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CN116336700A - Condenser with built-in oil separation structure - Google Patents

Condenser with built-in oil separation structure Download PDF

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Publication number
CN116336700A
CN116336700A CN202310330795.1A CN202310330795A CN116336700A CN 116336700 A CN116336700 A CN 116336700A CN 202310330795 A CN202310330795 A CN 202310330795A CN 116336700 A CN116336700 A CN 116336700A
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China
Prior art keywords
separation
oil
chamber
condenser
separation structure
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Pending
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CN202310330795.1A
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Chinese (zh)
Inventor
梅露
苏秀平
马小魁
王利
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York Wuxi Air Conditioning and Refrigeration Co Ltd
Johnson Controls Tyco IP Holdings LLP
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York Wuxi Air Conditioning and Refrigeration Co Ltd
Johnson Controls Tyco IP Holdings LLP
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Application filed by York Wuxi Air Conditioning and Refrigeration Co Ltd, Johnson Controls Tyco IP Holdings LLP filed Critical York Wuxi Air Conditioning and Refrigeration Co Ltd
Priority to CN202310330795.1A priority Critical patent/CN116336700A/en
Publication of CN116336700A publication Critical patent/CN116336700A/en
Priority to PCT/CN2024/085055 priority patent/WO2024199497A1/en
Priority to TW113112178A priority patent/TW202441115A/en
Pending legal-status Critical Current

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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
    • F25B39/00Evaporators; Condensers
    • F25B39/04Condensers
    • 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
    • F25B43/02Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat for separating lubricants from the refrigerant
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/09Improving heat transfers
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/12Sound

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Power Engineering (AREA)
  • Applications Or Details Of Rotary Compressors (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The application provides a condenser with an oil separation structure inside, which comprises a shell and the oil separation structure. The housing includes a length, a width, and a height and defines a cavity, and at least one inlet tube is provided to receive a refrigerant to be condensed containing a lubricant oil. An oil separation structure is secured in the cavity and includes a separation chamber for separating lubricant oil from refrigerant gas in the refrigerant. At least one inlet pipe extends into the separation chamber. The receiving chamber includes first and second condensing chambers separated by an oil separating structure and located at both sides of the separating chamber in a width direction of the housing, respectively, and extending along a length direction of the housing, respectively. The upper part of the oil separating structure is provided with a first and a second exhaust ports which respectively connect the first and the second condensing chambers with the separating chamber in fluid communication so that the refrigerant gas separated by the separating chamber can enter the first and the second condensing chambers to be condensed, and the bottom part of the oil separating structure is provided with at least one oil drain port so that the lubricating oil separated by the separating chamber can be discharged from the separating chamber.

Description

内设油分离结构的冷凝器Condenser with built-in oil separation structure

技术领域technical field

本申请涉及一种冷凝器,尤其是一种内设油分离结构的冷凝器。The present application relates to a condenser, in particular to a condenser with an internal oil separation structure.

背景技术Background technique

制冷空调系统中包括冷凝器,用于将压缩机排出的高温高压气相制冷剂冷凝成中温高压液相制冷剂。在螺杆压缩机中,转子之间需要润滑油以降低压缩机噪音,同时润滑油能够减少转子啮合过程中的气体泄漏,提高压缩机性能。因此,螺杆压缩机实际运行过程中,压缩机排出的气体除气相制冷剂外还包括冷冻油液滴。若较多润滑油进入冷凝器和蒸发器,不仅会造成供油系统缺油增加压缩机运动部件缺油损毁,而且过多的润滑油会以薄膜状态附着在换热管上,造成整个制冷空调系统的换热效果达不到设计状态。因此,需要设置油分离结构将压缩机排出的气相制冷剂及油液进行分离,分离后的油液返回压缩机油箱供压缩机使用。The refrigeration and air-conditioning system includes a condenser, which is used to condense the high-temperature and high-pressure gas-phase refrigerant discharged from the compressor into a medium-temperature and high-pressure liquid-phase refrigerant. In screw compressors, lubricating oil is required between the rotors to reduce compressor noise, while lubricating oil can reduce gas leakage during rotor meshing and improve compressor performance. Therefore, during the actual operation of the screw compressor, the gas discharged from the compressor includes refrigerated oil droplets in addition to the gas-phase refrigerant. If more lubricating oil enters the condenser and evaporator, it will not only cause oil shortage in the oil supply system, increase oil shortage and damage to the moving parts of the compressor, but also excessive lubricating oil will adhere to the heat exchange tube in a thin film state, causing the entire refrigeration and air conditioning The heat transfer effect of the system cannot reach the design state. Therefore, it is necessary to set up an oil separation structure to separate the gas-phase refrigerant and oil discharged from the compressor, and the separated oil is returned to the oil tank of the compressor for use by the compressor.

发明内容Contents of the invention

本申请提供一种包括内置油分离结构的冷凝器。该冷凝器中的内置油分离结构提供优良的油分离,并且该冷凝器提供优良的换热效率。The present application provides a condenser including a built-in oil separation structure. The built-in oil separation structure in the condenser provides excellent oil separation, and the condenser provides excellent heat exchange efficiency.

根据本申请的一个方面,本申请提供一种内设油分离结构的冷凝器,该冷凝器包括壳体和油分离结构。所述壳体限定容腔,所述壳体上设有至少一个入口管,用于接收含有润滑油的待被冷凝的制冷剂,所述壳体包括长度方向、高度方向和宽度方向。所述油分离结构被固定在所述容腔中,所述油分离结构包括分离室,所述至少一个入口管伸入所述分离室,其中,所述分离室被配置为将所述制冷剂中的所述润滑油和制冷剂气体分离开。其中,所述容腔包括由所述油分离结构分隔开的第一冷凝室和第二冷凝室,所述第一冷凝室和所述第二冷凝室在所述壳体的宽度方向上分别位于所述分离室的两侧,并且分别沿所述壳体的长度方向延伸。其中,所述油分离结构的上部设有分别将所述第一冷凝室和所述第二冷凝室与所述分离室流体连通的第一排气口和第二排气口,以使经所述分离室分离的制冷剂气体能够进入所述第一冷凝室和所述第二冷凝室中进行冷凝,并且所述油分离结构的底部设有至少一个排油口,以使经所述分离室分离的润滑油能够排出所述分离室。According to one aspect of the present application, the present application provides a condenser with a built-in oil separation structure, and the condenser includes a shell and an oil separation structure. The casing defines a cavity, and at least one inlet pipe is provided on the casing for receiving the refrigerant to be condensed containing lubricating oil, and the casing includes a length direction, a height direction and a width direction. The oil separation structure is fixed in the cavity, the oil separation structure includes a separation chamber, and the at least one inlet pipe extends into the separation chamber, wherein the separation chamber is configured to transfer the refrigerant The lubricating oil and refrigerant gas are separated. Wherein, the cavity includes a first condensing chamber and a second condensing chamber separated by the oil separation structure, and the first condensing chamber and the second condensing chamber are respectively They are located on both sides of the separation chamber and extend along the length direction of the casing respectively. Wherein, the upper part of the oil separation structure is provided with a first exhaust port and a second exhaust port respectively connecting the first condensing chamber and the second condensing chamber with the separation chamber in fluid communication, so that through the The refrigerant gas separated by the separation chamber can enter the first condensation chamber and the second condensation chamber for condensation, and at least one oil discharge port is provided at the bottom of the oil separation structure so that The separated lubricating oil can exit the separation chamber.

在如上所述的内设油分离结构的冷凝器中,所述分离室在所述壳体的宽度方向上居中布置在所述容腔中。In the above-mentioned condenser with built-in oil separation structure, the separation chamber is centrally arranged in the cavity in the width direction of the housing.

在如上所述的内设油分离结构的冷凝器中,所述油分离结构包括沿所述壳体的长度方向间隔设置在所述分离室中的数个竖向分离板,所述数个竖向分离板各自横向于所述分离室的延伸方向布置。其中,至少一部分所述数个竖向分离板设置为对所述分离室中的上部流体通路进行阻挡,至少另一部分所述数个竖向分离板设置为对所述分离室中的下部流体通路进行阻挡。In the above-mentioned condenser with built-in oil separation structure, the oil separation structure includes several vertical separation plates arranged at intervals in the separation chamber along the length direction of the casing, the several vertical separation plates The separating plates are each arranged transversely to the direction of extension of the separating chamber. Wherein, at least a part of the several vertical separation plates is set to block the upper fluid passage in the separation chamber, and at least another part of the several vertical separation plates is set to block the lower fluid passage in the separation chamber. to block.

在如上所述的内设油分离结构的冷凝器中,在所述第一排气口和所述第二排气口的一侧上,对所述分离室中的上部流体通路进行阻挡的所述至少一部分所述竖向分离板与对所述分离室中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板交替布置。In the condenser with built-in oil separation structure as described above, on one side of the first exhaust port and the second exhaust port, the upper fluid passage in the separation chamber is blocked. Said at least one part of said vertical separation plates is alternately arranged with said at least another part of said vertical separation plates blocking a lower fluid passage in said separation chamber.

在如上所述的内设油分离结构的冷凝器中,所述至少一个入口管在所述壳体的顶部在所述壳体的宽度方向上居中布置。In the condenser with built-in oil separation structure as described above, the at least one inlet pipe is centrally arranged on the top of the casing in the width direction of the casing.

在如上所述的内设油分离结构的冷凝器中,所述至少一个入口管的伸入所述分离室的部分沿所述壳体的高度方向延伸。所述油分离结构还包括位于所述至少一个入口管下方的横向分离板。In the above-mentioned condenser with built-in oil separation structure, the part of the at least one inlet pipe protruding into the separation chamber extends along the height direction of the casing. The oil separation structure also includes a transverse separation plate located below the at least one inlet pipe.

在如上所述的内设油分离结构的冷凝器中,所述至少一个入口管的伸入所述分离室的部分朝向远离所述第一排气口和所述第二排气口的方向弯折成弯管状。In the above-mentioned condenser with built-in oil separation structure, the part of the at least one inlet pipe protruding into the separation chamber is bent toward the direction away from the first exhaust port and the second exhaust port Bend into a tube shape.

在如上所述的内设油分离结构的冷凝器中,所述分离室沿所述壳体的长度方向延伸,所述分离室的平行于所述壳体的高度方向和宽度方向构成的平面的截面大体上呈漏斗形,使得所述分离室具有口部和柄部,所述柄部的宽度尺寸被设计为略大于所述至少一个入口管的直径d。In the above-mentioned condenser with a built-in oil separation structure, the separation chamber extends along the length direction of the casing, and the separation chamber is parallel to the plane formed by the height direction and the width direction of the casing. The cross-section is substantially funnel-shaped such that the separation chamber has a mouth and a shank, the width of which is dimensioned slightly larger than the diameter d of the at least one inlet pipe.

在如上所述的内设油分离结构的冷凝器中,所述油分离结构包括外壳,所述外壳限定所述分离室。所述外壳包括彼此连接的相对的侧壁、相对的端壁以及相对的顶壁和底壁。所述顶壁与所述壳体的顶部内表面抵接,且所述相对的侧壁上部分别设有所述第一排气口和所述第二排气口。对所述分离室中的上部流体通路进行阻挡的所述至少一部分所述竖向分离板自所述顶壁延伸所述分离室的至少部分高度,对所述分离室中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板自所述油分离结构的底部延伸所述分离室的至少部分高度。In the above-mentioned condenser provided with an oil separation structure, the oil separation structure includes a casing, and the casing defines the separation chamber. The housing includes opposing side walls, opposing end walls, and opposing top and bottom walls connected to each other. The top wall abuts against the top inner surface of the housing, and the upper parts of the opposite side walls are respectively provided with the first exhaust port and the second exhaust port. said at least a portion of said vertical separation plate blocking an upper fluid passage in said separation chamber extends at least part of the height of said separation chamber from said top wall, blocking a lower fluid passage in said separation chamber The at least another portion of the vertical separation plate extends from the bottom of the oil separation structure at least part of the height of the separation chamber.

在如上所述的内设油分离结构的冷凝器中,所述油分离结构包括外壳,所述外壳限定所述分离室。所述外壳包括彼此连接的相对的侧壁、相对的端壁以及底壁。所述相对的侧壁和所述相对的端壁的顶部与所述壳体的顶部内表面抵接,且所述相对的侧壁上部分别设有所述第一排气口和所述第二排气口。In the above-mentioned condenser provided with an oil separation structure, the oil separation structure includes a casing, and the casing defines the separation chamber. The housing includes opposite side walls, opposite end walls, and a bottom wall connected to each other. The tops of the opposite side walls and the opposite end walls abut against the top inner surface of the housing, and the upper parts of the opposite side walls are respectively provided with the first exhaust port and the second exhaust port. exhaust vent.

在如上所述的内设油分离结构的冷凝器中,对所述分离室中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板与所述底壁间隔一定距离以限定导油通道。In the condenser with built-in oil separation structure as described above, the at least another part of the vertical separation plate that blocks the lower fluid passage in the separation chamber is spaced from the bottom wall by a certain distance to define a guide. oil channel.

在如上所述的内设油分离结构的冷凝器中,所述油分离结构的所述底壁抵接所述壳体的底部内表面,所述至少一个排油口被设置在所述底壁上。所述冷凝器包括位于所述容腔底部的第一过冷盒和第二过冷盒,所述第一过冷盒和所述第二过冷盒在所述壳体的宽度方向上分别位于所述油分离结构的两侧。In the above-mentioned condenser with built-in oil separation structure, the bottom wall of the oil separation structure abuts against the bottom inner surface of the housing, and the at least one oil discharge port is arranged on the bottom wall superior. The condenser includes a first subcooling box and a second subcooling box located at the bottom of the cavity, and the first subcooling box and the second subcooling box are respectively located in the width direction of the housing Both sides of the oil separation structure.

在如上所述的内设油分离结构的冷凝器中,所述冷凝器包括设置在所述容腔底部的过冷盒,所述油分离结构的所述底壁抵接所述过冷盒。所述油分离结构还包括设置在所述油分离结构底部与所述分离室的底部连通的至少一个储油腔,所述至少一个排油口被设置在相应的所述至少一个储油腔底部。其中,所述至少一个储油腔被容纳在所述第一冷凝室和所述第二冷凝室之一的底部。In the above-mentioned condenser provided with an oil separation structure, the condenser includes a subcooling box arranged at the bottom of the cavity, and the bottom wall of the oil separation structure abuts against the subcooling box. The oil separation structure also includes at least one oil storage chamber arranged at the bottom of the oil separation structure and communicating with the bottom of the separation chamber, and the at least one oil discharge port is arranged at the bottom of the corresponding at least one oil storage chamber . Wherein, the at least one oil storage chamber is accommodated at the bottom of one of the first condensation chamber and the second condensation chamber.

根据本申请的另一个方面,本申请提供一种制冷空调系统,所述制冷空调系统包括根据本申请的内设油分离结构的冷凝器。According to another aspect of the present application, the present application provides a refrigerating and air-conditioning system, the refrigerating and air-conditioning system comprising the condenser with built-in oil separation structure according to the present application.

附图说明Description of drawings

图1a是根据本申请的一个实施例的冷凝器的截面图。Figure 1a is a cross-sectional view of a condenser according to one embodiment of the present application.

图1b是图1a所示的冷凝器沿A-A方向的截面图。Fig. 1b is a cross-sectional view of the condenser shown in Fig. 1a along the direction A-A.

图1c示出图1b所示的冷凝器中的油分离结构的外壳。Fig. 1c shows the shell of the oil separation structure in the condenser shown in Fig. 1b.

图2a是根据本申请的另一个实施例的冷凝器的截面图。Fig. 2a is a cross-sectional view of a condenser according to another embodiment of the present application.

图2b是图2a所示的冷凝器沿B-B方向的截面图。Fig. 2b is a cross-sectional view of the condenser shown in Fig. 2a along the direction B-B.

图3a是根据本申请的又一个实施例的冷凝器的截面图。Fig. 3a is a cross-sectional view of a condenser according to yet another embodiment of the present application.

图3b是图3a所示的冷凝器沿C-C方向的截面图。Fig. 3b is a cross-sectional view of the condenser shown in Fig. 3a along the direction C-C.

具体实施方式Detailed ways

下面将参考构成本说明书一部分的附图对本申请的各种具体实施方式进行描述。应该理解的是,在可能的情况下,本申请中使用的相同或者相类似的附图标记指的是相同的部件。虽然在本申请中使用表示方向的术语,诸如“上、下、左、右、顶、底”等描述本申请的各种示例结构部分和元件,但在此使用这些术语只是为了方便说明的目的,基于附图中显示的示例方位而确定。由于本申请所公开的实施例可以按照不同的方向设置,这些表示方向的术语只是作为说明而不应视作为限制。Various embodiments of the present application will be described below with reference to the accompanying drawings, which form a part hereof. It should be understood that, where possible, the same or similar reference numerals used in this application refer to the same components. Although directional terms, such as "up, down, left, right, top, bottom," etc., are used throughout this application to describe various example structural parts and elements of this application, these terms are used herein for convenience of description only. , determined based on the example orientations shown in the accompanying drawings. Since the embodiments disclosed in this application can be arranged in different orientations, these directional terms are for illustration only and should not be regarded as limiting.

图1a-图1c示出根据本申请的一个实施例的冷凝器10a。图1a是根据本申请的一个实施例的冷凝器10a的截面图。图1b是图1a所示的冷凝器10a沿A-A方向的截面图。图1c示出图1b所示的冷凝器10a中的油分离结构201a的外壳202a。Figures 1a-1c illustrate a condenser 10a according to an embodiment of the present application. Figure 1a is a cross-sectional view of a condenser 10a according to one embodiment of the present application. Fig. 1b is a cross-sectional view of the condenser 10a shown in Fig. 1a along the direction A-A. Fig. 1c shows the shell 202a of the oil separation structure 201a in the condenser 10a shown in Fig. 1b.

如图1a和图1b所示,冷凝器10a包括壳体101,壳体101包括如图1a中所示长度方向、宽度方向和高度方向。壳体101限定容腔102,油分离结构201a被固定在容腔102中,且沿壳体101的长度方向延伸。在图1a中,油分离结构201a延伸所述容腔102的长度。油分离结构201a包括分离室203a。As shown in Figures 1a and 1b, the condenser 10a includes a housing 101 including a length direction, a width direction and a height direction as shown in Figure 1a. The casing 101 defines a cavity 102 , and the oil separation structure 201 a is fixed in the cavity 102 and extends along the length direction of the casing 101 . In FIG. 1 a , the oil separation structure 201 a extends the length of the cavity 102 . The oil separation structure 201a includes a separation chamber 203a.

如图1b所示,容腔102包括由油分离结构201a分隔开的第一冷凝室104a和第二冷凝室105a,第一冷凝室104a和第二冷凝室105a在壳体101的宽度方向上分别位于分离室203a的两侧,且分别延伸容腔102的长度。第一冷凝室104a和第二冷凝室105a中分别设有数个冷凝管106用于接收冷却流体。如下文中将详细讨论的,自分离室203a进入第一冷凝室104a和第二冷凝室105a的制冷剂气体同冷凝管106中的冷却流体热交换,从而制冷剂气体被冷却成液态制冷剂。在图1b所示的实施例中,分离室203a在壳体101的宽度方向上居中布置在容腔102中。在一些实施例中,分离室203a在壳体101的宽度方向上非居中布置在容腔102中。As shown in FIG. 1b, the cavity 102 includes a first condensation chamber 104a and a second condensation chamber 105a separated by an oil separation structure 201a, and the first condensation chamber 104a and the second condensation chamber 105a are located in the width direction of the housing 101 They are respectively located on two sides of the separation chamber 203a, and extend the length of the cavity 102 respectively. A plurality of condensation pipes 106 are respectively provided in the first condensation chamber 104a and the second condensation chamber 105a for receiving cooling fluid. As will be discussed in detail below, the refrigerant gas entering the first condensation chamber 104a and the second condensation chamber 105a from the separation chamber 203a exchanges heat with the cooling fluid in the condensation pipe 106, so that the refrigerant gas is cooled into liquid refrigerant. In the embodiment shown in FIG. 1 b , the separation chamber 203 a is centrally arranged in the cavity 102 in the width direction of the housing 101 . In some embodiments, the separation chamber 203 a is arranged non-centrally in the cavity 102 in the width direction of the housing 101 .

容腔102中还设有过冷盒107.1和107.2,用于将经冷凝管106中的冷却流体冷却的制冷剂进一步冷却。完成冷却的制冷剂被送往制冷空调系统的节流阀。过冷盒107.1和107.2位于油分离结构201a的两侧,被分别容纳于第一冷凝室104a和第二冷凝室105a下部。这种分体式过冷盒的构造使得油分离结构201a与冷凝器10a的壳体101的底部内表面抵接(下文中将详细描述),从而分离室203a延伸壳体101的整个高度。这使得能够为进入分离室203a的制冷剂提供最大的飞行高度,从而增加制冷剂在分离室203a中的飞行时间,以提高重力分离效果,从而有利于润滑油的充分分离。这也使得允许将分离室203a设计为具有更小的宽度,使得两个冷凝室(第一冷凝室104a和第二冷凝室105a)具有更大的空间,以布置更多冷凝管106,从而提供冷凝器10a的换热能力。The chamber 102 is also provided with subcooling boxes 107.1 and 107.2 for further cooling the refrigerant cooled by the cooling fluid in the condensation pipe 106. The cooled refrigerant is sent to the throttle valve of the refrigeration and air conditioning system. The subcooling boxes 107.1 and 107.2 are located on both sides of the oil separation structure 201a, and are accommodated in the lower part of the first condensation chamber 104a and the second condensation chamber 105a respectively. The structure of the split subcooling box makes the oil separation structure 201a abut against the bottom inner surface of the shell 101 of the condenser 10a (described in detail below), so that the separation chamber 203a extends the entire height of the shell 101 . This makes it possible to provide the maximum flight height for the refrigerant entering the separation chamber 203a, thereby increasing the flight time of the refrigerant in the separation chamber 203a to improve the gravity separation effect, thereby facilitating sufficient separation of lubricating oil. This also allows the separation chamber 203a to be designed with a smaller width, so that the two condensation chambers (the first condensation chamber 104a and the second condensation chamber 105a) have more space to arrange more condensation pipes 106, thereby providing The heat exchange capacity of the condenser 10a.

壳体101在靠近壳体101两端的位置设有连通压缩机(图中未示出)的两个入口管301a,用于从压缩机接收含有液态润滑油的待被冷凝的制冷剂(下称“制冷剂”)。入口管301a伸入分离室203a中,从而将从压缩机接收的制冷剂送入分离室203a中,以在分离室203a中将制冷剂中的液态润滑油和制冷剂气体分离开。如图1a所示,入口管301a伸入分离室203a中的部分被弯折成弯管状,使得入口管301a的出口303a分别朝向油分离结构201a的两端。在一些实施例中,如图1b所示,两个入口管301a都在壳体101的宽度方向上在壳体101的顶部居中布置。在一些实施例中,入口管301a也可以在壳体101的宽度方向上在壳体101的顶部非居中布置。尽管图1a中示出入口管的数量是两个,应当理解,在其它实施例中,可以设置不同数量的入口管301a。作为一个示例,入口管301a的数量是一个。The casing 101 is provided with two inlet pipes 301a connected to the compressor (not shown in the figure) near both ends of the casing 101, for receiving the refrigerant to be condensed containing liquid lubricating oil from the compressor (hereinafter referred to as "Refrigerant"). The inlet pipe 301a protrudes into the separation chamber 203a so as to send refrigerant received from the compressor into the separation chamber 203a to separate liquid lubricating oil and refrigerant gas in the refrigerant in the separation chamber 203a. As shown in FIG. 1a, the part of the inlet pipe 301a protruding into the separation chamber 203a is bent into an elbow shape, so that the outlets 303a of the inlet pipe 301a are respectively facing the two ends of the oil separation structure 201a. In some embodiments, as shown in FIG. 1 b , both inlet pipes 301 a are centrally arranged on the top of the housing 101 in the width direction of the housing 101 . In some embodiments, the inlet pipe 301 a may also be arranged non-centered on the top of the housing 101 in the width direction of the housing 101 . Although the number of inlet pipes 301a is shown as two in FIG. 1a, it should be understood that in other embodiments, a different number of inlet pipes 301a may be provided. As an example, the number of inlet pipes 301a is one.

结合图1a-图1c描述油分离结构201a的结构。如图1a-图1c所示,油分离结构201a包括外壳202a,外壳202a限定分离室203a。外壳202a包括相对的侧壁204和205、相对的端壁206和207、以及相对的顶壁208和底壁209a,侧壁204和205、端壁206和207、以及顶壁208和底壁209a彼此连接形成外壳202a。The structure of the oil separation structure 201a is described with reference to FIGS. 1a-1c. As shown in Figures 1a-1c, the oil separation structure 201a includes a housing 202a defining a separation chamber 203a. Housing 202a includes opposed side walls 204 and 205, opposed end walls 206 and 207, and opposed top and bottom walls 208 and 209a, side walls 204 and 205, end walls 206 and 207, and top and bottom walls 208 and 209a They are connected to each other to form the housing 202a.

如图1a和1b所示,相对的侧壁204和205的上部分别设有第一排气口210.1和第二排气口210.2。第一排气口210.1与第一冷凝室104a连通,第二排气口210.2与第二冷凝室105a连通,从而经分离室203a分离得到的制冷剂气体通过第一排气口210.1和第二排气口210.2分别进入第一冷凝室104a和第二冷凝室105a中进行冷凝。两个入口管301a被远离第一排气口210.1和第二排气口210.2弯折,从而两个入口管301a的出口303a分别朝向油分离结构201a的端壁206和207中相应的一个。在图1a-图1c的实施例中,第一排气口210.1和第二排气口210.2相对设置在相对的侧壁204和205的上部中间。在仅设置一个入口管301a的一些实施例中,入口管301a设置为靠近其出口303a朝向的端壁206或207,而第一排气口210.1和第二排气口210.2相对设置在相对的侧壁204和205的上部靠近端壁206和207中的另一个处,以使得入口管301a的出口303a尽量远离第一排气口210.1和第二排气口210.2,从而制冷剂在分离室203a中有充分的飞行距离来实现对润滑油的分离。As shown in Figures 1a and 1b, the upper portions of the opposite side walls 204 and 205 are respectively provided with a first exhaust port 210.1 and a second exhaust port 210.2. The first exhaust port 210.1 communicates with the first condensing chamber 104a, and the second exhaust port 210.2 communicates with the second condensing chamber 105a, so that the refrigerant gas separated by the separation chamber 203a passes through the first exhaust port 210.1 and the second row The air port 210.2 respectively enters the first condensation chamber 104a and the second condensation chamber 105a for condensation. The two inlet pipes 301a are bent away from the first exhaust port 210.1 and the second exhaust port 210.2 so that the outlets 303a of the two inlet pipes 301a are respectively facing a corresponding one of the end walls 206 and 207 of the oil separation structure 201a. In the embodiment shown in Figs. 1a-1c, the first exhaust port 210.1 and the second exhaust port 210.2 are oppositely arranged in the upper middle of the opposite side walls 204 and 205. In some embodiments where only one inlet pipe 301a is provided, the inlet pipe 301a is arranged close to the end wall 206 or 207 towards which its outlet 303a faces, while the first exhaust port 210.1 and the second exhaust port 210.2 are oppositely arranged on opposite sides The upper part of the walls 204 and 205 is close to the other of the end walls 206 and 207, so that the outlet 303a of the inlet pipe 301a is as far away as possible from the first exhaust port 210.1 and the second exhaust port 210.2, so that the refrigerant in the separation chamber 203a There is sufficient flight distance to realize the separation of lubricating oil.

图1c示出,底壁209a上设有排油口214a。尽管图中未示出,应当理解的是,冷凝器10a的壳体101的相应位置具有与排油口214a相应的出口,使得经分离室203a分离的润滑油能够经排油口214a排出。在不同的实施例中,排油口214a的数量可以是不同的,作为示例,排油口214a的数量可以是一个、二个或更多个。As shown in Fig. 1c, an oil discharge port 214a is provided on the bottom wall 209a. Although not shown in the figure, it should be understood that the corresponding position of the shell 101 of the condenser 10a has an outlet corresponding to the oil discharge port 214a, so that the lubricating oil separated by the separation chamber 203a can be discharged through the oil discharge port 214a. In different embodiments, the number of oil discharge ports 214a may be different. As an example, the number of oil discharge ports 214a may be one, two or more.

如图1b和图1c所示,分离室203a的平行于壳体101的高度和宽度构成的平面的截面大体上呈漏斗形,使得分离室203a具有口部221a和柄部222a。柄部222a的宽度尺寸W1被设计为略大于入口管301a的直径d,这在有利于制冷剂进入分离室203a的同时使得柄部222a具有尽可能小的宽度。柄部222a的尽可能小的宽度使得制冷剂在柄部222a中的流动速度快,有利于润滑油的撞击分离和离心分离(下文中将详细讨论)。柄部222a的小的宽度也使得容腔102能够提供更多空间用于冷凝。如图1b所示,由于柄部222a可以具有很小的宽度,容腔102的大部分空间被第一冷凝室104a和第二冷凝室105a占据,从而,能够在第一冷凝室104a和第二冷凝室105a中设置很多冷凝管,以提高冷凝器10a的换热能力。口部221a自柄部222a向上逐渐张开,从而具有自柄部222a向上逐渐增加的宽度。这使得制冷剂在口部221a中流速减小,从而增加制冷剂在分离室203a中的飞行时间,提高重力分离效果,有利于润滑油的充分分离。如图1a和图1b所示,口部221a中在第一排气口210.1和第二排气口210.2所在位置的下方设有过滤网241,以在制冷剂离开分离室203a进入第一冷凝室104a和第二冷凝室105a之前,进一步分离制冷剂中的润滑油。口部221a自柄部222a向上逐渐张开的设计使得制冷剂在通过过滤网241时流速减小,使得过滤网241更好地对制冷剂中的润滑油完成捕捉分离。在一些实施例中,口部221a中不设过滤网241。As shown in Figures 1b and 1c, the section of the separation chamber 203a parallel to the plane formed by the height and width of the housing 101 is generally funnel-shaped such that the separation chamber 203a has a mouth 221a and a handle 222a. The width dimension W1 of the shank 222a is designed to be slightly larger than the diameter d of the inlet pipe 301a, which makes the shank 222a have as small a width as possible while facilitating the refrigerant to enter the separation chamber 203a. The as small a width as possible of the handle 222a makes the flow speed of the refrigerant in the handle 222a fast, which is beneficial to the impingement separation and centrifugal separation of lubricating oil (discussed in detail below). The small width of the handle 222a also enables the cavity 102 to provide more space for condensation. As shown in Figure 1b, since the handle 222a can have a very small width, most of the space of the cavity 102 is occupied by the first condensation chamber 104a and the second condensation chamber 105a, thus, the first condensation chamber 104a and the second condensation chamber can be Many condensation pipes are arranged in the condensation chamber 105a to improve the heat exchange capacity of the condenser 10a. The mouth portion 221a gradually expands upward from the handle portion 222a, so as to have a width gradually increasing upward from the handle portion 222a. This reduces the flow velocity of the refrigerant in the mouth portion 221a, thereby increasing the flight time of the refrigerant in the separation chamber 203a, improving the gravity separation effect, and facilitating the sufficient separation of lubricating oil. As shown in Figure 1a and Figure 1b, a filter screen 241 is provided below the positions of the first exhaust port 210.1 and the second exhaust port 210.2 in the port 221a, so that when the refrigerant leaves the separation chamber 203a and enters the first condensation chamber 104a and before the second condensing chamber 105a, the lubricating oil in the refrigerant is further separated. The mouth portion 221a is gradually opened upward from the handle portion 222a to reduce the flow velocity of the refrigerant when passing through the filter 241 , so that the filter 241 can better capture and separate the lubricating oil in the refrigerant. In some embodiments, the filter 241 is not provided in the mouth portion 221a.

如图1a和1b所示,油分离结构201a的底壁209a抵接壳体101的底部内表面,且顶壁208抵接壳体101的顶部内表面,从而油分离结构201a被固定在容腔102中。油分离结构201a的结构使得油分离结构201a容易制造且能够方便地固定到容腔102中。在一些实施方式中,通过弯折和/或连接合适的材料以获得油分离结构201a。制造得到的油分离结构201a被推入冷凝器10a的容腔102中抵接冷凝器10a的壳体101的底部和顶部内表面而容易地固定在容腔102中。在一些实施例中,油分离结构201a被构造为不具有顶壁208,在这种实施例中,油分离结构201a的侧壁204和205及端壁206和207被直接连接到壳体101的顶部内表面。As shown in Figures 1a and 1b, the bottom wall 209a of the oil separation structure 201a abuts against the bottom inner surface of the housing 101, and the top wall 208 abuts against the top inner surface of the housing 101, so that the oil separation structure 201a is fixed in the cavity 102 in. The structure of the oil separation structure 201 a makes the oil separation structure 201 a easy to manufacture and can be conveniently fixed in the cavity 102 . In some embodiments, the oil separation structure 201a is obtained by bending and/or connecting suitable materials. The manufactured oil separation structure 201a is pushed into the cavity 102 of the condenser 10a to abut against the bottom and top inner surfaces of the shell 101 of the condenser 10a to be easily fixed in the cavity 102 . In some embodiments, the oil separation structure 201a is configured without the top wall 208, in which case the side walls 204 and 205 and the end walls 206 and 207 of the oil separation structure 201a are directly connected to the housing 101. top inner surface.

分离室203a中设置竖向分离板211和212对制冷剂在分离室203a中的流动形成阻挡,从而有利于分离制冷剂中的润滑油。结合图1a和图1b说明竖向分离板211和212的设置。竖向分离板211和212各自横向于分离室203a的延伸方向布置,且分别抵接油分离结构201a的相对的侧壁204和205。竖向分离板211自油分离结构201a的顶壁208向下延伸分离室203a的部分高度,用于对分离室203a中的上部流体通路进行阻挡。竖向分离板212自油分离结构201a的底部向上延伸分离室203a的部分高度,对分离室203a中的下部流体通路进行阻挡。如图1a所示,在第一排气口210.1和第二排气口210.2所在位置一侧的竖向分离板211和212在壳体101的长度方向上交替布置。竖向分离板211和212在壳体101的长度方向上的距离及竖向分离板211与油分离结构201a的端壁206或207的距离被设计为使得能够获得符合要求的油分离效果。在一些实施例中,竖向分离板211和竖向分离板212的高度之和小于分离室203a的高度。在另一些实施例中,竖向分离板211和竖向分离板212的高度之和等于分离室203a的高度。在又一些实施例中,竖向分离板211和竖向分离板212的高度之和大于分离室203a的高度。Vertical separation plates 211 and 212 are arranged in the separation chamber 203a to block the flow of the refrigerant in the separation chamber 203a, thereby facilitating the separation of lubricating oil in the refrigerant. The arrangement of the vertical separation plates 211 and 212 is explained with reference to FIGS. 1a and 1b. The vertical separation plates 211 and 212 are each arranged transversely to the extension direction of the separation chamber 203a, and respectively abut against the opposite side walls 204 and 205 of the oil separation structure 201a. The vertical separation plate 211 extends downward from the top wall 208 of the oil separation structure 201a by part of the height of the separation chamber 203a for blocking the upper fluid passage in the separation chamber 203a. The vertical separation plate 212 extends upwards from the bottom of the oil separation structure 201a for part of the height of the separation chamber 203a, blocking the lower fluid passage in the separation chamber 203a. As shown in FIG. 1 a , the vertical separation plates 211 and 212 on the side where the first exhaust port 210 . 1 and the second exhaust port 210 . The distance between the vertical separation plates 211 and 212 in the length direction of the housing 101 and the distance between the vertical separation plate 211 and the end wall 206 or 207 of the oil separation structure 201a is designed such that a satisfactory oil separation effect can be obtained. In some embodiments, the sum of the heights of the vertical separation plate 211 and the vertical separation plate 212 is smaller than the height of the separation chamber 203a. In other embodiments, the sum of the heights of the vertical separation plate 211 and the vertical separation plate 212 is equal to the height of the separation chamber 203a. In some other embodiments, the sum of the heights of the vertical separation plate 211 and the vertical separation plate 212 is greater than the height of the separation chamber 203a.

如图1b中示出的,在图1a-图1c的实施例中,竖向分离板212与油分离结构201a的底壁209a之间间隔一定距离,从而在竖向分离板212与油分离结构201a的底壁209a之间限定导油通道219a,导油通道219a连通排油口214a。在分离室203a中分离得到的润滑油低落到导油通道219a中并流动到达排油口214a,以经排油口214a流出返回压缩机。导油通道219a使得油分离结构201a的底壁209a上可以仅设置一个排油口214a。在一些实施例中,竖向分离板212从油分离结构201a的底壁209a向上延伸而使得没有导油通道219a。如此,在这些实施例中,油分离结构201a的底壁209a上设置多个排油口214a,分别分布在竖向分离板212之间及竖向分离板212与油分离结构201a的端壁206或207之间。As shown in Figure 1b, in the embodiment of Figures 1a-1c, the vertical separation plate 212 is spaced from the bottom wall 209a of the oil separation structure 201a by a certain distance, so that An oil guide channel 219a is defined between the bottom walls 209a of the 201a, and the oil guide channel 219a communicates with the oil discharge port 214a. Lubricating oil separated in the separation chamber 203a falls into the oil guide passage 219a and flows to the oil discharge port 214a to flow out and return to the compressor through the oil discharge port 214a. The oil guide channel 219a enables only one oil discharge port 214a to be provided on the bottom wall 209a of the oil separation structure 201a. In some embodiments, the vertical separation plate 212 extends upward from the bottom wall 209a of the oil separation structure 201a such that there is no oil guiding channel 219a. Thus, in these embodiments, the bottom wall 209a of the oil separation structure 201a is provided with a plurality of oil discharge ports 214a, respectively distributed between the vertical separation plates 212 and the vertical separation plate 212 and the end wall 206 of the oil separation structure 201a or between 207.

如图1a所示,在图1a-图1c的实施例中,在第一排气口210.1和第二排气口210.2所在位置的一侧分别设置一个竖向分离板211和一个竖向分离板212。竖向分离板211靠近入口管301a,且位于入口管301a的与出口303a相反的一侧。竖向分离板212在壳体101的长度方向上位于竖向分离板211及第一排气口210.1和第二排气口210.2的所在位置之间。在其它实施例中,分离室203a中设置不同数量的竖向分离板211和212。As shown in Figure 1a, in the embodiment of Figures 1a-1c, a vertical separation plate 211 and a vertical separation plate are respectively provided on one side of the position of the first exhaust port 210.1 and the second exhaust port 210.2 212. The vertical separation plate 211 is close to the inlet pipe 301a and is located on the opposite side of the inlet pipe 301a from the outlet 303a. The vertical separation plate 212 is located between the vertical separation plate 211 and the positions of the first exhaust port 210.1 and the second exhaust port 210.2 in the length direction of the housing 101. In other embodiments, different numbers of vertical separation plates 211 and 212 are provided in the separation chamber 203a.

下面结合图1a说明从位于图1a所示的右侧的入口管301a进入油分离室203a中的制冷剂中分离润滑油和制冷剂气体的过程。应当理解,从位于图1a中左侧的入口管301a进入分离室203a中的制冷剂中分离润滑油和制冷剂气体的过程是类似的。The process of separating lubricating oil and refrigerant gas from the refrigerant entering the oil separation chamber 203a through the inlet pipe 301a on the right side shown in FIG. 1a will be described below with reference to FIG. 1a. It should be understood that the process of separating lubricating oil and refrigerant gas from the refrigerant entering the separation chamber 203a from the inlet pipe 301a located on the left side in FIG. 1a is similar.

如图1a所示,制冷剂从入口管301a的出口303a排出后朝向油分离结构201a的端壁207流动并撞击端壁207。通过撞击,制冷剂中的部分润滑油被分离,被分离的润滑油滴落到分离室203a底部的导油通道219a中,其余的制冷剂作为第一撞击分离后制冷剂在撞击端壁207后折返,且第一撞击分离后制冷剂中的一部分朝向竖向分离板211流动,一部分朝向竖向分离板212流动。朝向竖向分离板211流动的部分第一撞击分离后制冷剂撞击竖向分离板211,该撞击使得这部分第一撞击分离后制冷剂中的部分润滑油被分离并滴落到导油通道219a中,其余的制冷剂作为第二撞击分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动。由于第二撞击分离后制冷剂的流动受到竖向分离板211的阻挡,第二撞击分离后制冷剂改变流动方向以绕开竖向分离板211的阻挡,这种运动方向的改变使得第二撞击分离后制冷剂产生围绕竖向分离板211的旋转,旋转产生的离心力进一步使得第二撞击分离后制冷剂中的润滑油被离心分离,从而滴落至导油通道219a中,其余的制冷剂作为第一离心分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动,并经第一排气口210.1和第二排气口210.2分别进入第一冷凝室104a和第二冷凝室105a。朝向竖向分离板212流动的部分第一撞击分离后制冷剂撞击竖向分离板212,该撞击使得这部分第一撞击分离后制冷剂中的部分润滑油被分离并滴落到导油通道219a中,其余的制冷剂作为第三撞击分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动。由于第三撞击分离后制冷剂的流动受到竖向分离板212的阻挡,第三撞击分离后制冷剂改变流动方向以绕开竖向分离板212的阻挡,这种运动方向的改变使得第三撞击分离后制冷剂在流动时发生围绕竖向分离板212的旋转,旋转产生的离心力进一步使得第三撞击分离后制冷剂中的润滑油被离心分离,从而滴落至导油通道219a中,其余制冷剂作为第二离心分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动,并经第一排气口210.1和第二排气口210.2分别进入第一冷凝室104a和第二冷凝室105a。另外,由于根据本申请的分离室203a为制冷剂提供足够的飞行高度,在制冷剂从入口管301a的出口303a进入分离室203a至离开分离室203a的飞行过程中,制冷剂中的润滑油还基于重力而和制冷剂气体发生分离,重力分离后的润滑油也低落至导油通道219a。滴落至导油通道219a中的润滑油经排油口214a被排出以返回压缩机。在一些实施例中,当第一排气口210.1和第二排气口210.2两侧的竖向分离板211距离较近时,抵达第一排气口210.1和第二排气口210.2下方的制冷剂在两个竖向分离板211之间产生旋涡,旋涡产生的离心力进一步使得部分润滑油被分离并低落至导油通道219a中。如上所描述的,在分离室203a中,制冷剂中的润滑油和制冷剂气体发生撞击分离、离心分离和重力分离。同时存在这样的多种分离方式使得本申请为制冷剂提供充分的油分离。As shown in FIG. 1 a , the refrigerant flows toward and hits the end wall 207 of the oil separation structure 201 a after being discharged from the outlet 303 a of the inlet pipe 301 a. Through the impact, part of the lubricating oil in the refrigerant is separated, and the separated lubricating oil drops into the oil guide channel 219a at the bottom of the separation chamber 203a, and the rest of the refrigerant is separated as the first impact after the refrigerant hits the end wall 207 Turn back, and after the first collision and separation, part of the refrigerant flows toward the vertical separation plate 211 , and part of the refrigerant flows toward the vertical separation plate 212 . Part of the refrigerant after the first impact separation flowing toward the vertical separation plate 211 hits the vertical separation plate 211, and the impact causes part of the lubricating oil in this part of the refrigerant after the first impact separation to be separated and drop to the oil guide channel 219a. In this process, the rest of the refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2 as the refrigerant after the second impact separation. Since the flow of the refrigerant after the second impact separation is blocked by the vertical separation plate 211, the refrigerant changes the flow direction after the second impact separation to bypass the obstruction of the vertical separation plate 211. This change of the movement direction makes the second impact After separation, the refrigerant rotates around the vertical separation plate 211, and the centrifugal force generated by the rotation further makes the lubricating oil in the refrigerant after the second impact separation is centrifugally separated, thereby dripping into the oil guide channel 219a, and the rest of the refrigerant is used as After the first centrifugal separation, the refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2, and enters the first condensation chamber 104a and the second condensation chamber through the first exhaust port 210.1 and the second exhaust port 210.2 respectively. Chamber 105a. Part of the first-impact-separated refrigerant flowing toward the vertical separation plate 212 hits the vertical separation plate 212, and the impact causes part of the lubricating oil in this part of the first-impact-separated refrigerant to be separated and drop to the oil guide channel 219a. , the rest of the refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2 after the third collision separation. Since the flow of the refrigerant after the third impact separation is blocked by the vertical separation plate 212, the refrigerant changes the flow direction after the third impact separation to bypass the obstruction of the vertical separation plate 212, and this change of the movement direction makes the third impact The separated refrigerant rotates around the vertical separation plate 212 when it flows, and the centrifugal force generated by the rotation further makes the lubricating oil in the third impact separated refrigerant be centrifugally separated, thereby dripping into the oil guide channel 219a, and the rest of the refrigeration After the second centrifugal separation, the refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2, and enters the first condensation chamber 104a and the second exhaust port 210.2 through the first exhaust port 210.1 and the second exhaust port 210.2 respectively. Two condensation chambers 105a. In addition, since the separation chamber 203a according to the present application provides enough flight height for the refrigerant, the lubricating oil in the refrigerant will still The lubricating oil separated from the refrigerant gas by gravity also falls to the oil guide passage 219a. Lubricating oil dropped into the oil guide passage 219a is discharged through the oil discharge port 214a to return to the compressor. In some embodiments, when the distance between the vertical separation plates 211 on both sides of the first exhaust port 210.1 and the second exhaust port 210.2 is relatively close, the refrigerant that reaches the bottom of the first exhaust port 210.1 and the second exhaust port 210.2 The lubricant generates a vortex between the two vertical separation plates 211, and the centrifugal force generated by the vortex further causes part of the lubricating oil to be separated and drop into the oil guide channel 219a. As described above, in the separation chamber 203a, the lubricating oil in the refrigerant and the refrigerant gas undergo collision separation, centrifugal separation, and gravity separation. At the same time, there are multiple separation methods so that the present application provides sufficient oil separation for the refrigerant.

图2a-图2b示出根据本申请的另一个实施例的冷凝器10b。图2a是根据本申请的另一个实施例的冷凝器10b的截面图。图2b是图2a所示的冷凝器10b沿B-B方向的截面图。Figures 2a-2b illustrate a condenser 10b according to another embodiment of the present application. Fig. 2a is a cross-sectional view of a condenser 10b according to another embodiment of the present application. Fig. 2b is a cross-sectional view of the condenser 10b shown in Fig. 2a along the direction B-B.

图2a-图2b所示实施例的冷凝器10b和图1a-图1c所示实施例的冷凝器10a类似,不同之处在于油分离结构构造的改变及由此带来的第一冷凝室和第二冷凝室的变化、以及竖向分离板的不同设置。出于使得描述简洁的目的,下面只描述冷凝器10b与冷凝器10a的不同之处。The condenser 10b of the embodiment shown in Figure 2a-Figure 2b is similar to the condenser 10a of the embodiment shown in Figure 1a-Figure 1c, the difference lies in the change of the oil separation structure and the resulting first condensation chamber and Variation of the second condensation chamber, and different arrangement of the vertical separation plate. For the purpose of making the description concise, only the differences between the condenser 10b and the condenser 10a will be described below.

如图2a和图2b所示,冷凝器10b的容腔内设有油分离结构201b,油分离结构201b包括分离室203b。与油分离结构201a不同,油分离结构201b没有顶壁,因此,其相对的侧壁及相对的端壁直接连接到冷凝器10b的壳体内表面。应当理解的是,在一些实施例中,油分离结构201b也被设计成具有顶壁208。冷凝器10b的容腔底部设有一体式过冷盒107,油分离结构201b的底壁209b抵接过冷盒107,因此,分离室203b的高度小于分离室203a的高度。分离室203b的柄部具有宽度W2。考虑到由于分离室203b的高度小于分离室203a导致的制冷剂在分离室203b中的飞行高度减小,及由此带来的飞行时间缩短,分离室203b的柄部的宽度W2被设计为略大于分离室203a的柄部的宽度W1,这使得制冷剂在分离室203b中的飞行速度略减小,由此制冷剂在分离室203b中的飞行时间增加,且飞行过程中的压力损失减小。飞行时间提供制冷剂在分离室203b中的重力分离效果,,而压力损失减小有利于制冷剂的撞击分离和离心分离,从而有利于实现润滑油的充分分离。油分离结构201b的底部设有储油腔215,且储油腔215被容纳在第二冷凝室105b中。储油腔215与油分离结构201b底部的导油通道219b连通,以从分离室203b收集分离得到的润滑油。储油腔215底部设有排油口214b,以将储油腔215收集得到的润滑油排出到压缩机。由于储油腔215占据了第二冷凝室105b的部分空间,在使用根据该实施例中的油分离结构201b的制冷空调系统中,制冷剂的充注量可以被减少。As shown in Fig. 2a and Fig. 2b, an oil separation structure 201b is provided in the cavity of the condenser 10b, and the oil separation structure 201b includes a separation chamber 203b. Different from the oil separation structure 201a, the oil separation structure 201b has no top wall, therefore, its opposite side walls and opposite end walls are directly connected to the shell inner surface of the condenser 10b. It should be understood that, in some embodiments, the oil separation structure 201b is also designed to have a top wall 208 . An integrated subcooling box 107 is provided at the bottom of the cavity of the condenser 10b, and the bottom wall 209b of the oil separation structure 201b abuts against the subcooling box 107, so the height of the separation chamber 203b is smaller than that of the separation chamber 203a. The shank of the separation chamber 203b has a width W2. Considering that the height of the separation chamber 203b is smaller than that of the separation chamber 203a, the flight height of the refrigerant in the separation chamber 203b is reduced, and the resulting flight time is shortened, the width W2 of the handle of the separation chamber 203b is designed to be slightly It is larger than the width W1 of the shank of the separation chamber 203a, which makes the flight speed of the refrigerant in the separation chamber 203b slightly reduced, whereby the flight time of the refrigerant in the separation chamber 203b increases and the pressure loss during flight decreases . The time of flight provides the gravitational separation effect of the refrigerant in the separation chamber 203b, while the reduced pressure loss facilitates the impact separation and centrifugal separation of the refrigerant, thereby facilitating the sufficient separation of lubricating oil. The bottom of the oil separation structure 201b is provided with an oil storage chamber 215, and the oil storage chamber 215 is accommodated in the second condensation chamber 105b. The oil storage chamber 215 communicates with the oil guide channel 219b at the bottom of the oil separation structure 201b to collect the separated lubricating oil from the separation chamber 203b. An oil discharge port 214b is provided at the bottom of the oil storage chamber 215 to discharge the lubricating oil collected in the oil storage chamber 215 to the compressor. Since the oil storage chamber 215 occupies part of the space of the second condensing chamber 105b, in the refrigerating and air-conditioning system using the oil separation structure 201b according to this embodiment, the charging amount of refrigerant can be reduced.

相比图1a-图1c的实施例,在图2a-图2b的实施例中,在靠近第一排气口210.1和第二排气口210.2所在位置的一侧,增加竖向分离板213,竖向分离板213与竖向分离板211具有类似的布置。如图2a所示,在第一排气口210.1和第二排气口210.2所在位置的一侧,设置两个竖向分离板211和213用于对分离室203b中的上部流体通路形成阻挡,设置竖向分离板212对分离室203b中的下部流体通路形成阻挡。竖向分离板211靠近入口管301a且位于与入口管301a的出口303a相反的一侧,竖向分离板213靠近第一排气口210.1和第二排气口210.2所在的位置,竖向分离板212在冷凝器壳体的长度方向上位于竖向分离板211和213之间。应当理解的是,由于图2a-图2b的实施例中的油分离结构201b没有顶壁,图2a-图2b的实施例中的竖向分离板211和213自冷凝器10b的壳体顶部内表面向下延伸。应当理解的是,在其它实施例中,分离室203b中设置不同数量的竖向分离板211和212。Compared with the embodiment of Fig. 1a-Fig. 1c, in the embodiment of Fig. 2a-Fig. 2b, a vertical separation plate 213 is added on the side close to the position of the first exhaust port 210.1 and the second exhaust port 210.2, The vertical separation plate 213 has a similar arrangement to the vertical separation plate 211 . As shown in Figure 2a, on one side where the first exhaust port 210.1 and the second exhaust port 210.2 are located, two vertical separation plates 211 and 213 are arranged to form a barrier to the upper fluid passage in the separation chamber 203b, The provision of the vertical separation plate 212 forms a barrier to the lower fluid passage in the separation chamber 203b. The vertical separation plate 211 is close to the inlet pipe 301a and is located on the side opposite to the outlet 303a of the inlet pipe 301a. The vertical separation plate 213 is close to the position where the first exhaust port 210.1 and the second exhaust port 210.2 are located. The vertical separation plate 212 is located between the vertical separation plates 211 and 213 in the length direction of the condenser housing. It should be understood that since the oil separation structure 201b in the embodiment of FIGS. 2a-2b has no top wall, the vertical separation plates 211 and 213 in the embodiment of FIGS. The surface extends downwards. It should be understood that in other embodiments, different numbers of vertical separation plates 211 and 212 are provided in the separation chamber 203b.

制冷剂在分离室203b中的部分分离过程与在分离室203a中的分离过程类似。具体是,如同在分离室203a中分离过程一样,进入分离室203b中的制冷剂在经过竖向分离板211和212后得到第一离心分离后制冷剂及第二离心分离后制冷剂。与在分离室203a中不同的是,由于分离室203b相比分离室203a在靠近第一排气口210.1和第二排气口210.2的位置处增加了竖向分离板213,第一离心分离后制冷剂及第二离心分离后制冷剂在到达第一排气口210.1和第二排气口210.2之前进一步基于竖向分离板213的阻挡而发生分离。具体是,第一离心分离后制冷剂及第二离心分离后制冷剂朝向竖向分离板213流动,并撞击竖向分离板213。因撞击分离的润滑油滴落至导油通道219b中,其余的制冷剂作为第四撞击分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动。由于第四撞击分离后制冷剂的流动受到竖向分离板213的阻挡,第四撞击分离后制冷剂改变流动方向以绕开竖向分离板213的阻挡,这种运动方向的改变使得第四撞击分离后制冷剂在流动时发生围绕竖向分离板213的旋转,旋转产生的离心力进一步使得第四撞击分离后制冷剂中的润滑油被离心分离,从而滴落至导油通道219b中,其余制冷剂作为第三离心分离后制冷剂继续朝向第一排气口210.1和第二排气口210.2流动。由于第一排气口210.1和第二排气口210.2两侧都设有靠近这两个排气口的竖向分离板213,在距离较近的两块竖向分离板213的作用下,第三离心分离后制冷剂在第一排气口210.1和第二排气口210.2所在位置下方形成旋涡。基于旋涡产生的离心力,第三离心分离后制冷剂中的部分润滑油在第一排气口210.1和第二排气口210.2所在位置下方进一步发生离心分离,并低落至导油通道219b中,其余的制冷剂作为第四离心分离后制冷剂经第一排气口210.1和第二排气口210.2分别进入第一冷凝室104b和第二冷凝室105b中。与在分离室203a中相同,制冷剂在分离室203b中朝向第一排气口210.1和第二排气口210.2流动的过程中,润滑油还发生重力分离。在一些实施例中,当竖向分离板211和213的距离较近时,抵达竖向分离板211和213之间的制冷剂在竖向分离板211和213之间产生旋涡,旋涡产生的离心力进一步使得部分润滑油被分离并低落至导油通道219b中。如上所描述的,在分离室203b中,制冷剂中的润滑油和制冷剂气体发生撞击分离、离心分离和重力分离。同时存在这样的多种分离方式使得本申请为制冷剂提供充分的油分离。The partial separation process of the refrigerant in the separation chamber 203b is similar to that in the separation chamber 203a. Specifically, like the separation process in the separation chamber 203a, the refrigerant entering the separation chamber 203b obtains the first centrifugally separated refrigerant and the second centrifugally separated refrigerant after passing through the vertical separation plates 211 and 212 . Different from that in the separation chamber 203a, since the separation chamber 203b has a vertical separation plate 213 at a position close to the first exhaust port 210.1 and the second exhaust port 210.2 compared with the separation chamber 203b, after the first centrifugal separation The refrigerant and the second centrifugally separated refrigerant are further separated based on the blocking of the vertical separation plate 213 before reaching the first exhaust port 210.1 and the second exhaust port 210.2. Specifically, the first centrifugally separated refrigerant and the second centrifugally separated refrigerant flow toward the vertical separation plate 213 and collide with the vertical separation plate 213 . The lubricating oil separated due to impact drops into the oil guide channel 219b, and the rest of the refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2 as the fourth impact-separated refrigerant. Since the flow of the refrigerant after the fourth impact separation is blocked by the vertical separation plate 213, the refrigerant changes the flow direction after the fourth impact separation to bypass the obstruction of the vertical separation plate 213. This change of the movement direction makes the fourth impact The separated refrigerant rotates around the vertical separation plate 213 when it flows, and the centrifugal force generated by the rotation further makes the lubricating oil in the fourth collision separated refrigerant be centrifugally separated, thereby dripping into the oil guide channel 219b, and the rest of the refrigeration The refrigerant continues to flow toward the first exhaust port 210.1 and the second exhaust port 210.2 after the third centrifugal separation. Since both sides of the first exhaust port 210.1 and the second exhaust port 210.2 are provided with vertical separation plates 213 close to the two exhaust ports, under the action of the two vertical separation plates 213 that are closer to each other, the second After three centrifugal separations, the refrigerant forms a vortex below the positions of the first exhaust port 210.1 and the second exhaust port 210.2. Based on the centrifugal force generated by the vortex, after the third centrifugal separation, part of the lubricating oil in the refrigerant is further centrifugally separated below the positions of the first exhaust port 210.1 and the second exhaust port 210.2, and falls into the oil guide channel 219b, and the rest The refrigerant used as the fourth centrifugally separated refrigerant enters the first condensing chamber 104b and the second condensing chamber 105b through the first exhaust port 210.1 and the second exhaust port 210.2 respectively. As in the separation chamber 203a, during the flow of the refrigerant in the separation chamber 203b towards the first exhaust port 210.1 and the second exhaust port 210.2, the lubricating oil also undergoes gravity separation. In some embodiments, when the distance between the vertical separation plates 211 and 213 is relatively close, the refrigerant arriving between the vertical separation plates 211 and 213 generates a vortex between the vertical separation plates 211 and 213, and the centrifugal force generated by the vortex Further, part of the lubricating oil is separated and dropped into the oil guide passage 219b. As described above, in the separation chamber 203b, the lubricating oil in the refrigerant and the refrigerant gas undergo collision separation, centrifugal separation, and gravity separation. At the same time, there are multiple separation methods so that the present application provides sufficient oil separation for the refrigerant.

图3a-图3b示出根据本申请的又一个实施例的冷凝器10c。图3a是根据本申请的又一个实施例的冷凝器10c的截面图。图3b是图3a所示的冷凝器10c沿C-C方向的截面图。Figures 3a-3b illustrate a condenser 10c according to yet another embodiment of the present application. Fig. 3a is a cross-sectional view of a condenser 10c according to yet another embodiment of the present application. Fig. 3b is a cross-sectional view of the condenser 10c shown in Fig. 3a along the direction C-C.

在图3a-图3b所示实施例的冷凝器10c及其中的油分离结构201c分别与图2a-图2b所示实施例中的冷凝器10b及油分离结构201b类似,不同之处在于入口管的构造及分离室中分离板的设置。出于使得描述简洁的目的,下面只描述冷凝器10c与冷凝器10b不同之处。The condenser 10c and the oil separation structure 201c in the embodiment shown in Figure 3a-Figure 3b are similar to the condenser 10b and the oil separation structure 201b in the embodiment shown in Figure 2a-Figure 2b respectively, the difference is that the inlet pipe The structure and the setting of the separation plate in the separation chamber. For the purpose of making the description concise, only the differences between the condenser 10c and the condenser 10b will be described below.

如图3a和图3b所示,冷凝器10c包括入口管301c,不同于入口管301a,入口管301c伸入分离室203c中的部分是直管,从而具有朝下的出口303c。As shown in Figures 3a and 3b, the condenser 10c includes an inlet pipe 301c, different from the inlet pipe 301a, the part of the inlet pipe 301c protruding into the separation chamber 203c is a straight pipe, thereby having a downward outlet 303c.

继续参考图3a和图3b,油分离结构201c的分离室203c中设置竖向分离板217和218,竖向分离板217与竖向分离板211具有类似的布置,竖向分离板218与竖向分离板212具有类似的布置。竖向分离板217用于对分离室203c中的上部气流通路进行阻挡,竖向分离板218用于对分离室203c中的下部气流通路进行阻挡。由于油分离结构201c与油分离结构201b一样,同样没有顶壁,图3a-图3b的实施例中的竖向分离板217自冷凝器10c的壳体顶部内表面向下延伸。在其它实施例中,分离室203c中设置不同数量的竖向分离板217和218。3a and 3b, vertical separation plates 217 and 218 are arranged in the separation chamber 203c of the oil separation structure 201c. The separation plate 212 has a similar arrangement. The vertical separation plate 217 is used to block the upper air flow path in the separation chamber 203c, and the vertical separation plate 218 is used to block the lower air flow path in the separation chamber 203c. Since the oil separation structure 201c has no top wall like the oil separation structure 201b, the vertical separation plate 217 in the embodiment of Fig. 3a-3b extends downward from the top inner surface of the condenser 10c. In other embodiments, different numbers of vertical separation plates 217 and 218 are provided in the separation chamber 203c.

分离室203c中还设有横向分离板231,横向分离板231横向于所述分离室203c的延伸方向布置并抵接油分离结构201c的两个侧壁,且横向分离板231位于相应的入口管301c下方,朝向入口管301c的出口303c。在第一排气口210.1和第二排气口210.2所在位置的一侧,竖向分离板218位于竖向分离板217和横向分离板231之间。尽管图中未示出,应当理解的是,也可以将本实施例中的入口管301c及分离板布置应用到图1a-图1c及图2a-图2b的实施例中,替换其中的入口管及分离板布置。A transverse separation plate 231 is also provided in the separation chamber 203c. The transverse separation plate 231 is arranged transversely to the extension direction of the separation chamber 203c and abuts against the two side walls of the oil separation structure 201c, and the transverse separation plate 231 is located at the corresponding inlet pipe. Below 301c, towards the outlet 303c of the inlet pipe 301c. On one side where the first exhaust port 210.1 and the second exhaust port 210.2 are located, the vertical separation plate 218 is located between the vertical separation plate 217 and the transverse separation plate 231 . Although not shown in the figure, it should be understood that the arrangement of the inlet pipe 301c and the separation plate in this embodiment can also be applied to the embodiments of Fig. 1a-Fig. 1c and Fig. 2a- Fig. 2b, replacing the inlet pipe and separation board layout.

下面结合图3a说明从位于图3a所示的右侧的入口管301c进入油分离室203c中的制冷剂中分离润滑油和制冷剂气体的过程。应当理解,从位于图3a中左侧的入口管301c进入油分离室203c中的制冷剂中分离润滑油和制冷剂气体的过程是类似的。The process of separating lubricating oil and refrigerant gas from the refrigerant entering the oil separation chamber 203c from the inlet pipe 301c on the right side shown in FIG. 3a will be described below with reference to FIG. 3a. It should be understood that the process of separating lubricating oil and refrigerant gas from the refrigerant entering the oil separation chamber 203c from the inlet pipe 301c located on the left side in FIG. 3a is similar.

如图3a所示,制冷剂从入口管301c的出口303c排出后朝向横向分离板231流动并撞击横向分离板231。通过撞击,制冷剂中的部分润滑油被分离,被分离的润滑油滴落到分离室203c底部的导油通道219b中。其余的制冷剂作为第一撞击分离后制冷剂继续在分离室203c中流动。部分第一撞击分离后制冷剂朝向竖向分离板217流动并撞击竖向分离板217,该撞击使得这部分第一撞击分离后制冷剂中的部分润滑油被分离并滴落到导油通道219b中,其余的制冷剂作为第二撞击分离后制冷剂朝向第一排气口210.1和第二排气口210.2流动。由于第二撞击分离后制冷剂的流动受到竖向分离板217的阻挡,第二撞击分离后制冷剂在流动时发生围绕竖向分离板217的旋转以变化方向绕开竖向分离板217的阻挡,旋转产生的离心力进一步使得第二撞击分离后制冷剂中的润滑油被离心分离,从而滴落至导油通道219a中,其余制冷剂作为第一离心分离后制冷剂经第一排气口210.1和第二排气口210.2分别进入分离室203c两侧的冷凝室中进行冷却。部分第一撞击分离后制冷剂朝向竖向分离板218流动并撞击竖向分离板218,该撞击使得这部分第一撞击分离后制冷剂中的部分润滑油被分离并滴落到导油通道219b中,其余的制冷剂作为第三撞击分离后制冷剂朝向第一排气口210.1和第二排气口210.2流动。由于第三撞击分离后制冷剂的流动受到竖向分离板218的阻挡,第三撞击分离后制冷剂在流动时发生围绕竖向分离板218的旋转以变化方向绕开竖向分离板218的阻挡,旋转产生的离心力进一步使得第三撞击分离后制冷剂中的润滑油被离心分离,从而滴落至导油通道219b中,其余制冷剂作为第二离心分离后制冷剂经第一排气口210.1和第二排气口210.2分别进入分离室203c两侧的冷凝室中进行冷却。另外,还有部分第一撞击分离后制冷剂朝向端壁207流动并撞击端壁207,该撞击使得这部分第一撞击分离后制冷剂中的部分润滑油被分离并滴落到分离室203c底部的导油通道219b中,其余的制冷剂作为第四撞击分离后制冷剂改变方向朝向第一排气口210.1和第二排气口210.2流动,并在竖向分离板217和218处进一步发生撞击和离心分离。与在分离室203a和203b中相同,制冷剂在分离室203c中朝向第一排气口210.1和第二排气口210.2流动的过程中,润滑油还发生重力分离。在一些实施例中,当第一排气口210.1和第二排气口210.2两侧的竖向分离板217距离较近时,抵达第一排气口210.1和第二排气口210.2的制冷剂在两个竖向分离板217之间产生旋涡,旋涡产生的离心力进一步使得部分润滑油被分离并低落至导油通道219b中。如上所描述的,在分离室203c中,制冷剂中的润滑油和制冷剂气体发生撞击分离、离心分离和重力分离。同时存在这样的多种分离方式使得本申请提供充分的油分离。As shown in FIG. 3 a , the refrigerant flows toward the transverse separation plate 231 after being discharged from the outlet 303 c of the inlet pipe 301 c and hits the transverse separation plate 231 . Through the collision, part of the lubricating oil in the refrigerant is separated, and the separated lubricating oil drops into the oil guide channel 219b at the bottom of the separation chamber 203c. The rest of the refrigerant continues to flow in the separation chamber 203c as the refrigerant after the first impact separation. Part of the refrigerant after the first impact separation flows toward the vertical separation plate 217 and hits the vertical separation plate 217, and the impact causes part of the lubricating oil in this part of the first impact separation refrigerant to be separated and drop to the oil guide channel 219b In this process, the rest of the refrigerant flows toward the first exhaust port 210.1 and the second exhaust port 210.2 as the second impact-separated refrigerant. Since the flow of the refrigerant after the second impact separation is blocked by the vertical separation plate 217, the refrigerant after the second impact separation rotates around the vertical separation plate 217 to change direction to bypass the obstruction of the vertical separation plate 217 when flowing. , the centrifugal force generated by the rotation further causes the lubricating oil in the refrigerant after the second impact separation to be centrifugally separated, thereby dripping into the oil guide channel 219a, and the rest of the refrigerant as the first centrifugally separated refrigerant passes through the first exhaust port 210.1 and the second exhaust port 210.2 respectively enter the condensation chambers on both sides of the separation chamber 203c for cooling. Part of the refrigerant after the first impact separation flows toward the vertical separation plate 218 and hits the vertical separation plate 218. The impact causes part of the lubricating oil in this part of the first impact separation refrigerant to be separated and drop to the oil guide channel 219b In this process, the rest of the refrigerant flows toward the first exhaust port 210.1 and the second exhaust port 210.2 as the third impact-separated refrigerant. Since the flow of the refrigerant after the third impact separation is blocked by the vertical separation plate 218, the refrigerant after the third impact separation rotates around the vertical separation plate 218 to change direction to bypass the obstruction of the vertical separation plate 218 when flowing. , the centrifugal force generated by the rotation further causes the lubricating oil in the refrigerant after the third impact separation to be centrifugally separated, thereby dripping into the oil guide channel 219b, and the rest of the refrigerant is used as the second centrifugally separated refrigerant through the first exhaust port 210.1 and the second exhaust port 210.2 respectively enter the condensation chambers on both sides of the separation chamber 203c for cooling. In addition, part of the refrigerant after the first impact separation flows toward the end wall 207 and hits the end wall 207, and the impact causes part of the lubricating oil in this part of the first impact separation refrigerant to be separated and drop to the bottom of the separation chamber 203c In the oil guide channel 219b, the rest of the refrigerant flows towards the first exhaust port 210.1 and the second exhaust port 210.2 after being separated by the fourth collision, and further collides at the vertical separation plates 217 and 218. and centrifugal separation. As in the separation chambers 203a and 203b, the lubricating oil is also gravitationally separated during the flow of the refrigerant in the separation chamber 203c towards the first exhaust port 210.1 and the second exhaust port 210.2. In some embodiments, when the distance between the vertical separation plates 217 on both sides of the first exhaust port 210.1 and the second exhaust port 210.2 is relatively close, the refrigerant reaching the first exhaust port 210.1 and the second exhaust port 210.2 A vortex is generated between the two vertical separation plates 217, and the centrifugal force generated by the vortex further causes part of the lubricating oil to be separated and drop into the oil guide channel 219b. As described above, in the separation chamber 203c, the lubricating oil in the refrigerant and the refrigerant gas undergo impact separation, centrifugal separation, and gravity separation. Simultaneously there are such multiple separation ways that the present application provides sufficient oil separation.

根据本申请的实施例至少都具有以下技术效果:Embodiments according to the present application at least have the following technical effects:

1.本申请使用的油分离结构提供多种分离方式,包括撞击分离、离心分离及重力分离,因而本申请的油分离结构能够提供充分的油分离。1. The oil separation structure used in this application provides multiple separation methods, including impact separation, centrifugal separation and gravity separation, so the oil separation structure of this application can provide sufficient oil separation.

2.由于本申请的油分离结构的构造及其提供的优良的油分离效果,使得不要求油分离结构提供大的分离室来进行油分离。本申请的分离室中设置的竖向分离板在制冷剂朝向第一和第二排出口流动的过程中形成阻挡,从而降低制冷剂在分离室中的流动速度,确保制冷剂在分离室中飞行足够的时间用于完成油分离。因次,本申请的油分离结构被设计为具有小尺寸的分离室。本申请的油分离结构的小尺寸使得冷凝器容腔的大部分被用作冷凝室,从而提高冷凝器的换热能力。具体来说,如上文中陈述的,分离室柄部的宽度尺寸被设计为略大于入口管的直径,这使得柄部具有很小的宽度。因此,在本申请中,油分离结构仅占据冷凝器容腔的很小部分,这使得冷凝器容腔能够提供很大空间用于冷凝。因此在本申请中,冷凝器容腔的大部分空间被油分离结构两侧的两个冷凝室占据,从而不需要增加冷凝器的尺寸,就能够在两个冷凝室中设置很多冷凝管,以确保冷凝器的换热能力。相反地,如果没有在分离室中设置竖向分离板,为了使得制冷剂在分离室中飞行足够时间来完成油分离,需要将分离室设计成具有大尺寸以减小制冷剂在其中的飞行速度。这样的话,由于分离室占用冷凝器容腔的很多空间,只有较少的冷凝器容腔能够被用作冷凝室完成对制冷剂气体的冷凝,从而降低冷凝器的换热能力。2. Due to the structure of the oil separation structure of the present application and the excellent oil separation effect it provides, the oil separation structure is not required to provide a large separation chamber for oil separation. The vertical separation plate set in the separation chamber of the present application forms a barrier when the refrigerant flows towards the first and second discharge ports, thereby reducing the flow speed of the refrigerant in the separation chamber and ensuring that the refrigerant flies in the separation chamber Sufficient time for complete oil separation. Accordingly, the oil separation structure of the present application is designed to have a small-sized separation chamber. The small size of the oil separation structure of the present application enables most of the condenser cavity to be used as a condensation chamber, thereby improving the heat exchange capacity of the condenser. Specifically, as stated above, the width dimension of the separation chamber shank is designed to be slightly larger than the diameter of the inlet pipe, which makes the shank have a small width. Therefore, in the present application, the oil separation structure only occupies a small portion of the condenser cavity, which enables the condenser cavity to provide a large space for condensation. Therefore, in this application, most of the space of the condenser cavity is occupied by two condensation chambers on both sides of the oil separation structure, so that without increasing the size of the condenser, many condensation pipes can be arranged in the two condensation chambers to Ensure the heat exchange capacity of the condenser. On the contrary, if there is no vertical separation plate in the separation chamber, in order to allow the refrigerant to fly in the separation chamber for a sufficient time to complete the oil separation, the separation chamber needs to be designed with a large size to reduce the flight speed of the refrigerant in it . In this case, since the separation chamber occupies a lot of space in the condenser cavity, only a small amount of the condenser cavity can be used as a condensation chamber to condense the refrigerant gas, thereby reducing the heat exchange capacity of the condenser.

3.本申请利用油分离结构使得冷凝器的容腔包括位于分离室两侧的两个冷凝室有利于提高换热效率。具体来说,假设将油分离结构设置在容腔的一侧,使得容腔包括分离室和单个冷凝室,则在沿冷凝器壳体的宽度方向上,假设的单个冷凝室的尺寸大于根据本申请的两个冷凝室中的任何一个的尺寸。从而,相比根据本申请的两个冷凝室中的任何一个冷凝室,假设的单个冷凝室中将布置更多数量的冷凝管。这使得,进入假设的单个的冷凝室中的待冷却的制冷器气体朝向位于假设的单个的冷凝室中部的冷凝管流动时受到更多阻力,更难抵达位于假设的单个的冷凝室中部的冷凝管,从而难以同位于假设的单个的冷凝室中部的冷凝管中的冷却流体进行热交换来实现冷却。因此,假设将油分离结构设置在容腔的一侧,使得容腔包括分离室和单个冷凝室,冷凝器的换热效率会受到损失。相反地,本申请的油分离结构使得冷凝器容腔包括位于油分离结构两侧的两个冷凝室的构造使得每个冷凝室分别设置较少数量的冷凝管,从而进入每个冷凝室的待冷却的制冷剂气体易于到达位于两个冷凝室中部的冷凝管,以和这些冷凝管中的冷却流体实现热交换,从而有利于换热效率的提高。3. This application utilizes the oil separation structure so that the cavity of the condenser includes two condensation chambers located on both sides of the separation chamber, which is beneficial to improve the heat exchange efficiency. Specifically, assuming that the oil separation structure is arranged on one side of the cavity, so that the cavity includes a separation chamber and a single condensation chamber, then along the width direction of the condenser shell, the size of the assumed single condensation chamber is larger than that according to the present invention. The size of either of the two condensation chambers applied. Thus, a greater number of condensation pipes will be arranged in a hypothetical single condensation chamber than in any one of the two condensation chambers according to the present application. This makes it more difficult for the refrigerant gas to be cooled entering the hypothetical single condensing chamber to flow towards the condensing pipe located in the middle of the hypothetical single condensing chamber, and it is more difficult to reach the condensate located in the middle of the hypothetical single condensing chamber. tube, so it is difficult to exchange heat with the cooling fluid in the cooling tube located in the middle of the hypothetical single condensation chamber to achieve cooling. Therefore, if the oil separation structure is arranged on one side of the cavity, so that the cavity includes a separation chamber and a single condensation chamber, the heat exchange efficiency of the condenser will be lost. On the contrary, the oil separation structure of the present application makes the condenser cavity include two condensation chambers located on both sides of the oil separation structure, so that each condensation chamber is respectively provided with a smaller number of condensation pipes, thereby entering each condensation chamber. The cooled refrigerant gas can easily reach the condensing pipes located in the middle of the two condensing chambers, so as to exchange heat with the cooling fluid in these condensing pipes, which is beneficial to the improvement of heat exchange efficiency.

4.当分离室在冷凝器壳体的宽度方向上居中布置在冷凝器容腔中时,分离室两侧的两个冷凝室具有相同尺寸。因此,两个冷凝室的沿冷凝器壳体的宽度方向的尺寸都不会过大,使得在沿壳体的宽度方向上,两个冷凝室都布置合适数量的冷凝管。这进一步有利于进入每个冷凝室的待冷却的制冷器气体易于到达位于各冷凝室中部的冷凝管,也即,进一步有利于换热效率的提高。4. When the separation chamber is centrally arranged in the condenser cavity in the width direction of the condenser shell, the two condensation chambers on both sides of the separation chamber have the same size. Therefore, the size of the two condensing chambers along the width direction of the condenser housing will not be too large, so that an appropriate number of condensing pipes are arranged in the two condensing chambers along the width direction of the housing. This further facilitates the refrigerator gas to be cooled entering each condensation chamber to easily reach the condensation pipe located in the middle of each condensation chamber, that is, further facilitates the improvement of heat exchange efficiency.

5.当入口管在冷凝器壳体的宽度方向上在壳体顶部居中布置且分离室在冷凝器壳体的宽度方向上居中布置在冷凝器容腔中时,制冷剂在进入分离室后具有最大的飞行高度,因此制冷剂在分离室中具有最长的飞行时间,进一步有利于在分离室中充分分离制冷剂中的润滑油。5. When the inlet pipe is centrally arranged on the top of the shell in the width direction of the condenser shell and the separation chamber is centrally arranged in the condenser cavity in the width direction of the condenser shell, the refrigerant has after entering the separation chamber The maximum flight altitude, so the refrigerant has the longest flight time in the separation chamber, which further facilitates the sufficient separation of lubricating oil in the refrigerant in the separation chamber.

6.本申请的分离室的漏斗形构造,使得制冷剂在分离室的柄部具有较大的流动速度,以有利于润滑油借助于竖向分离板实现撞击分离和离心分离,而在分离室的口部具有减小的流动速度,使得增加制冷剂在口部的飞行时间,以有利于润滑油的重力分离。同时在配合使用过滤网的实施例中,分离室口部制冷剂流速的降低有利于过滤网对润滑油的进一步捕捉分离。6. The funnel-shaped structure of the separation chamber of the present application enables the refrigerant to have a relatively high flow velocity at the handle of the separation chamber, so as to facilitate the impact separation and centrifugal separation of the lubricating oil by means of the vertical separation plate, while in the separation chamber The mouth has a reduced flow velocity, so that the flight time of the refrigerant in the mouth is increased to facilitate the gravity separation of the lubricating oil. At the same time, in the embodiment where the filter is used together, the reduction of the flow rate of the refrigerant at the mouth of the separation chamber is beneficial to the further capture and separation of the lubricating oil by the filter.

尽管已经结合以上概述的实施例的实例描述了本公开,但是对于本领域中至少具有普通技术的人员而言,各种替代方案、修改、变化、改进和/或基本等同方案,无论是已知的或是现在或可以不久预见的,都可能是显而易见的。另外,本说明书中所描述的技术效果和/或技术问题是示例性而不是限制性的;所以本说明书中的披露可能用于解决其他技术问题和具有其他技术效果和/或可以解决其他技术问题。因此,如上陈述的本公开的实施例的实例旨在是说明性而不是限制性的。在不背离本公开的精神或范围的情况下,可以进行各种改变。因此,本公开旨在包括所有已知或较早开发的替代方案、修改、变化、改进和/或基本等同方案。Although the present disclosure has been described in conjunction with the examples of embodiments outlined above, various alternatives, modifications, changes, improvements and/or substantial equivalents, whether known or not, will occur to those having at least ordinary skill in the art may be obvious, either now or in the foreseeable future. In addition, the technical effects and/or technical problems described in this specification are exemplary rather than limiting; therefore, the disclosures in this specification may be used to solve other technical problems and have other technical effects and/or can solve other technical problems . Accordingly, the examples of embodiments of the present disclosure set forth above are intended to be illustrative and not restrictive. Various changes may be made without departing from the spirit or scope of the disclosure. Accordingly, the present disclosure is intended to embrace all known or earlier developed alternatives, modifications, variations, improvements and/or substantial equivalents.

Claims (14)

1.一种内设油分离结构的冷凝器,其特征在于:包括:1. A condenser with built-in oil separation structure, characterized in that: comprising: 壳体(101),所述壳体(101)限定容腔(102),所述壳体(101)上设有至少一个入口管(301a,301c),用于接收含有润滑油的待被冷凝的制冷剂,所述壳体(101)包括长度方向、高度方向和宽度方向;A housing (101), the housing (101) defines a cavity (102), and the housing (101) is provided with at least one inlet pipe (301a, 301c) for receiving lubricating oil to be condensed refrigerant, the housing (101) includes a length direction, a height direction and a width direction; 油分离结构(201a,201b,201c),所述油分离结构(201a,201b,201c)被固定在所述容腔(102)中,所述油分离结构(201a,201b,201c)包括分离室(203a,203b,203c),所述至少一个入口管(301a,301c)伸入所述分离室(203a,203b,203c),其中,所述分离室(203a,203b,203c)被配置为将所述制冷剂中的所述润滑油和制冷剂气体分离开;an oil separation structure (201a, 201b, 201c), the oil separation structure (201a, 201b, 201c) is fixed in the cavity (102), the oil separation structure (201a, 201b, 201c) comprises a separation chamber (203a, 203b, 203c), said at least one inlet pipe (301a, 301c) extends into said separation chamber (203a, 203b, 203c), wherein said separation chamber (203a, 203b, 203c) is configured to the lubricating oil and refrigerant gas in the refrigerant are separated; 其中,所述容腔(102)包括由所述油分离结构(201a,201b,201c)分隔开的第一冷凝室(104a,104b)和第二冷凝室(105a,105b),所述第一冷凝室(104a,104b)和所述第二冷凝室(105a,105b)在所述壳体(101)的宽度方向上分别位于所述分离室(203a,203b,203c)的两侧,并且分别沿所述壳体(101)的长度方向延伸;且Wherein, the cavity (102) includes a first condensation chamber (104a, 104b) and a second condensation chamber (105a, 105b) separated by the oil separation structure (201a, 201b, 201c), the first a condensation chamber (104a, 104b) and the second condensation chamber (105a, 105b) are respectively located on both sides of the separation chamber (203a, 203b, 203c) in the width direction of the housing (101), and respectively extending along the length direction of the casing (101); and 其中,所述油分离结构(201a,201b,201c)的上部设有分别将所述第一冷凝室(104a,104b)和所述第二冷凝室(105a,105b)与所述分离室(203a,203b,203c)流体连通的第一排气口(210.1)和第二排气口(210.2),以使经所述分离室(203a,203b,203c)分离的制冷剂气体能够进入所述第一冷凝室(104a,104b)和所述第二冷凝室(105a,105b)中进行冷凝,并且所述油分离结构(201a,201b,201c)的底部设有至少一个排油口(214a,214b),以使经所述分离室(203a,203b,203c)分离的润滑油能够排出所述分离室(203a,203b,203c)。Wherein, the upper part of the oil separation structure (201a, 201b, 201c) is provided with the first condensation chamber (104a, 104b) and the second condensation chamber (105a, 105b) and the separation chamber (203a , 203b, 203c) fluidly connected first exhaust port (210.1) and second exhaust port (210.2), so that the refrigerant gas separated by the separation chamber (203a, 203b, 203c) can enter the first Condensation is carried out in a condensation chamber (104a, 104b) and the second condensation chamber (105a, 105b), and at least one oil discharge port (214a, 214b) is provided at the bottom of the oil separation structure (201a, 201b, 201c) ), so that the lubricating oil separated by the separation chamber (203a, 203b, 203c) can be discharged from the separation chamber (203a, 203b, 203c). 2.根据权利要求1所述的内设油分离结构的冷凝器,其特征在于:2. The condenser with built-in oil separation structure according to claim 1, characterized in that: 所述分离室(203a,203b,203c)在所述壳体(101)的宽度方向上居中布置在所述容腔(102)中。The separation chamber (203a, 203b, 203c) is centrally arranged in the cavity (102) in the width direction of the casing (101). 3.根据权利要求2所述的内设油分离结构的冷凝器,其特征在于:3. The condenser with built-in oil separation structure according to claim 2, characterized in that: 所述油分离结构(201a,201b,201c)包括沿所述壳体(101)的长度方向间隔设置在所述分离室(203a,203b,203c)中的数个竖向分离板(211,212,213,217,218),所述数个竖向分离板(211,212,213,217,218)各自横向于所述分离室(203a,203b,203c)的延伸方向布置,其中,至少一部分所述数个竖向分离板(211,213,217)设置为对所述分离室(203a,203b,203c)中的上部流体通路进行阻挡,至少另一部分所述数个竖向分离板(212,218)设置为对所述分离室(203a,203b,203c)中的下部流体通路进行阻挡。The oil separation structure (201a, 201b, 201c) includes several vertical separation plates (211, 212) arranged at intervals along the length direction of the housing (101) in the separation chamber (203a, 203b, 203c) . The several vertical separation plates (211, 213, 217) are arranged to block the upper fluid passage in the separation chamber (203a, 203b, 203c), at least another part of the several vertical separation plates (212 , 218) arranged to block the lower fluid passage in said separation chamber (203a, 203b, 203c). 4.根据权利要求3所述的内设油分离结构的冷凝器,其特征在于:4. The condenser with built-in oil separation structure according to claim 3, characterized in that: 在所述第一排气口(210.1)和所述第二排气口(210.2)的一侧上,对所述分离室(203a,203b,203c)中的上部流体通路进行阻挡的所述至少一部分所述竖向分离板(211,213,217)与对所述分离室(203a,203b,203c)中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板(212,218)交替布置。On one side of the first exhaust port (210.1) and the second exhaust port (210.2), the at least A part of said vertical separation plate (211, 213, 217) is connected with said at least another part of said vertical separation plate (212, 218) blocking a lower fluid passage in said separation chamber (203a, 203b, 203c). ) are arranged alternately. 5.根据权利要求4所述的内设油分离结构的冷凝器,其特征在于:5. The condenser with built-in oil separation structure according to claim 4, characterized in that: 所述至少一个入口管(301a,301c)在所述壳体(101)的顶部在所述壳体(101)的宽度方向上居中布置。The at least one inlet pipe (301a, 301c) is centrally arranged at the top of the housing (101) in the width direction of the housing (101). 6.根据权利要求5所述的内设油分离结构的冷凝器,其特征在于:6. The condenser with built-in oil separation structure according to claim 5, characterized in that: 所述至少一个入口管(301c)的伸入所述分离室(203c)的部分沿所述壳体(101)的高度方向延伸;且A portion of the at least one inlet pipe (301c) protruding into the separation chamber (203c) extends along the height direction of the housing (101); and 所述油分离结构(201c)还包括位于所述至少一个入口管(301c)下方的横向分离板(231)。The oil separation structure (201c) also includes a transverse separation plate (231) located below the at least one inlet pipe (301c). 7.根据权利要求5所述的内设油分离结构的冷凝器,其特征在于:7. The condenser with built-in oil separation structure according to claim 5, characterized in that: 所述至少一个入口管(301a)的伸入所述分离室(203a,203b)的部分朝向远离所述第一排气口(210.1)和所述第二排气口(210.2)的方向弯折成弯管状。A portion of the at least one inlet pipe (301a) protruding into the separation chamber (203a, 203b) is bent toward a direction away from the first exhaust port (210.1) and the second exhaust port (210.2) Into a curved tube shape. 8.根据权利要求5所述的内设油分离结构的冷凝器,其特征在于:8. The condenser with built-in oil separation structure according to claim 5, characterized in that: 所述分离室(203a,203b,203c)沿所述壳体(101)的长度方向延伸,所述分离室(203a,203b,203c)的平行于所述壳体(101)的高度方向和宽度方向构成的平面的截面大体上呈漏斗形,使得所述分离室(203a,203b,203c)具有口部(221a)和柄部(222a),所述柄部(222a)的宽度尺寸(W1,W2)被设计为略大于所述至少一个入口管(301a,301c)的直径d。The separation chamber (203a, 203b, 203c) extends along the length direction of the casing (101), and the separation chamber (203a, 203b, 203c) is parallel to the height direction and width of the casing (101). The cross-section of the plane formed by the direction is generally funnel-shaped, so that the separation chamber (203a, 203b, 203c) has a mouth (221a) and a handle (222a), the width dimension of the handle (222a) (W1, W2) is designed slightly larger than the diameter d of said at least one inlet pipe (301a, 301c). 9.根据权利要求4所述的内设油分离结构的冷凝器,其特征在于:9. The condenser with built-in oil separation structure according to claim 4, characterized in that: 所述油分离结构(201a)包括外壳(202a),所述外壳(202a)限定所述分离室(203a),所述外壳(202a)包括彼此连接的相对的侧壁(204,205)、相对的端壁(206,207)以及相对的顶壁(208)和底壁(209a),所述顶壁(208)与所述壳体(101)的顶部内表面抵接,且所述相对的侧壁(204,205)上部分别设有所述第一排气口(210.1)和所述第二排气口(210.2);且The oil separation structure (201a) includes a casing (202a) defining the separation chamber (203a), the casing (202a) including opposite side walls (204, 205) connected to each other, opposite The end walls (206, 207) and the opposite top wall (208) and bottom wall (209a), the top wall (208) abuts against the top inner surface of the housing (101), and the opposite The first exhaust port (210.1) and the second exhaust port (210.2) are respectively provided on the upper part of the side wall (204, 205); and 对所述分离室(203a)中的上部流体通路进行阻挡的所述至少一部分所述竖向分离板(211)自所述顶壁(208)延伸所述分离室(203a)的至少部分高度,对所述分离室(203a)中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板(212)自所述油分离结构(201a)的底部延伸所述分离室(203a)的至少部分高度。said at least a portion of said vertical separation plate (211 ) blocking an upper fluid passage in said separation chamber (203a) extends from said top wall (208) at least part of the height of said separation chamber (203a), Said at least another part of said vertical separation plate (212) blocking a lower fluid passage in said separation chamber (203a) extends from the bottom of said oil separation structure (201a) to the bottom of said separation chamber (203a) At least part of the height. 10.根据权利要求4所述的内设油分离结构的冷凝器,其特征在于:10. The condenser with built-in oil separation structure according to claim 4, characterized in that: 所述油分离结构(201b,201c)包括外壳,所述外壳限定所述分离室(203b,203c),所述外壳包括彼此连接的相对的侧壁(204,205)、相对的端壁(206,207)以及底壁(209b),所述相对的侧壁(204,205)和所述相对的端壁(206,207)的顶部与所述壳体(101)的顶部内表面抵接,且所述相对的侧壁(204,205)上部分别设有所述第一排气口(210.1)和所述第二排气口(210.2);且The oil separation structure (201b, 201c) comprises a housing defining the separation chamber (203b, 203c), the housing comprising opposing side walls (204, 205), opposing end walls (206) connected to each other , 207) and a bottom wall (209b), the tops of the opposite side walls (204, 205) and the opposite end walls (206, 207) abut against the top inner surface of the housing (101), And the upper parts of the opposite side walls (204, 205) are respectively provided with the first exhaust port (210.1) and the second exhaust port (210.2); and 对所述分离室(203b,203c)中的上部流体通路进行阻挡的所述至少一部分所述竖向分离板(211,213,217)自所述冷凝器的所述壳体(101)的顶部内表面延伸所述分离室(203b,203c)的至少部分高度,对所述分离室(203b,203c)中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板(212,218)自所述油分离结构(201b,201c)的底部延伸所述分离室(203b,203c)的至少部分高度。Said at least a portion of said vertical separation plate (211, 213, 217) blocking an upper fluid passage in said separation chamber (203b, 203c) exits from the top of said casing (101) of said condenser The inner surface extends at least part of the height of said separation chamber (203b, 203c), said at least another part of said vertical separation plate (212, 218 ) blocking a lower fluid passage in said separation chamber (203b, 203c) ) extends at least part of the height of the separation chamber (203b, 203c) from the bottom of the oil separation structure (201b, 201c). 11.根据权利要求9或10所述的内设油分离结构的冷凝器,其特征在于:11. The condenser with built-in oil separation structure according to claim 9 or 10, characterized in that: 对所述分离室(203a,203b,203c)中的下部流体通路进行阻挡的所述至少另一部分所述竖向分离板(212,218)与所述底壁(209a,209b)间隔一定距离以限定导油通道(219a,219b)。Said at least another part of said vertical separation plate (212, 218) blocking a lower fluid passage in said separation chamber (203a, 203b, 203c) is spaced a distance from said bottom wall (209a, 209b) to Oil guide passages (219a, 219b) are defined. 12.根据权利要求9或10所述的内设油分离结构的冷凝器,其特征在于:12. The condenser with built-in oil separation structure according to claim 9 or 10, characterized in that: 所述油分离结构(201a)的所述底壁(209a)抵接所述壳体(101)的底部内表面,所述至少一个排油口(214a)被设置在所述底壁(209a)上;且The bottom wall (209a) of the oil separation structure (201a) abuts against the bottom inner surface of the housing (101), and the at least one oil discharge port (214a) is arranged on the bottom wall (209a) on; and 所述冷凝器包括位于所述容腔(102)底部的第一过冷盒(107.1)和第二过冷盒(107.2),所述第一过冷盒(107.1)和所述第二过冷盒(107.2)在所述壳体(101)的宽度方向上分别位于所述油分离结构(201a)的两侧。The condenser includes a first subcooling box (107.1) and a second subcooling box (107.2) located at the bottom of the cavity (102), and the first subcooling box (107.1) and the second subcooling box The boxes (107.2) are respectively located on both sides of the oil separation structure (201a) in the width direction of the housing (101). 13.根据权利要求9或10所述的内设油分离结构的冷凝器,其特征在于:13. The condenser with built-in oil separation structure according to claim 9 or 10, characterized in that: 所述冷凝器包括设置在所述容腔(102)底部的过冷盒(107),所述油分离结构(201b,201c)的所述底壁(209b)抵接所述过冷盒(107);且The condenser includes a subcooling box (107) arranged at the bottom of the cavity (102), and the bottom wall (209b) of the oil separation structure (201b, 201c) abuts against the subcooling box (107 );and 所述油分离结构(201b,201c)还包括设置在所述油分离结构(201b,201c)底部与所述分离室(203b,203c)的底部连通的至少一个储油腔(215),所述至少一个排油口(214b)被设置在相应的所述至少一个储油腔(215)底部,其中,所述至少一个储油腔(215)被容纳在所述第一冷凝室(104)和所述第二冷凝室(105)之一的底部。The oil separation structure (201b, 201c) further includes at least one oil storage chamber (215) arranged at the bottom of the oil separation structure (201b, 201c) and communicating with the bottom of the separation chamber (203b, 203c), the At least one oil discharge port (214b) is arranged at the bottom of the corresponding at least one oil storage chamber (215), wherein the at least one oil storage chamber (215) is accommodated in the first condensation chamber (104) and The bottom of one of the second condensation chambers (105). 14.一种制冷空调系统,其特征在于:14. A refrigeration and air conditioning system, characterized in that: 所述制冷空调系统包括根据权利要求1-13中任意一项所述的内设油分离结构的冷凝器。The refrigerating and air-conditioning system includes the condenser with built-in oil separation structure according to any one of claims 1-13.
CN202310330795.1A 2023-03-30 2023-03-30 Condenser with built-in oil separation structure Pending CN116336700A (en)

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WO2024199497A1 (en) * 2023-03-30 2024-10-03 约克(无锡)空调冷冻设备有限公司 Condenser provided with oil separation structure therein
EP4549843A1 (en) * 2023-10-04 2025-05-07 Carrier Corporation A condenser vessel, system, and method for separating oil from an oil-refrigerant mixture
CN118499992A (en) * 2024-04-26 2024-08-16 约克(无锡)空调冷冻设备有限公司 Condenser
WO2025223234A1 (en) * 2024-04-26 2025-10-30 约克(无锡)空调冷冻设备有限公司 Condenser

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