CN116336700A - Condenser with built-in oil separation structure - Google Patents
Condenser with built-in oil separation structure Download PDFInfo
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B39/00—Evaporators; Condensers
- F25B39/04—Condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
- F25B43/02—Arrangements 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/09—Improving heat transfers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
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Abstract
Description
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
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
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
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
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
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
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
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
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
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
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。
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
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
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
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
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
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
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
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
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
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
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
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
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,
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
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
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
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)
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
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| CN202310330795.1A CN116336700A (en) | 2023-03-30 | 2023-03-30 | Condenser with built-in oil separation structure |
| PCT/CN2024/085055 WO2024199497A1 (en) | 2023-03-30 | 2024-03-29 | Condenser provided with oil separation structure therein |
| TW113112178A TW202441115A (en) | 2023-03-30 | 2024-03-29 | Condenser with built-in oil separation structure |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202310330795.1A CN116336700A (en) | 2023-03-30 | 2023-03-30 | Condenser with built-in oil separation structure |
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| CN202310330795.1A Pending CN116336700A (en) | 2023-03-30 | 2023-03-30 | Condenser with built-in oil separation structure |
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| Country | Link |
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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 |
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Also Published As
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| WO2024199497A1 (en) | 2024-10-03 |
| TW202441115A (en) | 2024-10-16 |
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