CN1318145A - Refrigerating device - Google Patents
Refrigerating device Download PDFInfo
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- CN1318145A CN1318145A CN 00801448 CN00801448A CN1318145A CN 1318145 A CN1318145 A CN 1318145A CN 00801448 CN00801448 CN 00801448 CN 00801448 A CN00801448 A CN 00801448A CN 1318145 A CN1318145 A CN 1318145A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B39/00—Component parts, details, or accessories, of pumps or pumping systems specially adapted for elastic fluids, not otherwise provided for in, or of interest apart from, groups F04B25/00 - F04B37/00
- F04B39/16—Filtration; Moisture separation
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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
- F25B31/00—Compressor arrangements
- F25B31/002—Lubrication
- F25B31/004—Lubrication oil recirculating arrangements
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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
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/07—Details of compressors or related parts
- F25B2400/075—Details of compressors or related parts with parallel compressors
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- Mechanical Engineering (AREA)
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- Thermal Sciences (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
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Abstract
Description
技术领域technical field
本发明涉及制冷装置中朝向压缩机的回油结构。The invention relates to an oil return structure facing a compressor in a refrigeration device.
背景技术Background technique
在多台(例如2台)压缩机并列连接的制冷装置中,各自的压缩机容量往往不一样。这种制冷装置在所有的压缩机运转时,各自的压缩机中圆顶腔(ド一ム)内部压力产生差别。另外,压缩机中的圆顶腔内的底部的制冷机油通过均压管从内压高的压缩机向内压低的压缩机移动。In a refrigerating apparatus in which a plurality of (for example, two) compressors are connected in parallel, the capacities of the respective compressors are often different. In such a refrigeration device, when all the compressors are in operation, the internal pressures of the dome chambers (dome) of the respective compressors are different. In addition, the refrigerating machine oil at the bottom of the dome cavity in the compressor moves from a compressor with a high internal pressure to a compressor with a low internal pressure through a pressure equalizing pipe.
一旦持续这种状态的运转,则圆顶腔内压高的压缩机的制冷机油不断地向圆顶腔内压低的压缩机移动。若这种状态持续下去,就会使圆顶腔内压高的压缩机的制冷机油流尽,损坏压缩机。As long as the operation in this state continues, the refrigerating machine oil of the compressor whose pressure is high in the dome chamber continues to move to the compressor whose pressure is low in the dome chamber. If this state continues, the refrigerating machine oil of the compressor with high pressure in the dome cavity will be exhausted and the compressor will be damaged.
为解决上述不良现象,有一种方法是油的均量运转控制。这种油的均量运转控制是每隔一定时间交替运转压缩机,以确保各自压缩机中的制冷机油量。In order to solve the above-mentioned undesirable phenomenon, there is a method of oil equalization operation control. This oil equalization operation control is to alternately operate the compressors at regular intervals to ensure the amount of refrigerating machine oil in each compressor.
然而,在执行上述油的均量运转控制时,只能在一定时间内进行所有压缩机的同时运转。结果是存在着无法获得制冷装置所需容量的问题。However, when the above-mentioned oil equalization operation control is performed, all the compressors can only be operated simultaneously for a certain period of time. As a result, there is a problem that the required capacity of the refrigeration unit cannot be obtained.
鉴于上述问题,本发明目的在于,提供一种装有不同容量的多个压缩机的制冷装置,其能可靠地进行制冷机油向各自压缩机的回流。In view of the above-mentioned problems, an object of the present invention is to provide a refrigerator equipped with a plurality of compressors having different capacities, which can reliably perform return flow of refrigerator oil to the respective compressors.
发明的公开disclosure of invention
为解决上述课题,本发明采取如下措施。In order to solve the above-mentioned problems, the present invention takes the following measures.
第1发明是以具有相互并列连接且容量不同的多个压缩机1A、1B…的设有制冷剂回路A的制冷装置为对象。并且为使在所述制冷剂回路A循环的制冷剂中的制冷机油按照各压缩机1A、1B…的不同容量向各压缩机1A、1B…进行分配,设置有使该制冷机油返回到压缩机1A、1B…的分配机构R。The 1st invention is aimed at the refrigeration apparatus provided with the refrigerant circuit A which has
在第1发明中,当压缩机1A、1B…运转时,制冷机油按照各压缩机1A、1B…进行分配。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保多个压缩机1A、1B…的制冷机油。In the first invention, when the
第2发明是以具有相互并列连接且容量不同的多个压缩机1A、1B…的设有制冷剂回路A的制冷装置为对象。并且,为使在所述制冷剂回路A循环的制冷剂中的制冷机油从最小容量的压缩机1A向其它压缩机1B…分配,设置有使该制冷机油返回到压缩机1A、1B…的分配机构R。The 2nd invention is aimed at the refrigerating apparatus provided with the refrigerant circuit A which has the some
在第2发明中,当压缩机1A、1B…运转时,制冷机油从最小容量的压缩机1A向其它压缩机1B…分配。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保多个压缩机1A、1B…的制冷机油。In the second invention, when the
第3发明是以具有相互并列连接且容量不同的多个压缩机1A、1B…的设有制冷剂回路A的制冷装置为对象。并且,为使在所述制冷剂回路A循环的制冷剂中的制冷机油从最大容量的压缩机1A向其它压缩机1B…分配,设置有使该制冷机油返回到压缩机1A、1B…的分配机构R。The 3rd invention is aimed at the refrigerating apparatus provided with the refrigerant circuit A which has the some
在第3发明中,当压缩机1A、1B…运转时,制冷机油从最大容量的压缩机1A向其它压缩机1B…分配。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保多个压缩机1A、1B…的制冷机油。In the third invention, when the
第4发明是,在上述第2发明中,压缩机1A、1B…采用低压圆顶腔型压缩机。并且,所述分配机构R具有与压缩机1A、1B…连通的均油管109以及设在所述压缩机1A、1B…排出侧的分离排出制冷剂中的制冷机油用的油分离器116,由所述油分离器116分离的制冷机油和所述压缩机1A、1B…的吸入制冷剂中包含的制冷机油被优先回流到最小容量的压缩机1A。In the fourth invention, in the above-mentioned second invention, the
在第4发明中,从压缩机1A、1B…排出的制冷机油由油分离器116回收。该油分离器116的制冷机油和回流到压缩机1A、1B…吸入侧的制冷机油被优先流回到最小容量的压缩机1A。然后,因圆顶腔的内压差,从所述最小容量的压缩机1A经过均油管109回流到圆顶腔内压低的压缩机1B、1C…。In the fourth invention, the refrigerating machine oil discharged from the
第5发明是,在上述第3发明中,压缩机1A、1B…采用高压圆顶腔型压缩机。并且,所述分配机构R具有与压缩机1A、1B…连通的均油管48以及设在所述压缩机1A、1B…排出侧的分离排出制冷剂中的制冷机油用的油分离器36,由所述油分离器36分离的制冷机油和所述压缩机1A、1B…的吸入制冷剂中包含的制冷机油被优先流回到最大容量的压缩机1A。In the fifth invention, in the above-mentioned third invention, the
在第5发明中,从压缩机1A、1B…排出的制冷机油由油分离器36回收。该油分离器36的制冷机油和流回到压缩机1A、1B…吸入侧的制冷机油被优先流回到最大容量的压缩机1A。然后,因圆顶腔的内压差,从所述最大容量的压缩机1A经过均油管48回流到圆顶腔内压低的压缩机1B…。In the fifth invention, the refrigerating machine oil discharged from the
第6发明具有通过制冷剂配管按顺序将相互并联连接的各自不同容量的多个低压圆顶腔型压缩机1A、1B…、热源侧交换器2、减压机构3及使用侧热交换器4予以连接的制冷剂回路A,以通过均油管9、9使所述压缩机1A、1B…相互连通的制冷装置为对象。The sixth invention has a plurality of low-pressure dome-
并且,在所述压缩机1A、1B…的排出配管15上,设有分离排出气体制冷剂中的制冷机油用的油分离器16,又在所述压缩机1A、1B…的吸入线路X中,设置优先将吸入气体制冷剂中包含的制冷机油返回到所述压缩机1A、1B…中的最小容量的压缩机1A用的回油机构Z。另外,设有将所述油分离器36中分离后的制冷机油返回到所述压缩机1A、1B…中的最小容量的压缩机1A用的回油通道37。In addition, an oil separator 16 for separating refrigerating machine oil in the discharged gas refrigerant is provided on the discharge piping 15 of the
在第6发明中,当压缩机1A、1B…运转时,由油分离器16分离的制冷机油和吸入气体制冷剂中的制冷机油被优先返回到最小容量的压缩机1A。然后,制冷机油因圆顶腔的内压差(压缩机1A的内压>压缩机1B的内压>压缩机1C的内压>…),而按顺序从最小容量的压缩机1A返回到圆顶腔内压低的压缩机1B、1C…。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保多个压缩机1A、1B…的制冷机油。In the sixth invention, when the
第7发明是在上述第6发明中,所述回油机构Z包括:构成所述吸入线路X的一部分并与所述压缩机1A、1B…中的最小容量的压缩机1A连接的略水平状的一定长度的吸入配管25和从该第1吸入配管25的上部分支并分别与所述压缩机1A、1B…中的最小容量的压缩机1A以外的压缩机1B、1C…连接的第2吸入配管26、26…。The seventh invention is the above-mentioned sixth invention, wherein the oil return mechanism Z includes: a substantially horizontal structure that forms a part of the suction line X and is connected to the
在第7发明的第1吸入配管25中,制冷机油因制冷机油与气体制冷剂比重差异而分离并流向管底部。分离后的制冷机油从第1吸入配管25返回到最小容量的压缩机1A。因此,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B…中的制冷机油。In the first suction pipe 25 of the seventh invention, the refrigerating machine oil is separated due to the difference in specific gravity between the refrigerating machine oil and the gas refrigerant, and flows to the bottom of the pipe. The separated refrigerating machine oil is returned from the first suction pipe 25 to the
第8发明是在上述第6发明中,所述回油机构Z包括:构成所述吸入线路X的一部分并向下形成下端开放的垂直管27;面对该垂直管27的下部且水平剖面截面积大于该垂直管27的管体28;与该管体28下端连接并与所述压缩机1A、1B…中的最小容量的压缩机1A连接的第1吸入配管25;以及与所述管体28的侧壁连接并分别与所述压缩机1A、1B…中的最小容量的压缩机1A以外的压缩机1B、1C…连接的第2吸入配管26、26…。The eighth invention is the above-mentioned sixth invention, wherein the oil return mechanism Z includes: a vertical pipe 27 that forms a part of the suction line X and is downwardly opened at the lower end; The pipe body 28 whose area is larger than the vertical pipe 27; the first suction pipe 25 connected to the lower end of the pipe body 28 and connected to the
在第8发明中,因从垂直管27流入管体28的吸入气体制冷剂在该管体28内急剧膨胀,故制冷机油与吸入气体制冷剂分离。分离后的制冷机油因重力和惯性的作用,而从第1吸入配管25返回到最小容量的压缩机1A。因此,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B……中的制冷机油。In the eighth invention, since the suction gas refrigerant flowing into the pipe body 28 from the vertical pipe 27 rapidly expands in the pipe body 28, the refrigerating machine oil and the suction gas refrigerant are separated. The separated refrigerating machine oil returns from the first suction pipe 25 to the
第9发明是在上述第6发明中,所述回油机构Z包括:构成所述吸入线路X的一部分且垂直剖面截面积大于该吸入线路X的水平大直径管29;与该水平大直径管29管壁连接并与所述压缩机1A、1B…中的最小容量的压缩机1A连接的第1吸入配管25;以及同心状地面对所述水平大直径管29的中心部并分别与所述压缩机1A、1B…中的最小容量的压缩机1A以外的压缩机1B、1C…连接的第2吸入配管26、26…。The ninth invention is that in the sixth invention above, the oil return mechanism Z includes: a horizontal large-diameter pipe 29 that constitutes a part of the suction line X and has a vertical cross-sectional area larger than the suction line X; 29 the first suction pipe 25 connected to the pipe wall and connected to the
在第9发明中,因可缓和流过水平大直径管29的吸入气体制冷剂的流速,故在流速慢的管壁侧产生制冷机油的环状流,使吸入气体制冷剂与制冷机油分离。分离后的制冷机油从第1吸入配管25返回到最小容量的压缩机1A。因此,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B…中的制冷机油。In the ninth invention, since the flow velocity of the suction gas refrigerant flowing through the horizontal large-diameter tube 29 can be eased, an annular flow of the refrigerating machine oil is generated on the tube wall side where the flow velocity is slow, and the suction gas refrigerant and the refrigerating machine oil are separated. The separated refrigerating machine oil is returned from the first suction pipe 25 to the
第10发明是在上述第7至第9的任一项发明中,所述回油通道17与所述第1吸入配管25连接。A tenth invention is any one of the seventh to ninth inventions, wherein the oil return passage 17 is connected to the first suction pipe 25 .
在第10发明中,由油分离器36分离的制冷机油在第1吸入配管25中与从吸入气体制冷剂分离的制冷机油合流后,返回到最小容量的压缩机1A。其结果,不需要变更压缩机1A的构造(如外壳结构等)。In the tenth invention, the refrigerating machine oil separated by the
第11发明是以具有通过制冷剂配管按顺序将相互并联连接的各自容量不同的一对高压圆顶腔型压缩机1A、1B、四通转换阀2、热源侧热交换器3、减压机构4及使用侧热交换器5予以连接的制冷剂回路A、通过均油管48使所述压缩机1A、1B相互连通的制冷装置为对象。The eleventh invention comprises a pair of high-pressure dome-
并且,在所述压缩机1A、1B的排出配管47上,设有分离排出气体制冷剂中的制冷机油用的油分离器36,且设置将该油分离器36中分离后的制冷机油返回到所述压缩机1A、1B吸入侧的回油通道37。另外,在该回油通道37中,设有在所述压缩机1A、1B一起停止运转时关闭的开闭阀39。In addition, an
在第11发明中,在压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入气体制冷剂中的制冷机油经过回油通道37而分别返回到压缩机1A、1B。此时,大部分制冷机油返回到容量大的压缩机1A。容量大的压缩机1A的内压大于容量小的压缩机1B的内压。结果是,制冷机油通过均油管而从容量大的压缩机1A向容量小的压缩机1B移动,可靠地回流到两压缩机1A、1B。In the eleventh invention, when the
因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。并且,在压缩机1A、1B一起停止运转时,开闭阀39关闭,回油通道37成为非连通状态。因此,制冷剂在停止运转期间,不会从油分离器36流向压缩机1A的吸入侧。Therefore, it is possible to secure the refrigerating machine oil for the
第12发明以具有通过制冷剂配管按顺序将相互并联连接的各自容量不同的一对高压圆顶腔型压缩机1A、1B、四通转换阀2、热源侧热交换器3、减压机构4、使用侧热交换器5予以连接的制冷剂回路A、通过均油管48使所述压缩机1A、1B相互连通的制冷装置为对象。The twelfth invention comprises a pair of high-pressure dome-
并且,在所述压缩机1A、1B的排出配管47上,设有分离排出气体制冷剂中的制冷机油用的油分离器36,且设置将该油分离器36中分离后的制冷机油分别返回到所述压缩机1A、1B的吸入侧的回油通道37A、37B。另外,在该回油通道37A、38B中,分别设有在所述压缩机1A、1B一起停止运转时关闭的开闭阀39A、39B。In addition, the
在第12发明中,在压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入气体制冷剂中的制冷机油经过回油通道37A、37B而分别返回到压缩机1A、1B。此时,大部分制冷机油回流到容量大的压缩机1A。容量大的压缩机1A的内压大于容量小的压缩机1B的内压。结果是,制冷机油通过均油管48而从容量大的压缩机1A向容量小的压缩机1B移动,可靠地回流到两压缩机1A、1B。In the twelfth invention, when the
因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。并且,在压缩机1A、1B一起停止运转期间,开闭阀39A、39B关闭,回油通道37A、37B成为非连通状态。因此,在制冷剂停止运转时,不会从油分离器36流向压缩机1A、1B的吸入侧。Therefore, it is possible to secure the refrigerating machine oil for the
第13发明是,在上述第11和第12中任一项发明中,所述均油管48设有在所述压缩机1A、1B中的某1个停止运转时关闭的开闭阀49。According to a thirteenth invention, in any one of the above-mentioned eleventh and twelfth inventions, the
在第13发明中,当压缩机1A、1B中的某1个运转停止时,开闭阀49关闭,禁止制冷机油通过均油管48的移动。结果是,可阻止制冷机油从运转中的压缩机向运转停止状态的压缩机移动,不会使运转中的压缩机产生制冷机油不足。In the thirteenth invention, when one of the
第14发明以具有通过制冷剂配管按顺序将相互并联连接的各自容量不同的一对高压圆顶腔型压缩机1A、1B、四通转换阀2、热源侧热交换器3、减压机构4及使用侧热交换器5予以连接的制冷剂回路A、通过均油管48使所述压缩机1A、1B相互连通的制冷装置为对象。The fourteenth invention comprises a pair of high-pressure dome-
并且,在所述压缩机1A、1B的排出配管47上,设有分离排出气体制冷剂中的制冷机油用的油分离器36,又在该油分离器36中,设置将分离的制冷机油返回到所述压缩机1A、1B吸入侧的回油通道37。另外,在所述均油管48上,设有在所述压缩机1A、1B中的某1个运转停止时关闭的开闭阀49。In addition, an
在第14发明中,当压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入气体制冷剂中的制冷机油经过回油通道37而分别返回到压缩机1A、1B。此时,大部分制冷机油回流到容量大的压缩机1A。容量大的压缩机1A的内压大于容量小的压缩机1B的内压。结果是,制冷机油通过均油管48而从容量大的压缩机1A向容量小的压缩机1B移动,可靠地流回到两压缩机1A、1B。In the fourteenth invention, when the
因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。Therefore, it is possible to secure the refrigerating machine oil for the
并且,在压缩机1A、1B中的某1个运转停止时,开闭阀49关闭,禁止制冷机油经过均油管48的移动。结果是,可阻止制冷机油从运转中的压缩机向运转停止状态的压缩机移动,不会使运转中的压缩机产生制冷机油不足。Furthermore, when one of the
第15发明是,在上述第11、第12和第14的任一项发明中,所述压缩机1A、1B的吸入管38位于压缩机1A、1B的吸入口50A、50B的下方。According to a fifteenth invention, in any one of the eleventh, twelfth and fourteenth inventions, the
在第15发明中,当容量大的压缩机运转停止而容量小的压缩机处于运转状态时,可防止制冷机油通过吸入管38而流入容量大的压缩机。In the fifteenth invention, when the compressor with a large capacity is stopped and the compressor with a small capacity is in operation, the refrigerating machine oil can be prevented from flowing into the compressor with a large capacity through the
采用本发明,由于利用压缩机1A、1B…的容量不同这一点来使制冷机油回流到各压缩机1A、1B,因此,不需要象以往那样执行压缩机交替运转的油均量运转控制。结果是,在始终发挥所需的制冷能力的同时,能可靠地确保多个压缩机1A、1B…的制冷机油。According to the present invention, since the refrigerating machine oil is returned to the
采用第6发明,在压缩机1A、1B运转时,由油分离器116分离的制冷机油和吸入气体制冷剂中的制冷机油在优先返回到最小容量的压缩机1A后,因圆顶腔的内压差(压缩机1A的内压>压缩机1B的内压>压缩机1C的内压>…)按顺序从该压缩机1A返回到圆顶腔内压低的压缩机1B、1C。结果是即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能可靠地确保多个压缩机1A、1B…的制冷机油。According to the sixth invention, when the
采用第7发明,由于在第1吸入配管125中,制冷机油因制冷机油与气体制冷剂的比重差异而分离,流入管底部,因此,分离后的制冷机油经过第1吸入配管125流回压缩机1A、1B中的最小容量的压缩机1A。因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B…中的制冷机油。According to the seventh invention, since the refrigerating machine oil is separated in the
采用第8发明,由于从垂直管127流入管体128的吸入气体制冷剂在该管体128内急剧膨胀,因此,制冷机油与吸入气体制冷剂分离,分离后的制冷机油利用重力和惯性,经过第1吸入配管125而返回到压缩机1A、1B…中的最小容量的压缩机1A。结果是,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B…中的制冷机油。According to the eighth invention, since the suction gas refrigerant flowing into the pipe body 128 from the vertical pipe 127 expands rapidly in the pipe body 128, the refrigerating machine oil is separated from the suction gas refrigerant, and the separated refrigerating machine oil passes through gravity and inertia. The
采用第9发明,由于可缓和流过水平大直径管129的吸入气体制冷剂的流速,因此,在流速慢的管壁侧会产生制冷机油的环状流,使制冷机油与吸入气体制冷剂分离,分离后的制冷机油经过第1吸入配管回流到压缩机1A、1B…中的最小容量的压缩机1A。结果是,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B…中的制冷机油。According to the ninth invention, since the flow velocity of the suction gas refrigerant flowing through the horizontal large-diameter tube 129 can be eased, an annular flow of refrigerating machine oil is generated on the side of the tube wall where the flow velocity is slow, and the refrigerating machine oil and the suction gas refrigerant are separated. , the separated refrigerating machine oil returns to the
采用第10发明,由油分离器116分离的制冷机油在第1吸入配管125中与从吸入气体制冷剂分离的制冷机油合流,返回到最小容量的压缩机1A。结果是,不需要变更压缩机1A的构造(如外壳结构等)。According to the tenth invention, the refrigerating machine oil separated by the
采用第11发明,在压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入制冷剂中的制冷机油经过回油通道37而分别返回到压缩机1A、1B。并且,大部分制冷机油回流到容量大的压缩机1A,但由于容量大的压缩机1A的内压大于容量小的压缩机1B的内压,因此,制冷机油通过均油管48向容量小的压缩机1B移动。结果是,可靠地回流到两压缩机1A、1B。即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。According to the eleventh invention, when the
并且,在压缩机1A、1B一起停止运转时,由于开闭阀39作出关闭动作,使回油通道37成为非连通状态,因此,停止运转时制冷剂不会从油分离器36流向吸入侧。In addition, when the
在第12发明中,当压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入气体制冷剂中的制冷机油经过回油通道37A、37B而分别返回到压缩机1A、1B。并且,大部分制冷机油返回到容量大的压缩机1A,但由于容量大的压缩机1A的内压大于容量小的压缩机1B的内压,因此,制冷机油通过均油管48向容量小的压缩机1B移动。结果是,可靠地回流到两压缩机1A、1B,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。In the twelfth invention, when the
并且,在压缩机1A、1B一起停止运转时,由于开闭阀39A、38B作出关闭动作,使回油通道37A、37B成为非连通状态,因此,运转停止时制冷剂不会从油分离器36流向吸入侧。In addition, when the
采用第13发明,在压缩机1A、1B中的某1个停止运转时,开闭阀49作出关闭动作,禁止制冷机油通过均油管48的移动。结果是,可阻止制冷机油从运转中的压缩机向运转停止状态的压缩机移动,不会使运转中的压缩机产生制冷机油不足。According to the thirteenth invention, when one of the
采用第14发明,在压缩机1A、1B一起运转时,由油分离器36分离的制冷机油和吸入气体制冷剂中的制冷机油经过回油通道37而分别返回到压缩机1A、1B。并且,大部分制冷机油流回容量大的压缩机1A,但由于容量大的压缩机1A的内压大于容量小的压缩机1B的内压,因此,制冷机油通过均油管48向容量小的压缩机1B移动。结果是,可靠地回流到两压缩机1A、1B,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。According to the fourteenth invention, when the
并且,在压缩机1A、1B中的某1个运转停止时,开闭阀48作出关闭动作,使通过均油管48的制冷机油不能移动。结果是,禁止制冷机油从运转中的压缩机向运转停止状态的压缩机移动,不会使运转中的压缩机产生制冷机油不足。Furthermore, when one of the
采用第15发明,在容量大的压缩机处于运转停止状态而容量小的压缩机运转时,可防止制冷机油通过吸入管38流入容量大的压缩机。According to the fifteenth invention, when the compressor with a large capacity is stopped and the compressor with a small capacity is in operation, refrigerating machine oil can be prevented from flowing into the compressor with a large capacity through the
附图的简单说明A brief description of the drawings
图1为本发明第1实施形态的制冷装置的制冷剂配管系统图。Fig. 1 is a diagram of a refrigerant piping system of a refrigeration device according to a first embodiment of the present invention.
图2表示本发明第1实施形态的制冷装置中吸入线路部分结构的配管系统图。Fig. 2 is a piping system diagram showing the partial structure of the suction line in the refrigerating apparatus according to the first embodiment of the present invention.
图3表示本发明第2实施形态的制冷装置中吸入线路部分结构的配管系统图。Fig. 3 is a piping system diagram showing a partial structure of a suction line in a refrigerating apparatus according to a second embodiment of the present invention.
图4表示本发明第3实施形态的制冷装置中吸入线路部分结构的配管系统图。Fig. 4 is a piping system diagram showing a partial structure of a suction line in a refrigerating apparatus according to a third embodiment of the present invention.
图5表示本发明第4实施形态的制冷装置中吸入线路部分结构的配管系统图。Fig. 5 is a piping system diagram showing a partial structure of a suction line in a refrigerating apparatus according to a fourth embodiment of the present invention.
图6为本发明第5实施形态的制冷装置的制冷剂回路图。Fig. 6 is a refrigerant circuit diagram of a refrigeration system according to a fifth embodiment of the present invention.
图7表示本发明第5实施形态的制冷装置中吸入管部分结构的配管系统图。Fig. 7 is a piping system diagram showing a partial structure of a suction pipe in a refrigerating apparatus according to a fifth embodiment of the present invention.
图8为本发明第6实施形态的制冷装置中的压缩机及其电磁开闭阀动作状态的说明表。Fig. 8 is an explanatory table showing the operating states of the compressor and its electromagnetic on-off valve in the refrigeration system according to the sixth embodiment of the present invention.
图9表示本发明第6实施形态的制冷装置中吸入管部分结构的配管系统图。Fig. 9 is a piping system diagram showing a partial structure of a suction pipe in a refrigerating apparatus according to a sixth embodiment of the present invention.
实施发明的最佳形态The best form for carrying out the invention
下面,参照图纸说明本发明的实施形态。Next, embodiments of the present invention will be described with reference to the drawings.
图1和图2表示本发明第1实施形态的制冷装置的制冷剂配管系统。1 and 2 show a refrigerant piping system of a refrigeration device according to a first embodiment of the present invention.
如图1所示,本制冷装置具有相互并联连接的各自容量不同的2台压缩机1A、1B、起到热源侧热交换器作用的空冷冷凝器102、起到减压机构作用的膨胀阀103以及通过制冷剂配管按顺序将并联连接的起到使用侧热交换器作用的一对蒸发器104、104予以连接而构成的制冷剂回路A。As shown in Fig. 1, this refrigeration device has two
其中,所述第1压缩机1A的容量为4HP,第2压缩机1B的容量为5HP。所述第1压缩机1A的储油部与第2压缩机1B的储油部通过均油管109连接。Wherein, the capacity of the
在所述冷凝器102与膨胀阀103之间,设有与该冷凝器102出口侧连接的储蓄罐105、利用室外空气对来自该储蓄罐105的液相部的液态制冷剂进行过冷却的第1过冷却热交换器106以及通过气液混合制冷剂的蒸发潜热对来自该第1过冷却热交换器106的过冷却液态制冷剂进一步进行过冷却的第2过冷却热交换器107。在所述冷凝器102与第1过冷却热交换器106之间设有1个室外风扇108。Between the condenser 102 and the expansion valve 103, there is a storage tank 105 connected to the outlet side of the condenser 102, and a second unit for supercooling the liquid refrigerant from the liquid phase part of the storage tank 105 by using outdoor air. A subcooling heat exchanger 106 and a second subcooling heat exchanger 107 for further subcooling the subcooled liquid refrigerant from the first subcooling heat exchanger 106 by latent heat of evaporation of the gas-liquid mixed refrigerant. One outdoor fan 108 is provided between the condenser 102 and the first subcooling heat exchanger 106 .
来自所述储蓄罐105的液相部的液态制冷剂的一部分经感温膨胀阀110减压而供给到所述第2过冷却热交换器107。在将所述第2过冷却热交换器107与构成所述压缩机1A、1B的吸入线路X一部分的吸入管111予以连接的气体配管112上,设有该感温膨胀阀110的感温筒110a。即,感温膨胀阀110根据在气体配管112中流动的气体制冷剂温度来控制开度。A part of the liquid refrigerant from the liquid phase portion of the accumulator tank 105 is decompressed through the thermosensing expansion valve 110 and supplied to the second subcooling heat exchanger 107 . The thermosensitive cylinder of the thermosensitive expansion valve 110 is provided on the gas piping 112 connecting the second subcooling heat exchanger 107 to the
在所述制冷剂回路A中,设有连接压缩机1A、1B的排出侧与吸入侧的热气体旁通回路113。在该热气体旁通回路113中,装有电磁开闭阀114,当低压力过低时,该电磁开闭阀114作出打开动作,以防止真空运转。In the refrigerant circuit A, a hot gas bypass circuit 113 that connects the discharge side and the suction side of the
在所述压缩机1A、1B的排出配管115上,设有分离气体制冷剂中包含的制冷机油用的油分离器116。由该油分离器116分离的制冷机油如后所述,经过回油通道117回流到最小容量的压缩机1A。在所述回油通道117中,设有回油时作出打开动作的电磁开闭阀118和毛细管119。An
在所述蒸发器104、104上,设有室内风扇120。在所述制冷剂回路A中的压缩机1A、1B的排出侧设有单向阀121。另外,在所述制冷剂回路A中,还设有控制向蒸发器104、104的制冷剂供给的电磁开闭阀122、控制向第2过冷却热交换器107的制冷剂供给的电磁开闭阀123以及闭锁阀124。An indoor fan 120 is provided on the evaporators 104 , 104 . On the discharge side of the
如图2所示,在所述压缩机1A、1B的吸入线路X中,设有将从吸入气体制冷剂中分离的制冷机油优先返回到最小容量的压缩机1A的回油机构Z。该回油机构Z由构成所述吸入线路X的一部分并与最小容量的压缩机1A连接的略水平状的一定长度的第1吸入配管125和从该第1吸入配管125的上部分支并与容量大的压缩机1B连接的第2吸入配管126所构成。As shown in FIG. 2 , the suction lines X of the
另外,来自所述油分离器116的回油通道117与所述第1吸入配管125连接。In addition, the
即,所述制冷剂回路A具有将制冷机油回流到压缩机1A、1B的分配机构R。该分配机构R根据各压缩机1A、1B的不同容量,将制冷剂回路A循环的制冷剂中的制冷机油向各压缩机1A、1B进行分配。本实施形态的分配机构R按照从最小容量的第1压缩机1A向其它的第2压缩机1B进行分配的原则,而将在制冷剂回路A循环的制冷剂中的制冷机油回流到压缩机1A、1B。That is, the refrigerant circuit A has a distribution mechanism R that returns the refrigerating machine oil to the
具体地讲,所述分配机构R具有所述均油管109、油分离器116、回油通道117和回油机构Z。并且,所述分配机构R可使在所述油分离器116中分离的制冷机油和所述压缩机1A、1B的吸入气体制冷剂中包含的制冷机油优先回流到最小容量的压缩机1A。Specifically, the distribution mechanism R has the
采用这种结构,当压缩机1A、1B运转时,由油分离器116分离的制冷机油和吸入气体制冷剂中的制冷机油返回到最小容量的压缩机1A。然后,所述制冷机油因圆顶腔的内压差(压缩机1A的内压>压缩机1B的内压),而从第1压缩机1A回流到圆顶腔内压低的第2压缩机1B。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B的制冷机油。With this configuration, when the
并且,在第1吸入配管125内,因制冷机油与气体制冷剂的比重差异,而使制冷机油F分离后流入管底部,分离后的制冷机油F经过第1吸入配管125回流到最小容量的压缩机1A。因此,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B中的制冷机油。In addition, in the
又由于所述回油通道117与第1吸入配管125连接,因此,由油分离器116分离的制冷机油在第1吸入配管125内与从吸入气体制冷剂分离的制冷机油合流后,返回到第1压缩机1A,不需要变更该压缩机1A的构造(如外壳结构等)。另外,回油通道117也可直接与第1压缩机1A连接。Since the
第2实施形态Second Embodiment
图3表示本发明第2实施形态的制冷装置中的吸入线路部分。Fig. 3 shows a portion of a suction line in a refrigerating apparatus according to a second embodiment of the present invention.
其中,制冷装置具有各自容量不同的3个压缩机1A、1B、1C。与第1压缩机1A相连接的第1吸入配管125的上部,通过第2吸入配管126、126而分别与第2压缩机2B及第2压缩机1C连接。其它结构及其作用效果均与第1实施形态相同,故省略说明。Among them, the refrigeration device has three
第3实施形态3rd embodiment
图4表示本发明第3实施形态的制冷装置中的吸入线路部分。Fig. 4 shows a portion of a suction line in a refrigerating apparatus according to a third embodiment of the present invention.
其中,回油机构X包括:构成所述吸入线路X的一部分并向下形成下端开放的垂直管127;面对该垂直管127的下部且水平剖面截面积大于该垂直管127的管体128;与该管体128下端连接并与最小容量的第1压缩机1A连接的第1吸入配管125;以及与所述管体128的侧壁连接并与第2压缩机1B连接的第2吸入配管126。Wherein, the oil return mechanism X includes: a vertical pipe 127 that forms a part of the suction line X and has an open lower end downward; a pipe body 128 facing the lower part of the vertical pipe 127 and having a horizontal cross-sectional area larger than the vertical pipe 127; A
这样,从垂直管127流入管体128内的吸入气体制冷剂因在该管体128内急剧膨胀,而使制冷机油与吸入气体制冷剂分离,分离后的制冷机油利用重力和惯性,经过第1吸入配管125而返回到压缩机1A。结果是,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B中的制冷机油。In this way, the suction gas refrigerant flowing into the pipe body 128 from the vertical pipe 127 rapidly expands in the pipe body 128, so that the refrigerator oil is separated from the suction gas refrigerant, and the separated refrigerator oil passes through the first stage by gravity and inertia. The
另外,吸入气体制冷剂按照压缩机1A、1B的吸入压力进行吸入。这种场合也能设置3个以上压缩机。其它结构及其作用效果均与第1实施形态相同,故省略说明。In addition, the suction gas refrigerant is sucked in accordance with the suction pressure of the
第4实施形态Fourth Embodiment
图5表示本发明第4实施例形态的制冷装置中的吸入线路部分。Fig. 5 shows a portion of a suction line in a refrigerating apparatus according to a fourth embodiment of the present invention.
此时,回油机构X包括:构成吸入线路X的一部分且垂直剖面截面积大于该吸入线中X的水平大直径管129;与该水平大直径管129的管壁连接并与最小容量的第1压缩机1A连接的第1吸入配管125;以及同心状地面对所述水平大直径管129的中心部并与第2压缩机1B连接的第2吸入配管126。At this time, the oil return mechanism X includes: a horizontal large-diameter pipe 129 that constitutes a part of the suction line X and has a vertical cross-sectional area larger than X in the suction line; it is connected to the pipe wall of the horizontal large-diameter pipe 129 and connected to the first pipe with the smallest capacity. A
这样,如流速分布Y所示,因可缓和在水平大直径管129内流动的吸入气体制冷剂的流速,故在流速慢的管壁侧产生制冷机油的环状流,使制冷机油与吸入气体制冷剂分离,分离后的制冷机油经过第1吸入配管125而返回到最小容量的第1压缩机1A。结果是,因变更配管结构简单,故可低成本且高效率地确保压缩机1A、1B中的制冷机油。In this way, as shown in the flow velocity distribution Y, since the flow velocity of the suction gas refrigerant flowing in the horizontal large-diameter tube 129 can be eased, an annular flow of the refrigerating machine oil is generated on the side of the tube wall where the flow velocity is slow, and the refrigerating machine oil and the suction gas are separated. The refrigerant is separated, and the separated refrigerating machine oil passes through the
另外,吸入气体制冷剂按照压缩机1A、1B的吸入压力进行吸入。这种场合也可设置3个以上压缩机。其它结构及其作用效果均与第1实施形态相同,故省略说明。In addition, the suction gas refrigerant is sucked in accordance with the suction pressure of the
第5实施形态Fifth Embodiment
图6和图7表示本发明第5实施形态的制冷装置的制冷剂配管系统。6 and 7 show a refrigerant piping system of a refrigeration device according to a fifth embodiment of the present invention.
如图6所示,该制冷装置具有热泵式空调用回路A和冷藏用制冷剂回路B。热泵式空调用制冷剂回路A的结构是,通过制冷剂配管而按顺序将相互并联连接的各自容量不同的一对压缩机1A、1B、四通转换阀2、附设有室外风扇11的热源侧热交换器3、起减压机构作用的膨胀阀4及使用侧热交换器5予以连接而成;冷藏用制冷剂回路B是,从该热泵式空调用制冷剂回路A中的所述膨胀阀4的下游侧分支并通过冷藏用蒸发器6与所述压缩机1A、1B的吸入侧连接而成。该冷藏用制冷剂回路B也可称为热回收回路。As shown in FIG. 6 , this refrigeration device has a circuit A for heat pump air conditioning and a refrigerant circuit B for refrigeration. The structure of the refrigerant circuit A for the heat pump air conditioner is that a pair of
其中,与上述实施例1不同之点在于,第1压缩机1A的容量为5HP,第2压缩机1B的容量为4HP。并且所述第1压缩机1A的储油部与第2压缩机1B的储油部通过均油管48连接。Among them, the difference from the above-mentioned
在所述热源侧热交换器3与膨胀阀4之间,设置有制冷运转时与所述热源侧热交换器3的出口侧部分连接的储蓄罐7、用外部热媒体(如室外空气)对来自该储蓄罐7液相部的液态制冷剂进行过冷却的空冷式的第1过冷却热交换器8以及将来自该第1过冷却热交换器8的过冷却液态制冷剂利用由感温膨胀阀10减压该过冷却液态制冷剂部分所获得的气液混合制冷剂的蒸发潜热作进一步过冷却的三重管式的第2过冷却热交换器9。在该第2过冷却热交换器9中,蒸发气化后的气体制冷剂经过低压气体配管12供给到压缩机1A、1B的吸入侧供给。所述感温膨胀阀10的感温筒10a安装在所述低压气体配管12上。Between the heat source
在所述空调用制冷剂回路A中,设有只能在向第2过冷却热交换器9部分供给液态制冷剂时不作出打开动作的电磁开闭阀13。在本实施形态中,热源侧热交换器3和第1过冷却热交换器8共用上述室外风扇11。The air-conditioning refrigerant circuit A is provided with an electromagnetic on-off valve 13 that does not open only when liquid refrigerant is supplied to the second
在所述储蓄罐7的入口侧,设置具有4个单向阀14a-14d的桥接回路14。该桥接回路14起到如下的流路切换机构的作用:在制冷运转时将来自热源侧热交换器3的液态制冷剂导入储蓄罐7,同时将来自储蓄罐7的液态制冷剂径由膨胀阀4后导入使用侧热交换器5;在制热运转时,将来自使用侧热交换器5的液态制冷剂导入储气管7,同时将来自储蓄罐7的液态制冷剂经由膨胀阀4后导入热源侧热交换器3。On the inlet side of said
在所述空调用制冷剂回路A中,设有只能在制冷运转时允许液态制冷剂从热源侧热交换器3向储蓄罐7流通的单向阀15,并且,还设有电磁开闭阀16。该电磁开闭阀16在制热运转时作出打开动作,允许制冷剂从膨胀阀4向使用侧热交换器3流通,且在制热的热回收运转时作出关闭动作,只能允许制冷剂从膨胀阀4向冷藏用蒸发器6流通。In the air-conditioning refrigerant circuit A, there is provided a check valve 15 that allows liquid refrigerant to flow from the heat source
在所述冷藏用制冷剂回路B的冷藏用蒸发器6的上游侧液管17处,安装有后述的制冷用制冷剂回路C中的与制冷用压缩机18的排出气体制冷剂进行热交换的板式热交换器19。In the upstream side liquid pipe 17 of the refrigerating evaporator 6 of the refrigerating refrigerant circuit B, there is installed a refrigerant in the refrigerating refrigerant circuit C described later that exchanges heat with the exhaust gas refrigerant of the refrigerating
所述制冷用制冷剂回路C是通过制冷剂配管按顺序将制冷用压缩机18、所述板式热交换器19、感温膨胀阀20、制冷用蒸发器21和储能器22连接而成。The refrigerating refrigerant circuit C is formed by sequentially connecting the refrigerating
在所述使用侧热交换器5与所述桥接回路14之间,安装着由电磁开闭阀24与只能在制冷运转时才允许制冷剂流通的单向阀25的串联回路23a以及电磁开闭阀26与只能在制热运转时才允许制冷剂流通的单向阀27的串联回路23b所组成的可逆流通机构23。另外,在所述可逆流通机构23中,设有迂回电磁开闭阀26的放液用的毛细管28。Between the use-side heat exchanger 5 and the bridging circuit 14, a series circuit 23a consisting of an electromagnetic on-off valve 24 and a one-way valve 25 that allows refrigerant to flow only in cooling operation and an electromagnetic on-off valve are installed. The reversible flow mechanism 23 is composed of the closed valve 26 and the series circuit 23b of the one-way valve 27 which allows the refrigerant to flow only in the heating operation. In addition, the reversible flow mechanism 23 is provided with a capillary tube 28 for liquid discharge that bypasses the electromagnetic on-off valve 26 .
在所述冷藏用制冷剂回路13中,设有迂回所述冷藏用蒸发器6的旁通回路29。在该旁通回路29中,安装着只能在冷藏用蒸发器6停止运转时才作出打开动作的电磁开闭阀30。The refrigerant circuit 13 for refrigeration is provided with a bypass circuit 29 that bypasses the evaporator 6 for refrigeration. In this bypass circuit 29, an electromagnetic on-off valve 30 that opens only when the refrigerating evaporator 6 is stopped is installed.
又,在所述冷藏用制冷剂回路B中,设有只能在冷藏用蒸发器6停止运转时才作出关闭动作的电磁开闭阀31。在所述制冷用制冷剂回路C中,设有只能在制冷用蒸发器21停止运转时才作出关闭动作的电磁开闭阀32。Furthermore, in the refrigerant circuit B for refrigeration, there is provided an electromagnetic on-off valve 31 that is closed only when the evaporator 6 for refrigeration is stopped. In the cooling refrigerant circuit C, there is provided an electromagnetic on-off valve 32 that is closed only when the cooling evaporator 21 is stopped.
又,在所述使用侧热交换器5上设有室内风扇33,在所述冷藏用蒸发器6上设有冷藏用风扇34,在所述制冷用蒸发器21上设有制冷用风扇35。Furthermore, an indoor fan 33 is provided on the use-side heat exchanger 5 , a cooling fan 34 is provided on the cooling evaporator 6 , and a cooling fan 35 is provided on the cooling evaporator 21 .
在所述压缩机1A、1B的排出管47上,设有分离气体制冷剂中包含的润滑油用的油分离器36。由该油分离器36分离的润滑油经过回油通道37而回流到压缩机1A、1B的吸入管38。在该回油通道37中,设有在回油时作出打开动作的电磁开闭阀39。An
又,在所述压缩机1A、1B的排出侧,设有检测该压缩机1A、1B排出压力即高压压力的起到高压压力检测装置作用的压力传感器40。所述制冷装置具有检测室内空气温度的室温传感器41,并在所述压缩机1A、1B的排出侧,设有检测排出气体制冷剂温度的排出温度传感器42,在所述压缩机1A、1B的吸入侧,设有检测吸入气体制冷剂压力的压力传感器43。所述制冷装置具有检测外部空气温度的外部空气温传感器44。在所述空调用制冷剂回路A和制冷用制冷剂回路C中,设有闭锁阀45、46。Also, on the discharge side of the
在上述结构的制冷装置中,可获得如下作用效果。In the refrigerating apparatus configured as described above, the following effects can be obtained.
(Ⅰ)制冷运转(I) Cooling operation
此时,四通转换阀2如图6的实线所示那样进行转换,电磁开闭阀13作出打开动作,电磁开闭阀16作出关闭动作,电磁开闭阀24作出打开动作,电磁开闭阀26作出关闭动作,电磁开闭阀30作出关闭动作,电磁开闭阀31、32作出打开动作,电磁开闭阀39作出打开动作。At this time, the four-
在空调用制冷剂回路A中,从压缩机1A、1B排出的气体制冷剂在起冷凝器作用的热源侧热交换器3中冷凝液化后,经过单向阀15和桥接回路14而被送入储蓄罐7。来自该储蓄罐7的液相部的液态制冷剂在第1过冷却热交换器8中经过与室外空气的热交换后被过冷却。若需要进一步过冷却,即在电磁开闭阀13作出打开动作时,来自所述第1过冷却热交换器8的过冷却液态制冷剂在第2过冷却热交换器9中是该过冷却液态制冷剂的一部分,并利用由感温膨胀阀10减压后的气液混合制冷剂的蒸发潜热而被进一步过冷却。所述液态制冷剂经膨胀阀4减压而供给到使用侧热交换器5进行蒸发,获得的蒸发潜热就可用于制冷用冷热源。然后,所述制冷剂回流到压缩机1A、1B。In the air-conditioning refrigerant circuit A, the gas refrigerant discharged from the
又,在冷藏用制冷剂回路B中,经所述膨胀阀4减压后的制冷剂从所述空调用制冷剂回路A分支,再经过板式热交换器19而供给到冷藏用蒸发器6进行蒸发,获得的蒸发潜热就可用于冷藏用冷热源。然后,所述制冷剂回流到压缩机1A、1B。In addition, in the refrigerant circuit B for refrigeration, the refrigerant decompressed by the expansion valve 4 is branched from the refrigerant circuit A for air conditioning, and then supplied to the evaporator 6 for refrigeration through the plate heat exchanger 19 for further processing. Evaporation, the latent heat of evaporation obtained can be used as a cold and heat source for refrigeration. Then, the refrigerant is returned to the
此外,在制冷用制冷剂回路C中,从制冷用压缩机18排出的气体制冷剂在起到冷凝器作用的板式热交换器19中,与冷藏用制冷剂回路B中的流过液管17的液态制冷剂热交换后形成冷凝液化。然后,冷凝后的液态制冷剂经膨胀阀20减压而供给到制冷用蒸发器21进行蒸发,获得的蒸发潜热就可用于冷冻用冷热源。然后,所述制冷剂经过储能器22回流到压缩机18。In addition, in the refrigerant circuit C for refrigeration, the gas refrigerant discharged from the
但在冷藏、制冷的库内温度较高时,为防止冷藏、冷冻的通风,最好让室内风扇33低速运转。But when temperature is higher in the storehouse of refrigeration, refrigeration, for preventing the ventilation of refrigeration, freezing, preferably allow indoor fan 33 low-speed operation.
(Ⅱ)制热运转(Ⅱ) Heating operation
此时,四通转换阀2如图6的虚线所示那样进行转换,电磁开闭阀13作出打开动作,电磁开闭阀16作出关闭动作,电磁开闭阀24作出关闭动作,电磁开闭阀26作出打开动作,电磁开闭阀30作出关闭动作,电磁开闭阀31、32作出打开动作,电磁开闭阀39作出打开动作。At this time, the four-
在空调用制冷剂回路A中,从压缩机1A、1B排出的气体制冷剂在起到冷凝器作用的使用侧热交换器5中被冷凝液化,获得的冷凝潜热就可用于制热热源。然后,所述液态制冷剂经过单向阀15和桥接回路14被送入储蓄罐7,来自该储蓄罐7的液相部的液态制冷剂在第1过冷却热交换器8中与室外空气热交换而被过冷却。若需要进一步过冷却,即在电磁开闭阀13作出打开动作时,来自所述第1过冷却热交换器8的过冷却液态制冷剂在第2过冷却热交换器9中是该过冷却液态制冷剂的一的那部分,并利用由感温膨胀阀10减压后的气液混合制冷剂的蒸发潜热而被进一步过冷却。然后,所述液态制冷剂由膨胀阀4减压并经过冷藏用制冷剂回路B中的板式热交换器19而供给到蒸发器6进行蒸发,获得的蒸发潜热就可用于冷藏用冷热源。然后,所述制冷剂回流到压缩机1A、1B。In the air-conditioning refrigerant circuit A, the gas refrigerant discharged from the
另外,在制冷用制冷剂回路C中,从制冷用压缩机18排出的气体制冷剂在起到冷凝器作用的板式热交换器19中,与冷藏用制冷剂回路B中的流过液管17的液态制冷剂热交换后被冷凝液化。然后,所述液态制冷剂经膨胀阀20减压而供给到制冷用蒸发器21进行蒸发,获得的蒸发潜热就可用于冷冻用冷热源。然后,所述制冷剂经过储能器22回流到压缩机18。In addition, in the refrigerant circuit C for refrigeration, the gas refrigerant discharged from the
如上所述,在本实施形态中,制热运转时在冷藏用制冷剂回路B的蒸发器6中用作冷藏用冷热源的废热可以在使用侧热交换器5中作为制热热源回收。此时,压缩机1A、1B中的1个停止运转。换言之,压缩机能力减弱。As described above, in the present embodiment, waste heat used as a cold heat source for refrigeration in the evaporator 6 of the refrigerant circuit B for refrigeration during heating operation can be recovered as a heating heat source in the use-side heat exchanger 5 . At this time, one of the
然而,在制热负载较小时,即在设定温度与室温之差较小时,蒸发器6中的冷藏用热源显得有点不足。为此,只要将四通转换阀2转换到制冷运转侧进行制冷循环,同时使电磁开闭阀16作出打开动作,使热源侧热交换器3起到冷凝器作用即可。另外,在该制冷循环的运转中,一旦制热负载加大,即设定温度与室温之差增大时,只要将四通转换阀2转换到制热运转侧进行制热循环,同时使电磁开闭阀16作出关闭动作,使使用侧热交换器5起到冷凝器作用,恢复到制热热回收运转即可。However, when the heating load is small, that is, when the difference between the set temperature and the room temperature is small, the heat source for refrigeration in the evaporator 6 is somewhat insufficient. To this end, it is only necessary to switch the four-
另外,在制热运转中,当冷藏负载和冷冻负载变小时,换言之,当压缩机1A、1B的吸入压力即低压压力减小时,若室内风扇33的风量自动减小,则可使使用侧热交换器5与蒸发器6之间的能力平衡。In addition, in the heating operation, when the refrigerating load and the refrigerating load become smaller, in other words, when the suction pressure of the
并且,在制热运转中,当冷藏·冷冻负载变小时,换言之,当压缩机1A、1B的吸入压力即低压压力减小时,由于使用侧热交换器5中的制热热源显得不足,因此,只要将电磁开闭阀16打开,让热源侧热交换器3起到蒸发器作用即可。In addition, in the heating operation, when the refrigerating/freezing load becomes small, in other words, when the suction pressure of the
另外,在室内风扇33停止驱动时,即,在使用侧热交换器5停止运转时,若室温不足规定的温度,也可将四通转换阀2转换到制热运转侧,并将电磁开闭阀16关闭,自动进行制热热回收运转。In addition, when the indoor fan 33 stops driving, that is, when the use-side heat exchanger 5 stops running, if the room temperature is lower than a predetermined temperature, the four-
在本实施形态中,如图7所示,所述吸入管38位于所述压缩机1A、1B的吸入口50A、50B的下方。所述回油通道37在所述第1压缩机1A(即容量大的压缩机)吸入口50A附近,与所述吸入管38连接,又在所述均油管48上,设置当所述压缩机1A、1B中的某1个停止运转时作出关闭动作的电磁开闭阀49。另外,在所述回油通道37中,设有过滤器51。In this embodiment, as shown in FIG. 7 , the
如图3所示,对所述压缩机1A、1B和电磁开闭阀39、40进行开闭(ON/OFF)动作。图中,O为打开,X为关闭。As shown in FIG. 3 , the
即,所述空调用制冷剂回路A具有将制冷机油返回到压缩机1A、1B的分配机构R。该分配机构R按照各压缩机1A、1B不同的容量而将空调用制冷剂回路A循环的制冷剂中的制冷机油向各压缩机1A、1B进行分配。本实施形态的分配机构R是按照将制冷剂回路A循环的制冷剂中的制冷机油从最大容量的压缩机1A向其它压缩机1B进行分配的原则而使该制冷机油回流到压缩机1A、1B。That is, the air-conditioning refrigerant circuit A has a distribution mechanism R for returning the refrigerating machine oil to the
具体来讲,所述分配机构R具有所述均油管48、油分离器36和回油通道37。所述分配机构R的结构是将由所述油分离器36分离的制冷机油和所述压缩机1A、1B的吸入气体制冷剂中包含的制冷机油优先回流到最大容量的第1压缩机1A。Specifically, the distribution mechanism R has the
采用上述结构,当压缩机1A、1B一起运转时,电磁开闭阀39、49一起作出打开动作。由油分离器36分离的制冷机油F经过回油通道37返回到吸入管38,与吸入气体制冷剂中的制冷机油F一起随着吸入压力而各自回流到压缩机1A、1B。With the above structure, when the
此时,大部分的制冷机油F返回到容量大的第1压缩机1A。并且,因容量大的第1压缩机1A的内压大于第2压缩机1B,故制冷机油F经过均油管48而向容量小的第2压缩机1B移动,能可靠地回流到两压缩机1A、1B。因此,即使不象以往那样执行压缩机交替运转的油的均量运转控制,也能确保压缩机1A、1B中的制冷机油F。At this time, most of the refrigerating machine oil F is returned to the
并且,在压缩机1A、1B一起停止运转时,因开闭阀39作出关闭动作,回油通道37成为非连通状态,故运转停止时制冷剂不会从油分离器36流向吸入侧。Furthermore, when the
另外,当压缩机1A、1B中的某1个停止运转时,开闭阀49作出关闭动作,经过均油管48的制冷机油F就不会移动。结果是,禁止制冷机油F从运转中的压缩机向运转停止状态的压缩机移动,不会使运转中的压缩机产生制冷机油F的不足。In addition, when one of the
另外,由于连接压缩机1A、1B的吸入管38位于压缩机1A、1B的吸入口50A、50B的下方,因此,在容量大的压缩机1A停止运转而容量小的压缩机1B运转时,可防止制冷机油F经过吸入管38流入容量大的压缩机1A。In addition, since the
第6实施形态Embodiment 6
图9表示本发明第6实施形态的制冷装置中的吸入管部分。Fig. 9 shows a portion of a suction pipe in a refrigeration device according to a sixth embodiment of the present invention.
本实施形态是在吸入口50A、50B的附近连接2条回油通道37A、37B,这样就能将由油分离器36分离的制冷机油F可靠地回流到第1压缩机1A和第2压缩机1B的吸入口50A、50B。另外,在所述回油通道37A、37B中,分别设有在压缩机1A、1B一起停止运转时作出关闭动作的开闭阀39A、39B。In this embodiment, two
这样,当压缩机1A、1B一起运转时,由油分离器36分离的制冷机油经过回油通道37A、37B后,与吸入气体制冷剂中的制冷机油一起分别回流到压缩机1A、1B。结果是更加可靠地进行油回油。其它结构及其作用效果与第5实施形态相同,故省略说明。In this way, when the
其它实施形态Other implementation forms
在所述第1、第3和第4实施形态中,对具有不同容量的2个压缩机的制冷装置作了说明。然而,本发明也可具有不同容量的3个以上压缩机。例如,本发明也可适用于具有3HP、4HP、4HP容量的3个压缩机的制冷装置或者具有3HP、4HP、5HP容量的3个压缩机的制冷装置。In the above-mentioned first, third and fourth embodiments, a refrigerator having two compressors with different capacities has been described. However, the invention is also possible with more than 3 compressors of different capacities. For example, the present invention can also be applied to a refrigerating apparatus having three compressors with capacities of 3HP, 4HP, and 4HP or a refrigerating apparatus having three compressors with capacities of 3HP, 4HP, and 5HP.
工业上利用的可能性Possibility of industrial use
综上所述,本发明的制冷装置适用于具有多个压缩机的空调装置,尤其适用于具有不同容量的多个压缩机。To sum up, the refrigerating device of the present invention is suitable for an air-conditioning device with multiple compressors, especially suitable for multiple compressors with different capacities.
Claims (15)
Applications Claiming Priority (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP206064/1999 | 1999-07-21 | ||
| JP206064/99 | 1999-07-21 | ||
| JP20606499A JP3407697B2 (en) | 1999-07-21 | 1999-07-21 | Refrigeration equipment |
| JP2000097093A JP2001280719A (en) | 2000-03-31 | 2000-03-31 | Refrigeration equipment |
| JP097093/00 | 2000-03-31 | ||
| JP097093/2000 | 2000-03-31 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1318145A true CN1318145A (en) | 2001-10-17 |
| CN100453920C CN100453920C (en) | 2009-01-21 |
Family
ID=26515429
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB008014485A Expired - Fee Related CN100453920C (en) | 1999-07-21 | 2000-07-19 | refrigeration unit |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP1120611A4 (en) |
| CN (1) | CN100453920C (en) |
| AU (1) | AU749518B2 (en) |
| WO (1) | WO2001006181A1 (en) |
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| CN103062841A (en) * | 2013-01-18 | 2013-04-24 | 四川长虹电器股份有限公司 | Air-conditioning system, control system and air-conditioning control method |
| CN104641116A (en) * | 2012-07-31 | 2015-05-20 | 比策尔制冷机械制造有限公司 | Suction Head Units for Oil Management in Multiple Compressor Systems |
| CN104641117A (en) * | 2012-07-31 | 2015-05-20 | 比策尔制冷机械制造有限公司 | Method of active oil management for multiple scroll compressors |
| CN104641117B (en) * | 2012-07-31 | 2016-11-30 | 比策尔制冷机械制造有限公司 | Active oil management method for multiple scroll compressors |
| CN108562021A (en) * | 2018-04-25 | 2018-09-21 | 青岛海信日立空调系统有限公司 | A kind of dehumidification control method and device, air conditioner of air conditioner indoor unit |
| CN110023693A (en) * | 2016-11-24 | 2019-07-16 | 大金工业株式会社 | Refrigerating plant |
| US10760831B2 (en) | 2016-01-22 | 2020-09-01 | Bitzer Kuehlmaschinenbau Gmbh | Oil distribution in multiple-compressor systems utilizing variable speed |
| WO2021169213A1 (en) * | 2020-02-27 | 2021-09-02 | 艾默生环境优化技术(苏州)有限公司 | Multi-split air conditioning system, oil balancing device thereof, and oil balancing control method thereof |
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| CN110023693A (en) * | 2016-11-24 | 2019-07-16 | 大金工业株式会社 | Refrigerating plant |
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| CN108562021B (en) * | 2018-04-25 | 2020-05-15 | 青岛海信日立空调系统有限公司 | Dehumidification control method and device for indoor unit of air conditioner and air conditioner |
| WO2021169213A1 (en) * | 2020-02-27 | 2021-09-02 | 艾默生环境优化技术(苏州)有限公司 | Multi-split air conditioning system, oil balancing device thereof, and oil balancing control method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| AU749518B2 (en) | 2002-06-27 |
| AU6020000A (en) | 2001-02-05 |
| WO2001006181A1 (en) | 2001-01-25 |
| CN100453920C (en) | 2009-01-21 |
| EP1120611A4 (en) | 2012-05-23 |
| EP1120611A1 (en) | 2001-08-01 |
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