CN107906777A - Heat pump unit - Google Patents
Heat pump unit Download PDFInfo
- Publication number
- CN107906777A CN107906777A CN201711003712.9A CN201711003712A CN107906777A CN 107906777 A CN107906777 A CN 107906777A CN 201711003712 A CN201711003712 A CN 201711003712A CN 107906777 A CN107906777 A CN 107906777A
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- Prior art keywords
- heat exchanger
- heat
- pump unit
- defrosting
- heat pump
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- 239000007788 liquid Substances 0.000 claims abstract description 93
- 238000010257 thawing Methods 0.000 claims abstract description 65
- 239000011552 falling film Substances 0.000 claims description 30
- 239000007921 spray Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 abstract description 16
- 238000004378 air conditioning Methods 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 25
- 238000000034 method Methods 0.000 description 21
- 238000001816 cooling Methods 0.000 description 6
- 230000006835 compression Effects 0.000 description 5
- 238000007906 compression Methods 0.000 description 5
- 239000010687 lubricating oil Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Classifications
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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
- F25B13/00—Compression machines, plants or systems, with reversible cycle
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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
- F25B41/00—Fluid-circulation arrangements
- F25B41/20—Disposition of valves, e.g. of on-off valves or flow control valves
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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
- F25B47/00—Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
- F25B47/02—Defrosting cycles
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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
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/023—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units
- F25B2313/0232—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units with bypasses
- F25B2313/02322—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units with bypasses during defrosting
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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
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/023—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units
- F25B2313/0234—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units in series arrangements
- F25B2313/02342—Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units in series arrangements during defrosting
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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
- F25B2313/00—Compression machines, plants or systems with reversible cycle not otherwise provided for
- F25B2313/027—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
- F25B2313/02741—Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
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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
- F25B2347/00—Details for preventing or removing deposits or corrosion
- F25B2347/02—Details of defrosting cycles
- F25B2347/021—Alternate defrosting
-
- 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
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Abstract
本发明属于空调技术领域,具体涉及一种热泵机组。本发明旨在解决现有热泵机组在除霜模式转换至制热模式时,大量液态换热介质涌入气液分离器中很容易导致压缩机吸气带液的问题。为此,本发明的热泵机组包括主循环回路以及与主循环回路相连通的除霜回液管路;主循环回路上设置有彼此连通的压缩机、第一换热器和第二换热器,在除霜模式下,第一换热器用作冷凝器,第二换热器用作蒸发器;除霜回液管路用于在除霜结束后,将第一换热器中的液态换热介质直接导流至第二换热器中,从而有效防止除霜结束后大量液态换热介质从第一换热器中流入至气液分离器中而导致其超负荷工作,进而导致部分液态换热介质直接进入到压缩机中,致使压缩机吸气带液而被损坏。
The invention belongs to the technical field of air conditioning, and in particular relates to a heat pump unit. The invention aims to solve the problem that when a large amount of liquid heat exchange medium pours into the gas-liquid separator when the existing heat pump unit is switched from the defrosting mode to the heating mode, it is easy to cause the compressor to absorb liquid. For this reason, the heat pump unit of the present invention includes a main circulation loop and a defrosting liquid return pipeline communicated with the main circulation loop; a compressor, a first heat exchanger and a second heat exchanger communicated with each other are arranged on the main circulation loop , in the defrosting mode, the first heat exchanger is used as a condenser, and the second heat exchanger is used as an evaporator; the defrosting return line is used to exchange heat from the liquid in the first heat exchanger after defrosting The medium is directly diverted to the second heat exchanger, which effectively prevents a large amount of liquid heat exchange medium from flowing into the gas-liquid separator from the first heat exchanger after defrosting, which will cause it to overload and cause partial liquid exchange. The heat medium directly enters the compressor, causing the compressor to be damaged due to the suction of liquid.
Description
技术领域technical field
本发明属于空调技术领域,具体涉及一种热泵机组。The invention belongs to the technical field of air conditioning, and in particular relates to a heat pump unit.
背景技术Background technique
随着人们生活水平的不断提高,人们对生活环境也提出了越来越高的要求。为了维持舒适的环境温度,空调设备已经成为人们生活中必不可少的一种设备。具体地,现有空调设备大多使用的是热泵机组,当热泵机组的外部环境温度很低时,热泵机组的蒸发装置很容易产生结霜现象,此时,热泵机组就需要对蒸发装置进行除霜处理,技术人员就热泵机组的除霜问题提出了很多种方案。With the continuous improvement of people's living standards, people have also put forward higher and higher requirements for the living environment. In order to maintain a comfortable ambient temperature, air conditioners have become an essential device in people's lives. Specifically, most of the existing air conditioners use heat pump units. When the external ambient temperature of the heat pump unit is very low, the evaporator of the heat pump unit is prone to frosting. At this time, the heat pump unit needs to defrost the evaporator. To deal with it, the technicians put forward many solutions for the defrosting of the heat pump unit.
具体地,现有热泵机组大多使用制热模式的逆循环过程为蒸发装置进行除霜;这种除霜模式虽然能够在有效除霜的基础上节省生产成本;但是,当热泵机组需要从除霜模式转换至制热模式时,控制装置控制四通阀转向,大量液态换热介质突然逆流,此时,大量液态换热介质都会涌入气液分离器,当换热介质单位时间流入气液分离器的量超过该气液分离器的额定工作量时,液态换热介质很容易直接进入到压缩机中,对压缩机造成吸气带液的危险,极大程度地缩短了压缩机的寿命,影响了热泵机组的可靠性。Specifically, most existing heat pump units use the reverse cycle process of the heating mode to defrost the evaporator; although this defrosting mode can save production costs on the basis of effective defrosting; however, when the heat pump unit needs to defrost from When the mode is switched to the heating mode, the control device controls the direction of the four-way valve, and a large amount of liquid heat exchange medium suddenly flows backwards. At this time, a large amount of liquid heat exchange medium will pour into the gas-liquid separator. When the volume of the gas-liquid separator exceeds the rated workload of the gas-liquid separator, the liquid heat exchange medium is easy to directly enter the compressor, causing the danger of the compressor being sucked with liquid, which greatly shortens the life of the compressor. Affect the reliability of the heat pump unit.
相应地,本领域需要一种新的热泵机组来解决上述问题。Correspondingly, the field needs a new heat pump unit to solve the above problems.
发明内容Contents of the invention
为了解决现有技术中的上述问题,即为了解决现有热泵机组在除霜模式转换至制热模式时,大量液态换热介质涌入气液分离器中很容易导致压缩机吸气带液的问题,本发明提供了一种热泵机组,所述热泵机组包括主循环回路以及与所述主循环回路相连通的除霜回液管路;其中,所述主循环回路上设置有彼此连通的压缩机、第一换热器和第二换热器,在除霜模式下,所述第一换热器用作冷凝器,所述第二换热器用作蒸发器;所述除霜回液管路用于在除霜结束后,将所述第一换热器中的液态换热介质直接导流至所述第二换热器中。In order to solve the above-mentioned problems in the prior art, that is, in order to solve the problem that when the existing heat pump unit switches from the defrosting mode to the heating mode, a large amount of liquid heat exchange medium pours into the gas-liquid separator, which can easily cause the compressor to suck liquid Problem, the present invention provides a heat pump unit, the heat pump unit includes a main circulation loop and a defrost return pipeline connected with the main circulation loop; wherein, the main circulation loop is provided with compressors communicating with each other Machine, the first heat exchanger and the second heat exchanger, in the defrosting mode, the first heat exchanger is used as a condenser, and the second heat exchanger is used as an evaporator; the defrosting liquid return line After defrosting, the liquid heat exchange medium in the first heat exchanger is directly guided into the second heat exchanger.
在上述热泵机组的优选技术方案中,所述除霜回液管路上设置有开关阀,所述除霜回液管路通过所述开关阀来实现所述除霜回液管路的通断。In the preferred technical solution of the above heat pump unit, a switching valve is arranged on the defrosting liquid return line, and the defrosting liquid return line is switched on and off through the switching valve.
在上述热泵机组的优选技术方案中,所述开关阀为电磁阀。In a preferred technical solution of the above heat pump unit, the on-off valve is a solenoid valve.
在上述热泵机组的优选技术方案中,所述主循环回路包括以并联方式设置在所述第一换热器与所述第二换热器之间的第一主循环支路和第二主循环支路,所述除霜回液管路与所述第二主循环支路连通。In a preferred technical solution of the above heat pump unit, the main circulation loop includes a first main circulation branch and a second main circulation arranged in parallel between the first heat exchanger and the second heat exchanger branch, the defrosting liquid return line communicates with the second main circulation branch.
在上述热泵机组的优选技术方案中,所述主循环回路还包括设置在所述第一主循环支路与所述第二主循环支路之间的桥接支路,所述桥接支路中设置有膨胀阀。In the preferred technical solution of the above-mentioned heat pump unit, the main circulation loop further includes a bridge branch arranged between the first main circulation branch and the second main circulation branch, and the bridge branch is set With expansion valve.
在上述热泵机组的优选技术方案中,所述桥接支路将所述第一主循环支路和所述第二主循环支路分别划分为第一部分和第二部分,所述除霜回液管路与所述第二主循环支路的第二部分并联;其中,所述第一主循环支路的第一部分设置有第一单向阀,所述第一主循环支路的第二部分设置有第二单向阀,所述第二主循环支路的第一部分设置有第三单向阀,所述第二主循环支路的第二部分设置有第四单向阀;所述第一单向阀仅允许换热介质流入所述第一换热器,所述第二单向阀仅允许换热介质流入所述第二换热器,所述第三单向阀仅允许换热介质流出所述第一换热器,所述第四单向阀仅允许换热介质流出所述第二换热器。In the preferred technical solution of the above-mentioned heat pump unit, the bridging branch divides the first main circulation branch and the second main circulation branch into a first part and a second part respectively, and the defrosting liquid return pipe The road is connected in parallel with the second part of the second main circulation branch; wherein, the first part of the first main circulation branch is provided with a first check valve, and the second part of the first main circulation branch is provided with There is a second one-way valve, the first part of the second main circulation branch is provided with a third one-way valve, and the second part of the second main circulation branch is provided with a fourth one-way valve; the first The one-way valve only allows the heat exchange medium to flow into the first heat exchanger, the second one-way valve only allows the heat exchange medium to flow into the second heat exchanger, and the third one-way valve only allows the heat exchange medium to out of the first heat exchanger, the fourth one-way valve only allows the heat exchange medium to flow out of the second heat exchanger.
在上述热泵机组的优选技术方案中,所述第一换热器为翅片式换热器。In a preferred technical solution of the above heat pump unit, the first heat exchanger is a finned heat exchanger.
在上述热泵机组的优选技术方案中,所述第二换热器为降膜式换热器。In a preferred technical solution of the above heat pump unit, the second heat exchanger is a falling film heat exchanger.
在上述热泵机组的优选技术方案中,所述降膜式换热器包括喷淋元件和换热元件;在除霜过程中,所述喷淋元件将液态换热介质直接喷淋至所述换热元件上,以便缩短除霜时间。In the preferred technical solution of the above-mentioned heat pump unit, the falling film heat exchanger includes a spray element and a heat exchange element; during the defrosting process, the spray element directly sprays the liquid heat exchange medium to the on the heating element to shorten the defrost time.
在上述热泵机组的优选技术方案中,所述压缩机为双级螺杆压缩机。In a preferred technical solution of the above heat pump unit, the compressor is a two-stage screw compressor.
本领域技术人员能够理解的是,在本发明的优选技术方案中,本发明的热泵机组包括主循环回路以及与主循环回路相连通的除霜回液管路;其中,主循环回路上设置有彼此连通的压缩机、第一换热器和第二换热器,在除霜模式下,第一换热器用作冷凝器,第二换热器用作蒸发器;除霜回液管路用于在除霜结束后,将第一换热器中的液态换热介质直接导流至第二换热器中,从而有效防止除霜结束后大量液态换热介质从第一换热器中流入至气液分离器中而导致气液分离器超负荷工作,进而导致一部分液态换热介质直接进入到压缩机中,致使压缩机吸气带液而被损坏。Those skilled in the art can understand that, in the preferred technical solution of the present invention, the heat pump unit of the present invention includes a main circulation loop and a defrosting liquid return pipeline connected with the main circulation loop; wherein, the main circulation loop is provided with The compressor, the first heat exchanger and the second heat exchanger communicate with each other. In the defrosting mode, the first heat exchanger is used as a condenser, and the second heat exchanger is used as an evaporator; the defrosting return line is used for After defrosting, the liquid heat exchange medium in the first heat exchanger is directly guided into the second heat exchanger, thereby effectively preventing a large amount of liquid heat exchange medium from flowing into the first heat exchanger after defrosting. In the gas-liquid separator, the gas-liquid separator is overloaded, which in turn causes a part of the liquid heat exchange medium to directly enter the compressor, causing the compressor to be damaged due to the suction of liquid.
附图说明Description of drawings
图1是本发明的热泵机组的简化示意图;Fig. 1 is a simplified schematic diagram of the heat pump unit of the present invention;
图2是本发明的热泵机组的优选实施例的整体示意图。Fig. 2 is an overall schematic diagram of a preferred embodiment of the heat pump unit of the present invention.
附图标记说明:1、压缩机;2、油分离器;3、压力维持阀;4、四通阀;5、降膜式换热器;61、第一单向阀;62、第二单向阀;63、第三单向阀;64、第四单向阀;7、过滤器;8、经济器;9、膨胀阀;10、翅片式换热器;11、气液分离器;12、电磁阀;13、风机;14、油冷却器;15、流量计;16、经济器膨胀阀;17、油冷却膨胀阀;18、旁通电磁阀;19、供油电磁阀;101、第一主循环支路;102、第二主循环支路。Explanation of reference signs: 1. Compressor; 2. Oil separator; 3. Pressure maintaining valve; 4. Four-way valve; 5. Falling film heat exchanger; 61. First one-way valve; 62. Second one-way valve 63. The third one-way valve; 64. The fourth one-way valve; 7. Filter; 8. Economizer; 9. Expansion valve; 10. Finned heat exchanger; 11. Gas-liquid separator; 12. Solenoid valve; 13. Fan; 14. Oil cooler; 15. Flow meter; 16. Economizer expansion valve; 17. Oil cooling expansion valve; 18. Bypass solenoid valve; 19. Oil supply solenoid valve; 101. The first main circulation branch; 102, the second main circulation branch.
具体实施方式Detailed ways
下面参照附图来描述本发明的优选实施方式。本领域技术人员应当理解的是,这些实施方式仅仅用于解释本发明的技术原理,并非旨在限制本发明的保护范围。本领域技术人员可以根据需要对其作出调整,以便适应具体的应用场合。同时,尽管本申请中按照特定顺序描述了本发明的方法的各个步骤,但是这些顺序并不是限制性的,在不偏离本发明的基本原理的前提下,本领域技术人员可以按照不同的顺序来执行所述步骤。Preferred embodiments of the present invention are described below with reference to the accompanying drawings. Those skilled in the art should understand that these embodiments are only used to explain the technical principles of the present invention, and are not intended to limit the protection scope of the present invention. Those skilled in the art can make adjustments as needed so as to adapt to specific applications. At the same time, although the various steps of the method of the present invention are described in a specific order in the application, these orders are not limiting, and those skilled in the art can perform the steps in different orders without departing from the basic principles of the present invention. Follow the steps described.
需要说明的是,在本发明的描述中,术语“上”、“下”、“左”、“右”等指示的方向或位置关系的术语是基于附图中所示的方向或位置关系,这样仅仅是为了便于描述,而不是指示或暗示所述装置或元件必须具有特定的方位或者必须以特定的方位构造和操作,因此不能理解为对本发明的限制。此外,术语“第一”、“第二”、“第三”、“第四”仅用于描述目的,而不能理解为指示或暗示相对重要性。It should be noted that, in the description of the present invention, terms such as "upper", "lower", "left", "right" and other indicated directions or positional relationships are based on the directions or positional relationships shown in the drawings, This is for ease of description only, and does not indicate or imply that the device or element must have a particular orientation or must be constructed and operated in a particular orientation, and thus should not be construed as limiting the invention. In addition, the terms "first", "second", "third", and "fourth" are used for descriptive purposes only, and should not be construed as indicating or implying relative importance.
基于背景技术中提出的现有热泵机组大多使用制热模式的逆循环过程为蒸发装置进行除霜的方式;这种除霜方式虽然能够在有效除霜的基础上节省生产成本;但是,当热泵机组需要从除霜模式转换至制热模式时,热泵机组的控制装置控制四通阀转向,此时,大量液态换热介质突然逆流并涌入气液分离器中,当换热介质单位时间流入气液分离器的量超过该气液分离器的额定工作量时,液态换热介质很容易直接进入到压缩机中,对压缩机带来吸气带液的风险。为此,本发明提供了一种新的热泵机组来解决现有技术中的上述问题。Most of the existing heat pump units proposed in the background technology use the reverse cycle process of the heating mode to defrost the evaporator; although this defrosting method can save production costs on the basis of effective defrosting; however, when the heat pump When the unit needs to switch from the defrosting mode to the heating mode, the control device of the heat pump unit controls the direction of the four-way valve. When the amount of the gas-liquid separator exceeds the rated workload of the gas-liquid separator, the liquid heat exchange medium is easy to directly enter the compressor, which brings the risk of suction and liquid to the compressor. Therefore, the present invention provides a new heat pump unit to solve the above-mentioned problems in the prior art.
首先参阅图1,该图为本发明的热泵机组的简化示意图。如图1所示,本发明的热泵机组包括主循环回路以及与所述主循环回路相连通的除霜回液管路;其中,所述主循环回路上设置有彼此连通的压缩机1、翅片式换热器10和降膜式换热器5,在除霜模式下,翅片式换热器10用作冷凝器,降膜式换热器5用作蒸发器;所述除霜回液管路用于在除霜结束后,将翅片式换热器10中的液态换热介质直接导流至降膜式换热器5中,从而有效防止除霜结束后大量液态换热介质从翅片式换热器10中流入至气液分离器11中而导致气液分离器11超负荷工作,进而导致部分液态换热介质直接进入到压缩机1中,致使压缩机1吸气带液而被损坏。Referring first to FIG. 1 , this figure is a simplified schematic diagram of the heat pump unit of the present invention. As shown in Figure 1, the heat pump unit of the present invention includes a main circulation loop and a defrosting liquid return pipeline connected with the main circulation loop; wherein, the main circulation loop is provided with a compressor 1, a fin The fin heat exchanger 10 and the falling film heat exchanger 5, in the defrosting mode, the fin heat exchanger 10 is used as a condenser, and the falling film heat exchanger 5 is used as an evaporator; the defrosting return The liquid pipeline is used to direct the liquid heat exchange medium in the finned heat exchanger 10 to the falling film heat exchanger 5 after defrosting, so as to effectively prevent a large amount of liquid heat exchange medium after defrosting Flowing from the finned heat exchanger 10 into the gas-liquid separator 11 will cause the gas-liquid separator 11 to work overloaded, and then cause part of the liquid heat exchange medium to directly enter the compressor 1, causing the compressor 1 to take suction. liquid will be damaged.
本领域技术人员能够理解的是,虽然在本优选实施例中,所述第一换热器为翅片式换热器10,并且所述第二换热器为降膜式换热器5;但是,所述第一换热器和所述第二换热器显然还可以是其他类型的换热器,这种换热器类型的改变并不偏离本发明的基本原理,因此都将落入本发明的保护范围之内。Those skilled in the art can understand that although in this preferred embodiment, the first heat exchanger is a finned heat exchanger 10, and the second heat exchanger is a falling film heat exchanger 5; However, the first heat exchanger and the second heat exchanger can obviously also be other types of heat exchangers, and the change of this type of heat exchanger does not deviate from the basic principle of the present invention, so it will all fall into the within the protection scope of the present invention.
进一步地,如图1所示,所述主循环回路包括以并联方式设置在翅片式换热器10与降膜式换热器5之间的第一主循环支路101和第二主循环支路102;其中,第一主循环支路101位于上虚线框中,第二主循环支路102位于下虚线框中,并且所述除霜回液管路与第二主循环支路102连通,所述除霜回液管路上设置有电磁阀12,所述除霜回液管路通过电磁阀12来实现所述除霜回液管路的通断。需要说明的是,虽然本优选实施例中所述的设置在所述除霜回液管路上的开关阀为电磁阀12,但是,所述开关阀显然还可以是其他能够控制管路通断的电气件,只要所述开关阀能够控制所述除霜回液管路的通断即可。同时,所述主循环回路还包括设置在第一主循环支路101与第二主循环支路102之间的桥接支路,所述桥接支路中设置有膨胀阀9,膨胀阀9能够控制第一主循环支路101与第二主循环支路102之间的通断。Further, as shown in FIG. 1 , the main circulation loop includes a first main circulation branch 101 and a second main circulation branch arranged in parallel between the finned heat exchanger 10 and the falling film heat exchanger 5 Branches 102; wherein, the first main circulation branch 101 is located in the upper dotted line box, the second main circulation branch 102 is located in the lower dotted line box, and the defrosting liquid return pipeline communicates with the second main circulation branch 102 A solenoid valve 12 is arranged on the defrosting liquid return line, and the defrosting liquid return line is switched on and off through the solenoid valve 12 . It should be noted that although the on-off valve set on the defrosting liquid return pipeline described in this preferred embodiment is a solenoid valve 12, the on-off valve can obviously also be other valves that can control the on-off of the pipeline. Electrical components, as long as the on-off valve can control the on-off of the defrosting liquid return pipeline. At the same time, the main circulation circuit also includes a bridging branch arranged between the first main circulation branch 101 and the second main circulation branch 102, and an expansion valve 9 is arranged in the bridging branch, and the expansion valve 9 can control On-off between the first main circulation branch 101 and the second main circulation branch 102 .
继续参阅图1,所述桥接支路将第一主循环支路101和第二主循环支路102分别划分为第一部分和第二部分,其中,所述除霜回液管路与第二主循环支路102的第二部分并联,同时,所述除霜回液管路还能够与第三单向阀63连通。具体地,第一主循环支路101的第一部分设置有第一单向阀61,第一主循环支路101的第二部分设置有第二单向阀62,第二主循环支路102的第一部分设置有第三单向阀63,第二主循环支路102的第二部分设置有第四单向阀64。需要说明的是,第一单向阀61仅允许换热介质流入翅片式换热器10,第二单向阀62仅允许换热介质流入降膜式换热器5,第三单向阀63仅允许换热介质流出翅片式换热器10,第四单向阀64仅允许换热介质流出降膜式换热器5。Continuing to refer to FIG. 1, the bridging branch divides the first main circulation branch 101 and the second main circulation branch 102 into a first part and a second part respectively, wherein the defrosting liquid return line is connected to the second main circulation branch The second part of the circulation branch 102 is connected in parallel, and at the same time, the defrosting liquid return line can also communicate with the third one-way valve 63 . Specifically, the first part of the first main circulation branch 101 is provided with the first one-way valve 61, the second part of the first main circulation branch 101 is provided with the second one-way valve 62, and the second main circulation branch 102 The first part is provided with a third one-way valve 63 , and the second part of the second main circulation branch 102 is provided with a fourth one-way valve 64 . It should be noted that the first one-way valve 61 only allows the heat exchange medium to flow into the finned heat exchanger 10, the second one-way valve 62 only allows the heat exchange medium to flow into the falling film heat exchanger 5, and the third one-way valve 63 only allows the heat exchange medium to flow out of the finned heat exchanger 10 , and the fourth one-way valve 64 only allows the heat exchange medium to flow out of the falling film heat exchanger 5 .
以下结合图1来具体描述本发明的热泵机组的制热模式和除霜模式的运行过程;当所述热泵机组运行制热模式时,所述热泵机组中的换热介质的循环流程为:压缩机1→油分离器2→压力维持阀3→四通阀4→降膜式换热器5→第四单向阀64→膨胀阀9→第一单向阀61→翅片式换热器10→四通阀4→气液分离器11→压缩机1。当所述热泵机组运行除霜模式时,翅片式换热器10用作冷凝器,降膜式换热器5用作蒸发器,此时,所述热泵机组中的换热介质的循环流程为:压缩机1→油分离器2→压力维持阀3→四通阀4→翅片式换热器10→第三单向阀63→膨胀阀9→第二单向阀62→降膜式换热器5→四通阀4→气液分离器11→压缩机1。Below in conjunction with Fig. 1, the operation process of the heating mode and the defrosting mode of the heat pump unit of the present invention will be specifically described; when the heat pump unit operates in the heating mode, the circulation process of the heat exchange medium in the heat pump unit is: compression Machine 1→oil separator 2→pressure maintenance valve 3→four-way valve 4→falling film heat exchanger 5→fourth one-way valve 64→expansion valve 9→first one-way valve 61→finned heat exchanger 10→four-way valve 4→gas-liquid separator 11→compressor 1. When the heat pump unit operates in defrosting mode, the finned heat exchanger 10 is used as a condenser, and the falling film heat exchanger 5 is used as an evaporator. At this time, the circulation process of the heat exchange medium in the heat pump unit It is: compressor 1→oil separator 2→pressure maintenance valve 3→four-way valve 4→finned heat exchanger 10→third check valve 63→expansion valve 9→second check valve 62→falling film type Heat exchanger 5→four-way valve 4→gas-liquid separator 11→compressor 1.
具体地,在所述热泵机组处于除霜模式时,翅片式换热器10处于高压状态,降膜式换热器5为低压状态;此时,翅片式换热器10中的换热介质在化霜过程中液化放热,以便运用换热介质液化放出的热量对翅片式换热器10进行化霜处理。需要说明的是,现有热泵机组在除霜结束后,直接使四通阀4换向,从而使得所述热泵机组开始运行制热模式,四通阀4换向后,翅片式换热器10中的液态换热介质通过四通阀4大量涌入气液分离器11中,从而导致气液分离器11超负荷工作,进而很容易导致部分液态换热介质直接进入到压缩机1中,致使压缩机1吸气带液而被损坏。Specifically, when the heat pump unit is in the defrosting mode, the finned heat exchanger 10 is in a high pressure state, and the falling film heat exchanger 5 is in a low pressure state; at this time, the heat exchange in the finned heat exchanger 10 The heat released by the liquefaction of the medium during the defrosting process is used to defrost the finned heat exchanger 10 by using the heat released by the liquefaction of the heat exchange medium. It should be noted that after the defrosting of the existing heat pump unit, the four-way valve 4 is directly reversed, so that the heat pump unit starts to operate in the heating mode. After the four-way valve 4 is reversed, the finned heat exchanger The liquid heat exchange medium in 10 floods into the gas-liquid separator 11 through the four-way valve 4 in large quantities, thus causing the gas-liquid separator 11 to work overloaded, and then it is easy to cause part of the liquid heat exchange medium to directly enter the compressor 1, Cause the compressor 1 to suck liquid and be damaged.
进一步地,本发明的热泵机组在除霜结束以后,四通阀4换向之前,先将电磁阀12打开;此时,由于翅片式换热器10处于高压状态,降膜式换热器5处于低压状态,在压力作用下,翅片式换热器10中的换热介质沿图1中的箭头方向直接流入至降膜式换热器5中,经过预定时间后,所述热泵机组控制电磁阀12关闭,同时使四通阀4换向,所述热泵机组重新运行制热模式。此时,翅片式换热器10中的大量液态换热介质已经回流至降膜式换热器5中,只有少部分或者根本没有液态换热介质会流入至气液分离器11中,同时,这部分液态换热介质的量也绝不可能超过气液分离器11的额定负荷;因此,在气液分离器11的保护作用下,压缩机1中也就不会有液态换热介质进入,使得压缩机1吸气带液的风险大大降低,从而极大程度地降低了压缩机1的损坏率,进而有效延长了压缩机1的使用寿命。Further, in the heat pump unit of the present invention, after the defrosting is completed, the electromagnetic valve 12 is opened before the four-way valve 4 changes direction; at this time, since the finned heat exchanger 10 is in a high pressure state, the falling film heat exchanger 5 is in a low-pressure state, and under pressure, the heat exchange medium in the fin heat exchanger 10 flows directly into the falling film heat exchanger 5 along the direction of the arrow in Figure 1, and after a predetermined time, the heat pump unit The solenoid valve 12 is controlled to close, and at the same time, the four-way valve 4 is reversed, and the heat pump unit resumes the heating mode. At this time, a large amount of liquid heat exchange medium in the finned heat exchanger 10 has flowed back into the falling film heat exchanger 5, only a small part or no liquid heat exchange medium will flow into the gas-liquid separator 11, and at the same time , the amount of this part of the liquid heat exchange medium can never exceed the rated load of the gas-liquid separator 11; therefore, under the protection of the gas-liquid separator 11, no liquid heat exchange medium will enter the compressor 1 , so that the risk of the compressor 1 being sucked with liquid is greatly reduced, thereby greatly reducing the damage rate of the compressor 1 , thereby effectively prolonging the service life of the compressor 1 .
本领域技术人员能够理解的是,本发明不对除霜是否结束的判断方法作任何限制,因为判断除霜是否结束的方法不在本发明的保护范围内,因此,技术人员可以根据实际产品的需要自行选定现有技术中的判断除霜结束的方法,这种判断方法的改变并不偏离本发明的基本原理,因此都将落入本发明的保护范围之内。另外,技术人员还可以根据产品的实际情况以及用户需求等条件自行设定所述预定时间的长短,只要经过所述预定时间后,通过翅片式换热器10流入至气液分离器11中的液态换热介质不会超过气液分离器11的额定工作量即可。Those skilled in the art can understand that the present invention does not impose any restrictions on the method of judging whether the defrosting is over, because the method of judging whether the defrosting is over is not within the protection scope of the present invention, therefore, technicians can make their own decisions according to the needs of actual products. The method of judging the end of defrosting in the prior art is selected, and the change of this judging method does not deviate from the basic principle of the present invention, so all will fall within the protection scope of the present invention. In addition, technicians can also set the length of the predetermined time according to the actual situation of the product and user needs and other conditions. As long as the predetermined time passes, it will flow into the gas-liquid separator 11 It is sufficient that the liquid heat exchange medium does not exceed the rated workload of the gas-liquid separator 11.
下面参阅图2,该图是本发明的热泵机组的优选实施例的整体示意图,需要说明的是,图2所示的实施例只是本发明的一种优选实施例,并不作为对本发明保护范围的限制。如图2所示,本优选实施例中的热泵机组运行制热模式时,所述热泵机组中的换热介质的循环流程为:压缩机1→油分离器2→压力维持阀3→四通阀4→降膜式换热器5→第四单向阀64→过滤器7→经济器8→膨胀阀9→第一单向阀61→翅片式换热器10→四通阀4→气液分离器11→压缩机1。在所述热泵机组运行制热模式时,翅片式换热器10用作蒸发器,翅片式换热器10中的液态换热介质蒸发吸热,降膜式换热器5用作冷凝器,同时,降膜式换热器5中的气态换热介质液化放热,以便对水进行加热。另外,从经济器8的出口处分流出的辅路中的换热介质通过经济器膨胀阀16进行节流后再回流至经济器8中,并且与主路中的换热介质进行充分的热交换,使得主路中的换热介质过冷,同时,辅路中过热态的换热介质通过压缩机1的中间补气口与完成第一级压缩后的换热介质混合后再进行第二级压缩,从而使得进入第二级压缩的换热介质的温度得到有效降低,同时还能够有效提升第二级压缩的吸气量,从而极大程度地增大所述热泵机组的制热量。Referring to Fig. 2 below, this figure is an overall schematic diagram of a preferred embodiment of the heat pump unit of the present invention. It should be noted that the embodiment shown in Fig. 2 is only a preferred embodiment of the present invention, and is not regarded as a protection scope of the present invention. limits. As shown in Figure 2, when the heat pump unit in this preferred embodiment operates in heating mode, the circulation process of the heat exchange medium in the heat pump unit is: compressor 1 → oil separator 2 → pressure maintenance valve 3 → four-way Valve 4→falling film heat exchanger 5→fourth one-way valve 64→filter 7→economizer 8→expansion valve 9→first one-way valve 61→finned heat exchanger 10→four-way valve 4→ Gas-liquid separator 11→compressor 1. When the heat pump unit operates in heating mode, the finned heat exchanger 10 is used as an evaporator, the liquid heat exchange medium in the finned heat exchanger 10 evaporates and absorbs heat, and the falling film heat exchanger 5 is used as a condensation At the same time, the gaseous heat exchange medium in the falling film heat exchanger 5 liquefies and releases heat to heat the water. In addition, the heat exchange medium in the auxiliary path branched out from the outlet of the economizer 8 is throttled by the economizer expansion valve 16 and then returns to the economizer 8, and fully exchanges heat with the heat exchange medium in the main path. The heat exchange medium in the main path is supercooled, and at the same time, the overheated heat exchange medium in the auxiliary path is mixed with the heat exchange medium after the first stage of compression through the intermediate air supply port of compressor 1, and then the second stage of compression is performed, thereby The temperature of the heat exchange medium entering the second-stage compression is effectively reduced, and at the same time, the suction volume of the second-stage compression can be effectively increased, thereby greatly increasing the heating capacity of the heat pump unit.
继续参阅图2,所述热泵机组还设置有回油系统和油冷却系统;具体地,所述热泵机组的回油系统的运行过程为:从油分离器2中分离出的润滑油依次流经过滤器7、旁通电磁阀18、流量计15和供油电磁阀19后,再回流至压缩机1的供油口。另外,当压缩机1的排气温度超过预定温度时,所述热泵机组的油冷却系统的运行过程为:关闭旁通电磁阀18,同时,打开油冷却膨胀阀17;此时,润滑油能够通过油冷却器14进行充分降温,然后再依次流经流量计15和供油电磁阀19,再回流至压缩机1的供油口;此外,油冷却辅路中的润滑油经过油冷却膨胀阀17进行节流后,再流入至油冷却器14中,并且与主路中的润滑油进行充分的热交换,从而有效减低润滑油的温度,使得所述热泵机组能够始终处于平稳运行的状态。Continuing to refer to Fig. 2, the heat pump unit is also provided with an oil return system and an oil cooling system; specifically, the operation process of the oil return system of the heat pump unit is: the lubricating oil separated from the oil separator 2 flows through After the filter 7, the bypass solenoid valve 18, the flow meter 15 and the oil supply solenoid valve 19, it returns to the oil supply port of the compressor 1. In addition, when the discharge temperature of the compressor 1 exceeds a predetermined temperature, the operation process of the oil cooling system of the heat pump unit is: close the bypass solenoid valve 18, and at the same time, open the oil cooling expansion valve 17; at this time, the lubricating oil can The temperature is fully cooled through the oil cooler 14, and then flows through the flow meter 15 and the oil supply solenoid valve 19 in sequence, and then returns to the oil supply port of the compressor 1; in addition, the lubricating oil in the oil cooling auxiliary circuit passes through the oil cooling expansion valve 17 After throttling, it flows into the oil cooler 14 and fully exchanges heat with the lubricating oil in the main circuit, thereby effectively reducing the temperature of the lubricating oil, so that the heat pump unit can always run smoothly.
进一步地,本优选实施例中的热泵机组运行除霜模式时,所述热泵机组中的换热介质的循环流程为:压缩机1→油分离器2→压力维持阀3→四通阀4→翅片式换热器10→第三单向阀63→过滤器7→经济器8→膨胀阀9→第二单向阀62→降膜式换热器5→四通阀4→气液分离器11→压缩机1。在所述热泵机组运行除霜模式时,降膜式换热器5用作蒸发器,并且降膜式换热器5中的液态换热介质蒸发吸热,同时,翅片式换热器10用作冷凝器,并且翅片式换热器10中的气态换热介质液化放热,以便对翅片式换热器10进行有效的除霜处理。此时,翅片式换热器10中的换热介质在化霜过程中液化放热,以便运用换热介质液化时放出的热量对翅片式换热器10进行化霜处理。Further, when the heat pump unit in this preferred embodiment operates in the defrosting mode, the circulation process of the heat exchange medium in the heat pump unit is: compressor 1 → oil separator 2 → pressure maintenance valve 3 → four-way valve 4 → Finned heat exchanger 10→third one-way valve 63→filter 7→economizer 8→expansion valve 9→second one-way valve 62→falling film heat exchanger 5→four-way valve 4→gas-liquid separation Device 11→Compressor 1. When the heat pump unit operates in the defrosting mode, the falling film heat exchanger 5 is used as an evaporator, and the liquid heat exchange medium in the falling film heat exchanger 5 evaporates and absorbs heat, and at the same time, the finned heat exchanger 10 It is used as a condenser, and the gaseous heat exchange medium in the finned heat exchanger 10 is liquefied to release heat, so that the finned heat exchanger 10 can be effectively defrosted. At this time, the heat exchange medium in the finned heat exchanger 10 liquefies and releases heat during the defrosting process, so that the finned heat exchanger 10 can be defrosted using the heat released when the heat exchange medium is liquefied.
本发明的热泵机组在除霜结束后,四通阀4换向之前,先将电磁阀12打开,此时,由于翅片式换热器10处于高压状态,降膜式换热器5处于低压状态,在压力作用下,翅片式换热器10中的换热介质沿图2中的箭头方向直接流入至降膜式换热器5中,经过预定时间后,所述热泵机组控制电磁阀12关闭,同时使四通阀4换向,所述热泵机组重新运行制热模式。此时,翅片式换热器10中的大量液态换热介质已经回流至降膜式换热器5中,只有少部分或者根本没有液态换热介质会流入至气液分离器11中,并且这部分液态换热介质的量也绝不可能超过气液分离器11的额定负荷;因此,在气液分离器11的保护作用下,压缩机1中也就不会有液态换热介质进入,使得压缩机1吸气带液的风险大大降低,从而极大程度地降低了压缩机1的损坏率,进而有效延长了压缩机1的使用寿命。In the heat pump unit of the present invention, after the defrosting is completed, the electromagnetic valve 12 is opened before the four-way valve 4 changes direction. At this time, since the fin heat exchanger 10 is in a high pressure state, the falling film heat exchanger 5 is in a low pressure state. state, under pressure, the heat exchange medium in the finned heat exchanger 10 flows directly into the falling film heat exchanger 5 along the direction of the arrow in Figure 2, and after a predetermined time, the heat pump unit controls the solenoid valve 12 is closed, and at the same time, the four-way valve 4 is reversed, and the heat pump unit resumes the heating mode. At this time, a large amount of liquid heat exchange medium in the finned heat exchanger 10 has flowed back into the falling film heat exchanger 5, only a small part or no liquid heat exchange medium will flow into the gas-liquid separator 11, and The amount of this part of the liquid heat exchange medium can never exceed the rated load of the gas-liquid separator 11; therefore, under the protection of the gas-liquid separator 11, no liquid heat exchange medium will enter the compressor 1, The risk of the compressor 1 being sucked with liquid is greatly reduced, thereby greatly reducing the damage rate of the compressor 1 , thereby effectively prolonging the service life of the compressor 1 .
本领域技术人员能够理解的是,在本发明的实施例中,压缩机1优选为双级螺杆压缩机,由于使用所述双级螺杆压缩机以及补气增焓技术能够有效降低压缩机1的排气温度;同时,油冷却器14能够有效稳定所述热泵机组的供油温度,以便在所述热泵机组具有高出水温度的情况下,所述热泵机组的供油温度和排气温度还能够保持稳定状态,从而使得所述热泵机组也能够时刻保持稳定运行,进而使得本发明的热泵机组在外界环境温度较低的情况下还能够保持稳定运行的状态,同时还能够保证所述热泵机组能够始终输出预定温度的热水。Those skilled in the art can understand that, in the embodiment of the present invention, the compressor 1 is preferably a two-stage screw compressor, because the use of the two-stage screw compressor and the gas supplement enthalpy increase technology can effectively reduce the compressor 1. exhaust temperature; at the same time, the oil cooler 14 can effectively stabilize the oil supply temperature of the heat pump unit, so that the oil supply temperature and exhaust temperature of the heat pump unit can also be maintained under the condition that the heat pump unit has a high outlet water temperature Maintain a stable state, so that the heat pump unit can also maintain a stable operation at all times, so that the heat pump unit of the present invention can also maintain a stable operation state when the external environment temperature is low, and can also ensure that the heat pump unit can Always deliver hot water at a predetermined temperature.
进一步地,降膜式换热器5包括喷淋元件和换热元件,在所述热泵机组的除霜过程中,所述喷淋元件能够将换热介质直接喷淋至所述换热元件上,以便降膜式换热器5能够快速进入吸热状态,同时,使得翅片式换热器10也能够快速进入放热状态,从而有效缩短所述热泵机组的除霜时间。另外,这种喷淋式换热方式还能够有效减少除霜所需的换热介质的量,从而使得所述热泵机组运行制热模式时所需的换热介质的量能够与运行除霜模式时所需的换热介质的量相等,以便本发明的热泵机组能够取消储液器的设置,进而有效简化该热泵机组的结构。Further, the falling film heat exchanger 5 includes a spray element and a heat exchange element, and during the defrosting process of the heat pump unit, the spray element can directly spray the heat exchange medium onto the heat exchange element , so that the falling film heat exchanger 5 can quickly enter the heat absorption state, and at the same time, enable the finned heat exchanger 10 to quickly enter the heat release state, thereby effectively shortening the defrosting time of the heat pump unit. In addition, this spray heat exchange method can also effectively reduce the amount of heat exchange medium required for defrosting, so that the amount of heat exchange medium required by the heat pump unit in the heating mode can be compared with that in the defrosting mode. The amount of heat exchange medium required is equal, so that the heat pump unit of the present invention can cancel the arrangement of the liquid reservoir, thereby effectively simplifying the structure of the heat pump unit.
最后需要说明的是,上述实施例均是本发明的优选实施方案,并不作为对本发明保护范围的限制。本领域技术人员在实际使用本发明时,可以根据需要适当添加或删减一部分步骤,或者调换不同步骤之间的顺序。这种改变并没有超出本发明的基本原理,属于本发明的保护范围。Finally, it should be noted that the above examples are all preferred implementations of the present invention, and are not intended to limit the protection scope of the present invention. When actually using the present invention, those skilled in the art may appropriately add or delete some steps as required, or exchange the order of different steps. This change does not go beyond the basic principles of the present invention and belongs to the protection scope of the present invention.
至此,已经结合附图描述了本发明的优选实施方案,但是,本领域技术人员容易理解的是,本发明的保护范围显然不局限于这些具体实施方式。在不偏离本发明的原理的前提下,本领域技术人员可以对相关技术特征作出等同的更改或替换,这些更改或替换之后的技术方案都将落入本发明的保护范围之内。So far, the preferred embodiments of the present invention have been described with reference to the accompanying drawings, but those skilled in the art will easily understand that the protection scope of the present invention is obviously not limited to these specific embodiments. Without departing from the principles of the present invention, those skilled in the art can make equivalent changes or substitutions to relevant technical features, and the technical solutions after these changes or substitutions will all fall within the protection scope of the present invention.
Claims (10)
- A kind of 1. heat pump unit, it is characterised in that the heat pump unit include main circulation loop and with the main circulation loop The defrosting liquid back pipe road being connected;Wherein, the compressor to communicate with each other, First Heat Exchanger and the second heat exchanger are provided with the main circulation loop, is being defrosted Under pattern, the First Heat Exchanger is used as condenser, and second heat exchanger is used as evaporator;The defrosting liquid back pipe road is used for after defrosting, by the direct water conservancy diversion of liquid heat transferring medium in the First Heat Exchanger Into second heat exchanger.
- 2. heat pump unit according to claim 1, it is characterised in that switch valve is provided with the defrosting liquid back pipe road, The break-make on the defrosting liquid back pipe road is realized by the switch valve in the defrosting liquid back pipe road.
- 3. heat pump unit according to claim 2, it is characterised in that the switch valve is solenoid valve.
- 4. heat pump unit according to any one of claim 1 to 3, it is characterised in that the main circulation loop include with Parallel way is arranged on the first major cycle branch and the second major cycle between the First Heat Exchanger and second heat exchanger Branch, the defrosting liquid back pipe road are connected with the second major cycle branch.
- 5. heat pump unit according to claim 4, it is characterised in that the main circulation loop, which further includes, is arranged on described Bridge joint branch between one major cycle branch and the second major cycle branch, described bridge in branch are provided with expansion valve.
- 6. heat pump unit according to claim 5, it is characterised in that the branch that bridges is by the first major cycle branch Part I and Part II, the defrosting liquid back pipe road and the described second master are respectively divided into the second major cycle branch The Part II of circulation branch road is in parallel;Wherein, the Part I of the first major cycle branch is provided with the first check valve, and the of the first major cycle branch Two parts are provided with the second check valve, and the Part I of the second major cycle branch is provided with the 3rd check valve, and described second The Part II of major cycle branch is provided with the 4th check valve;First check valve only allows heat transferring medium to flow into the First Heat Exchanger, and second check valve only allows heat exchange to be situated between Mass flow enters second heat exchanger, and the 3rd check valve only allows heat transferring medium to flow out the First Heat Exchanger, and the described 4th Check valve only allows heat transferring medium to flow out second heat exchanger.
- 7. heat pump unit according to claim 1, it is characterised in that the First Heat Exchanger is finned heat exchanger.
- 8. heat pump unit according to claim 1, it is characterised in that second heat exchanger is falling-film heat exchanger.
- 9. heat pump unit according to claim 8, it is characterised in that the falling-film heat exchanger includes spray element and changes Thermal element;During defrosting, liquid heat transferring medium is directly sprayed on the heat exchange element by the spray element, to shorten Defrosting time.
- 10. heat pump unit according to claim 1, it is characterised in that the compressor is two-stage screw compressor.
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