第二特征。In this application, unless otherwise expressly specified or limited, a first feature is "on" or "on" a second feature. “Under” means that the first and second features are in direct contact, or the first and second features are in indirect contact through an intermediate medium. Moreover, the first feature “above”, “above” and “above” the second feature may mean that the first feature is directly above or obliquely above the second feature, or simply means that the first feature is higher in level than the second feature. The first feature “under”, “below” and “below” the second feature may mean that the first feature is directly below or obliquely below the second feature, or simply means that the first feature is lower in level than the second feature.
需要说明的是,当元件被称为“固定于”或“设置于”另一个元件,它可以直接在另一个元件上或者也可以存在居中的元件。当一个元件被认为是“连接”另一个元件,它可以是直接连接到另一个元件或者可能同时存在居中元件。本申请所使用的术语“垂直的”、“水平的”、“上”、“下”、“左”、“右”以及类似的表述只是为了说明的目的,并不表示是唯一的实施方式。It should be noted that when an element is referred to as being "fixed to" or "disposed on" another element, it may be directly on the other element or there may be a central element. When an element is considered to be "connected to" another element, it may be directly connected to the other element or there may be a central element at the same time. The terms "vertical", "horizontal", "upper", "lower", "left", "right" and similar expressions used in this application are for illustrative purposes only and do not represent the only implementation method.
除非另有定义,本申请所使用的所有的技术和科学术语与属于本申请的技术领域的技术人员通常理解的含义相同。在本申请的说明书中所使用的术语只是为了描述具体的实施方式的目的,不是旨在于限制本申请。本申请所使用的术语“及/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used in this application have the same meaning as those commonly understood by those skilled in the art to which this application belongs. The terms used in the specification of this application are only for the purpose of describing specific embodiments and are not intended to limit this application. The term "and/or" used in this application includes any and all combinations of one or more related listed items.
如图5所示,在新能源汽车空调系统1000中,气液分离装置100一般设置于蒸发器901和压缩机902之间,也即,冷媒从蒸发器901进入气液分离装置之后再进入压缩机902。气液分离装置的一个重要的功能便是对从蒸发器901流出的气液两相的冷媒进行气液分离,从而最大限度地降低液态冷媒被吸入压缩机902的概率,以防止液态冷媒对压缩机902造成液击。As shown in FIG5 , in the new energy vehicle air conditioning system 1000, the gas-liquid separation device 100 is generally arranged between the evaporator 901 and the compressor 902, that is, the refrigerant enters the gas-liquid separation device from the evaporator 901 and then enters the compressor 902. An important function of the gas-liquid separation device is to separate the gas-liquid two-phase refrigerant flowing out of the evaporator 901 into gas and liquid, thereby minimizing the probability of the liquid refrigerant being sucked into the compressor 902, so as to prevent the liquid refrigerant from causing liquid hammer to the compressor 902.
因此,气液分离装置需要尽可能地将液态冷媒从气液两相的冷媒中的分离开来,为了实现上述目的,相关技术中的气液分离装置通常会设计U型管实现冷媒的气液分离,但是,气液混合的冷媒在U型管内的停留时间较短,如此,导致冷媒的气液分离不彻底,进而降低冷媒气液分离的效果。 Therefore, the gas-liquid separation device needs to separate the liquid refrigerant from the gas-liquid two-phase refrigerant as much as possible. In order to achieve the above purpose, the gas-liquid separation device in the related technology usually designs a U-shaped tube to realize the gas-liquid separation of the refrigerant. However, the residence time of the gas-liquid mixed refrigerant in the U-shaped tube is relatively short, which leads to incomplete gas-liquid separation of the refrigerant, thereby reducing the effect of gas-liquid separation of the refrigerant.
请参阅图1-图4,为了解决现有的气液混合的冷媒在U型管内的停留时间较短导致冷媒气液分离不彻底的问题,本申请提供一种气液分离装置100。气液分离装置100设有进流口313、分流腔700、第一气液分离通道110和第二气液分离通道120,分流腔700设有底壁710、第一侧壁720和第二侧壁730,第一侧壁720和第二侧壁730呈锥形夹角设置,以围设形成横截面呈锥形的分流腔700。第一侧壁720远离第二侧壁730的一端连通第一气液分离通道110,第二侧壁730远离第一侧壁720的一端连通第二气液分离通道120,进流口313的进流方向垂直于分流腔700的底壁710,冷媒能够通过进流口313进入分流腔700,且分流腔700内的冷媒能够沿着第一侧壁720进入第一气液分离通道110,以及沿着第二侧壁730进入第二气液分离通道120。Please refer to Figures 1 to 4. In order to solve the problem that the existing gas-liquid mixed refrigerant has a short residence time in the U-shaped tube, resulting in incomplete separation of the refrigerant gas and liquid, the present application provides a gas-liquid separation device 100. The gas-liquid separation device 100 is provided with an inlet 313, a diverter cavity 700, a first gas-liquid separation channel 110 and a second gas-liquid separation channel 120. The diverter cavity 700 is provided with a bottom wall 710, a first side wall 720 and a second side wall 730. The first side wall 720 and the second side wall 730 are arranged at a conical angle to enclose the diverter cavity 700 with a conical cross section. One end of the first side wall 720 away from the second side wall 730 is connected to the first gas-liquid separation channel 110, and one end of the second side wall 730 away from the first side wall 720 is connected to the second gas-liquid separation channel 120. The flow direction of the inlet port 313 is perpendicular to the bottom wall 710 of the diversion chamber 700. The refrigerant can enter the diversion chamber 700 through the inlet port 313, and the refrigerant in the diversion chamber 700 can enter the first gas-liquid separation channel 110 along the first side wall 720, and enter the second gas-liquid separation channel 120 along the second side wall 730.
需要说明的是,锥形夹角设置指的是第一侧壁720和第二侧壁730围设形成一个锥形的夹角,该夹角大于0°且小于180°。It should be noted that the conical angle setting refers to that the first side wall 720 and the second side wall 730 are arranged to form a conical angle, and the angle is greater than 0° and less than 180°.
进一步地,需要说明的是,进流方向指的是气液两相的冷媒的流动方向。Furthermore, it should be noted that the inflow direction refers to the flow direction of the gas-liquid two-phase refrigerant.
通过设置分流腔700,由于进流口313的进流方向垂直于分流腔700的底壁710,因此,气液两相的冷媒从进流口313垂直冲击于分流腔700的底壁710上,之后,冷媒向分流腔700的四周扩散。又由于第一侧壁720和第二侧壁730呈锥形夹角设置,以围设形成横截面呈锥形的分流腔700,因此,冷媒在分流腔700内扩散的过程中会与分流腔700的底壁710、第一侧壁720以及第二侧壁730充分接触,以使液态的冷媒凝结在分流腔700的底壁710、第一侧壁720以及第二侧壁730上。由于第一侧壁720远离第二侧壁730的一端连通第一气液分离通道110,第二侧壁730远离第一侧壁720的一端连通第二气液分离通道120,因此,当气液两相的冷媒充满整个分流腔700时,在气压差的推动下,气液两相的冷媒能够沿着第一侧壁720进入第一气液分离通道 110,以及沿着第二侧壁730进入第二气液分离通道120,如此,进一步增强了液态冷媒在第一侧壁720和第二侧壁730上的凝结效果,进而提高了冷媒的气液分离效果。并且,第一侧壁720和第二侧壁730对冷媒具有一定的导流作用,避免冷媒在分流腔700内产生紊流,如此设置,提高了气液分离装置100的分离效率。By setting the flow diversion chamber 700, since the flow direction of the inlet 313 is perpendicular to the bottom wall 710 of the flow diversion chamber 700, the gas-liquid two-phase refrigerant vertically impacts the bottom wall 710 of the flow diversion chamber 700 from the inlet 313, and then the refrigerant diffuses to the surrounding of the flow diversion chamber 700. In addition, since the first side wall 720 and the second side wall 730 are arranged at a conical angle to enclose the flow diversion chamber 700 with a conical cross section, the refrigerant will fully contact the bottom wall 710, the first side wall 720 and the second side wall 730 of the flow diversion chamber 700 during the diffusion process in the flow diversion chamber 700, so that the liquid refrigerant condenses on the bottom wall 710, the first side wall 720 and the second side wall 730 of the flow diversion chamber 700. Since the end of the first side wall 720 away from the second side wall 730 is connected to the first gas-liquid separation channel 110, and the end of the second side wall 730 away from the first side wall 720 is connected to the second gas-liquid separation channel 120, when the gas-liquid two-phase refrigerant fills the entire diversion cavity 700, the gas-liquid two-phase refrigerant can enter the first gas-liquid separation channel along the first side wall 720 under the promotion of the gas pressure difference. 110, and enter the second gas-liquid separation channel 120 along the second side wall 730, so that the condensation effect of the liquid refrigerant on the first side wall 720 and the second side wall 730 is further enhanced, thereby improving the gas-liquid separation effect of the refrigerant. In addition, the first side wall 720 and the second side wall 730 have a certain flow-guiding effect on the refrigerant, avoiding turbulence of the refrigerant in the diversion cavity 700, so that the separation efficiency of the gas-liquid separation device 100 is improved.
进一步地,在一实施例中,第一侧壁720和第二侧壁730之间的夹角大于或等于45°且小于或等于135°。Further, in one embodiment, the angle between the first side wall 720 and the second side wall 730 is greater than or equal to 45° and less than or equal to 135°.
如此,第一侧壁720和第二侧壁730之间的夹角大于或等于45°,有利于扩大分流腔700的体积,使得分流腔700内能够容纳更多的气液两相的冷媒,第一侧壁720和第二侧壁730之间的夹角小于或等于135°,可避免第一侧壁720和第二侧壁730之间的夹角过大而影响冷媒进入第一气液分离通道110和第二气液分离通道120。In this way, the angle between the first side wall 720 and the second side wall 730 is greater than or equal to 45°, which is conducive to expanding the volume of the diversion chamber 700 so that the diversion chamber 700 can accommodate more gas-liquid two-phase refrigerant. The angle between the first side wall 720 and the second side wall 730 is less than or equal to 135°, which can avoid the angle between the first side wall 720 and the second side wall 730 being too large and affecting the refrigerant entering the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120.
可选地,第一侧壁720和第二侧壁730之间的夹角为90°。Optionally, the included angle between the first side wall 720 and the second side wall 730 is 90°.
在一实施例中,如图4所示,第一侧壁720和第二侧壁730之间设有弧形过渡段740,且进流口313在分流腔700底壁710上正投影的部分外轮廓与弧形过渡段740重合。In one embodiment, as shown in FIG. 4 , an arcuate transition section 740 is provided between the first side wall 720 and the second side wall 730 , and a portion of the outer contour of the inlet 313 projected onto the bottom wall 710 of the diversion cavity 700 coincides with the arcuate transition section 740 .
如此,可使冷媒能够沿着弧形过渡段740平顺地进入第一侧壁720一侧和第二侧壁730一侧,避免气液两相的冷媒在分流腔700内产生紊流,进而提高了气液分离装置100的分流效率。In this way, the refrigerant can smoothly enter the first side wall 720 and the second side wall 730 along the arc transition section 740, avoiding turbulence of the gas-liquid two-phase refrigerant in the diversion chamber 700, thereby improving the diversion efficiency of the gas-liquid separation device 100.
在一实施例中,如图3和图4所示,第一气液分离通道110和第二气液分离通道120中的一者或者两者内均设有一个或多个回流结构200,回流结构200包括沿着第一方向依次分布的第一回流板210和第二回流板220,其中,第一方向为第一气液分离通道110的延伸方向或者第二气液分离通道120的 延伸方向。第一回流板210设有第一通流孔211和第一回流面212,第二回流板220设有第二通流孔221和第二回流面222,第一通流孔211和第二回流面222沿着第一方向对应分布,且第二通流孔221和第一回流面212沿着第一方向对应分布,第二回流面222能够将通过第一通流孔211进入的冷媒回流至第一回流面212,且第一回流面212能够将第二回流面222回流的冷媒回流至第二通流孔221。In one embodiment, as shown in FIGS. 3 and 4 , one or both of the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 are provided with one or more reflux structures 200, and the reflux structure 200 includes a first reflux plate 210 and a second reflux plate 220 sequentially distributed along a first direction, wherein the first direction is an extension direction of the first gas-liquid separation channel 110 or a direction of the second gas-liquid separation channel 120. The first return plate 210 is provided with a first through-hole 211 and a first return surface 212, and the second return plate 220 is provided with a second through-hole 221 and a second return surface 222. The first through-hole 211 and the second return surface 222 are correspondingly distributed along the first direction, and the second through-hole 221 and the first return surface 212 are correspondingly distributed along the first direction, and the second return surface 222 can return the refrigerant entering through the first through-hole 211 to the first return surface 212, and the first return surface 212 can return the refrigerant returned by the second return surface 222 to the second through-hole 221.
需要说明的是,第一方向并不是固定不变的方向,当回流结构200位于第一气液分离通道110时,第一方向为第一气液分离通道110的延伸方向,当回流结构200位于第二气液分离通道120时,第一方向为第二气液分离通道120的延伸方向。进一步地,第一方向可以是沿着某一直线的方向,还可以是沿着某一曲线的方向,还可以是沿着任意形状延伸的特定方向,在此不作一一限定。It should be noted that the first direction is not a fixed direction. When the reflux structure 200 is located in the first gas-liquid separation channel 110, the first direction is the extension direction of the first gas-liquid separation channel 110. When the reflux structure 200 is located in the second gas-liquid separation channel 120, the first direction is the extension direction of the second gas-liquid separation channel 120. Furthermore, the first direction may be a direction along a straight line, a direction along a curve, or a specific direction extending along an arbitrary shape, which is not limited here.
进一步地,需要注意的是,在本实施例中,第一侧壁720和第二侧壁730为不同第一回流板210的侧壁。Further, it should be noted that, in the present embodiment, the first side wall 720 and the second side wall 730 are side walls of different first reflow plates 210 .
由于第一气液分离通道110和第二气液分离通道120内设有一个或多个回流结构200。因此,冷媒在第一气液分离通道110和第二气液分离通道120内流动时,会通过一个或多个回流结构200。Since one or more reflux structures 200 are disposed in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 , the refrigerant will pass through one or more reflux structures 200 when flowing in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 .
进一步地,回流结构200包括沿着第一方向依次分布的第一回流板210和第二回流板220,第一回流板210设有第一通流孔211和第一回流面212,对应地,第二回流板220设有第二通流孔221和第二回流面222。需要注意的是,第一通流孔211和第二回流面222沿着第一方向对应分布,且第二通流孔221和第一回流面212沿着第一方向对应分布,第二回流面222能够将通过第一通流孔211进入的冷媒回流至第二回流面222,且第二回流面222能够 将第一回流面212回流的冷媒回流至第二通流孔221。Further, the reflux structure 200 includes a first reflux plate 210 and a second reflux plate 220 sequentially distributed along the first direction, the first reflux plate 210 is provided with a first through-hole 211 and a first reflux surface 212, and correspondingly, the second reflux plate 220 is provided with a second through-hole 221 and a second reflux surface 222. It should be noted that the first through-hole 211 and the second reflux surface 222 are correspondingly distributed along the first direction, and the second through-hole 221 and the first reflux surface 212 are correspondingly distributed along the first direction, and the second reflux surface 222 can reflux the refrigerant entering through the first through-hole 211 to the second reflux surface 222, and the second reflux surface 222 can The refrigerant returning from the first return surface 212 is returned to the second flow hole 221 .
如此,当冷媒从第一回流板210的第一通流孔211沿着第一方向经过第二回流板220的第二回流面222时,第二回流面222将冷媒回流至第一回流板210的第一回流面212,之后,第一回流面212将冷媒回流至第二回流板220的第二通流孔221,最后,冷媒从第二通流孔221离开回流结构200。通过第一回流板210和第二回流板220的多次回流作用,显著增加了气液两相的冷媒同第一回流板210和第二回流板220的接触面积和接触时间,也即,显著增加了冷媒在第一气液分离通道110和第二气液分离通道120内的停留时间,以及,显著增加了冷媒和气液分离装置100的接触面积,从而有利于液态冷媒吸附于第一回流板210、第二回流板220以及第一气液分离通道110和第二气液分离通道120的内壁上,进而显著提高了气液分离装置100的气液分离效果。In this way, when the refrigerant passes through the second return surface 222 of the second return plate 220 from the first flow hole 211 of the first return plate 210 along the first direction, the second return surface 222 returns the refrigerant to the first return surface 212 of the first return plate 210, and then the first return surface 212 returns the refrigerant to the second flow hole 221 of the second return plate 220, and finally, the refrigerant leaves the return structure 200 from the second flow hole 221. Through the multiple reflux effects of the first reflux plate 210 and the second reflux plate 220, the contact area and contact time of the gas-liquid two-phase refrigerant with the first reflux plate 210 and the second reflux plate 220 are significantly increased, that is, the residence time of the refrigerant in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 is significantly increased, and the contact area between the refrigerant and the gas-liquid separation device 100 is significantly increased, which is conducive to the adsorption of liquid refrigerant on the inner walls of the first reflux plate 210, the second reflux plate 220 and the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120, thereby significantly improving the gas-liquid separation effect of the gas-liquid separation device 100.
并且,相对于相关技术中气液分离装置内的U型管设计,为了实现较好的气液分离效果需要设计长度较长的U型管,本申请通过在第一气液分离通道110和第二气液分离通道120内布置一个或多个回流结构200实现更好的气液分离效果,而不需要通过加长传统的气液分离通道实现更好的气液分离效果。因此,本申请提供的气液分离装置100的体积较小,更容易实现气液分离装置100的安装。Moreover, compared with the U-shaped tube design in the gas-liquid separation device in the related art, in order to achieve a better gas-liquid separation effect, a longer U-shaped tube needs to be designed. In the present application, one or more reflux structures 200 are arranged in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 to achieve a better gas-liquid separation effect, without the need to lengthen the traditional gas-liquid separation channel to achieve a better gas-liquid separation effect. Therefore, the gas-liquid separation device 100 provided in the present application is smaller in size, and it is easier to install the gas-liquid separation device 100.
进一步地,在一实施例中,如图4所示,回流结构200还包括第三回流板230,第一回流板210、第二回流板220和第三回流板230沿着第一方向依次分布,第三回流板230设有第三通流孔231和第三回流面232,第二回流板220背离第二回流面222的一端设有背向回流面223,第三通流孔231和背向回流面223沿着第一方向对应分布,且第三回流面232和第二通流孔221沿 着第一方向对应分布,第三回流面232能够将通过第二通流孔221进入的冷媒回流至背向回流面223,且背向回流面223能够将第三回流面232回流的冷媒回流至第三通流孔231。Further, in one embodiment, as shown in FIG. 4, the reflux structure 200 further includes a third reflux plate 230, the first reflux plate 210, the second reflux plate 220 and the third reflux plate 230 are sequentially distributed along the first direction, the third reflux plate 230 is provided with a third through-flow hole 231 and a third reflux surface 232, the second reflux plate 220 is provided with a back reflux surface 223 at one end away from the second reflux surface 222, the third through-flow hole 231 and the back reflux surface 223 are correspondingly distributed along the first direction, and the third reflux surface 232 and the second through-flow hole 221 are arranged along the first direction. Corresponding to the distribution in the first direction, the third return surface 232 can return the refrigerant entering through the second through-flow hole 221 to the back return surface 223 , and the back return surface 223 can return the refrigerant returning from the third return surface 232 to the third through-flow hole 231 .
如此,当冷媒从第二回流板220的第二通流孔221沿着第一方向经过第三回流板230的第三回流面232时,第三回流面232能够将冷媒回流至第二回流板220的背向回流面223,之后,背向回流面223将冷媒回流至第三回流板230的第三通流孔231,最后,冷媒从第三通流孔231离开回流结构200。通过第一回流板210、第二回流板220和第三回流板230的多次回流作用,显著增加了气液两相的冷媒同第一回流板210、第二回流板220和第三回流板230的接触面积和接触时间,也即,显著增加了冷媒在第一气液分离通道110和第二气液分离通道120内的停留时间,以及,显著增加了冷媒和气液分离装置100的接触面积,从而有利于液态冷媒吸附于第一回流板210、第二回流板220、第三回流板230以及第一气液分离通道110和第二气液分离通道120的内壁上,进而显著提高了气液分离装置100的气液分离效果。In this way, when the refrigerant passes through the third return surface 232 of the third return plate 230 from the second flow hole 221 of the second return plate 220 along the first direction, the third return surface 232 can return the refrigerant to the back return surface 223 of the second return plate 220, and then the back return surface 223 returns the refrigerant to the third flow hole 231 of the third return plate 230, and finally, the refrigerant leaves the return structure 200 from the third flow hole 231. Through the multiple reflux effects of the first reflux plate 210, the second reflux plate 220 and the third reflux plate 230, the contact area and contact time of the gas-liquid two-phase refrigerant with the first reflux plate 210, the second reflux plate 220 and the third reflux plate 230 are significantly increased, that is, the residence time of the refrigerant in the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 is significantly increased, and the contact area between the refrigerant and the gas-liquid separation device 100 is significantly increased, which is conducive to the adsorption of liquid refrigerant on the inner walls of the first reflux plate 210, the second reflux plate 220, the third reflux plate 230 and the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120, thereby significantly improving the gas-liquid separation effect of the gas-liquid separation device 100.
在一实施例中,如图4所示,第一通流孔211的边缘设有朝向第二回流面222延伸的第一导流板240。In one embodiment, as shown in FIG. 4 , a first guide plate 240 extending toward the second return surface 222 is disposed at an edge of the first through hole 211 .
如此,有利于冷媒通过第一导流板240流向第二回流面222。In this way, the refrigerant is facilitated to flow toward the second return surface 222 through the first guide plate 240 .
同样地,在一实施例中,如图4所示,第二通流孔221的边缘设有朝向第三回流面232延伸的第二导流板250。Likewise, in one embodiment, as shown in FIG. 4 , a second guide plate 250 extending toward the third return surface 232 is disposed at an edge of the second through-hole 221 .
如此,有利于冷媒通过第二导流板250流向第三回流面232。In this way, the refrigerant is facilitated to flow to the third return surface 232 through the second guide plate 250 .
更进一步地,在一实施例中,如图4所示,第二导流板250远离第三回流板230的一端朝向靠近第一回流面212的方向延伸。Furthermore, in one embodiment, as shown in FIG. 4 , one end of the second guide plate 250 away from the third return plate 230 extends toward a direction close to the first return surface 212 .
如此,有利于冷媒从第一回流面212通过第二导流板250进入第二通流 孔221,从而进一步增强了第二导流板250的导流效果。In this way, the refrigerant is facilitated to enter the second flow path from the first return surface 212 through the second guide plate 250. The hole 221 further enhances the flow guiding effect of the second guide plate 250.
同样地,在一实施例中,如图4所示,第三通流孔231的边缘设有朝向背向回流面223延伸的第三导流板290。Likewise, in one embodiment, as shown in FIG. 4 , a third guide plate 290 extending toward the back-flow surface 223 is disposed at the edge of the third through-hole 231 .
如此,有利于冷媒通过第三导流板290流向背向回流面223。This is conducive to the refrigerant flowing toward the back-flow surface 223 through the third guide plate 290 .
在一实施例中,如图4所示,第一通流孔211的底部设有竖直设置的第一挡液板260。In one embodiment, as shown in FIG. 4 , a vertically disposed first liquid baffle plate 260 is disposed at the bottom of the first flow hole 211 .
通常,气液两相的冷媒中,液态冷媒由于密度较大通常集中于冷媒的下方,因此,通过在第一通流孔211的底部设置竖直设置的第一挡液板260,有利于增加液态冷媒和第一挡液板260的接触时间,进而有利于提高液态冷媒的分离效果。Usually, in the gas-liquid two-phase refrigerant, the liquid refrigerant is usually concentrated at the bottom of the refrigerant due to its higher density. Therefore, by providing a vertically arranged first liquid baffle plate 260 at the bottom of the first flow hole 211, it is beneficial to increase the contact time between the liquid refrigerant and the first liquid baffle plate 260, thereby helping to improve the separation effect of the liquid refrigerant.
在一实施例中,如图4所示,第二通流孔221的底部设有竖直设置的第二挡液板270。In one embodiment, as shown in FIG. 4 , a second liquid baffle plate 270 is vertically disposed at the bottom of the second through-hole 221 .
通过在第二通流孔221的底部设置竖直设置的第二挡液板270,有利于增加液态冷媒和第二挡液板270的接触时间,进而有利于提高液态冷媒的分离效果。By providing a vertically arranged second liquid baffle plate 270 at the bottom of the second flow hole 221 , it is helpful to increase the contact time between the liquid refrigerant and the second liquid baffle plate 270 , thereby helping to improve the separation effect of the liquid refrigerant.
同样的,在一实施例中,如图4所示,第三通流孔231的底部设有竖直设置的第三挡液板280。Likewise, in one embodiment, as shown in FIG. 4 , a third liquid baffle plate 280 is vertically disposed at the bottom of the third through-hole 231 .
通过在第三通流孔231的底部设置竖直设置的第三挡液板280,有利于增加液态冷媒和第三挡液板280的接触时间,进而有利于提高液态冷媒的分离效果。By providing a vertically arranged third liquid baffle plate 280 at the bottom of the third flow hole 231 , it is helpful to increase the contact time between the liquid refrigerant and the third liquid baffle plate 280 , thereby helping to improve the separation effect of the liquid refrigerant.
在一实施例中,如图2和图3所示,气液分离装置100包括外壳300、隔板400、进流管800以及出气管600,外壳300设有容纳腔310以及分别连通容纳腔310的进流口313和出气口315,进流管800插置于进流口313并连通 进流口313,出气管600一端插置于容纳腔310内,另一端伸出容纳腔310并插置于出气口315,隔板400一端直接或间接连接出气管600的外壁,另一端朝向靠近容纳腔310的侧壁的方向延伸,以将容纳腔310分隔成第一腔311和第二腔312,并且,隔板400设有连通第一腔311和第二腔312的连通口500。In one embodiment, as shown in FIG. 2 and FIG. 3, the gas-liquid separation device 100 includes a housing 300, a partition 400, an inlet pipe 800, and an outlet pipe 600. The housing 300 is provided with a receiving chamber 310 and an inlet port 313 and an outlet port 315 respectively connected to the receiving chamber 310. The inlet pipe 800 is inserted into the inlet port 313 and connected to the outlet port 315. Inlet 313, one end of the air outlet pipe 600 is inserted into the accommodating chamber 310, and the other end extends out of the accommodating chamber 310 and is inserted into the air outlet 315, one end of the partition 400 is directly or indirectly connected to the outer wall of the air outlet pipe 600, and the other end extends toward the direction close to the side wall of the accommodating chamber 310 to separate the accommodating chamber 310 into a first chamber 311 and a second chamber 312, and the partition 400 is provided with a connecting port 500 connecting the first chamber 311 and the second chamber 312.
需要注意的是,回流结构200设于第一腔311。It should be noted that the reflux structure 200 is disposed in the first cavity 311 .
如此,气液两相的冷媒从进流管800通过进流口313进入第一气液分离通道110和第二气液分离通道120,之后,冷媒在回流结构200的作用下发生气液分离,然后,冷媒通过连通口500进入第二腔312,并且,液态的冷媒沉积在第二腔312的底部,气态的冷媒通过出气管600离开第二腔312,从而实现了气液两相的冷媒的气液分离。In this way, the gas-liquid two-phase refrigerant enters the first gas-liquid separation channel 110 and the second gas-liquid separation channel 120 from the inlet pipe 800 through the inlet port 313. After that, the refrigerant undergoes gas-liquid separation under the action of the reflux structure 200. Then, the refrigerant enters the second cavity 312 through the connecting port 500, and the liquid refrigerant is deposited at the bottom of the second cavity 312. The gaseous refrigerant leaves the second cavity 312 through the outlet pipe 600, thereby realizing the gas-liquid separation of the gas-liquid two-phase refrigerant.
进一步地,如图3所示,外壳300包括筒体320和密封盖330,密封盖330密封设置于筒体320的开口处,进流口313和出气口315设于密封盖330,回流结构200和隔板400均设于筒体320内。Further, as shown in FIG. 3 , the housing 300 includes a cylinder 320 and a sealing cover 330 , the sealing cover 330 is sealingly disposed at the opening of the cylinder 320 , the inlet 313 and the outlet 315 are disposed at the sealing cover 330 , and the reflux structure 200 and the partition 400 are both disposed in the cylinder 320 .
进流口313和出气口315设于密封盖330,大大降低了进流管800和外壳300的连接难度,以及降低了出气管600和外壳300的连接难度。The inlet 313 and the outlet 315 are arranged on the sealing cover 330 , which greatly reduces the difficulty of connecting the inlet pipe 800 and the housing 300 , and reduces the difficulty of connecting the outlet pipe 600 and the housing 300 .
在一实施例中,如图2所示,隔板400与容纳腔310内壁之间设有连通第一腔311和第二腔312的出液间隙314。In one embodiment, as shown in FIG. 2 , a liquid outlet gap 314 communicating with the first cavity 311 and the second cavity 312 is provided between the partition plate 400 and the inner wall of the accommodating cavity 310 .
如此,液态的冷媒能够通过出液间隙314从第一腔311进入第二腔312。In this way, the liquid refrigerant can enter the second chamber 312 from the first chamber 311 through the liquid outlet gap 314 .
更进一步地,在一实施例中,隔板400靠近第一腔311的一侧端面从远离出液间隙314的一端至靠近出液间隙314的一端朝向远离第一腔311的方向倾斜设置。Furthermore, in one embodiment, the end surface of one side of the partition 400 close to the first cavity 311 is inclined from an end away from the liquid outlet gap 314 to an end close to the liquid outlet gap 314 toward a direction away from the first cavity 311 .
如此,有利于聚集在隔板400靠近第一腔311的一侧端面上的液态冷媒 汇入出液间隙314,并通过出液间隙314从第一腔311进入第二腔312。This is conducive to the liquid refrigerant gathering on the side end surface of the partition 400 close to the first chamber 311. The liquid flows into the liquid outlet gap 314 , and enters the second chamber 312 from the first chamber 311 through the liquid outlet gap 314 .
以上所述实施例的各技术特征可以进行任意的组合,为使描述简洁,未对上述实施例中的各个技术特征所有可能的组合都进行描述,然而,只要这些技术特征的组合不存在矛盾,都应当认为是本说明书记载的范围。The technical features of the above-described embodiments may be arbitrarily combined. To make the description concise, not all possible combinations of the technical features in the above-described embodiments are described. However, as long as there is no contradiction in the combination of these technical features, they should be considered to be within the scope of this specification.
以上所述实施例仅表达了本申请的几种实施方式,其描述较为具体和详细,但并不能因此而理解为对申请专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本申请构思的前提下,还可以做出若干变形和改进,这些都属于本申请的保护范围。因此,本申请的专利保护范围应以所附权利要求为准。 The above-described embodiments only express several implementation methods of the present application, and the descriptions thereof are relatively specific and detailed, but they cannot be construed as limiting the scope of the patent application. It should be pointed out that, for a person of ordinary skill in the art, several variations and improvements can be made without departing from the concept of the present application, and these all belong to the protection scope of the present application. Therefore, the scope of patent protection of the present application shall be subject to the attached claims.

Claims (11)

  1. 一种气液分离装置,其特征在于,设有进流口、分流腔、第一气液分离通道和第二气液分离通道,所述分流腔设有底壁、第一侧壁和第二侧壁,所述第一侧壁和所述第二侧壁呈锥形夹角设置,以围设形成横截面呈锥形的所述分流腔;所述第一侧壁远离所述第二侧壁的一端连通所述第一气液分离通道,所述第二侧壁远离所述第一侧壁的一端连通所述第二气液分离通道,所述进流口的进流方向垂直于所述分流腔的底壁,冷媒能够通过所述进流口进入所述分流腔,且所述分流腔内的冷媒能够沿着所述第一侧壁进入所述第一气液分离通道,以及沿着所述第二侧壁进入所述第二气液分离通道。A gas-liquid separation device, characterized in that it is provided with an inlet, a diverter chamber, a first gas-liquid separation channel and a second gas-liquid separation channel, the diverter chamber is provided with a bottom wall, a first side wall and a second side wall, the first side wall and the second side wall are arranged at a conical angle to enclose the diverter chamber with a conical cross-section; the end of the first side wall away from the second side wall is connected to the first gas-liquid separation channel, and the end of the second side wall away from the first side wall is connected to the second gas-liquid separation channel, the inlet direction of the inlet is perpendicular to the bottom wall of the diverter chamber, the refrigerant can enter the diverter chamber through the inlet, and the refrigerant in the diverter chamber can enter the first gas-liquid separation channel along the first side wall, and enter the second gas-liquid separation channel along the second side wall.
  2. 根据权利要求1所述的气液分离装置,其中,所述第一侧壁和所述第二侧壁之间的夹角大于或等于45°且小于或等于135°。The gas-liquid separation device according to claim 1, wherein the angle between the first side wall and the second side wall is greater than or equal to 45° and less than or equal to 135°.
  3. 根据权利要求1所述的气液分离装置,其中,所述第一侧壁和所述第二侧壁之间设有弧形过渡段,且所述进流口在所述分流腔底壁上的正投影的部分外轮廓与所述弧形过渡段重合。The gas-liquid separation device according to claim 1, wherein an arc-shaped transition section is provided between the first side wall and the second side wall, and a portion of the outer contour of the positive projection of the inlet on the bottom wall of the diversion chamber coincides with the arc-shaped transition section.
  4. 根据权利要求1所述的气液分离装置,其中,所述气液分离装置包括外壳、隔板、进流管以及出气管,所述外壳设有容纳腔以及分别连通所述容纳腔的所述进流口和出气口,所述进流管插置于所述进流口并连通所述进流口,所述出气管一端插置于所述容纳腔内,另一端伸出所述容纳腔并插置于所述出气口,所述隔板一端直接或间接连接所述出气管的外壁,另一端朝向靠近所述容纳腔侧壁的方向延伸,以将所述容纳腔分隔成第一腔和第二腔,并且,所述隔板设有连通所述第一腔和所述第二腔的连通口。The gas-liquid separation device according to claim 1, wherein the gas-liquid separation device comprises a shell, a partition, an inlet pipe and an outlet pipe, the shell is provided with a accommodating chamber and the inlet and outlet respectively connected to the accommodating chamber, the inlet pipe is inserted into the inlet and connected to the inlet, one end of the outlet pipe is inserted into the accommodating chamber, and the other end extends out of the accommodating chamber and is inserted into the outlet, one end of the partition is directly or indirectly connected to the outer wall of the outlet pipe, and the other end extends toward the direction close to the side wall of the accommodating chamber to separate the accommodating chamber into a first chamber and a second chamber, and the partition is provided with a connecting port connecting the first chamber and the second chamber.
  5. 根据权利要求4所述的气液分离装置,其中,所述外壳包括筒体和密封盖,所述密封盖密封设置于所述筒体的开口处,所述进流口和所述出气口 设于所述密封盖。The gas-liquid separation device according to claim 4, wherein the housing comprises a cylinder and a sealing cover, the sealing cover is sealed at the opening of the cylinder, the inlet and the outlet The sealing cover is provided.
  6. 根据权利要求4所述的气液分离装置,其中,所述隔板与所述容纳腔内壁之间设有连通所述第一腔和所述第二腔的出液间隙。The gas-liquid separation device according to claim 4, wherein a liquid outlet gap connecting the first cavity and the second cavity is provided between the partition plate and the inner wall of the accommodating cavity.
  7. 根据权利要求1所述的气液分离装置,其中,所述第一气液分离通道和所述第二气液分离通道中的一者或者两者内设有一个或多个回流结构,所述回流结构包括沿着第一方向依次分布的第一回流板和第二回流板,其中,第一方向为所述第一气液分离通道的延伸方向或者第一方向为所述第二气液分离通道的延伸方向,所述第一回流板设有第一通流孔和第一回流面,所述第二回流板设有第二通流孔和第二回流面,所述第一通流孔和所述第二回流面沿着第一方向对应分布,且所述第二通流孔和所述第一回流面沿着第一方向对应分布,所述第二回流面能够将通过所述第一通流孔进入的冷媒回流至所述第一回流面,且所述第一回流面能够将所述第二回流面回流的冷媒回流至所述第二通流孔。The gas-liquid separation device according to claim 1, wherein one or both of the first gas-liquid separation channel and the second gas-liquid separation channel are provided with one or more reflux structures, and the reflux structure includes a first reflux plate and a second reflux plate sequentially distributed along a first direction, wherein the first direction is the extension direction of the first gas-liquid separation channel or the first direction is the extension direction of the second gas-liquid separation channel, the first reflux plate is provided with a first through-flow hole and a first reflux surface, the second reflux plate is provided with a second through-flow hole and a second reflux surface, the first through-flow hole and the second reflux surface are correspondingly distributed along the first direction, and the second through-flow hole and the first reflux surface are correspondingly distributed along the first direction, the second reflux surface can reflux the refrigerant entering through the first through-flow hole to the first reflux surface, and the first reflux surface can reflux the refrigerant refluxed from the second reflux surface to the second through-flow hole.
  8. 根据权利要求7所述的气液分离装置,其中,所述回流结构还包括第三回流板,所述第一回流板、所述第二回流板和所述第三回流板沿着第一方向依次分布,所述第三回流板设有第三通流孔和第三回流面,所述第二回流板背离所述第二回流面的一端设有背向回流面,所述第三通流孔和所述背向回流面沿着第一方向对应分布,且所述第三回流面和所述第二通流孔沿着第一方向对应分布,所述第三回流面能够将通过所述第二通流孔进入的冷媒回流至所述背向回流面,且所述背向回流面能够将所述第三回流面回流的冷媒回流至所述第三通流孔。According to the gas-liquid separation device according to claim 7, wherein the reflux structure also includes a third reflux plate, the first reflux plate, the second reflux plate and the third reflux plate are distributed in sequence along the first direction, the third reflux plate is provided with a third through-flow hole and a third reflux surface, the second reflux plate is provided with a back reflux surface at one end away from the second reflux surface, the third through-flow hole and the back reflux surface are correspondingly distributed along the first direction, and the third reflux surface and the second through-flow hole are correspondingly distributed along the first direction, the third reflux surface can reflux the refrigerant entering through the second through-flow hole to the back reflux surface, and the back reflux surface can reflux the refrigerant refluxed from the third reflux surface to the third through-flow hole.
  9. 根据权利要求8所述的气液分离装置,其中,所述第一通流孔的边缘设有朝向所述第二回流面延伸的第一导流板; The gas-liquid separation device according to claim 8, wherein the edge of the first flow hole is provided with a first guide plate extending toward the second return surface;
    及/或,所述第二通流孔的边缘设有朝向所述第三回流面延伸的第二导流板;And/or, a second guide plate extending toward the third return surface is provided at the edge of the second flow hole;
    及/或,所述第三通流孔的边缘设有朝向所述背向回流面延伸的第三导流板。And/or, a third guide plate extending toward the back-flow surface is provided at the edge of the third through-flow hole.
  10. 根据权利要求8所述的气液分离装置,其中,所述第一通流孔的底部设有竖直设置的第一挡液板;The gas-liquid separation device according to claim 8, wherein a first liquid baffle plate is vertically arranged at the bottom of the first flow hole;
    及/或,所述第二通流孔的底部设有竖直设置的第二挡液板;And/or, a second liquid baffle plate is vertically arranged at the bottom of the second flow hole;
    及/或,所述第三通流孔的底部设有竖直设置的第三挡液板。And/or, a third liquid baffle plate is vertically arranged at the bottom of the third flow hole.
  11. 一种新能源汽车空调系统,其特征在于,包括蒸发器、压缩机和如权利要求1-10任一项所述的气液分离装置,所述气液分离装置设置于所述蒸发器和所述压缩机之间,冷媒从所述蒸发器进入所述气液分离装置之后再进入所述压缩机。 A new energy automobile air conditioning system, characterized in that it comprises an evaporator, a compressor and a gas-liquid separation device as described in any one of claims 1 to 10, wherein the gas-liquid separation device is arranged between the evaporator and the compressor, and the refrigerant enters the gas-liquid separation device from the evaporator and then enters the compressor.
PCT/CN2023/080684 2022-09-28 2023-03-10 Gas-liquid separation device and new energy vehicle air-conditioning system WO2024066212A1 (en)

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Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103307821A (en) * 2013-05-21 2013-09-18 浙江盾安冷链系统有限公司 Gas/liquid separator
CN206247720U (en) * 2016-10-20 2017-06-13 广东美的暖通设备有限公司 Gas-liquid separator and air-conditioner
CN112432401A (en) * 2020-02-29 2021-03-02 浙江三花智能控制股份有限公司 Gas-liquid separator
CN112944746A (en) * 2019-12-10 2021-06-11 珠海格力电器股份有限公司 Liquid distributor, falling film type heat exchanger and air conditioner
US20210247114A1 (en) * 2018-08-23 2021-08-12 Zhejiang Sanhua Intelligent Controls Co., Ltd. Gas-liquid separator and air conditioning system
CN113266970A (en) * 2021-05-25 2021-08-17 三花控股集团有限公司 Gas-liquid separator
WO2022017183A1 (en) * 2020-07-20 2022-01-27 约克(无锡)空调冷冻设备有限公司 Gas-liquid separator
CN115540411A (en) * 2022-09-28 2022-12-30 浙江银轮机械股份有限公司 Gas-liquid separator

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103307821A (en) * 2013-05-21 2013-09-18 浙江盾安冷链系统有限公司 Gas/liquid separator
CN206247720U (en) * 2016-10-20 2017-06-13 广东美的暖通设备有限公司 Gas-liquid separator and air-conditioner
US20210247114A1 (en) * 2018-08-23 2021-08-12 Zhejiang Sanhua Intelligent Controls Co., Ltd. Gas-liquid separator and air conditioning system
CN112944746A (en) * 2019-12-10 2021-06-11 珠海格力电器股份有限公司 Liquid distributor, falling film type heat exchanger and air conditioner
CN112432401A (en) * 2020-02-29 2021-03-02 浙江三花智能控制股份有限公司 Gas-liquid separator
WO2022017183A1 (en) * 2020-07-20 2022-01-27 约克(无锡)空调冷冻设备有限公司 Gas-liquid separator
CN113266970A (en) * 2021-05-25 2021-08-17 三花控股集团有限公司 Gas-liquid separator
CN115540411A (en) * 2022-09-28 2022-12-30 浙江银轮机械股份有限公司 Gas-liquid separator

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