CN113686044B - Heat pump unit - Google Patents

Heat pump unit Download PDF

Info

Publication number
CN113686044B
CN113686044B CN202111007226.0A CN202111007226A CN113686044B CN 113686044 B CN113686044 B CN 113686044B CN 202111007226 A CN202111007226 A CN 202111007226A CN 113686044 B CN113686044 B CN 113686044B
Authority
CN
China
Prior art keywords
subcooler
economizer
heat exchanger
heat pump
compressor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202111007226.0A
Other languages
Chinese (zh)
Other versions
CN113686044A (en
Inventor
张琍敏
徐亮
龙海峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Trane Air Conditioning Systems China Co Ltd
Original Assignee
Trane Air Conditioning Systems China Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Trane Air Conditioning Systems China Co Ltd filed Critical Trane Air Conditioning Systems China Co Ltd
Priority to CN202111007226.0A priority Critical patent/CN113686044B/en
Publication of CN113686044A publication Critical patent/CN113686044A/en
Application granted granted Critical
Publication of CN113686044B publication Critical patent/CN113686044B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B40/00Subcoolers, desuperheaters or superheaters
    • F25B40/02Subcoolers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/20Disposition of valves, e.g. of on-off valves or flow control valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems

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

本发明实施例提供一种热泵机组。该热泵机组包括通过制冷剂管路依次连接的压缩机、换向阀、第一换热器、经济器、过冷器和第二换热器,压缩机具有吸气口、排气口及中间补气口,经济器与压缩机的中间补气口连接,过冷器包括主路和辅路,其中,过冷器的主路的入口连接到经济器,过冷器的主路的出口连接第一换热器和第二换热器,过冷器的辅路的入口通过过冷器节流阀连接到过冷器的主路,过冷器的辅路的出口连接到压缩机的吸气口。本发明实施例的热泵机组能够有效确保在机组制冷量保持不变的前提下,降低机组的功耗,提升机组的效率。

An embodiment of the present invention provides a heat pump unit. The heat pump unit includes a compressor, a reversing valve, a first heat exchanger, an economizer, a subcooler and a second heat exchanger connected in sequence through refrigerant pipelines. The compressor has a suction port, a discharge port and an intermediate The air supply port, the economizer is connected to the middle air supply port of the compressor. The subcooler includes a main circuit and an auxiliary circuit. The inlet of the main circuit of the subcooler is connected to the economizer, and the outlet of the main circuit of the subcooler is connected to the first exchanger. Heater and second heat exchanger, the inlet of the auxiliary circuit of the subcooler is connected to the main circuit of the subcooler through the subcooler throttle valve, and the outlet of the auxiliary circuit of the subcooler is connected to the suction port of the compressor. The heat pump unit according to the embodiment of the present invention can effectively ensure that the power consumption of the unit is reduced and the efficiency of the unit is improved while the cooling capacity of the unit remains unchanged.

Description

热泵机组heat pump unit

技术领域Technical field

本发明实施例涉及空调技术领域,尤其涉及一种热泵机组。Embodiments of the present invention relate to the technical field of air conditioning, and in particular, to a heat pump unit.

背景技术Background technique

传统风冷冷水(热泵)机组,为了提升机组制冷能力或机组效率一般都会选用在压缩机壳体上增设中间补气口。依此利用中间补气口的工作原理,让原先的一级压缩变成二级压缩,来扩大机组制冷量或机组效率。目前压缩机应用补气技术在制冷行业中得到了广泛应用。然而,在应用补气技术后,若要提高机组制冷量百分比达10%,则中间补气量与主侧制冷剂流量之比通常要高于10%。由此带来的结果是虽然机组制冷量提升了,但是,机组的效率(COP,Coefficient of Performance)却下降了。若要提升机组的效率,则补气量需要减少、甚至不能补气。In traditional air-cooled chilled water (heat pump) units, in order to improve the cooling capacity or efficiency of the unit, an intermediate air supply port is usually added to the compressor casing. Based on this, the working principle of the middle air supply port is used to change the original one-stage compression into two-stage compression to expand the cooling capacity or efficiency of the unit. At present, compressor air supply technology has been widely used in the refrigeration industry. However, after applying air supplement technology, if you want to increase the cooling capacity percentage of the unit by 10%, the ratio of the intermediate air supplement volume to the main side refrigerant flow rate is usually higher than 10%. The result is that although the cooling capacity of the unit has increased, the unit's efficiency (COP, Coefficient of Performance) has decreased. To improve the efficiency of the unit, the air supply volume needs to be reduced or even eliminated.

发明内容Contents of the invention

本发明实施例的目的在于提供一种热泵机组,能够有效确保在机组制冷量保持不变的前提下,降低机组的功耗,提升机组的效率。The purpose of embodiments of the present invention is to provide a heat pump unit that can effectively ensure that the power consumption of the unit is reduced and the efficiency of the unit is improved while the cooling capacity of the unit remains unchanged.

本发明实施例的一个方面提供一种热泵机组。所述热泵机组包括通过制冷剂管路连接的压缩机、换向阀、第一换热器、经济器、过冷器和第二换热器,所述压缩机具有吸气口、排气口及中间补气口,所述经济器与所述压缩机的中间补气口连接,所述过冷器包括主路和辅路,其中,所述过冷器的主路的入口连接到所述经济器,所述过冷器的主路的出口连接所述第一换热器和所述第二换热器,所述过冷器的辅路的入口通过过冷器节流阀连接到所述过冷器的主路,所述过冷器的辅路的出口连接到所述压缩机的吸气口。One aspect of embodiments of the present invention provides a heat pump unit. The heat pump unit includes a compressor, a reversing valve, a first heat exchanger, an economizer, a subcooler and a second heat exchanger connected through a refrigerant pipeline. The compressor has a suction port and an exhaust port. and an intermediate air supply port, the economizer is connected to the intermediate air supply port of the compressor, the subcooler includes a main path and an auxiliary path, wherein the inlet of the main path of the subcooler is connected to the economizer, The outlet of the main circuit of the subcooler is connected to the first heat exchanger and the second heat exchanger, and the inlet of the auxiliary circuit of the subcooler is connected to the subcooler through a subcooler throttle valve. The main circuit and the outlet of the auxiliary circuit of the subcooler are connected to the suction port of the compressor.

进一步地,所述过冷器的辅路的入口通过所述过冷器节流阀连接到所述过冷器的主路的入口或者所述过冷器的主路的出口。Further, the inlet of the auxiliary circuit of the subcooler is connected to the inlet of the main circuit of the subcooler or the outlet of the main circuit of the subcooler through the subcooler throttle valve.

进一步地,所述经济器包括主路和辅路,所述经济器的主路的入口连接到所述第一换热器,所述经济器的主路的出口连接所述过冷器的主路的入口,所述经济器的辅路的入口通过经济器节流阀连接到所述经济器的主路的入口或者所述经济器的主路的出口,所述经济器的辅路的出口连接到所述压缩机的中间补气口。Further, the economizer includes a main path and an auxiliary path, the inlet of the main path of the economizer is connected to the first heat exchanger, and the outlet of the main path of the economizer is connected to the main path of the subcooler. The inlet of the auxiliary path of the economizer is connected to the inlet of the main path of the economizer or the outlet of the main path of the economizer through the economizer throttle valve, and the outlet of the auxiliary path of the economizer is connected to the The middle air supply port of the compressor.

进一步地,所述过冷器的主路的出口通过制冷节流阀连接到所述第二换热器,所述过冷器的主路的出口通过制热节流阀连接到所述第一换热器。Further, the outlet of the main circuit of the subcooler is connected to the second heat exchanger through a refrigeration throttle valve, and the outlet of the main circuit of the subcooler is connected to the first heat exchanger through a heating throttle valve. Heat Exchanger.

进一步地,所述热泵机组还包括与所述压缩机连接的油冷却器,所述过冷器的主路的出口还通过油冷节流器连接到所述油冷却器。Further, the heat pump unit further includes an oil cooler connected to the compressor, and the outlet of the main circuit of the subcooler is also connected to the oil cooler through an oil cooling throttle.

进一步地,所述第一换热器包括多个冷却盘管,所述热泵机组还包括预分配器,所述多个冷却盘管连接至所述预分配器。Further, the first heat exchanger includes a plurality of cooling coils, the heat pump unit further includes a pre-distributor, and the plurality of cooling coils are connected to the pre-distributor.

进一步地,所述热泵机组还包括过滤器和油分离器,所述预分配器通过所述过滤器连接到所述经济器,所述压缩机的排气口通过所述油分离器连接到所述换向阀。Further, the heat pump unit also includes a filter and an oil separator, the pre-distributor is connected to the economizer through the filter, and the exhaust port of the compressor is connected to the economizer through the oil separator. The reversing valve.

进一步地,所述第二换热器包括水侧换热器,所述水侧换热器具有出水端和进水端。Further, the second heat exchanger includes a water-side heat exchanger, and the water-side heat exchanger has a water outlet end and a water inlet end.

进一步地,所述热泵机组还包括控制器,所述控制器在所述压缩机满载运行的情况下控制同时启用所述经济器和所述过冷器。Further, the heat pump unit further includes a controller, which controls the simultaneous activation of the economizer and the subcooler when the compressor is running at full load.

进一步地,所述控制器在所述压缩机部分负荷运行的情况下控制启用所述过冷器。Further, the controller controls activation of the subcooler when the compressor is operating at partial load.

本发明实施例的热泵机组通过在第一级经济器后面增设了另一个板式换热器,即过冷器,从而可以将热泵机组获取目标制冷量所需要达到的目标焓差值(h5-h7)不完全由第一级的经济器来完成,而是由前后两级板式换热器(即充当经济器的第一级板式换热器和充当过冷器的第二级板式换热器)联合作用后共同完成。The heat pump unit in the embodiment of the present invention adds another plate heat exchanger, that is, a subcooler, behind the first-stage economizer, so that the target enthalpy difference (h 5 - h 7 ) is not completely completed by the first-stage economizer, but by the front and rear two-stage plate heat exchangers (i.e., the first-stage plate heat exchanger acting as an economizer and the second-stage plate heat exchanger acting as a subcooler device) and are completed together after the combined action.

本发明实施例的热泵机组可以通过对经济器和过冷器两个板式换热器辅侧的流量进行优化配置后,可以使得由第一级经济器流向压缩机的中间补气口的流量得到有效管理,进而有效控制整个热泵机组的总功耗,并最终有效提升热泵机组的运行效率。The heat pump unit according to the embodiment of the present invention can optimize the flow rate from the first-stage economizer to the intermediate air supply port of the compressor by optimizing the flow rate on the auxiliary side of the two plate heat exchangers of the economizer and the subcooler. Management, thereby effectively controlling the total power consumption of the entire heat pump unit, and ultimately effectively improving the operating efficiency of the heat pump unit.

附图说明Description of the drawings

图1为一种压缩机带有中间补气口的热泵机组的示意图;Figure 1 is a schematic diagram of a heat pump unit with a compressor with an intermediate air supply port;

图2为图1中的压缩机两级压缩的制冷循环图;Figure 2 is a refrigeration cycle diagram of the two-stage compression of the compressor in Figure 1;

图3为图1中的经济器的主辅侧制冷剂流向图;Figure 3 is a refrigerant flow diagram on the main and auxiliary sides of the economizer in Figure 1;

图4为本发明一个实施例的热泵机组的示意图。Figure 4 is a schematic diagram of a heat pump unit according to an embodiment of the present invention.

具体实施方式Detailed ways

这里将详细地对示例性实施例进行说明,其示例表示在附图中。下面的描述涉及附图时,除非另有表示,不同附图中的相同数字表示相同或相似的要素。以下示例性实施例中所描述的实施例并不代表与本发明相一致的所有实施例。相反,它们仅是与如所附权利要求书中所详述的、本发明的一些方面相一致的装置的例子。Exemplary embodiments will be described in detail herein, examples of which are illustrated in the accompanying drawings. When the following description refers to the drawings, the same numbers in different drawings refer to the same or similar elements unless otherwise indicated. The embodiments described in the following exemplary embodiments do not represent all embodiments consistent with the invention. Rather, they are merely examples of means consistent with aspects of the invention as detailed in the appended claims.

在本发明实施例使用的术语是仅仅出于描述特定实施例的目的,而非旨在限制本发明。除非另作定义,本发明实施例使用的技术术语或者科学术语应当为本发明所属领域内具有一般技能的人士所理解的通常意义。本发明说明书以及权利要求书中使用的“第一”“第二”以及类似的词语并不表示任何顺序、数量或者重要性,而只是用来区分不同的组成部分。同样,“一个”或者“一”等类似词语也不表示数量限制,而是表示存在至少一个。“多个”或者“若干”表示两个及两个以上。除非另行指出,“前部”、“后部”、“下部”和/或“上部”等类似词语只是为了便于说明,而并非限于一个位置或者一种空间定向。“包括”或者“包含”等类似词语意指出现在“包括”或者“包含”前面的元件或者物件涵盖出现在“包括”或者“包含”后面列举的元件或者物件及其等同,并不排除其他元件或者物件。“连接”或者“相连”等类似的词语并非限定于物理的或者机械的连接,而且可以包括电性的连接,不管是直接的还是间接的。在本发明说明书和所附权利要求书中所使用的单数形式的“一种”、“所述”和“该”也旨在包括多数形式,除非上下文清楚地表示其他含义。还应当理解,本文中使用的术语“和/或”是指并包含一个或多个相关联的列出项目的任何或所有可能组合。The terminology used in the embodiments of the present invention is only for the purpose of describing specific embodiments and is not intended to limit the present invention. Unless otherwise defined, the technical terms or scientific terms used in the embodiments of the present invention should have the usual meanings understood by those with ordinary skills in the field to which the present invention belongs. "First", "second" and similar words used in the description and claims of the present invention do not indicate any order, quantity or importance, but are only used to distinguish different components. Likewise, "a" or "one" and similar words do not indicate a quantitative limit, but rather indicate the presence of at least one. "Multiple" or "several" means two or more than two. Unless otherwise indicated, similar terms such as "front", "rear", "lower" and/or "upper" are for convenience of description only and are not intended to limit one position or one spatial orientation. "Including" or "including" and other similar words mean that the elements or objects appearing before "includes" or "includes" cover the elements or objects listed after "includes" or "includes" and their equivalents, and do not exclude other elements. or objects. Words such as "connected" or "connected" are not limited to physical or mechanical connections, but may include electrical connections, whether direct or indirect. As used in this specification and the appended claims, the singular forms "a," "the" and "the" are intended to include the plural forms as well, unless the context clearly dictates otherwise. It will also be understood that the term "and/or" as used herein refers to and includes any and all possible combinations of one or more of the associated listed items.

图1揭示了一种压缩机10带有中间补气口23的热泵机组100的示意图。如图1所示,该热泵机组100包括通过制冷剂管路依次连接的压缩机10、换向阀20、第一换热器31、经济器41和第二换热器32。压缩机10具有吸气口1、排气口4及中间补气口23。FIG. 1 shows a schematic diagram of a heat pump unit 100 with a compressor 10 and an intermediate air supply port 23 . As shown in FIG. 1 , the heat pump unit 100 includes a compressor 10 , a reversing valve 20 , a first heat exchanger 31 , an economizer 41 and a second heat exchanger 32 that are connected in sequence through refrigerant pipelines. The compressor 10 has an air suction port 1 , an exhaust port 4 and an intermediate air supply port 23 .

经济器41与压缩机10的中间补气口23连接,经济器41包括主路和辅路,其中,经济器41的主路的入口连接到第一换热器31,经济器41的主路的出口通过制冷节流阀EXV2连接到第二换热器32,经济器41的辅路的入口通过经济器节流阀EXV1连接到经济器41的主路的入口,经济器41的辅路的出口连接到压缩机10的中间补气口23。从而,可以用来对主路中的制冷剂进行冷却,并对压缩机10进行补气增焓。The economizer 41 is connected to the intermediate air supply port 23 of the compressor 10. The economizer 41 includes a main path and an auxiliary path. The inlet of the main path of the economizer 41 is connected to the first heat exchanger 31, and the outlet of the main path of the economizer 41 is connected to the first heat exchanger 31. It is connected to the second heat exchanger 32 through the refrigeration throttle valve EXV2, the inlet of the auxiliary path of the economizer 41 is connected to the inlet of the main path of the economizer 41 through the economizer throttle valve EXV1, and the outlet of the auxiliary path of the economizer 41 is connected to the compressor The middle air supply port 23 of the machine 10. Therefore, it can be used to cool the refrigerant in the main circuit and supply air to the compressor 10 to increase the enthalpy.

图2揭示了图1中的压缩机两级压缩的制冷循环图。在图2中,EXV1表示经济器节流阀EXV1,EXV2表示制冷节流阀EXV2,图2中的数字分别表示压缩机10的各个工作状态点,其中,1表示压缩机10的吸气口,2表示压缩机10制冷剂刚刚排出来的点,23表示压缩机10的中间补气口,3表示经济器41辅侧的出口,4表示压缩机10的排气口(即压缩机10制冷剂完全排出来的点),5表示从第一换热器31出来的点(即经济器节流阀EXV1的入口),6表示经济器节流阀EXV1的出口,7表示经济器41主路的出口,8表示制冷节流阀EXV2节流后的点,9表示第二换热器32连接换向阀20的端口。Figure 2 reveals the refrigeration cycle diagram of the two-stage compression of the compressor in Figure 1. In Figure 2, EXV1 represents the economizer throttle valve EXV1, and EXV2 represents the refrigeration throttle valve EXV2. The numbers in Figure 2 represent each operating state point of the compressor 10, where 1 represents the suction port of the compressor 10, 2 represents the point where the refrigerant of the compressor 10 has just been discharged, 23 represents the middle air supply port of the compressor 10, 3 represents the outlet of the auxiliary side of the economizer 41, and 4 represents the exhaust port of the compressor 10 (that is, the refrigerant of the compressor 10 is completely discharged). discharge point), 5 represents the point coming out of the first heat exchanger 31 (i.e., the inlet of the economizer throttle valve EXV1), 6 represents the outlet of the economizer throttle valve EXV1, and 7 represents the outlet of the main path of the economizer 41 , 8 represents the point after throttling of the refrigeration throttle valve EXV2, and 9 represents the port of the second heat exchanger 32 connected to the reversing valve 20 .

图3揭示了图1中的经济器41的主辅侧制冷剂流向图。如图3所示,5-7构成经济器41的主路,3-6构成经济器41的辅路。FIG. 3 reveals the main and auxiliary side refrigerant flow diagram of the economizer 41 in FIG. 1 . As shown in Figure 3, 5-7 constitute the main path of the economizer 41, and 3-6 constitute the auxiliary path of the economizer 41.

压缩机10带有中间补气口23时可以实现如图2所示的工作循环,其中,1-2-23-4-5-7-8-9-1构成热泵机组100的主循环,辅侧5-6-3-23参与部分的循环过程。When the compressor 10 is equipped with an intermediate air supply port 23, the working cycle shown in Figure 2 can be realized, in which 1-2-23-4-5-7-8-9-1 constitutes the main cycle of the heat pump unit 100, and the auxiliary side 5-6-3-23 participate in part of the cycle process.

利用工程热力学的工作原理,可以求得热泵机组100的制冷量和总功耗,如以下公式所示:Using the working principle of engineering thermodynamics, the cooling capacity and total power consumption of the heat pump unit 100 can be obtained, as shown in the following formula:

Q=Gd×(h9-h7) (1)Q=G d ×(h 9 -h 7 ) (1)

Nd=Gd×(h2-h1) (2)N d =G d ×(h 2 -h 1 ) (2)

Ng=Gg×(h4-h23) (3)N g =G g ×(h 4 -h 23 ) (3)

N=Nd+Ng (4)N= Nd + Ng (4)

其中,Q为制冷量(kW),N为总功耗(kW),Nd为第一级(低压级)的功耗(kW),Ng为第二级(高压级)的功耗(kW),Gd为低压级制冷剂流量,Gg为高压级制冷剂流量,h代表压缩机10对应工作状态点的焓值,COP为效率。Among them, Q is the cooling capacity (kW), N is the total power consumption (kW), N d is the power consumption of the first stage (low voltage stage) (kW), and N g is the power consumption of the second stage (high pressure stage) ( kW), G d is the low-pressure stage refrigerant flow, G g is the high-pressure stage refrigerant flow, h represents the enthalpy value of the corresponding working state point of the compressor 10, and COP is the efficiency.

下面将结合图1至图3来详细描述带有中间补气口23的压缩机10的工作原理。The working principle of the compressor 10 with the intermediate air supply port 23 will be described in detail below with reference to FIGS. 1 to 3 .

根据能量守恒规律,热源侧放出的能量必然等于冷源侧获得的能量,因此,可以得出以下公式:According to the law of conservation of energy, the energy released by the heat source side must be equal to the energy obtained by the cold source side. Therefore, the following formula can be derived:

Gd×(h5-h7)=(Gg-Gd)×(h3-h6) (6)G d ×(h 5 -h 7 )=(G g -G d )×(h 3 -h 6 ) (6)

其中,(Gg-Gd)表示补气侧制冷剂流量。Among them, (G g -G d ) represents the refrigerant flow rate on the supply side.

由于h5=h6,因此,根据公式(6)可以推导得出高压级制冷剂流量Gg如以下公式所示:Since h 5 =h 6 , therefore, according to formula (6), it can be deduced that the high-pressure stage refrigerant flow rate G g is as shown in the following formula:

Gg=Gd×(h3-h7)/(h3-h6) (7)G g =G d ×(h 3 -h 7 )/(h 3 -h 6 ) (7)

因此,只要合理降低第二级的制冷剂流量Gg,则可以有效降低整个机组的功耗N,由此实现机组效率COP的提升。Therefore, as long as the second-stage refrigerant flow rate Gg is reasonably reduced, the power consumption N of the entire unit can be effectively reduced, thereby improving the unit efficiency COP.

有鉴于此,本发明实施例提供了一种改进的热泵机组的技术方案。在保证热泵机组制冷量Q保持不变的前提下,可以降低热泵机组的功耗N,提升热泵机组的效率COP。In view of this, embodiments of the present invention provide a technical solution for an improved heat pump unit. On the premise of ensuring that the cooling capacity Q of the heat pump unit remains unchanged, the power consumption N of the heat pump unit can be reduced and the efficiency COP of the heat pump unit can be improved.

图4揭示了本发明一个实施例的热泵机组200的示意图。如图4所示,本发明一个实施例的热泵机组200包括通过制冷剂管路依次连接的压缩机10、换向阀20、第一换热器31、经济器41、过冷器42和第二换热器32。压缩机10具有吸气口1、排气口4及中间补气口23。在一个实施例中,第一换热器31例如为一种翅片换热器,第二换热器32例如可以包括但不限于水侧换热器,水侧换热器具有出水端和进水端。Figure 4 reveals a schematic diagram of a heat pump unit 200 according to an embodiment of the present invention. As shown in Figure 4, a heat pump unit 200 according to an embodiment of the present invention includes a compressor 10, a reversing valve 20, a first heat exchanger 31, an economizer 41, a subcooler 42 and a third tube connected in sequence through a refrigerant pipeline. Second heat exchanger 32. The compressor 10 has an air suction port 1 , an exhaust port 4 and an intermediate air supply port 23 . In one embodiment, the first heat exchanger 31 is, for example, a fin heat exchanger, and the second heat exchanger 32 may include, for example, but is not limited to, a water-side heat exchanger. The water-side heat exchanger has a water outlet end and an inlet port. Water end.

本发明实施例的经济器41和过冷器42例如可以包括但并不局限于钎焊式板式换热器(BPHE,Blazed Plate Heat Exchanger)。本发明实施例的经济器41和过冷器42也可以采用其他的型式。The economizer 41 and the subcooler 42 in the embodiment of the present invention may include, but are not limited to, a brazed plate heat exchanger (BPHE). The economizer 41 and the subcooler 42 in the embodiment of the present invention can also adopt other types.

经济器41与压缩机10的中间补气口23连接,经济器41包括主路和辅路,其中,经济器41的主路的入口连接到第一换热器31,经济器41的主路的出口连接过冷器42的主路的入口,经济器41的辅路的入口通过经济器节流阀EXV1连接到经济器41的主路的入口(或者经济器41的辅路的入口也可以通过经济器节流阀EXV1连接到经济器41的主路的出口),经济器41的辅路的出口连接到压缩机10的中间补气口23。经济器41的辅路从经济器41的主路分支出一股制冷剂,经过经济器节流阀EXV1的节流降压后,使得辅路制冷剂的温度冷却降低,在与主路的制冷剂进行热量交换后,辅路制冷剂吸收主路制冷剂的热量,经济器41辅路吸收热量之后的制冷剂再回到压缩机10的中间补气口23,从而可以对压缩机10进行补气增焓。The economizer 41 is connected to the intermediate air supply port 23 of the compressor 10. The economizer 41 includes a main path and an auxiliary path. The inlet of the main path of the economizer 41 is connected to the first heat exchanger 31, and the outlet of the main path of the economizer 41 is connected to the first heat exchanger 31. The entrance of the main circuit of the subcooler 42 is connected to the entrance of the auxiliary circuit of the economizer 41 through the economizer throttle valve EXV1. The flow valve EXV1 is connected to the outlet of the main path of the economizer 41 ), and the outlet of the auxiliary path of the economizer 41 is connected to the intermediate air supply port 23 of the compressor 10 . The auxiliary circuit of the economizer 41 branches off a stream of refrigerant from the main circuit of the economizer 41. After being throttled and depressurized by the economizer throttle valve EXV1, the temperature of the refrigerant in the auxiliary circuit is reduced, and then interacts with the refrigerant in the main circuit. After the heat exchange, the refrigerant in the auxiliary circuit absorbs the heat of the refrigerant in the main circuit. The refrigerant after absorbing the heat in the auxiliary circuit of the economizer 41 returns to the middle air supply port 23 of the compressor 10, so that the compressor 10 can be supplied with air to increase the enthalpy.

过冷器42包括主路和辅路,其中,过冷器42的主路的入口连接到经济器41,过冷器42的主路的出口连接第一换热器31和第二换热器32,过冷器42的辅路的入口通过过冷器节流阀EXV5连接到过冷器42的主路,过冷器42的辅路的出口连接到压缩机10的吸气口1。如图4所示,在一个实施例中,过冷器42的辅路的入口通过过冷器节流阀EXV5连接到过冷器42的主路的入口。在另一个实施例中,过冷器42的辅路的入口通过过冷器节流阀EXV5连接到过冷器42的主路的出口。过冷器42的辅路从过冷器42的主路分支出一股制冷剂,经过过冷器节流阀EXV5的节流降压后,使得辅路制冷剂的温度冷却降低,在与主路的制冷剂进行热量交换后,辅路制冷剂吸收主路制冷剂的热量,过冷器42辅路吸收热量之后的制冷剂再回到压缩机10的吸气口1。The subcooler 42 includes a main circuit and an auxiliary circuit, wherein the inlet of the main circuit of the subcooler 42 is connected to the economizer 41 , and the outlet of the main circuit of the subcooler 42 is connected to the first heat exchanger 31 and the second heat exchanger 32 , the inlet of the auxiliary circuit of the subcooler 42 is connected to the main circuit of the subcooler 42 through the subcooler throttle valve EXV5, and the outlet of the auxiliary circuit of the subcooler 42 is connected to the suction port 1 of the compressor 10 . As shown in FIG. 4 , in one embodiment, the inlet of the auxiliary circuit of the subcooler 42 is connected to the inlet of the main circuit of the subcooler 42 through the subcooler throttle valve EXV5. In another embodiment, the inlet of the auxiliary circuit of the subcooler 42 is connected to the outlet of the main circuit of the subcooler 42 through the subcooler throttle valve EXV5. The auxiliary circuit of the subcooler 42 branches off a stream of refrigerant from the main circuit of the subcooler 42. After being throttled and depressurized by the subcooler throttle valve EXV5, the temperature of the refrigerant in the auxiliary circuit is reduced. After the refrigerant exchanges heat, the auxiliary circuit refrigerant absorbs the heat of the main circuit refrigerant, and the refrigerant after the auxiliary circuit absorbs the heat in the subcooler 42 returns to the suction port 1 of the compressor 10 .

本发明实施例的热泵机组200并不局限于图4所示的具体连接方式,本发明实施例的热泵机组200旨在涵盖启用经济器41和过冷器42的组合模式,经济器41和过冷器42的布置方式在位置上两者也可以前后互换。另外,本发明实施例的经济器41和过冷器42的辅侧制冷剂的取点并不局限于图4所示的从上游取(指辅侧制冷剂均从主侧没有流入经济器或过冷器的制冷剂流量中取样,即从主路的入口取),在其他实施例种,本发明实施例的经济器41和过冷器42的辅侧制冷剂的取点也可以从下游取(即从主路的出口取)。The heat pump unit 200 of the embodiment of the present invention is not limited to the specific connection method shown in Figure 4. The heat pump unit 200 of the embodiment of the present invention is intended to cover the combined mode of enabling the economizer 41 and the subcooler 42. The economizer 41 and the supercooler are The arrangement of the cooler 42 can also be interchanged in terms of position. In addition, the point of taking the auxiliary side refrigerant of the economizer 41 and the subcooler 42 in the embodiment of the present invention is not limited to taking it from the upstream as shown in Figure 4 (meaning that neither the auxiliary side refrigerant flows into the economizer from the main side or The refrigerant flow of the subcooler is sampled (that is, from the entrance of the main circuit). In other embodiments, the sampling point of the auxiliary side refrigerant of the economizer 41 and the subcooler 42 in the embodiment of the present invention can also be sampled from the downstream. Take it (that is, take it from the exit of the main road).

本发明实施例的热泵机组200通过在第一级经济器41后面增设了另一个板式换热器,即过冷器42,从而可以将热泵机组200获取目标制冷量所需要达到的目标焓差值(h5-h7)不完全由第一级的经济器41来完成,而是由前后两级板式换热器(即充当经济器41的第一级板式换热器和充当过冷器42的第二级板式换热器)联合作用后共同完成。The heat pump unit 200 in the embodiment of the present invention adds another plate heat exchanger, that is, the subcooler 42, behind the first-stage economizer 41, so that the heat pump unit 200 can obtain the target enthalpy difference required to obtain the target cooling capacity. (h 5 -h 7 ) is not completely completed by the first-stage economizer 41, but by the front and rear two-stage plate heat exchangers (i.e., the first-stage plate heat exchanger acting as the economizer 41 and the subcooler 42 The second stage plate heat exchanger) is completed together after the combined action.

本发明实施例的热泵机组200可以通过对经济器41和过冷器42两个板式换热器辅侧的流量进行优化配置后,可以使得由第一级经济器41流向压缩机10的中间补气口23的流量得到有效管理,进而有效控制整个热泵机组200的总功耗,并最终有效提升热泵机组200的运行效率。The heat pump unit 200 in the embodiment of the present invention can optimize the flow of the two plate heat exchangers auxiliary side of the economizer 41 and the subcooler 42, so that the intermediate supplementary flow from the first-stage economizer 41 to the compressor 10 can be optimized. The flow rate of the air port 23 is effectively managed, thereby effectively controlling the total power consumption of the entire heat pump unit 200, and ultimately effectively improving the operating efficiency of the heat pump unit 200.

继续参照图4所示,过冷器42的主路的出口通过制冷节流阀EXV2连接到第二换热器32,过冷器42的主路的出口通过制热节流阀EXV4连接到第一换热器31。Continuing to refer to FIG. 4 , the outlet of the main circuit of the subcooler 42 is connected to the second heat exchanger 32 through the cooling throttle valve EXV2, and the outlet of the main circuit of the subcooler 42 is connected to the second heat exchanger 32 through the heating throttle valve EXV4. A heat exchanger 31.

本发明实施例的热泵机组200还包括与压缩机10连接的油冷却器60。过冷器42的主路的出口还通过油冷节流阀EXV3连接到油冷却器60。The heat pump unit 200 in the embodiment of the present invention also includes an oil cooler 60 connected to the compressor 10 . The outlet of the main circuit of the subcooler 42 is also connected to the oil cooler 60 through the oil cooling throttle valve EXV3.

在一些实施例中,第一换热器31包括多个冷却盘管。本发明实施例的热泵机组200还包括预分配器80。多个冷却盘管连接至预分配器80。在一些实施例中,本发明实施例的热泵机组200还包括过滤器70,预分配器80通过过滤器70连接到经济器41。In some embodiments, first heat exchanger 31 includes multiple cooling coils. The heat pump unit 200 of the embodiment of the present invention also includes a pre-distributor 80 . A plurality of cooling coils are connected to the predistributor 80 . In some embodiments, the heat pump unit 200 of the embodiment of the present invention further includes a filter 70 , and the predistributor 80 is connected to the economizer 41 through the filter 70 .

预分配器80可以对多个冷却盘管的制冷剂量进行初分配。本发明实施例通过在经济器41之后增设一个过冷器42,从而可以有效地控制预分配器80入口处的制冷剂成分,使得制冷剂中液体成分比较多,液体越多,则可以使得制冷剂的分配越均匀。因此,本发明实施例可以使得第一换热器31中多个冷却盘管的制冷剂更加均匀分配。The predistributor 80 can initially distribute the amount of refrigerant among the plurality of cooling coils. In the embodiment of the present invention, by adding a subcooler 42 after the economizer 41, the refrigerant composition at the inlet of the predistributor 80 can be effectively controlled so that there is more liquid in the refrigerant. The more liquid, the better the cooling efficiency. The more evenly the agent is distributed. Therefore, the embodiment of the present invention can make the refrigerant of the multiple cooling coils in the first heat exchanger 31 more evenly distributed.

本发明实施例的热泵机组200还包括油分离器50和储液器90,压缩机10的排气口4通过油分离器50连接到换向阀20。The heat pump unit 200 in the embodiment of the present invention also includes an oil separator 50 and a liquid reservoir 90 . The exhaust port 4 of the compressor 10 is connected to the reversing valve 20 through the oil separator 50 .

本发明实施例的热泵机组200还包括控制器(未图示)。其中,在压缩机10满载运行的情况下,则控制器可以控制同时启用经济器41和过冷器42;而在压缩机10部分负荷运行的情况下,则控制器可以控制启用过冷器42。The heat pump unit 200 according to the embodiment of the present invention also includes a controller (not shown). Wherein, when the compressor 10 is running at full load, the controller can control the economizer 41 and the subcooler 42 to be activated at the same time; and when the compressor 10 is running at part load, the controller can control the activation of the subcooler 42 .

本发明实施例的热泵机组200通过在经济器41之后增设过冷器42,过冷器42在压缩机10部分负荷时可以启用,部分负荷运行时过冷度依然可以获得,有利于蒸发器的传热,从而解决了带有中间补气口23的压缩机10单纯使用经济器41仅能在满载时可启用而导致经济器41的利用率较低的问题。而且,过冷器42在部分负荷时开启,对制热分配也较有利,容易改善制热能力。The heat pump unit 200 in the embodiment of the present invention adds a subcooler 42 after the economizer 41. The subcooler 42 can be activated when the compressor 10 is partially loaded. The subcooling degree can still be obtained during partial load operation, which is beneficial to the evaporator. heat transfer, thereby solving the problem that the compressor 10 with the intermediate air supply port 23 simply uses the economizer 41 and can only be activated when it is fully loaded, resulting in low utilization of the economizer 41. Moreover, the subcooler 42 is opened during partial load, which is also beneficial to heating distribution and can easily improve the heating capacity.

当本发明实施例的热泵机组200运行在制冷模式下时,如图4中的箭头所示,制冷剂在压缩机10中被压缩,将原本低温低压的制冷剂气体压缩成高温高压的过热蒸汽后,由压缩机10的排气口4排出,通过油分离器50后进入换向阀20,通过换向阀20控制制冷剂的流向。高温高压的过热蒸汽从换向阀20的进口进入。由于在制冷模式下压缩机10的排气口4通过换向阀20与第一换热器31相连,因此,高温高压的过热蒸汽经换向阀20导入到第一换热器31中。此时,第一换热器31相当于冷凝器的作用。高温高压的过热蒸汽在第一换热器31中被冷却,过热的制冷剂由气态转变为液态。经过预分配器80后通过单向阀CV1,流经过滤器70进入经济器41的主路的入口,再从经济器41的主路的出口进入到过冷器42的主路的入口,从过冷器42的主路的出口经过制冷节流阀EXV2的节流降压,低温低压的制冷剂液体进入到第二换热器32中。此时,第二换热器32相当于蒸发器的作用,制冷剂液体在第二换热器32中吸热汽化,进而气化为低温低压的气态制冷剂。低温低压的气态制冷剂再经过换向阀20后,从压缩机10的吸气口1被压缩机10吸入,进入下一个制冷循环。When the heat pump unit 200 according to the embodiment of the present invention is running in the cooling mode, as shown by the arrow in Figure 4 As shown, the refrigerant is compressed in the compressor 10, and the original low-temperature and low-pressure refrigerant gas is compressed into high-temperature and high-pressure superheated steam, and is discharged from the exhaust port 4 of the compressor 10, and then enters the commutation after passing through the oil separator 50. The valve 20 controls the flow direction of the refrigerant through the reversing valve 20 . High-temperature and high-pressure superheated steam enters from the inlet of the reversing valve 20 . Since the exhaust port 4 of the compressor 10 is connected to the first heat exchanger 31 through the reversing valve 20 in the cooling mode, the superheated steam with high temperature and high pressure is introduced into the first heat exchanger 31 through the reversing valve 20 . At this time, the first heat exchanger 31 functions as a condenser. The high-temperature and high-pressure superheated steam is cooled in the first heat exchanger 31, and the superheated refrigerant changes from gaseous state to liquid state. After passing through the pre-distributor 80, it passes through the one-way valve CV1, flows through the filter 70, enters the main path inlet of the economizer 41, and then enters the main path inlet of the subcooler 42 from the outlet of the economizer 41. The outlet of the main path of the cooler 42 is throttled and depressurized by the refrigeration throttle valve EXV2, and the low-temperature and low-pressure refrigerant liquid enters the second heat exchanger 32 . At this time, the second heat exchanger 32 functions as an evaporator, and the refrigerant liquid absorbs heat and vaporizes in the second heat exchanger 32, and then vaporizes into a low-temperature and low-pressure gaseous refrigerant. After the low-temperature and low-pressure gaseous refrigerant passes through the reversing valve 20, it is sucked into the compressor 10 from the suction port 1 of the compressor 10 and enters the next refrigeration cycle.

当本发明实施例的热泵机组200运行在制热模式下时,如图4中的箭头所示,制冷剂在压缩机10中被压缩,将原本低温低压的制冷剂气体压缩成高温高压的过热蒸汽,经压缩机10压缩的高温高压过热蒸汽由压缩机10的排气口4排出,通过油分离器50之后,再经过换向阀20直接将高温高压的过热蒸汽送入到第二换热器32中。此时,第二换热器32相当于冷凝器的作用,过热的蒸汽通过第二换热器32进行散热,过热蒸汽冷却后形成低温高压的液体进入到储液器90中。储液器90中的低温高压的制冷剂液体之后通过单向阀CV2,流经过滤器70进入经济器41的主路的入口,再从经济器41的主路的出口进入到过冷器42的主路的入口,从过冷器42的主路的出口经过制热节流阀EXV4的节流降压后,低温低压的制冷剂再经过预分配器80被送入到第一换热器31中。此时,第一换热器31相当于蒸发器的作用。低温低压的制冷剂在第一换热器31中完成汽化的过程,制冷剂液体向外界释放大量的热,重新变成干饱和蒸汽。干饱和蒸汽最后通过换向阀20再返回压缩机10的吸气口1,继续下一个制热循环。When the heat pump unit 200 according to the embodiment of the present invention is running in the heating mode, as shown by the arrow in Figure 4 As shown, the refrigerant is compressed in the compressor 10, and the originally low-temperature and low-pressure refrigerant gas is compressed into high-temperature and high-pressure superheated steam. The high-temperature and high-pressure superheated steam compressed by the compressor 10 is discharged from the exhaust port 4 of the compressor 10. After passing through the oil separator 50, the high-temperature and high-pressure superheated steam is directly sent to the second heat exchanger 32 through the reversing valve 20. At this time, the second heat exchanger 32 functions as a condenser. The superheated steam dissipates heat through the second heat exchanger 32 . After the superheated steam is cooled, it forms a low-temperature and high-pressure liquid and enters the liquid reservoir 90 . The low-temperature and high-pressure refrigerant liquid in the accumulator 90 then passes through the one-way valve CV2, flows through the filter 70, enters the inlet of the main path of the economizer 41, and then enters the outlet of the main path of the economizer 41 into the subcooler 42. After the inlet of the main circuit and the outlet of the main circuit of the subcooler 42 are throttled and depressurized by the heating throttle valve EXV4, the low-temperature and low-pressure refrigerant is sent to the first heat exchanger 31 through the pre-distributor 80 middle. At this time, the first heat exchanger 31 functions as an evaporator. The low-temperature and low-pressure refrigerant completes the vaporization process in the first heat exchanger 31, and the refrigerant liquid releases a large amount of heat to the outside and becomes dry saturated steam again. The dry saturated steam finally passes through the reversing valve 20 and then returns to the suction port 1 of the compressor 10 to continue the next heating cycle.

本发明实施例的热泵机组200通过新增过冷器42,过冷器42可以实现和经济器41的联动,从而可以减少压缩机10的中间补气量,由于压缩机10的中间补气量减少,因此,可以使得压缩机10的功耗得到降低,本发明实施例的热泵机组200可以使得额定制冷效率和额定制热效率均得以提高。The heat pump unit 200 in the embodiment of the present invention adds a subcooler 42, and the subcooler 42 can be linked with the economizer 41, thereby reducing the intermediate air supply amount of the compressor 10. Since the intermediate air supply amount of the compressor 10 is reduced, Therefore, the power consumption of the compressor 10 can be reduced, and the heat pump unit 200 according to the embodiment of the present invention can improve both the rated cooling efficiency and the rated heating efficiency.

本发明实施例的热泵机组200在压缩机10中间补气口23的补气量减少后,经济器41的辅侧连接于压缩机10中间补气口23的振动也可以降低。由于压缩机10中间补气口23的尺寸是定值,因此,在经济器41的辅侧流量降低后,制冷剂管路流速可以有效降低。In the heat pump unit 200 according to the embodiment of the present invention, after the air supply volume of the middle air supply port 23 of the compressor 10 is reduced, the vibration of the auxiliary side of the economizer 41 connected to the middle air supply port 23 of the compressor 10 can also be reduced. Since the size of the middle air supply port 23 of the compressor 10 is fixed, after the auxiliary side flow rate of the economizer 41 is reduced, the refrigerant pipeline flow rate can be effectively reduced.

本发明实施例的热泵机组200通过新增过冷器42,低压级通过换向阀20制冷剂流量也降低,因而,换向阀20吸气侧(制冷、制热对应的吸气侧)压降均可下降。由于系统阻力下降,压缩机10排气口4的排气压力也可以下降,进而降低热泵机组200的功耗,有助于提升热泵机组200的效率。In the heat pump unit 200 according to the embodiment of the present invention, by adding the subcooler 42, the refrigerant flow rate of the low-pressure stage through the reversing valve 20 is also reduced. Therefore, the pressure on the suction side (the suction side corresponding to cooling and heating) of the reversing valve 20 is reduced. It can be lowered. As the system resistance decreases, the exhaust pressure at the exhaust port 4 of the compressor 10 can also decrease, thereby reducing the power consumption of the heat pump unit 200 and helping to improve the efficiency of the heat pump unit 200 .

申请人通过在实验室进行两种方案的热泵机组在额定制冷工况下的测试比较,即第一种方案是启用经济器41但过冷器42被旁通的热泵机组方案,第二种方案是联合启用经济器41和过冷器42的热泵机组方案,在工况稳定后采集系统得到的性能数据可以发现,第二种方案(即联合启用经济器41和过冷器42的热泵机组方案)相对于第一种方案(即仅启用经济器41的热泵机组方案),热泵机组的效率COP提升了近1.77%。另外,发现主要是因此联合启用经济器41和过冷器42的热泵机组方案相对于仅启用经济器41的热泵机组方案减少了补气侧制冷剂流量,从而减小了压缩机的功耗,依此降低了热泵机组的总功耗,实现了热泵机组的效率COP的提高。因此,验证了本发明实施例的热泵机组新增过冷器42的方案是非常有效的。The applicant conducted a test comparison of two schemes of heat pump units under rated refrigeration conditions in the laboratory, that is, the first scheme is a heat pump unit scheme in which the economizer 41 is enabled but the subcooler 42 is bypassed, and the second scheme is It is a heat pump unit scheme that jointly activates the economizer 41 and the subcooler 42. The performance data collected from the system after the working conditions are stable can be found. The second scheme (that is, the heat pump unit scheme that jointly activates the economizer 41 and the subcooler 42 ) Compared with the first solution (that is, the heat pump unit solution with only economizer 41 enabled), the efficiency COP of the heat pump unit has increased by nearly 1.77%. In addition, it was found that the main reason is that the heat pump unit solution in which the economizer 41 and the subcooler 42 are jointly enabled reduces the refrigerant flow rate on the supply side compared to the heat pump unit solution in which only the economizer 41 is enabled, thereby reducing the power consumption of the compressor. In this way, the total power consumption of the heat pump unit is reduced, and the efficiency COP of the heat pump unit is improved. Therefore, it is verified that the solution of adding a subcooler 42 to the heat pump unit according to the embodiment of the present invention is very effective.

申请人通过将本发明实施例的新增过冷器42的热泵机组在额定制冷和制热运行时的数据比较可以发现,本发明实施例的新增过冷器42的热泵机组不仅在制冷模式是有效的,在制热运行时验证依然是有效的。By comparing the data of the heat pump unit with a new subcooler 42 in the embodiment of the present invention during rated cooling and heating operations, the applicant can find that the heat pump unit with a new subcooler 42 in the embodiment of the present invention not only operates in the cooling mode is valid and is still valid when the heating is running.

另外,申请人通过将启用过冷器42和未启用过冷器42的热泵机组在压缩机部分负荷运行时的数据比较可以发现,本发明实施例的热泵机组在增设过冷器42之后,热泵机组在部分负荷运行时对应的效率COP都好于同等负荷下的效率。因此,通过增设过冷器42也是提升热泵机组综合部分负荷性能IPLV值的一个有效手段。In addition, by comparing the data of the heat pump unit with the subcooler 42 enabled and without the subcooler 42 when the compressor is running at partial load, the applicant can find that after the subcooler 42 is added to the heat pump unit according to the embodiment of the present invention, the heat pump The corresponding efficiency COP of the unit when operating at part load is better than the efficiency under the same load. Therefore, adding a subcooler 42 is also an effective means to improve the IPLV value of the comprehensive part load performance of the heat pump unit.

以上对本发明实施例所提供的热泵机组进行了详细的介绍。本文中应用了具体个例对本发明实施例的热泵机组进行了阐述,以上实施例的说明只是用于帮助理解本发明的核心思想,并不用以限制本发明。应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明的精神和原理的前提下,还可以对本发明进行若干改进和修饰,这些改进和修饰也均应落入本发明所附权利要求书的保护范围内。The heat pump unit provided by the embodiment of the present invention has been introduced in detail above. This article uses specific examples to illustrate the heat pump unit according to the embodiments of the present invention. The description of the above embodiments is only used to help understand the core idea of the present invention and is not intended to limit the present invention. It should be pointed out that for those of ordinary skill in the art, several improvements and modifications can be made to the present invention without departing from the spirit and principles of the present invention, and these improvements and modifications should also fall within the scope of the present invention. within the scope of protection of the claims.

Claims (8)

1. A heat pump unit comprising a compressor, a reversing valve, a first heat exchanger, an economizer, a subcooler and a second heat exchanger connected by refrigerant lines, the compressor having an intake, an exhaust and an intermediate make-up, the economizer being connected to the intermediate make-up of the compressor, the subcooler comprising a main and an auxiliary, the heat pump unit further comprising a reservoir, a solenoid valve disposed at the bottom of the reservoir, a first check valve and a second check valve, the reservoir being connected to the first heat exchanger by the solenoid valve and the first check valve, the reservoir being connected to the second heat exchanger by the solenoid valve and the second check valve, wherein an inlet of the main of the subcooler is connected to the economizer, an outlet of the main of the subcooler is connected to the first heat exchanger and the second heat exchanger, an inlet of the auxiliary of the subcooler is connected to the main of the subcooler by a subcooler throttle valve, an outlet of the auxiliary of the subcooler is connected to the first heat exchanger, the heat pump unit is further controlled to operate while the compressor is activated by the controller; the controller controls activation of the subcooler with the compressor part load operation.
2. The heat pump assembly of claim 1, wherein: the inlet of the auxiliary path of the subcooler is connected to the inlet of the main path of the subcooler or the outlet of the main path of the subcooler through the subcooler throttle valve.
3. The heat pump assembly of claim 1, wherein: the economizer comprises a main path and an auxiliary path, wherein an inlet of the main path of the economizer is connected to the first heat exchanger, an outlet of the main path of the economizer is connected to an inlet of the main path of the subcooler, an inlet of the auxiliary path of the economizer is connected to the inlet of the main path of the economizer or an outlet of the main path of the economizer through an economizer throttle valve, and an outlet of the auxiliary path of the economizer is connected to an intermediate air supplementing port of the compressor.
4. The heat pump assembly of claim 1, wherein: the outlet of the main path of the subcooler is connected to the second heat exchanger through a refrigeration throttle valve, and the outlet of the main path of the subcooler is connected to the first heat exchanger through a heating throttle valve.
5. The heat pump assembly of claim 1, wherein: and an oil cooler connected with the compressor, wherein an outlet of a main path of the subcooler is also connected with the oil cooler through an oil cooling restrictor.
6. The heat pump assembly of claim 1, wherein: the first heat exchanger includes a plurality of cooling coils, and the heat pump unit further includes a pre-distributor to which the plurality of cooling coils are connected.
7. The heat pump assembly of claim 6, wherein: also included is a filter through which the pre-distributor is connected to the economizer and an oil separator through which the compressor discharge is connected to the reversing valve.
8. The heat pump assembly of claim 1, wherein: the second heat exchanger includes a water side heat exchanger having a water outlet end and a water inlet end.
CN202111007226.0A 2021-08-30 2021-08-30 Heat pump unit Active CN113686044B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111007226.0A CN113686044B (en) 2021-08-30 2021-08-30 Heat pump unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111007226.0A CN113686044B (en) 2021-08-30 2021-08-30 Heat pump unit

Publications (2)

Publication Number Publication Date
CN113686044A CN113686044A (en) 2021-11-23
CN113686044B true CN113686044B (en) 2023-10-27

Family

ID=78584065

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111007226.0A Active CN113686044B (en) 2021-08-30 2021-08-30 Heat pump unit

Country Status (1)

Country Link
CN (1) CN113686044B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114111110A (en) * 2021-12-02 2022-03-01 广东日出东方空气能有限公司 Heat pump system with plate for exchanging supercooling

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101568776A (en) * 2006-10-27 2009-10-28 开利公司 Economized refrigeration cycle with expander
US20100005831A1 (en) * 2007-02-02 2010-01-14 Carrier Corporation Enhanced refrigerant system
CN101896778A (en) * 2007-12-19 2010-11-24 三菱重工业株式会社 Refrigeration device
CN104567159A (en) * 2014-12-26 2015-04-29 珠海格力电器股份有限公司 Differential pressure control method of refrigerating unit and refrigerating unit
CN206192006U (en) * 2016-11-14 2017-05-24 松下压缩机(大连)有限公司 Low temperature refrigeration system
CN110986417A (en) * 2019-11-25 2020-04-10 珠海格力节能环保制冷技术研究中心有限公司 Double-air-supplement heat pump system and control method thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101568776A (en) * 2006-10-27 2009-10-28 开利公司 Economized refrigeration cycle with expander
US20100005831A1 (en) * 2007-02-02 2010-01-14 Carrier Corporation Enhanced refrigerant system
CN101896778A (en) * 2007-12-19 2010-11-24 三菱重工业株式会社 Refrigeration device
CN104567159A (en) * 2014-12-26 2015-04-29 珠海格力电器股份有限公司 Differential pressure control method of refrigerating unit and refrigerating unit
CN206192006U (en) * 2016-11-14 2017-05-24 松下压缩机(大连)有限公司 Low temperature refrigeration system
CN110986417A (en) * 2019-11-25 2020-04-10 珠海格力节能环保制冷技术研究中心有限公司 Double-air-supplement heat pump system and control method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李凡.空气源热泵热水器.重庆大学出版社,2010,第116页. *

Also Published As

Publication number Publication date
CN113686044A (en) 2021-11-23

Similar Documents

Publication Publication Date Title
CN110332635B (en) Double-stage compression multi-air-supplementing refrigeration heat pump system, control method and air conditioner
CN103175344B (en) Cold-region used multi-connected heat pump system and control method thereof
CN103090579B (en) Air conditioner heat pump system of electric automobile
CN100529590C (en) Dual-purpose heat pump device for winter and summer
CN101140122B (en) Heat pump machine group of combined throttling set
CN107366621B (en) Rotary Rotary Compressor and Air Conditioning System with Three-Stage Air Make-up
CN102032705B (en) Two-stage compression heat pump system
CN108759138B (en) Operation method and system of secondary throttling middle incomplete cooling refrigerating system
CN103363717A (en) Refrigerating system and operation method thereof
CN107576090B (en) Refrigerating system
WO2022099748A1 (en) Heat pump system
CN105444476A (en) Heat exchange system
CN108036445A (en) A kind of improved heat source tower heat pump device
CN111486609B (en) Air conditioning system and control method
CN113686044B (en) Heat pump unit
CN205066233U (en) Heat pump heating system and heat pump water heater
CN103940135B (en) Refrigerating device
CN206988109U (en) Compressor with rolling rotor and air-conditioning system with three-level tonifying Qi
CN214469331U (en) heat pump system
CN205448417U (en) Heat exchange system
CN110470073B (en) Carbon dioxide heat pump system
CN118794156A (en) Air conditioning refrigeration system and air conditioning refrigeration method
CN216204444U (en) Air conditioner combining air supply compressor and indoor and outdoor auxiliary heat exchanger
CN211120083U (en) Air cooler system capable of alternately defrosting
CN210951964U (en) Air-cooled heat pump unit

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant