CN100458165C - Rotary compressor - Google Patents
Rotary compressor Download PDFInfo
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- CN100458165C CN100458165C CNB2006101399372A CN200610139937A CN100458165C CN 100458165 C CN100458165 C CN 100458165C CN B2006101399372 A CNB2006101399372 A CN B2006101399372A CN 200610139937 A CN200610139937 A CN 200610139937A CN 100458165 C CN100458165 C CN 100458165C
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C18/00—Rotary-piston pumps specially adapted for elastic fluids
- F04C18/30—Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members
- F04C18/34—Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F04C18/08 or F04C18/22 and relative reciprocation between the co-operating members
- F04C18/356—Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F04C18/08 or F04C18/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the outer member
- F04C18/3562—Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F04C18/08 or F04C18/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the outer member the inner and outer member being in contact along one line or continuous surfaces substantially parallel to the axis of rotation
- F04C18/3564—Rotary-piston pumps specially adapted for elastic fluids having the characteristics covered by two or more of groups F04C18/02, F04C18/08, F04C18/22, F04C18/24, F04C18/48, or having the characteristics covered by one of these groups together with some other type of movement between co-operating members having the movement defined in group F04C18/08 or F04C18/22 and relative reciprocation between the co-operating members with vanes reciprocating with respect to the outer member the inner and outer member being in contact along one line or continuous surfaces substantially parallel to the axis of rotation the surfaces of the inner and outer member, forming the working space, being surfaces of revolution
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C23/00—Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids
- F04C23/001—Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids of similar working principle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C23/00—Combinations of two or more pumps, each being of rotary-piston or oscillating-piston type, specially adapted for elastic fluids; Pumping installations specially adapted for elastic fluids; Multi-stage pumps specially adapted for elastic fluids
- F04C23/008—Hermetic pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C29/00—Component parts, details or accessories of pumps or pumping installations, not provided for in groups F04C18/00 - F04C28/00
- F04C29/0021—Systems for the equilibration of forces acting on the pump
- F04C29/0035—Equalization of pressure pulses
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C2240/00—Components
- F04C2240/40—Electric motor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C2240/00—Components
- F04C2240/50—Bearings
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
- Compressor (AREA)
Abstract
Description
技术领域 technical field
本发明涉及适用于对室内空气进行升降温的空调机等的冷冻循环装置中的回转压缩机。The present invention relates to a rotary compressor suitable for use in refrigeration cycle devices such as air conditioners for raising and lowering the temperature of indoor air.
背景技术 Background technique
以空调机为代表的冷冻循环装置,利用反复制冷剂的气化和液化的状态变化的冷冻循环而对空气或水等进行升降温。作为适用于该冷冻装置的制冷剂压缩机,已知有具有阶段性地压缩制冷剂的二级压缩机构的回转二级压缩机。例如,回转二级压缩机具有:压缩制冷剂的回转式的低压侧压缩部;相对于低压侧压缩部的压缩工序以反相位压缩制冷剂的回转式的高压侧压缩部;和具有与低压侧压缩部的制冷剂喷出口和高压侧压缩部的制冷剂吸引口连通的内部空间(以下称作喷出空间)的中间容器。A refrigerating cycle device typified by an air conditioner raises or lowers the temperature of air or water using a refrigerating cycle in which a refrigerant is repeatedly vaporized and liquefied. A two-stage rotary compressor having a two-stage compression mechanism for compressing refrigerant in stages is known as a refrigerant compressor suitable for this refrigeration system. For example, a rotary two-stage compressor has: a rotary low-pressure side compression section that compresses refrigerant; a rotary high-pressure side compression section that compresses refrigerant in an opposite phase to the compression process of the low-pressure side compression section; An intermediate container of an internal space (hereinafter referred to as a discharge space) in which the refrigerant discharge port of the side compression unit communicates with the refrigerant suction port of the high-pressure side compression unit.
在这样的回转二级压缩机的中间容器中,由于低压侧压缩部的喷出过程和高压侧压缩部的吸入过程的相位差(例如180度),而在喷出空间产生压力变动。即,反复进行:因向喷出空间喷出的制冷剂无法被吸入的状态而引起的压力增大、和因在向喷出空间喷出制冷剂之前开始了吸入的状态而引起的压力减少。In the intermediate vessel of such a rotary two-stage compressor, pressure fluctuations occur in the discharge space due to a phase difference (for example, 180 degrees) between the discharge process of the low-pressure side compressor and the suction process of the high-pressure side compressor. That is, a pressure increase due to a state in which the refrigerant discharged into the discharge space cannot be sucked and a pressure decrease due to a state in which suction starts before the refrigerant is discharged into the discharge space are repeated.
因此,为了减少在喷出空间产生的压力变动,而进行尽量地扩大喷出空间的容积。例如,提出了以下方案:通过使中间容器的内周壁在径方向上凹凸而形成为花瓣状,从而避开在中间容器的周壁安装的连接部件,同时极力确保喷出空间的容积、抑制喷出空间中的过压缩损失(例如专利文献1)。Therefore, in order to reduce the pressure fluctuation generated in the discharge space, the volume of the discharge space is enlarged as much as possible. For example, it has been proposed to make the inner peripheral wall of the intermediate container concave and convex in the radial direction to form a petal shape, thereby avoiding the connection member attached to the peripheral wall of the intermediate container, while ensuring the volume of the discharge space as much as possible, and suppressing the discharge. Overcompression loss in space (for example, Patent Document 1).
专利文献1:日本特开2003-166472号公报(第10页、第10图)Patent Document 1: Japanese Unexamined Patent Publication No. 2003-166472 (
但是,由于中间容器的喷出空间是没有遮蔽物的一样地扩大的空间,因此若向喷出空间喷出制冷剂,则由于有时在特定的转数下其脉动成分不会衰减而共振,因此存在喷出空间的压力变动增大的情况。尤其在压缩机的其特定的运转转数高时,压力变动有可能进一步增大。若压力变动增大,则由于压力变动引起的运动能量在制冷剂流路壁消散为摩擦热,能量损失增大,因此成为导致冷冻循环成绩系数(COP)降低的原因。专利文献1等以往的技术不考虑这样的压力变动,从而回转压缩机的能量效率存在应改善的余地。However, since the discharge space of the intermediate container is a uniformly enlarged space without a shield, if the refrigerant is discharged into the discharge space, the pulsation component may resonate without attenuation at a specific number of revolutions. There are cases where pressure fluctuations in the discharge space increase. Especially when the specific operating speed of the compressor is high, the pressure fluctuation may further increase. If the pressure fluctuation increases, the kinetic energy due to the pressure fluctuation will be dissipated as frictional heat on the refrigerant flow path wall, and the energy loss will increase, which will cause a decrease in the coefficient of performance (COP) of the refrigeration cycle. Conventional technologies such as Patent Document 1 do not consider such pressure fluctuations, and there is room for improvement in the energy efficiency of the rotary compressor.
发明内容 Contents of the invention
本发明的课题在于,实现一种更适合于对在中间容器的喷出空间产生的压力变动进行抑制而改善能量效率的回转压缩机。An object of the present invention is to realize a rotary compressor more suitable for suppressing pressure fluctuations generated in a discharge space of an intermediate container and improving energy efficiency.
为了解决上述课题,本发明的回转压缩机,其特征在于,In order to solve the above-mentioned problems, the rotary compressor of the present invention is characterized in that,
包括:include:
回转式低压侧压缩部,其对制冷剂进行压缩;Rotary low-pressure side compression part, which compresses the refrigerant;
回转式高压侧压缩部,其相对于该低压侧压缩部的压缩工序以反相位对制冷剂进行压缩;和a rotary high-pressure side compression section that compresses the refrigerant in anti-phase with respect to the compression process of the low-pressure side compression section; and
中间容器,其连通于所述低压侧压缩部的制冷剂喷出口和所述高压侧压缩部的制冷剂吸引口,an intermediate container communicating with the refrigerant discharge port of the low-pressure side compression unit and the refrigerant suction port of the high-pressure side compression unit,
所述中间容器的内部空间被隔离部件划分为至少两个空间,在一方的空间连通所述低压侧压缩部的制冷剂喷出口和所述高压侧压缩部的制冷剂吸引口,在所述隔离部件形成连结所述两个空间的制冷剂流路。The inner space of the intermediate container is divided into at least two spaces by a partition member, and the refrigerant discharge port of the low-pressure side compression part and the refrigerant suction port of the high-pressure side compression part are connected in one space, and the partition The component forms a refrigerant flow path connecting the two spaces.
在这种情况下,中间容器可以形成为,具有:圆板形的端板部;外壁部,其从端板部的周缘部在轴方向上立起而划分喷出空间的周方向;筒形的副轴承,其在端板部的中央在轴方向上立起;和闭塞板,其与端板部相面对而闭塞外壁部的前端侧开口。此处的隔离部件是从副轴承架设在外周壁而在端板部的板面立起设置的梁,该梁可以形成为,从端板部的轴方向尺寸小于外壁部,在与闭塞板之间形成制冷剂流路。In this case, the intermediate container may be formed to have: a disc-shaped end plate portion; an outer wall portion that rises from the peripheral portion of the end plate portion in the axial direction to define the circumferential direction of the discharge space; A sub-bearing standing upright in the axial direction at the center of the end plate portion; and a closing plate facing the end plate portion and closing the opening on the front end side of the outer wall portion. The spacer here is a beam erected from the sub-bearing on the outer peripheral wall and erected on the plate surface of the end plate. A refrigerant flow path is formed between them.
即,低压侧压缩部的制冷剂喷出口和高压侧压缩部的制冷剂吸引口连通的一方的空间,成为制冷剂的主流流通的主流侧空间。另外,在主流侧空间经由隔离部件连通的另一空间,成为制冷剂的脉动成分流入流出的反主流侧空间。That is, the space where the refrigerant discharge port of the low-pressure side compression unit communicates with the refrigerant suction port of the high-pressure side compression unit serves as the main flow side space through which the main flow of the refrigerant flows. In addition, another space communicated with the main flow side space via the partition member serves as an anti-main flow side space into which the pulsation component of the refrigerant flows in and out.
由此,若从低压侧压缩部向中间容器喷出制冷剂,则制冷剂的主流在流过主流侧空间之后被吸引到高压侧压缩部,但是该过程中的制冷剂的脉动成分的一部分或全部,在反主流侧空间流入流出。即,反主流侧空间发挥作为防止制冷剂的脉动成分的共振的所谓的空洞式的共鸣器即缓冲器的作用。由此,由于抑制脉动成分在喷出空间中的共振,因此抑制在喷出空间产生的压力变动。其结果是,能降低由于压力变动而引起的能量损失并改善能量效率。Thus, when the refrigerant is discharged from the low-pressure side compression unit to the intermediate tank, the main flow of the refrigerant is sucked into the high-pressure side compression unit after flowing through the main flow side space, but a part of the pulsation component of the refrigerant in this process or All, flow in and out of the space on the counter-mainstream side. That is, the anti-mainstream side space functions as a so-called cavitated resonator, ie, a buffer, which prevents resonance of the pulsation component of the refrigerant. Accordingly, since the resonance of the pulsation component in the discharge space is suppressed, the pressure fluctuation generated in the discharge space is suppressed. As a result, energy loss due to pressure fluctuations can be reduced and energy efficiency can be improved.
另外,优选的是,副轴承是由端板部侧的外径大于前端侧的外径的扩径部形成的,隔离部件的从端板部的轴方向尺寸小于扩径部。In addition, it is preferable that the sub-bearing is formed by an enlarged diameter portion whose outer diameter on the end plate side is larger than that on the front end side, and that the axial dimension of the spacer from the end plate portion is smaller than the enlarged diameter portion.
另外,隔离部件在前端侧形成有:与端板部的板面平行的平行部;随着从平行部的内周缘朝向轴方向、而向副轴承侧倾斜的内周侧锥部;和随着从平行部的内周缘朝向轴方向、而向外壁部侧倾斜的外周侧锥部,制冷剂流路可以形成为由平行部、内周侧锥部、外周侧锥部、和闭塞板划分出的截面梯形的开口。即,制冷剂流路,随着朝向轴方向而开口宽度逐渐增大等,可使开口宽度以某一宽度变化。换言之,通过调整内周侧锥部或外周侧锥部的倾斜角度,能够微调整制冷剂流路的流路截面积的大小。因此,并不局限于特定的运转转数,而能够在大范围的运转转数内降低压力变动。In addition, the spacer member is formed on the front end side: a parallel portion parallel to the plate surface of the end plate portion; an inner peripheral tapered portion inclined toward the sub-bearing side from the inner peripheral edge of the parallel portion toward the axial direction; and From the inner peripheral edge of the parallel portion toward the axial direction, the outer peripheral side taper portion inclined toward the outer wall portion side, the refrigerant flow path can be formed to be divided by the parallel portion, the inner peripheral side taper portion, the outer peripheral side taper portion, and the closing plate. Openings with trapezoidal cross-section. That is, the opening width of the refrigerant channel can be changed to a certain width such as gradually increasing the opening width toward the axial direction. In other words, by adjusting the inclination angle of the inner tapered portion or the outer tapered portion, the size of the cross-sectional area of the refrigerant flow path can be finely adjusted. Therefore, the pressure fluctuation can be reduced over a wide range of operating revolutions without being limited to a specific operating revolution.
另外,中间容器,可以将从副轴承架设在外周壁而在端板部的板面立起设置的增强用梁,设置于由所述隔离部件划分出的另一方的空间。此处的增强用梁形成为,从端板部的轴方向尺寸小于隔离部件。由此,能够提高中间容器的刚性,因此能够抑制由于基于压力负载或组装时的缔结要素的负载引起的变形。In addition, in the intermediate container, a reinforcement beam erected on the plate surface of the end plate portion from the sub-bearing to the outer peripheral wall may be installed in the other space partitioned by the spacer. Here, the reinforcing beam is formed so that the dimension in the axial direction from the end plate portion is smaller than that of the spacer member. Thereby, the rigidity of the intermediate container can be increased, so that deformation due to a pressure load or a load of the connecting elements at the time of assembly can be suppressed.
根据本发明,能够实现更适合于对在中间容器的喷出空间产生的压力变动进行抑制而改善能量效率的回转压缩机。According to the present invention, it is possible to realize a rotary compressor more suitable for suppressing pressure fluctuations generated in the discharge space of the intermediate container and improving energy efficiency.
附图说明 Description of drawings
图1是表示适用本发明的一个实施方式的回转压缩机的结构的纵剖面图;FIG. 1 is a longitudinal sectional view showing the structure of a rotary compressor to which one embodiment of the present invention is applied;
图2是表示图1的低压侧压缩部和高压侧压缩部的图;Fig. 2 is a diagram showing a low-pressure side compression section and a high-pressure side compression section of Fig. 1;
图3是从下侧观察图1的中间容器的仰视图;Fig. 3 is a bottom view of the intermediate container of Fig. 1 viewed from the lower side;
图4是图3的中间容器的A-A剖面图;Fig. 4 is the A-A sectional view of the intermediate container of Fig. 3;
图5是表示图1的中间容器的喷出空间中的制冷剂的流向的图;Fig. 5 is a diagram showing the flow of refrigerant in the discharge space of the intermediate container of Fig. 1;
图6是将图1的中间容器的压力振幅与以往技术相比较而表示的图;Fig. 6 is a graph showing a comparison of the pressure amplitude of the intermediate vessel of Fig. 1 with the prior art;
图7是图3的中间容器的B-B剖面图;Fig. 7 is the B-B sectional view of the intermediate container of Fig. 3;
图8是图3的中间容器的C-C剖面图;Fig. 8 is a C-C sectional view of the intermediate container of Fig. 3;
图9是图3的中间容器的D-D剖面图;Fig. 9 is a D-D sectional view of the intermediate container of Fig. 3;
图10是图1或图4的盖的俯视图;Figure 10 is a top view of the cover of Figure 1 or Figure 4;
图11是图1或图4的弹性体的剖面图;Fig. 11 is a sectional view of the elastomer of Fig. 1 or Fig. 4;
图12是表示适用本发明的一个实施方式的空调机的冷冻循环成绩系数(COP)的变化率的测量结果的图;Fig. 12 is a graph showing the measurement results of the rate of change of the refrigeration cycle coefficient of performance (COP) of the air conditioner to which the embodiment of the present invention is applied;
图13是表示适用本发明的中间容器的其他的第一例的剖面图;Fig. 13 is a sectional view showing another first example of the intermediate container to which the present invention is applied;
图14是表示适用本发明的中间容器的其他的第二例的剖面图。Fig. 14 is a sectional view showing another second example of the intermediate container to which the present invention is applied.
图中:In the picture:
1-回转压缩机;10-低压侧压缩部;12-高压侧压缩部;14-制冷剂喷出口;16-制冷剂吸引口;18-中间容器;20-喷出空间;20a-主流侧空间;20b-反主流侧空间;20c-制冷剂流路;22-隔离部件。1-rotary compressor; 10-low-pressure side compression part; 12-high-pressure side compression part; 14-refrigerant injection port; 16-refrigerant suction port; 18-intermediate container; 20-spray space; 20a-mainstream side space ; 20b-space on the side of the anti-main flow; 20c-refrigerant flow path; 22-isolating components.
具体实施方式 Detailed ways
参照附图对适用本发明的回转压缩机的一个实施方式进行说明。图1是表示本实施方式的回转压缩机的结构的纵剖面图。图2是表示图1的低压侧压缩部和高压侧压缩部的图。图3是从下侧观察图1的中间容器的仰视图。图4是图3的中间容器的A-A剖面图。One embodiment of a rotary compressor to which the present invention is applied will be described with reference to the drawings. FIG. 1 is a longitudinal sectional view showing the structure of a rotary compressor according to this embodiment. FIG. 2 is a diagram showing a low-pressure side compression unit and a high-pressure side compression unit in FIG. 1 . Fig. 3 is a bottom view of the intermediate container of Fig. 1 viewed from the lower side. Fig. 4 is an A-A sectional view of the intermediate container of Fig. 3 .
如图1所示,适用于空调机等冷冻循环装置的回转压缩机1,具有阶段性地压缩制冷剂的二级压缩机构。更具体地说,回转压缩机1具有:压缩制冷剂(例如R410A)的回转式的低压侧压缩部10;相对于低压侧压缩部10的压缩工序以反相位压缩制冷剂的回转式的高压侧压缩部12;和具有与低压侧压缩部10的制冷剂喷出口14和高压侧压缩部12的制冷剂吸引口16连通的内部空间20(以下称为喷出空间20)的中间容器18。As shown in FIG. 1 , a rotary compressor 1 applied to a refrigeration cycle apparatus such as an air conditioner has a two-stage compression mechanism for compressing refrigerant in stages. More specifically, the rotary compressor 1 has: a rotary low-
在此,适用于回转压缩机1的中间容器18,如图2~图4所示,喷出空间20例如被隔离部件22区划为两个空间20a、20b。并且,在一方的空间20a(以下称为主流侧空间20a)连通低压侧压缩部10的制冷剂喷出口14和高压侧压缩部12的制冷剂吸引口16,隔离部件22形成有连结主流侧空间20a和另一方的空间20b(以下称为反主流侧空间20b)的制冷剂流路20c。Here, applying to the
即,中间容器18具有:连通低压侧压缩部10的制冷剂喷出口14和高压侧压缩部12的制冷剂吸引口16的主流侧空间20a;和经由主流侧空间20a和隔离部件22而被区分的反主流侧空间20b,此处的隔离部件22形成有连通主流侧空间20a和反主流侧空间20b的开口即制冷剂流路20c。由此,由于反主流侧空间20b发挥作为防止制冷剂的脉动成分的共振的所谓空洞式的共鸣器即缓冲器的作用,因此能抑制在喷出空间20产生的压力变动而提高能量效率。That is, the
进一步详细地对本实施方式的回转压缩机1进行说明。如图1所示,回转压缩机1在密闭容器26中收纳有:电动机24、端板部38、高压侧压缩部12、中间隔离板13、低压侧压缩部10、以及中间容器18。具体而言,密闭容器26经由端板部38而被分为:配置有电动机24的密闭空间39、和配置有低压侧压缩部10和高压侧压缩部12等的旋转压缩要素用的空间。旋转压缩要素侧,从电动机24侧依次在轴方向上层叠高压侧压缩部12、中间隔离板13、低压侧压缩部10、中间容器18且由缔结要素15(例如为螺栓)一体固定。The rotary compressor 1 of this embodiment will be described in further detail. As shown in FIG. 1 , the rotary compressor 1 houses a
密闭容器26具有:筒形的躯体部28;对躯体部28的电动机24侧的开口进行闭锁的大致碗状的盖部29;对躯体部28的低压侧压缩部10侧的开口进行闭锁的底部30。盖部29配置有喷出压缩成高压Pd的制冷剂的喷出管31。此外,为了便于说明,将躯体部28的轴方向适当称作纵方向,将与轴方向正交的水平方向适当称作横方向。另外,将从躯体部28在轴方向上朝盖部29侧的方向适当称作上侧,将从躯体部28在轴方向上朝底部30侧的方向适当称作下侧。The
电动机24被配置于在密闭容器26内的上侧被端板部38区分的密闭空间39。该电动机24具有:沿着密闭容器26的内周面以环状安装的作为固定子的定子32;在定子32的内侧留有间隙地被插入配置的作为旋转子的转子34;上端部被轴安装于转子34的旋转轴36。旋转轴36在前端侧的部分设置有两个偏心部、即高压缩用的偏心部42和低压缩用的偏心部44。此处的偏心部42,在比偏心部44更靠向轴方向上侧错开位置而设置,其偏心方向相对于偏心部44是相反方向、即相位差例如为180度。The
端板部38是沿着密闭容器26的内周面通过焊接等而被固定的环状的板部件。该端板部38,轴支承旋转轴36的圆筒状的主轴承40向上方立起而形成于中央。另外端板部38形成有在厚度方向上贯通了的喷出口46。在该喷出口46配置有喷出阀48。此外,端板部38在其上端面的中央配置有喷出盖50。喷出盖50是包围旋转轴36的中空环状部件,其内部空间与喷出口46连通。另外,喷出盖50在电动机24侧的部分形成有喷出口51。The
高压侧压缩部12被端板部38和中间隔离板13夹持而配置。该高压侧压缩部12,如图1及图2所示,具有:近似圆筒状的汽缸52,其具有与密闭容器26的内径相同的外径的部分;圆筒状的辊54,其嵌合于位于汽缸52内的偏心部42的外周;翼56,其前端抵接于辊54的外周面、且能够进退地被弹力施加机构(例如为螺旋弹簧)支承于汽缸52;和制冷剂吸引口16,其在径方向上贯通而连通于汽缸52内。此处的汽缸52被端板部38的下端面和中间隔离板13的上端面夹持,堵塞住内部空间58。并且翼56,通过在接触于与偏心部42的偏心运动相配合而旋转的辊54的外周面的状态下、进行进退运动,从而将汽缸52的内部空间58区分为制冷剂压缩室和制冷剂吸引室。此外,制冷剂吸引室经由连接于制冷剂吸引口16的中间流路60,与中间容器18的喷出空间20连通。另外,制冷剂压缩室经由形成于端板部38的喷出口46与密闭空间39连通。The high-pressure-
中间隔离板13是被夹持在高压侧压缩部12和低压侧压缩部10之间的闭塞板。该中间隔离板13,在中央形成有插通旋转轴36的贯通孔。该贯通孔的轴心与旋转轴大致一致。The
低压侧压缩部10被中间隔离板13和中间容器18夹持而配置。该低压侧压缩部10,如图1及图2所示,具有:近似圆筒状的汽缸62,其具有与密闭容器26的内径相同的外径的部分;圆筒状的辊64,其嵌合于位于汽缸62内的偏心部44的外周;翼66,其前端抵接于辊64的外周面、且能够进退地被弹力施加机构(例如为螺旋弹簧)支承于汽缸62;和制冷剂吸引口70,其在径方向上贯通而连通于汽缸62内。此处的汽缸62被中间隔离板13的下端面和中间容器18的上端面夹持,堵塞住内部空间71。并且翼66,通过在接触于与偏心部44的偏心运动相配合而旋转的辊64的外周面的状态下、进行进退运动,从而将汽缸62的内部空间71区分为制冷剂压缩室和制冷剂吸引室。制冷剂吸引室经由与制冷剂吸入口70连接的制冷剂配管72,流入从冷冻循环装置的仪器类(例如为制冷剂蒸发器)排出的气体制冷剂。制冷剂压缩室连通于中间容器18内。The low-pressure
中间容器18,是暂时储存从低压侧压缩部10喷出的制冷剂的筒形容器。更具体地说,如图1所示,中间容器18是凹形的容器,其具有:与低压侧压缩部10的下端面相接的圆板状的端板部74;在端板部74的中央向下方立起形成的圆筒状的副轴承43;从端板部74的周缘部向下方突出来区分喷出空间20的周方向的外壁部78;和在水平方向上贯通外壁部78的制冷剂排出口79。即,中间容器18是相对于低压侧压缩部10侧朝反方向开口的凹形的容器。此外,端板部74,在厚度方向上贯通而形成有:与低压侧压缩部10的制冷剂压缩室连通的制冷剂喷出口14。制冷剂喷出口14配置有喷出阀80。另外,制冷剂排出口79配置有:将喷出空间20与高压侧压缩部12的制冷剂吸引室连通的中间流路60。这样的中间容器18配置有:堵塞下端面的开口的环状板的闭塞板即盖82。The
对于这样构成的回转压缩机1的基本动作进行说明。图1的箭头表示作为工作流体的气体制冷剂的流向。从冷冻循环装置的仪器类(例如为制冷剂蒸发器)排出的低压Ps的气体制冷剂,经由制冷剂配管72被吸引到低压侧压缩部10的汽缸62内。被吸引了的气体制冷剂,通过辊64的偏心旋转而在汽缸62的制冷剂压缩室内被压缩。若该制冷剂压缩室的压力达到预定的中间压力Pm,则制冷剂压缩室的气体制冷剂通过喷出阀80的开口经由制冷剂喷出口14而被喷出到喷出空间20。此处的喷出空间20,由于是隔离于中间容器18内的空间即从密闭容器26内的密闭空间39隔离的空间,因此其内部压力基本上变为中间压Pm。The basic operation of the rotary compressor 1 configured in this way will be described. Arrows in FIG. 1 indicate the flow of gas refrigerant as a working fluid. Low-pressure Ps gas refrigerant discharged from equipment of the refrigeration cycle apparatus (for example, a refrigerant evaporator) is sucked into the
喷出到喷出空间20的气体制冷剂,经由中间流路60,从制冷剂吸引口16被吸引到高压侧压缩部12的汽缸52内。被吸引了的气体制冷剂,通过辊54的偏心旋转而在汽缸52的制冷剂压缩室内被压缩。若该制冷剂压缩室的压力达到预定的高压Pd,则制冷剂压缩室的气体制冷剂通过喷出阀48的开口而从喷出口46喷出。被喷出后的气体制冷剂经由喷出盖50的喷出口51向密闭空间39流出。流出了的气体制冷剂,在流过电动机24的间隙之后,从喷出管31被喷出到冷冻循环装置的仪器类(例如为制冷剂冷凝器)。The gas refrigerant discharged into the
在这样的制冷剂的阶段性的压缩过程中,本实施方式,通过在中间容器18中具备具有空洞式的共鸣功能的反主流侧空间20b,从而降低由于低压侧压缩部10的喷出过程和高压侧压缩部12的吸入过程的相位差而引起的喷出空间20的压力变动。此外,压力变动,与制冷剂的音速和低压侧压缩部10的制冷剂喷出量,尤其与回转压缩机1的运转转数和喷出空间20的容积有关,但是本实施方式主要抑制与制冷剂的音速密切相关的制冷剂脉动成分的共振。In the stepwise compression process of the refrigerant, in the present embodiment, the
在此,参照图2~图4进一步对中间容器18进行详细的说明。如图2所示,中间容器18的喷出空间20,被隔离部件22分割为主流侧空间20a和反主流侧空间20b。隔离部件22形成有连通主流侧空间20a和反主流侧空间20b的开口即制冷剂流路20c。即,喷出空间20被分割为:以制冷剂流路20c为边界、制冷剂主要流过的主流侧空间20a、和主要流过制冷剂的时间变动成分的反主流侧空间20b。并且,主流侧空间20a跨过隔离部件22与反主流侧空间20b连通。此处的反主流侧空间20b,因制冷剂经由制冷剂流路20c而出入,起到空洞式的共鸣器的功能。Here, the
更具体地说,中间容器18是铸造部件或铁系的烧结部件,如图3及图4所示,端板部74、外壁部78、和副轴承43被一体成型。即,中间容器18形成为一端面在盖82侧开口的大致凹状。More specifically, the
端板部74是形成有台座84的圆板,所述台座84用于设置低压侧压缩部10的制冷剂喷出口14及喷出阀80。另外,外壁部78形成为大致圆筒形状,划分喷出空间20的周方向。该外壁部78,与端板部74的板面平行地形成的接触面81与盖82相接。此外,接触面81通过模具成型或切削、研磨而形成。另外,外壁部78,在轴方向上贯通而形成有多个(例如为四个)的缔结要素15用的孔86。这些多个孔86以等间隔形成在同一圆周上。另外,外壁部78形成为使内周壁在径方向上凹凸的花瓣状。更具体地说,外壁部78的内周壁,向径方向内侧凹状地形成配置有孔86的部分,一个孔86和与该孔相邻的另一孔86之间的部分向径方向外侧凸状地形成。通过如此将外壁部78的内周壁形成为花瓣状,从而能尽量避开孔86并确保喷出空间20的容积。另外,此处的喷出空间20的容积大于低压侧压缩部10的制冷剂喷出量。因此,在从低压侧压缩部10向喷出空间20喷出制冷剂时,能够抑制喷出空间20中的过压缩损失。The
副轴承43在端板部74的中央以近似圆筒状地立起而形成。该副轴承43在外径侧的面即外周壁上形成有台阶部。即,副轴承43是由端板部74侧的外径大于盖82侧的外径的扩径部形成的。该台阶部具有与盖82的平面相对的平坦面88。平坦面88是高度小于外壁部78的接触面81的凹部。在形成于平坦面88和盖82之间的间隙内夹入有弹性体90。此外,本实施方式中所称的高度是以端板部74为基准的轴方向的尺寸。The sub-bearing 43 is formed to rise in a substantially cylindrical shape at the center of the
另外,副轴承43通过端板部74侧的内径小于盖82侧的内径而形成有台阶部。即,副轴承43,在端板部74侧形成轴支承旋转轴36的接触部92,在盖82侧形成没有对旋转轴36进行轴支承的非接触部94。在此,在副轴承43的外周壁形成的平坦面88位于非接触部94的外周部分。由此,由于来自盖82或弹性体90的压力负载或夹紧负载被非接触部94吸收,因此能降低副轴承43和旋转轴36之间的摩擦力。此外,平坦面88作为中间容器18的一部分而被一体成型,但是也可以通过切削等机械加工来形成。In addition, in the sub-bearing 43 , the inner diameter on the side of the
并且,本实施方式的中间容器18,如图3及图4等所示,形成有隔离部件22,该隔离部件22将喷出空间20分割为主流侧空间20a和反主流侧空间20b。隔离部件22,如图3所示,是从副轴承43在径方向上架设在外周壁78上而立起设置于端板部74的下端面上的梁。即,隔离部件22是连结副轴承43的外侧壁和外壁部78的内侧壁的大致矩形剖面的堰板。此外,在本实施方式中,虽然在连结副轴承43的中心和连结用的孔86的中心的直线上形成两个梁,但是也可以从副轴承43呈放射状地形成两个以上的梁。总之,只要通过两个以上的梁将喷出空间20划分为主流侧空间20a和反主流侧空间20b即可。Furthermore, the
这样的隔离部件22,如图4所示,在与盖82之间形成开口剖面为大致梯形的制冷剂流路20c。更具体地说,隔离部件22在前端侧形成有:平行部22a,其高度M小于外壁部78的接触面81、并与端板部74的下端面平行;内周侧锥部22b,其随着从平行部22a的内周缘朝向轴方向而向副轴承43侧倾斜;以及外周侧锥部22c,其随着从平行部22a的外周缘朝向轴方向而向外壁部78侧倾斜。此处的内周侧锥部22b是连结平行部22a的内周缘和平坦面88的外周缘的倾斜面。另外,外周侧锥部22c是将平行部22a的外周缘连结于外壁部78的内周缘的倾斜面。即,通过平行部22a、内周侧锥部22b、外周侧锥部22c、和盖82划分出的空间成为制冷剂流路20c。此外,此处的内周侧锥部22b和外周侧锥部22c的倾斜角度,相对于旋转轴36例如为45度,但是可根据需要而变更。即,需要调整制冷剂流路20c的流路截面积S时,只要改变平行部22a的高度、或内周侧锥部22b及外周侧锥部22c的倾斜角度即可。As shown in FIG. 4 , such a
图5是表示图1的中间容器18的喷出空间20中的制冷剂的流向的图。如图5所示,若从低压侧压缩部10经由制冷剂喷出口14向中间容器18喷出气体制冷剂,则制冷剂的主流在流过了主流侧空间20a之后,经由制冷剂排出口79而被吸引到高压侧压缩部12,但是制冷剂的脉动成分即制冷剂变动成分的一部分或全部,在反主流侧空间20b流入流出。即,反主流侧空间20b,发挥作为防止制冷剂的脉动成分的共振的所谓的空洞式的共鸣器即缓冲器的作用。由此,由于抑制在喷出空间20中的脉动成分的共振,因此抑制在喷出空间20产生的压力变动的增大。其结果是,降低因压力变动而引起的能量损失,能提高能量效率。FIG. 5 is a diagram showing the flow of refrigerant in the
总之,喷出空间20,由于具有以制冷剂流路20c为边界并起到空洞式的共鸣器的作用的反主流侧空间20b,因此抑制在喷出空间20产生的中间压力Pm的压力变动。In short, since the
图6是将本实施方式的中间容器18的压力振幅与以往技术相比较而表示的图。图6的横轴表示回转压缩机1的运转转数(min-1),纵轴表示中间容器18对运转转数的压力振幅(MPa)。如图6所示,随着运转转数从最低转数增大、压力振幅增大。并且,在以往技术中,运转转数例如在4000(min-1)~6000(min-1)的范围内压力振幅变得极大。即,由于一般的运转转数的范围例如为1000(min-1)~8000(min-1),因此在以往技术中,可知压力振幅相对地在高旋转侧增大。这点,根据本实施方式,由于能降低高旋转侧的压力振幅的极大值,因此提高冷冻循环成绩系数(COP),抑制在回转压缩机1中产生的噪音及振动。FIG. 6 is a graph comparing the pressure amplitude of the
另外,根据本实施方式,由于使制冷剂流路20c的开口宽度随着朝向轴方向而使其逐渐增大等,使其开口宽度以某一宽度变化,因此不限于一定的运转转数(频率)而可以在大范围的运转转数中降低压力变动。更具体地说,关于本实施方式的中间容器18,通过改变隔离部件22的平行部22a的高度N,或改变内周侧锥部22b及外周侧锥部22c的倾斜角,从而能微调整制冷剂流路20c的流路截面积S的大小。例如,若使流路截面积S变小,则在高旋转侧的范围内发挥反主流侧空间20b的共鸣功能。另外,若使流路截面积S增大,则在低旋转侧的范围内发挥反主流侧空间20b的共鸣功能。但是,若使流路截面积S过度增大,则由于喷出空间20与一样扩大的以往的空间实际上相同,因此存在没有发挥共鸣功能而无法充分地抑制压力变动的情况。因此,对于流路截面积S的大小,优选形成为规定面积以上。流路截面积S的适当值例如可通过实际测量来求出。In addition, according to the present embodiment, since the opening width of the
另外,本实施方式的中间容器18,如图3及图4所示,在反主流侧空间20b设置有作为增强部件的第二梁96。该梁96,在从副轴承43在径方向上架设于外周壁78而一体形成在端板部74的下端面的这一点上,与隔离部件22类似,但是在具有高度L比隔离部件22的平行面22a的高度N小的平行面的这一点上不同。通过设置这样的梁96,由于能够提高中间容器18的刚性,因此能够抑制由于基于压力负载或组装时的缔结要素15的负载而引起的变形。In addition, in the
进一步地,对中间容器18进行说明。图7是图3的中间容器的B-B剖面图。该图7是表示B-B剖面中的隔离部件22的形态的图。如图7所示,隔离部件22形成为随着朝向端板部74、基部向下部扩大。即,隔离部件22在与端板部74的结合部形成有作为增强部件的腿部98。由此,即使在通过减小隔离部件22的厚度即制冷剂流路20c的流路长度来降低摩擦损失的情况下,也能确保隔离部件22的刚性。Further, the
图8是图3的中间容器的C-C剖面图。该图8是表示C-C剖面中的梁96的形态的图。如图8所示,梁96形成为随着朝向端板部74、基部向下部扩大。即,梁96在与端板部74的结合部形成有作为增强部件的腿部100。由此,即使在通过减小梁96的厚度来降低反主流侧空间20b的制冷剂通气阻力的情况下,由于也能确保梁96的刚性,因此能降低中间容器18的变形。Fig. 8 is a C-C sectional view of the intermediate container of Fig. 3 . This FIG. 8 is a diagram showing the form of the
图9是图3的中间容器的D-D剖面图。即,图9示出了外壁部78的接触面81的高度M、隔离部件22的平行部22a的高度N、和梁96的高度L的关系。如图9所示,通过使平行部22a的高度N小于接触面81的高度M,确保制冷剂流路20c的流路截面积S。另外,通过使梁96的高度L小于平行部22a的高度N,而能提高中间容器18的刚性并可确保反主流侧空间20b的容积V。Fig. 9 is a D-D sectional view of the intermediate container of Fig. 3 . That is, FIG. 9 shows the relationship between the height M of the
图10是图1或图4的盖82的俯视图。如图10所示,盖82是通过冲压加工被冲裁成型了的圆板形的部件。该盖82形成有多个(例如为四个)在板厚方向上贯通的缔结要素15用的孔102。这些多个孔102以等间隔形成在同一圆周上,与中间容器18的孔86的位置及个数相对应。另外,盖82在板面中央形成有在板厚方向贯通的孔104。该孔104用于通过副轴承40的非接触部94的前端部分。更具体地说,如图1及图4所示,孔104形成为其直径与副轴承40的非接触部94的外径相同。即,若将非接触部94的前端部分嵌入到孔104,则盖82与非接触部94接触。并且,通过在盖82和平坦面88之间的间隙里夹入弹性体90,从而形成密封面。FIG. 10 is a top view of the
图11是图1或图4的弹性体90的剖面图。如图11所示,弹性体90是对铜部件进行冲压加工而形成的大致环状圆锥台形的碟形弹簧。该弹性体90,如图4所示,沿着副轴承40的前端外周被配置在平坦面88上。即,弹性体90被夹入在平坦面88和盖82的间隙内。在配置弹性体90时,弹性体90的底面与盖82的平面接触。作为此处的弹性体90,可以适用圆板形的垫圈(gasket)或O形环等。但在使用垫圈时,最好适用更容易变形的橡胶材或树脂材。FIG. 11 is a cross-sectional view of the
图12是表示控制了制冷剂流路20c的流路截面积S时的冷冻循环成绩系数(COP)的变化率的测量结果的图。图12的横轴表示反主流侧空间20b的容积V(mm3)对制冷剂流路20c的流路截面积S(mm2)的比(S/V)。纵轴表示空调机的COP相对于比(S/V)的变化率(%)。此外,此处的COP是指用输入除空调机的调节能力。另外,以比(S/V)为零时的COP作为基准而进行了相对评价。FIG. 12 is a graph showing the measurement results of the rate of change in the coefficient of performance (COP) of the refrigeration cycle when the channel cross-sectional area S of the
如图12所示,空调机的COP的变化率随着比(S/V)从零增加而急剧增大,以某一比(S/V)为边界而逐渐减少。即,在使比(S/V)从零增加的最初,由于随着比(S/V)的增加而通过流路截面积S(mm2)的制冷剂量增加,所以发挥反主流侧空间20b的共鸣功能,因此抑制喷出空间20的压力变动的结果是提高了空调机的COP。但是,在使比(S/V)过度增加到超过某一值时,由于反主流侧空间20b和主流侧空间20a的区划变得模糊,所以喷出空间20变得与一样扩大的以往的空间实质上相同,因此不能充分地抑制喷出空间20的压力变动,空调机的COP降低。另外,随着比(S/V)增大,由于基于隔离部件22的端板部74的刚性提高的效果下降,因此由于端板部74的变形而引起的机械损失增大。鉴于这样的情况,希望的是本实施方式的比(S/V)在例如以0.1×10-2(mm-1)为下限值、例如以2.0×10-2(mm-1)为上限值的范围内。若在该范围内,能够得到在一般的空调机的性能测定装置的测定误差范围的例如1%以上的COP提高效果。As shown in FIG. 12 , the rate of change of the COP of the air conditioner increases sharply as the ratio (S/V) increases from zero, and gradually decreases with a certain ratio (S/V) as a boundary. That is, at the beginning of increasing the ratio (S/V) from zero, since the amount of refrigerant passing through the flow path cross-sectional area S (mm 2 ) increases as the ratio (S/V) increases, the anti-main
以上,说明了适用本发明的回转压缩机1的一个实施方式,但是并不局限于此。As mentioned above, although one embodiment of the rotary compressor 1 to which this invention is applied was demonstrated, it is not limited to this.
图13是表示本实施方式的中间容器18的其他的第一例子的剖面图。如图13所示,本例的中间容器18,在副轴承106的外周壁在轴方向上以相同的直径形成的这一点上,与在副轴承43的外周壁形成了具有平坦面88的台阶部的图4的方式不同。即,本例的中间容器18是使图4的平坦面88的高度与连接面81对合的容器。因此,副轴承106的下端面108的外周缘部与盖82的平面接触。此处的隔离部件22形成为,具有:高度小于副轴承106的下端面108的平行部22a;将平行部22a的内周缘连结于下端面108的外周缘的内周侧锥部22g;和将平行部22a的外周缘连结于外壁部78的内周缘的外周侧锥部22c。由此,能够确保在隔离部件22和盖82的平面之间形成的制冷剂流路20c的流路截面积S。此外,内周侧锥部22g的倾斜角度大于外周侧锥部22c,但是并不局限于此,根据需要进行调整即可。FIG. 13 is a cross-sectional view showing another first example of the
图14是表示本实施方式的中间容器的其他的第二例子的剖面图。如图14所示,本例的中间容器18,在制冷剂流路20c形成于隔离部件22的一部分的这一点上,与制冷剂流路20c形成于隔离部件22的整个区域的图13的方式不同。即,本例的中间容器18,在制冷剂流路20c的宽度小于隔离部件22的这一点上,与制冷剂流路20c的宽度与隔离部件22相同的图12的方式不同。换言之,隔离部件22的前端面的外周缘部与盖82的平面接触。此处的隔离部件22形成为,具有:高度小于副轴承106的下端面108的平行部22a;将平行部22a的内周缘连结于下端面108的外周缘的内周侧锥部22g;和从平行部22a的外周缘向盖82倾斜的外周侧锥部22h。由此,由于隔离部件22的刚性提高,所以其结果是中间容器18的刚性提高。Fig. 14 is a cross-sectional view showing another second example of the intermediate container of the present embodiment. As shown in FIG. 14 , the
以上,根据本实施方式,通过在中间容器18具有空洞式的共鸣功能,从而抑制中间容器18内的中间压力Pm的压力脉动,因此提高冷冻循环成绩系数(COP),能抑制在回转压缩机1中产生的噪音及振动。As described above, according to the present embodiment, since the
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| JP2005311393A JP4778772B2 (en) | 2005-10-26 | 2005-10-26 | Rotary compressor |
| JP2005311393 | 2005-10-26 |
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| CN100458165C true CN100458165C (en) | 2009-02-04 |
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| KR (1) | KR100782679B1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102803734B (en) | 2009-06-11 | 2015-06-10 | 三菱电机株式会社 | Refrigerant compressor and heat pump device |
| JP2016070229A (en) * | 2014-09-30 | 2016-05-09 | ダイキン工業株式会社 | Compressor |
| WO2016110982A1 (en) * | 2015-01-08 | 2016-07-14 | 三菱電機株式会社 | Multi-cylinder hermetic compressor |
| JP6914069B2 (en) * | 2017-03-23 | 2021-08-04 | 三菱電機株式会社 | Rotary compressor |
| CN113192118B (en) * | 2021-04-07 | 2021-10-29 | 中国兵器科学研究院宁波分院 | An accurate measurement method for the internal structure size of an air-conditioning compressor |
| CN113775527B (en) * | 2021-10-22 | 2024-08-09 | 珠海格力电器股份有限公司 | Compressor and air conditioner |
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- 2006-09-29 KR KR1020060095230A patent/KR100782679B1/en not_active Expired - Fee Related
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| US4636154A (en) * | 1984-06-04 | 1987-01-13 | Hitachi, Ltd. | Horizontal type rotary compressor |
| JPH07133781A (en) * | 1993-11-08 | 1995-05-23 | Sanyo Electric Co Ltd | Internal high pressure type compressor |
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| KR100782679B1 (en) | 2007-12-07 |
| CN1955475A (en) | 2007-05-02 |
| KR20070045092A (en) | 2007-05-02 |
| JP2007120354A (en) | 2007-05-17 |
| JP4778772B2 (en) | 2011-09-21 |
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