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CN107062670B - Double-channel variable-capacity heat exchanger - Google Patents

Double-channel variable-capacity heat exchanger Download PDF

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Publication number
CN107062670B
CN107062670B CN201710244656.1A CN201710244656A CN107062670B CN 107062670 B CN107062670 B CN 107062670B CN 201710244656 A CN201710244656 A CN 201710244656A CN 107062670 B CN107062670 B CN 107062670B
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refrigerant
channel
heat exchanger
heat
subsystem
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CN107062670A (en
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吴运运
王玉军
王颖
李俊红
杨奕
王天舒
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Changzhou Changbang Heat Exchanger Co ltd
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Jiangsu Tianshu Electric Appliance Co Ltd
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    • 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
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H4/00Fluid heaters characterised by the use of heat pumps
    • F24H4/02Water heaters
    • 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
    • F25B29/00Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
    • F25B29/003Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
    • 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
    • F25B30/00Heat pumps
    • F25B30/02Heat pumps of the compression type
    • 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
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/31Expansion valves

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

A double-channel variable-capacity heat exchanger relates to a heating and refrigerating combined system or a component, a device or a component of a heat pump system, in particular to a heat exchanger for a heat pump type combined cooling and heating system; the heat exchanger main body comprises two mutually independent refrigerant tube pass channels, and refrigerants in the two channels exchange heat with heat medium water in the shell pass channel at the same time; the shell pass channel establishes a water medium heat supply circulation through a hot water circulation pipeline and a hot water circulation pump; the first subsystem and the second subsystem are connected to two refrigerant tube pass channels through a control valve group to establish a dynamically controllable refrigerant circulation loop; the heat pump system realizes a double-channel variable volume mode through controlling the on-off state of a control valve group of the double-channel variable volume heat exchanger and the double-channel variable volume heat exchanger, and can effectively utilize the heat exchange area of the shell and tube heat exchanger, thereby meeting the requirement of stable output under a heavy load working condition, greatly improving the overall operation efficiency of the unit and further realizing the high-energy-efficiency operation of the heat pump system.

Description

一种双通道可变容量换热器A dual-channel variable-capacity heat exchanger

技术领域technical field

本发明涉及加热和制冷的联合系统或热泵系统的部件、装置或构件,尤其涉及一种用于热泵式冷热联供系统的换热器。The present invention relates to a combined heating and cooling system or a component, device or component of a heat pump system, in particular to a heat exchanger for a heat pump combined cooling and heating system.

背景技术Background technique

集约型社会建设口号的提出,促使建筑物本体内功能集成化程度更高,做到最大化能源利用已经成为当今议题。如今,商业和商务场所要求越来越高:空气侧要求控制适宜的温湿度和空气洁净度;用水侧水温度要求全年适宜。而传统的冷热源单独供给的方式在不同季节中显然造成了资源的错置,与此同时设备初投资成本亦大大提升。如图1所示的巧克力加工工艺,巧克力产品经过原料混合融化、精磨、精炼、过筛、保温、调温、浇模成型和冷却硬化最后包装成产品,不仅需要大量的热量和冷量供应,而且各个工艺环节对温度有着严格的要求。传统的温度控制一般通过电加热、蒸汽加热或是燃烧锅炉供给热量,而对不同温度要求得工艺往往是通过不同的供热方式来实现,这就增加了企业的运营成本且降低了工作效率,同时不能实现智能控制,需要大量人力投入。因此,需要对原有的耗能生产工艺流程进行改造,研发能够满足食品加工工艺要求的加热和制冷的联合系统。中国发明专利“饭店后厨热泵系统多模式运行控制方法及其控制装置”(发明专利号:201410478406.0,授权公告号:CN104197584B)公开了一种饭店后厨热泵系统多模式运行控制方法及其控制装置,涉及加热和制冷的联合系统的控制,尤其涉及一种适用于饭店后厨的热水供应、降温除湿和冷藏保鲜的热泵综合系统的控制方法及设备,控制装置通过检测和比较运行模式参数的实测值和设定值,控制多模式制冷剂循环回路切换机构改变制冷剂的循环路径,控制饭店后厨热泵系统按照预设的运行模式运行,实现自动多模式运行。The introduction of the slogan of intensive society construction has promoted a higher degree of functional integration in the building itself, and maximized energy utilization has become a current issue. Today, the requirements of commercial and commercial places are getting higher and higher: the air side needs to control the appropriate temperature, humidity and air cleanliness; the water side water temperature is required to be suitable throughout the year. The traditional method of supplying cold and heat sources separately has obviously caused misplacement of resources in different seasons, and at the same time, the initial investment cost of equipment has also greatly increased. The chocolate processing process shown in Figure 1, the chocolate products are mixed and melted, finely ground, refined, sieved, heat preservation, temperature adjusted, moulded and cooled and hardened, and finally packaged into products, which not only requires a large amount of heat and cold supply , and each process link has strict requirements on temperature. Traditional temperature control generally supplies heat through electric heating, steam heating or combustion boilers, and processes requiring different temperatures are often realized through different heating methods, which increases the operating cost of the enterprise and reduces work efficiency. At the same time, intelligent control cannot be achieved, requiring a lot of human input. Therefore, it is necessary to transform the original energy-consuming production process and develop a combined heating and cooling system that can meet the requirements of food processing technology. The Chinese invention patent "Multi-mode operation control method and control device of restaurant back kitchen heat pump system" (invention patent number: 201410478406.0, authorized announcement number: CN104197584B) discloses a restaurant back kitchen heat pump system multi-mode operation control method and control device. , involving the control of a combined heating and cooling system, in particular a control method and equipment for a heat pump integrated system for hot water supply, cooling and dehumidification, and refrigeration and preservation suitable for restaurant kitchens. The measured value and the set value, control the multi-mode refrigerant circulation circuit switching mechanism to change the refrigerant circulation path, and control the restaurant rear kitchen heat pump system to operate according to the preset operation mode to realize automatic multi-mode operation.

另一方面,现有具有热回收功能的热泵系统通常采用一个独立的冷凝器和一个独立热回收器连接组成制热换热器,不仅占用空间大而且成本高。中国实用新型专利“壳管换热器及空调”(实用新型专利号:201420417296.2,授权公告号:CN204084963U)公开了一种壳管换热器及包括该壳管换热器的空调,该壳管换热器包括冷凝器和热回收器,冷凝器一端设有冷却进水口与冷却出水口,另一端密封设置;热回收器一端设有热水进口与热水出口,另一端与冷凝器密封的一端固定连接:通过将冷凝器与热回收器各自的密封端固定连接,并通过连接管将热回收器与冷凝器的冷媒通道连接起来,既能保证壳管换热器正常的冷凝功能及热回收功能,还能使壳管换热器的结构紧凑,节省安装空间,降低成本。但是,该现有技术方案实质上只是把两个独立的功能部件机械上设计为一体,其各自的功能仍然是互相独立的,并不能提高换热器的整体换热效率。On the other hand, the existing heat pump system with heat recovery function usually adopts an independent condenser and an independent heat recovery device to form a heating heat exchanger, which not only occupies a large space but also has a high cost. Chinese utility model patent "Shell and Tube Heat Exchanger and Air Conditioner" (Utility Model Patent No.: 201420417296.2, Authorized Announcement No.: CN204084963U) discloses a shell and tube heat exchanger and an air conditioner including the shell and tube heat exchanger. The heat exchanger includes a condenser and a heat recovery device. One end of the condenser is provided with a cooling water inlet and a cooling water outlet, and the other end is sealed; one end of the heat recovery device is provided with a hot water inlet and a hot water outlet, and the other end is sealed with the condenser. Fixed connection at one end: by fixing the respective sealed ends of the condenser and the heat recovery device, and connecting the heat recovery device and the refrigerant channel of the condenser through the connecting pipe, it can ensure the normal condensing function and heat recovery of the shell and tube heat exchanger. The recovery function can also make the shell and tube heat exchanger compact, save installation space and reduce costs. However, the prior art solution essentially only mechanically designs two independent functional components into one, and their respective functions are still independent of each other, which cannot improve the overall heat exchange efficiency of the heat exchanger.

发明内容SUMMARY OF THE INVENTION

本发明的目的是要提供一种用于热泵式冷热联供系统的双通道可变容量换热器,用于解决热泵冷热联供系统取代传统加热方式过程中缩减设备尺度、节约设备投入和运行成本,提高换热效率和机组能效的技术问题。The purpose of the present invention is to provide a dual-channel variable-capacity heat exchanger for a heat pump combined cooling and heating system, which is used to reduce equipment size and save equipment investment in the process of replacing traditional heating methods with a heat pump combined cooling and heating system. and operating costs, and improve the technical issues of heat exchange efficiency and unit energy efficiency.

本发明解决上述技术问题所采用的技术方案是:The technical scheme adopted by the present invention to solve the above-mentioned technical problems is:

一种双通道可变容量换热器,用于带冷量回收的空气源热泵热水系统,所述的空气源热泵热水系统包括第一压缩机和冷量回收换热器组成的第一子系统,第二压缩机和翅片式换热器组成的第二子系统,其特征在于:A dual-channel variable-capacity heat exchanger is used for an air source heat pump hot water system with cold energy recovery, the air source heat pump hot water system includes a first compressor and a cold energy recovery heat exchanger. The subsystem, the second subsystem composed of the second compressor and the finned heat exchanger, is characterized in that:

所述的双通道可变容量换热器包括作为换热器主体的壳管式换热器和连接到壳管换热器之制冷剂管程通道的控制阀组;The double-channel variable-capacity heat exchanger includes a shell-and-tube heat exchanger as the main body of the heat exchanger and a control valve group connected to the refrigerant tube-side channel of the shell-and-tube heat exchanger;

所述的换热器主体内设有两个互相独立的第一制冷剂通道和第二制冷剂通道,两个制冷剂管程通道置于一个共用的壳程通道内;第一子系统和第二子系统通过所述的控制阀组连接到两个制冷剂管程通道,建立动态可控的制冷剂循环回路;The heat exchanger main body is provided with two mutually independent first refrigerant passages and second refrigerant passages, and the two refrigerant tube side passages are placed in a common shell side passage; The two subsystems are connected to the two refrigerant tube-side passages through the control valve group to establish a dynamically controllable refrigerant circulation loop;

两个制冷剂管程通道内的制冷剂同时与壳程通道中的水进行热交换;换热器主体的壳程通道通过热水循环管路和热水循环泵建立水媒供热循环;The refrigerant in the two refrigerant tube-side channels exchanges heat with the water in the shell-side channels at the same time; the shell-side channel of the heat exchanger main body establishes a water-medium heat supply cycle through the hot water circulation pipeline and the hot water circulation pump;

所述的控制阀组包括连接在制冷剂管程通道的三个电磁阀和两个单向阀;所述的电磁阀包括连接在第一制冷剂通道出口的第一电磁阀,连接在第一制冷剂通道出口和第二制冷剂通道入口之间的第二电磁阀,以及连接在第二制冷剂通道出口的第三电磁阀;所述的单向阀包括连接在第二制冷剂通道入口的第一单向阀,以及并联连接在第二制冷剂通道出口和第一电磁阀出口之间的第二单向阀;The control valve group includes three solenoid valves and two one-way valves connected to the refrigerant tube-side passage; the solenoid valve includes a first solenoid valve connected to the outlet of the first refrigerant passage and connected to the first solenoid valve. a second solenoid valve between the outlet of the refrigerant passage and the inlet of the second refrigerant passage, and a third solenoid valve connected to the outlet of the second refrigerant passage; the one-way valve includes a solenoid valve connected to the inlet of the second refrigerant passage a first check valve, and a second check valve connected in parallel between the outlet of the second refrigerant passage and the outlet of the first solenoid valve;

第一压缩机的制冷剂排气管路连接到第一制冷剂通道的入口;第一电磁阀的出口和第二单向阀的出口并联连接后,通过第一膨胀阀连接到冷量回收换热器的制冷剂通道;第二压缩机的制冷剂排气管路连接到第一单向阀的入口;第三电磁阀的出口通过第二膨胀阀连接到翅片式换热器的制冷剂通道;The refrigerant discharge line of the first compressor is connected to the inlet of the first refrigerant passage; after the outlet of the first solenoid valve and the outlet of the second one-way valve are connected in parallel, they are connected to the cold energy recovery exchanger through the first expansion valve. The refrigerant passage of the heat exchanger; the refrigerant discharge line of the second compressor is connected to the inlet of the first one-way valve; the outlet of the third solenoid valve is connected to the refrigerant of the fin heat exchanger through the second expansion valve aisle;

空气源热泵热水系统通过改变控制阀组的开关状态,实现双通道可变容量换热器的动态多模式运行。The air source heat pump hot water system realizes the dynamic multi-mode operation of the dual-channel variable-capacity heat exchanger by changing the switch state of the control valve group.

本发明的双通道可变容量换热器的一种较佳的技术方案,其特征在于所述的换热器主体采用壳程通道上下连通的立式结构,第一制冷剂通道置于壳程通道的上部,第二制冷剂通道置于壳程通道的下部;制冷剂的高温显热在第一制冷剂通道中传递给壳程通道上部的水,形成高温显热换热区;制冷剂的冷凝潜热在第二制冷剂通道中传递给壳程通道下部的水,形成冷凝潜热换热区。A preferred technical solution of the dual-channel variable-capacity heat exchanger of the present invention is characterized in that the main body of the heat exchanger adopts a vertical structure in which the shell-side channels are connected up and down, and the first refrigerant channel is placed on the shell-side The upper part of the channel, the second refrigerant channel is placed in the lower part of the shell side channel; the high temperature sensible heat of the refrigerant is transferred to the water in the upper part of the shell side channel in the first refrigerant channel, forming a high temperature sensible heat heat exchange area; The latent heat of condensation is transferred to the water in the lower part of the shell-side channel in the second refrigerant channel to form a latent heat of condensation heat exchange area.

本发明的双通道可变容量换热器的一种更好的技术方案,其特征在于所述的动态多模式运行包括以下四种运行模式:A better technical solution of the dual-channel variable-capacity heat exchanger of the present invention is characterized in that the dynamic multi-mode operation includes the following four operation modes:

(1)第一子系统冷热均衡模式:第一压缩机启动,第二压缩机停止,第一电磁阀打开,第二电磁阀关闭,本模式下第一压缩机排出的高温高压制冷剂循环进入第一制冷剂通道,再经由第一电磁阀和第一膨胀阀进入冷量回收换热器,建立第一子系统制冷剂循环回路;第一制冷剂通道内的制冷剂与壳程通道中的水进行热交换,将第一子系统制取冷水过程中冷量回收换热器回收的热能,传递给换热器主体壳程通道中制取的热水;(1) Cold and heat balance mode of the first subsystem: the first compressor is started, the second compressor is stopped, the first solenoid valve is opened, and the second solenoid valve is closed. In this mode, the high-temperature and high-pressure refrigerant discharged from the first compressor circulates Enter the first refrigerant passage, and then enter the cold energy recovery heat exchanger through the first solenoid valve and the first expansion valve to establish the first subsystem refrigerant circulation circuit; the refrigerant in the first refrigerant passage and the shell side passage The heat exchange is carried out with the water obtained by the first subsystem, and the heat energy recovered by the cold energy recovery heat exchanger in the process of producing cold water by the first subsystem is transferred to the hot water produced in the shell-side channel of the main body of the heat exchanger;

(2)第二子系统空气源热水模式:第一压缩机停止,第二压缩机启动,第二电磁阀关闭,第三电磁阀打开,本模式下第二压缩机排出的高温高压制冷剂通过第一单向阀进入第二制冷剂通道,再经由第三电磁阀和第二膨胀阀进入翅片式换热器,建立第二子系统制冷剂循环回路;第二制冷剂通道内的制冷剂与壳程通道中的水进行热交换,将第二子系统之翅片式换热器从空气源吸收的热能,传递给换热器主体壳程通道中制取的热水;(2) Air source hot water mode of the second subsystem: the first compressor is stopped, the second compressor is started, the second solenoid valve is closed, and the third solenoid valve is opened. In this mode, the high-temperature and high-pressure refrigerant discharged from the second compressor Enter the second refrigerant passage through the first one-way valve, and then enter the finned heat exchanger through the third solenoid valve and the second expansion valve to establish the refrigerant circulation circuit of the second subsystem; the refrigeration in the second refrigerant passage The agent exchanges heat with the water in the shell-side channel, and transfers the heat energy absorbed by the fin heat exchanger of the second subsystem from the air source to the hot water produced in the shell-side channel of the main body of the heat exchanger;

(3)双系统定容冷热水模式:第一压缩机和第二压缩机同时启动,第一电磁阀打开,第二电磁阀关闭,第三电磁阀打开;本模式下第一压缩机排出的高温高压制冷剂循环进入第一制冷剂通道,再经由第一电磁阀和第一膨胀阀进入冷量回收换热器,建立第一子系统制冷剂循环回路;第二压缩机排出的高温高压制冷剂通过第一单向阀进入第二制冷剂通道,再经由第三电磁阀和第二膨胀阀进入翅片式换热器,建立第二子系统制冷剂循环回路;第一制冷剂通道内的制冷剂与壳程通道中的水进行热交换,将第一子系统冷水制取过程中冷量回收换热器回收的热能,传递给换热器主体壳程通道中制取的热水;同时,第二制冷剂通道内的制冷剂与壳程通道中的水进行热交换,将第二子系统之翅片式换热器从空气源吸收的热能,传递给换热器主体壳程通道中制取的热水;(3) Dual-system constant volume hot and cold water mode: the first compressor and the second compressor are started at the same time, the first solenoid valve is opened, the second solenoid valve is closed, and the third solenoid valve is opened; in this mode, the first compressor discharges The high temperature and high pressure refrigerant circulates into the first refrigerant passage, and then enters the cold energy recovery heat exchanger through the first solenoid valve and the first expansion valve to establish the first subsystem refrigerant circulation circuit; the high temperature and high pressure discharged from the second compressor The refrigerant enters the second refrigerant passage through the first one-way valve, and then enters the finned heat exchanger through the third solenoid valve and the second expansion valve to establish the refrigerant circulation circuit of the second subsystem; The refrigerant in the heat exchanger exchanges heat with the water in the shell-side channel, and transfers the heat energy recovered by the cold-capacity recovery heat exchanger during the cold-water production process of the first subsystem to the hot water produced in the shell-side channel of the main body of the heat exchanger; At the same time, the refrigerant in the second refrigerant channel exchanges heat with the water in the shell-side channel, and transfers the heat energy absorbed by the fin heat exchanger of the second subsystem from the air source to the shell-side channel of the main body of the heat exchanger. hot water from the

(4)双通道变容运行模式:第一压缩机启动,第二压缩机停止,第一电磁阀关闭,第二电磁阀打开,第三电磁阀关闭,本模式下第一压缩机排出的高温高压制冷剂首先进入第一制冷剂通道,然后经由第二电磁阀进入第二制冷剂通道,再经由第二单向阀进入冷量回收换热器,建立双通道变容运行制冷剂循环回路;制冷剂通过第一制冷剂通道和第二制冷剂通道,与壳程通道中的水进行两次热交换,将第一子系统冷水制取过程中冷量回收换热器回收的热能,传递给换热器主体壳程通道中制取的热水。(4) Dual-channel variable capacity operation mode: the first compressor starts, the second compressor stops, the first solenoid valve is closed, the second solenoid valve is opened, and the third solenoid valve is closed. In this mode, the high temperature discharged by the first compressor The high-pressure refrigerant first enters the first refrigerant passage, then enters the second refrigerant passage through the second solenoid valve, and then enters the cold energy recovery heat exchanger through the second one-way valve to establish a dual-channel variable-capacity operation refrigerant circulation loop; The refrigerant passes through the first refrigerant channel and the second refrigerant channel, and exchanges heat twice with the water in the shell-side channel, and transfers the heat energy recovered by the cold energy recovery heat exchanger during the cold water production process of the first subsystem to the water. The hot water produced in the shell-side channel of the main body of the heat exchanger.

本发明的有益效果是:The beneficial effects of the present invention are:

1、本发明的双通道可变容量换热器通过双通道变容模式运行,能够有效利用壳管式换热器的换热面积,因而能够满足大负荷工况稳定出力的要求,机组整体运行效率大大提升,从而实现热泵系统的高能效运行。1. The dual-channel variable-capacity heat exchanger of the present invention operates in the dual-channel variable-capacity mode, which can effectively utilize the heat exchange area of the shell-and-tube heat exchanger, so it can meet the requirements of stable output under heavy load conditions, and the unit operates as a whole. The efficiency is greatly improved, thereby realizing the energy-efficient operation of the heat pump system.

2、本发明的双通道可变容量换热器,利用变容量模式运行的双通道可变容量换热器和冷量回收换热器实现部分冷量回收,能够大大提升子系统中制冷剂的过冷度,从而提高系统的制冷量。2. The dual-channel variable-capacity heat exchanger of the present invention utilizes the dual-channel variable-capacity heat exchanger operating in the variable-capacity mode and the cooling capacity recovery heat exchanger to achieve partial cooling capacity recovery, which can greatly improve the refrigerant efficiency in the subsystem. Subcooling degree, thereby increasing the cooling capacity of the system.

3、本发明的双通道可变容量换热器,可以使两套制冷系统共用一套水冷冷凝器实现耦合运行,利用冷量回收换热器以减小翅片式蒸发器尺寸,从而达到降低系统尺寸的目的,使冷热联供系统在不同冷热负荷下低耗稳定运行,达到高效节能运行的目的。3. The dual-channel variable-capacity heat exchanger of the present invention can make two sets of refrigeration systems share a set of water-cooled condensers to realize coupled operation, and use the cold energy recovery heat exchanger to reduce the size of the finned evaporator, thereby reducing the size of the finned evaporator. The purpose of the system size is to make the combined cooling and heating system operate stably with low consumption under different cooling and heating loads, so as to achieve the purpose of high-efficiency and energy-saving operation.

附图说明Description of drawings

图1是巧克力加工工艺流程图;Fig. 1 is the process flow chart of chocolate processing;

图2是冷量回收式变容量空气源热泵系统的系统原理图;Figure 2 is a system schematic diagram of a cooling capacity recovery variable-capacity air source heat pump system;

图3是冷量回收式变容量空气源热泵系统的装配结构示意图;Fig. 3 is a schematic diagram of the assembly structure of a cooling capacity recovery variable-capacity air source heat pump system;

图4是本发明的双通道可变容量换热器的结构示意图;4 is a schematic structural diagram of a dual-channel variable-capacity heat exchanger of the present invention;

图5是冷量回收式变容量空气源热泵系统的运行模式示意图。FIG. 5 is a schematic diagram of the operation mode of the cooling capacity recovery variable-capacity air source heat pump system.

以上图中各部件的附图标记:1-第一子系统,10-第一压缩机,11-第一四通阀,12-第一膨胀阀,13-冷量回收换热器,14-冷水循环管路,15-第一气液分离器,16-第一感温包,17-第一储液器,18-第一除霜单向电磁阀,2-第二子系统,20-第二压缩机,21-第二四通阀,22-第二膨胀阀,23-翅片式换热器,24-风机,25-第二气液分离器,26-第二感温包,27-第二储液器,28-第二除霜单向电磁阀,3-双通道可变容量换热器,30-换热器主体,31-第一制冷剂通道,32-第二制冷剂通道,33-第一电磁阀,34-第二电磁阀,35-第三电磁阀,36-第一单向阀,37-第二单向阀,38-热水循环管路,39-热水循环泵。The reference numbers of the components in the above figures: 1-first subsystem, 10-first compressor, 11-first four-way valve, 12-first expansion valve, 13-cold recovery heat exchanger, 14- Cold water circulation pipeline, 15-first gas-liquid separator, 16-first temperature bulb, 17-first accumulator, 18-first defrost one-way solenoid valve, 2-second subsystem, 20- The second compressor, 21-the second four-way valve, 22-the second expansion valve, 23-fin heat exchanger, 24-fan, 25-the second gas-liquid separator, 26-the second temperature bulb, 27-Second accumulator, 28-Second defrost one-way solenoid valve, 3-Dual-channel variable capacity heat exchanger, 30-Heat exchanger body, 31-First refrigerant channel, 32-Second refrigeration Agent channel, 33-first solenoid valve, 34-second solenoid valve, 35-third solenoid valve, 36-first check valve, 37-second check valve, 38-hot water circulation pipeline, 39- Hot water circulation pump.

具体实施方式Detailed ways

为了能更好地理解本发明的上述技术方案,下面结合附图和实施例进行进一步地详细描述。图2和图3是本发明的冷量回收式变容量空气源热泵系统的一个实施例,包括第一压缩机10和冷量回收换热器13组成的第一子系统1,第二压缩机20和翅片式换热器23组成的第二子系统2,如图2所示,所述的第一子系统1和第二子系统2共同使用一个双通道可变容量换热器3作为水冷冷凝器;所述的双通道可变容量换热器3包括换热器主体30和一组由电磁阀与单向阀组成的控制阀组;换热器主体30包括置于同一壳程通道的两个互相独立的制冷剂管程通道,两个制冷剂管程通道内的制冷剂同时与壳程通道中的水进行热交换;换热器主体30的壳程通道通过热水循环管路38和热水循环泵39建立水媒供热循环;第一子系统1和第二子系统2通过所述的控制阀组连接到两个制冷剂管程通道,建立动态可控的制冷剂循环回路;热泵系统通过控制双通道可变容量换热器3之控制阀组的开关状态,实现热泵系统的动态多模式运行。以某巧克力加工产线为例,1T原料从加工至最后包装成产品的生产过程需要稳定100KW热量和50KW冷量需求。在本实施例中,第一子系统1采用套管式蒸发器作为冷量回收换热器13,回收部分冷量用于巧克力加工的浇模成型、冷却硬化和包装等工艺过程中的冷量供应;第二子系统2采用翅片式换热器23从空气源吸取热量,根据冷热量需求的差异增加热泵系统的整体制热能力。In order to better understand the above technical solutions of the present invention, further detailed description is given below in conjunction with the accompanying drawings and embodiments. FIG. 2 and FIG. 3 are an embodiment of the cooling energy recovery variable-capacity air source heat pump system of the present invention, which includes a first subsystem 1 composed of a first compressor 10 and a cooling energy recovery heat exchanger 13, and a second compressor The second subsystem 2 composed of 20 and finned heat exchanger 23, as shown in FIG. 2, the first subsystem 1 and the second subsystem 2 jointly use a dual-channel variable capacity heat exchanger 3 as the Water-cooled condenser; the double-channel variable-capacity heat exchanger 3 includes a heat exchanger body 30 and a set of control valve groups consisting of solenoid valves and one-way valves; the heat exchanger body 30 includes a channel placed in the same shell side The refrigerant in the two refrigerant tube-side channels is independent of each other, and the refrigerant in the two refrigerant tube-side channels exchanges heat with the water in the shell-side channels at the same time; the shell-side channels of the heat exchanger main body 30 pass through the hot water circulation pipeline. 38 and the hot water circulation pump 39 to establish a water medium heating cycle; the first subsystem 1 and the second subsystem 2 are connected to the two refrigerant tube-side channels through the control valve group to establish a dynamically controllable refrigerant cycle The heat pump system realizes the dynamic multi-mode operation of the heat pump system by controlling the switch state of the control valve group of the dual-channel variable capacity heat exchanger 3. Taking a chocolate processing production line as an example, the production process of 1T raw materials from processing to final packaging into products needs to stabilize 100KW of heat and 50KW of cooling. In this embodiment, the first sub-system 1 adopts a casing evaporator as the cooling capacity recovery heat exchanger 13, and recovers part of the cooling capacity for the cooling capacity in the process of molding, cooling and hardening, and packaging of chocolate processing. Supply; the second subsystem 2 uses a fin heat exchanger 23 to absorb heat from the air source, and increases the overall heating capacity of the heat pump system according to the difference in cooling and heating requirements.

在图4所示的实施例中,所述的双通道可变容量换热器3包括作为换热器主体30的壳管式换热器和连接到壳管换热器之制冷剂管程通道的控制阀组;所述的换热器主体30内设有两个互相独立的第一制冷剂通道31和第二制冷剂通道32,两个制冷剂管程通道31和32置于一个共用的壳程通道内;所述的控制阀组包括连接在制冷剂管程通道的三个电磁阀和两个单向阀;所述的电磁阀包括连接在第一制冷剂通道31出口的第一电磁阀33,连接在第一制冷剂通道31出口和第二制冷剂通道32入口之间的第二电磁阀34,以及连接在第二制冷剂通道32出口的第三电磁阀35;所述的单向阀包括连接在第二制冷剂通道32入口的第一单向阀36,以及并联连接在第二制冷剂通道32出口和第一电磁阀33出口之间的第二单向阀37;第一压缩机10的排气口通过第一四通阀11连接到第一制冷剂通道31的入口;第一电磁阀33的出口和第二单向阀37的出口并联连接后,通过第一膨胀阀12连接到冷量回收换热器13的制冷剂通道,再通过第一四通阀11连接到第一压缩机10的进气口;第二压缩机20的排气口通过第二四通阀21连接到第一单向阀36的入口;第三电磁阀35的出口通过第二膨胀阀22连接到翅片式换热器23的制冷剂通道,再通过第二四通阀21连接到第二压缩机20的进气口。In the embodiment shown in FIG. 4 , the dual-channel variable-capacity heat exchanger 3 includes a shell-and-tube heat exchanger as the heat exchanger body 30 and a refrigerant tube-side channel connected to the shell-and-tube heat exchanger The heat exchanger body 30 is provided with two independent first refrigerant passages 31 and second refrigerant passages 32, and the two refrigerant tube-side passages 31 and 32 are placed in a common in the shell side channel; the control valve group includes three solenoid valves and two one-way valves connected to the refrigerant tube side channel; the solenoid valve includes a first solenoid valve connected to the outlet of the first refrigerant channel 31 valve 33, a second solenoid valve 34 connected between the outlet of the first refrigerant passage 31 and the inlet of the second refrigerant passage 32, and a third solenoid valve 35 connected to the outlet of the second refrigerant passage 32; the single The check valve includes a first check valve 36 connected to the inlet of the second refrigerant passage 32, and a second check valve 37 connected in parallel between the outlet of the second refrigerant passage 32 and the outlet of the first solenoid valve 33; the first The discharge port of the compressor 10 is connected to the inlet of the first refrigerant passage 31 through the first four-way valve 11; the outlet of the first solenoid valve 33 and the outlet of the second one-way valve 37 are connected in parallel, and then pass through the first expansion valve. 12 is connected to the refrigerant passage of the cold energy recovery heat exchanger 13, and then connected to the air inlet of the first compressor 10 through the first four-way valve 11; the exhaust port of the second compressor 20 is connected through the second four-way valve 21 is connected to the inlet of the first one-way valve 36; the outlet of the third solenoid valve 35 is connected to the refrigerant passage of the fin heat exchanger 23 through the second expansion valve 22, and then connected to the first through the second four-way valve 21. The intake port of the second compressor 20 .

根据本发明的双通道可变容量换热器的一个实施例,所述的换热器主体30采用壳程通道上下连通的立式结构,第一制冷剂通道31置于壳程通道的上部,第二制冷剂通道32置于壳程通道的下部;制冷剂的高温显热在第一制冷剂通道31中传递给壳程通道上部的水,形成高温显热换热区;制冷剂的冷凝潜热在第二制冷剂通道32中传递给壳程通道下部的水,形成冷凝潜热换热区。According to an embodiment of the dual-channel variable-capacity heat exchanger of the present invention, the heat exchanger main body 30 adopts a vertical structure in which the shell-side channels are connected up and down, and the first refrigerant channel 31 is placed on the upper part of the shell-side channel. The second refrigerant passage 32 is placed at the lower part of the shell side passage; the high temperature sensible heat of the refrigerant is transferred to the water in the upper part of the shell side passage in the first refrigerant passage 31 to form a high temperature sensible heat heat exchange area; the latent heat of condensation of the refrigerant The water transferred to the lower part of the shell side channel in the second refrigerant channel 32 forms a heat exchange area for latent heat of condensation.

根据图2所示的本发明的冷量回收式变容量空气源热泵系统的实施例,在第一制冷剂通道31与第一膨胀阀12之间的连接管路上设有第一储液器17,在第二制冷剂通道32与第二膨胀阀22之间的连接管路上设有第二储液器27。According to the embodiment of the cold energy recovery type variable capacity air source heat pump system of the present invention shown in FIG. 2 , a first accumulator 17 is provided on the connecting pipeline between the first refrigerant passage 31 and the first expansion valve 12 , a second accumulator 27 is provided on the connecting pipeline between the second refrigerant passage 32 and the second expansion valve 22 .

根据图5所示的本发明的冷量回收式变容量空气源热泵系统的实施例,所述的动态多模式运行包括以下四种运行模式:According to the embodiment of the cooling capacity recovery variable-capacity air source heat pump system of the present invention shown in FIG. 5 , the dynamic multi-mode operation includes the following four operation modes:

(1)第一子系统冷热均衡模式:第一压缩机10启动,第二压缩机20停止,第一电磁阀33打开,第二电磁阀34关闭,本模式的制冷剂循环路径如下:(1) Cold and heat balance mode of the first subsystem: the first compressor 10 is started, the second compressor 20 is stopped, the first solenoid valve 33 is opened, and the second solenoid valve 34 is closed. The refrigerant circulation path in this mode is as follows:

第一压缩机10-第一四通阀11-第一制冷剂通道31-第一电磁阀33-第一储液器17-第一膨胀阀12-冷量回收换热器13-第一四通阀11-第一气液分离器15-第一压缩机10;First compressor 10 - First four-way valve 11 - First refrigerant passage 31 - First solenoid valve 33 - First accumulator 17 - First expansion valve 12 - Cold energy recovery heat exchanger 13 - First four Through valve 11-first gas-liquid separator 15-first compressor 10;

本模式下,第一制冷剂通道31内的制冷剂与壳程通道中的水进行热交换,将第一子系统1制取冷水过程中冷量回收换热器13回收的热能,传递给换热器主体30壳程通道中制取的热水。In this mode, the refrigerant in the first refrigerant channel 31 exchanges heat with the water in the shell-side channel, and transfers the heat energy recovered by the cold energy recovery heat exchanger 13 during the process of producing cold water by the first subsystem 1 to the heat exchanger. The hot water produced in the shell side channel of the heater main body 30.

(2)第二子系统空气源热水模式:第一压缩机10停止,第二压缩机20启动,第二电磁阀34关闭,第三电磁阀35打开,本模式的制冷剂循环路径如下:(2) Air source hot water mode of the second subsystem: the first compressor 10 is stopped, the second compressor 20 is started, the second solenoid valve 34 is closed, and the third solenoid valve 35 is opened. The refrigerant circulation path in this mode is as follows:

第二压缩机20-第二四通阀21-第一单向阀36-第二制冷剂通道32-第三电磁阀35-第二储液器27-第二膨胀阀22-翅片式换热器23-第二四通阀21-第二气液分离器25-第二压缩机20;The second compressor 20 - the second four-way valve 21 - the first one-way valve 36 - the second refrigerant passage 32 - the third solenoid valve 35 - the second accumulator 27 - the second expansion valve 22 - the fin type changer Heater 23-second four-way valve 21-second gas-liquid separator 25-second compressor 20;

本模式下,第二制冷剂通道32内的制冷剂与壳程通道中的水进行热交换,将第二子系统2之翅片式换热器23从空气源吸收的热能,传递给换热器主体30壳程通道中制取的热水。In this mode, the refrigerant in the second refrigerant passage 32 exchanges heat with the water in the shell-side passage, and transfers the heat energy absorbed by the fin heat exchanger 23 of the second subsystem 2 from the air source to the heat exchange The hot water produced in the shell-side channel of the main body 30.

(3)双系统定容冷热水模式:第一压缩机10和第二压缩机20同时启动,第一电磁阀33打开,第二电磁阀34关闭,第三电磁阀35打开;(3) Dual-system constant volume hot and cold water mode: the first compressor 10 and the second compressor 20 are started at the same time, the first solenoid valve 33 is opened, the second solenoid valve 34 is closed, and the third solenoid valve 35 is opened;

第一子系统1的制冷剂循环路径如下:The refrigerant circulation path of the first subsystem 1 is as follows:

第一压缩机10-第一四通阀11-第一制冷剂通道31-第一电磁阀33-第一储液器17-第一膨胀阀12-冷量回收换热器13-第一四通阀11-第一气液分离器15-第一压缩机10;First compressor 10 - First four-way valve 11 - First refrigerant passage 31 - First solenoid valve 33 - First accumulator 17 - First expansion valve 12 - Cold energy recovery heat exchanger 13 - First four Through valve 11-first gas-liquid separator 15-first compressor 10;

第二子系统2的制冷剂循环路径如下:The refrigerant circulation path of the second subsystem 2 is as follows:

第二压缩机20-第二四通阀21-第一单向阀36-第二制冷剂通道32-第三电磁阀35-第二储液器27-第二膨胀阀22-翅片式换热器23-第二四通阀21-第二气液分离器25-第二压缩机20;The second compressor 20 - the second four-way valve 21 - the first one-way valve 36 - the second refrigerant passage 32 - the third solenoid valve 35 - the second accumulator 27 - the second expansion valve 22 - the fin type changer Heater 23-second four-way valve 21-second gas-liquid separator 25-second compressor 20;

在双系统定容冷热水模式下,第一制冷剂通道31内的制冷剂与壳程通道中的水进行热交换,将第一子系统1冷水制取过程中冷量回收换热器13回收的热能,传递给换热器主体30壳程通道中制取的热水;同时,第二制冷剂通道32内的制冷剂与壳程通道中的水进行热交换,将第二子系统2之翅片式换热器23从空气源吸收的热能,传递给换热器主体30壳程通道中制取的热水。In the dual-system constant volume cold and hot water mode, the refrigerant in the first refrigerant channel 31 exchanges heat with the water in the shell-side channel, and the cold energy in the cold water production process of the first subsystem 1 is recovered to the heat exchanger 13 The recovered heat energy is transferred to the hot water produced in the shell-side channel of the heat exchanger main body 30; at the same time, the refrigerant in the second refrigerant channel 32 exchanges heat with the water in the shell-side channel, and the second subsystem 2 The heat energy absorbed by the fin heat exchanger 23 from the air source is transferred to the hot water produced in the shell side channel of the heat exchanger body 30 .

(4)双通道变容模式:第一压缩机10启动,第二压缩机20停止,第一电磁阀33关闭,第二电磁阀34打开,第三电磁阀35关闭,本模式的制冷剂循环路径如下:(4) Dual-channel variable capacity mode: the first compressor 10 is started, the second compressor 20 is stopped, the first solenoid valve 33 is closed, the second solenoid valve 34 is opened, and the third solenoid valve 35 is closed, and the refrigerant in this mode circulates The path is as follows:

第一压缩机10-第一四通阀11-第一制冷剂通道31-第二电磁阀34-第二制冷剂通道32-第二单向阀37-第一储液器17-第一膨胀阀12-冷量回收换热器13-第一四通阀11-第一气液分离器15-第一压缩机10。First compressor 10 - First four-way valve 11 - First refrigerant passage 31 - Second solenoid valve 34 - Second refrigerant passage 32 - Second one-way valve 37 - First accumulator 17 - First expansion Valve 12-cold recovery heat exchanger 13-first four-way valve 11-first gas-liquid separator 15-first compressor 10.

在双通道变容模式下,本发明的冷量回收式变容量空气源热泵系统之第一压缩机10排气口排出的高温高压制冷剂气体,经第一四通阀11进入双通道可变容量换热器3中,流经第一制冷剂通道31进行第一段换热后,形成制冷剂气液混合物并通过第二电磁阀34回到双通道可变容量换热器3中,在第二制冷剂通道32中再次与换热器主体30的水侧充分换热,冷凝为高压常温的制冷剂液体,流经第二单向阀37后经第一膨胀阀12的节流作用,变为低压制冷剂液体,进入作为冷量回收换热器13的套管式蒸发器,吸热蒸发为低压制冷剂气体通过第一四通阀11进入第一气液分离器15,最终进入第一压缩机10进气口,形成双通道变容模式运行的制冷剂循环路径;在本模式下,制冷剂通过第一制冷剂通道31和第二制冷剂通道32,与壳程通道中的水进行两次热交换,将第一子系统1冷水制取过程中冷量回收换热器13回收的热能,传递给换热器主体30壳程通道中制取的热水。In the dual-channel variable-capacity mode, the high-temperature and high-pressure refrigerant gas discharged from the discharge port of the first compressor 10 of the cooling-capacity variable-capacity air source heat pump system of the present invention enters the dual-channel variable capacity through the first four-way valve 11 . In the capacity heat exchanger 3, after the first stage of heat exchange is performed through the first refrigerant passage 31, a refrigerant gas-liquid mixture is formed and returned to the dual-channel variable capacity heat exchanger 3 through the second solenoid valve 34. The second refrigerant passage 32 exchanges sufficient heat with the water side of the heat exchanger body 30 again, condenses into a refrigerant liquid of high pressure and normal temperature, flows through the second one-way valve 37 and then undergoes the throttling action of the first expansion valve 12 . It turns into a low-pressure refrigerant liquid, enters the sleeve-type evaporator as the cold energy recovery heat exchanger 13, absorbs heat and evaporates into a low-pressure refrigerant gas, enters the first gas-liquid separator 15 through the first four-way valve 11, and finally enters the first gas-liquid separator 15. An air inlet of the compressor 10 forms a refrigerant circulation path operating in the dual-channel variable capacity mode; in this mode, the refrigerant passes through the first refrigerant passage 31 and the second refrigerant passage 32, and communicates with the water in the shell side passage. Two heat exchanges are performed, and the heat energy recovered by the cold energy recovery heat exchanger 13 during the cold water production process of the first subsystem 1 is transferred to the hot water produced in the shell-side channel of the heat exchanger main body 30 .

本发明的冷量回收式变容量空气源热泵系统,利用变容量模式运行的双通道可变容量换热器3,能够大大提升第一子系统1中制冷剂的过冷度,从而提高系统的制冷量。在第二子系统2停机时,双通道变容模式能够有效利用壳管式换热器的换热面积,因而能够满足大负荷工况稳定出力的要求,机组整体运行效率大大提升,从而实现热泵系统的高能效运行。The cooling capacity recovery variable-capacity air source heat pump system of the present invention utilizes the dual-channel variable-capacity heat exchanger 3 operating in the variable-capacity mode, which can greatly improve the subcooling degree of the refrigerant in the first subsystem 1, thereby improving the system's performance. cooling capacity. When the second subsystem 2 is shut down, the dual-channel variable capacity mode can effectively utilize the heat exchange area of the shell-and-tube heat exchanger, so it can meet the requirements of stable output under heavy load conditions, and the overall operating efficiency of the unit is greatly improved, thereby realizing the heat pump Energy efficient operation of the system.

根据本发明的冷量回收式变容量空气源热泵系统的一个实施例,所述的空气源热泵系统根据制冷回收冷量改变翅片式换热器的换热面积,在保证机组制热量的同时缩减热泵系统的整体系统尺寸:According to an embodiment of the cooling capacity recovery variable-capacity air source heat pump system of the present invention, the air source heat pump system changes the heat exchange area of the fin heat exchanger according to the cooling capacity recovered, so as to ensure the heating capacity of the unit at the same time. Reduce the overall system size of the heat pump system:

翅片式换热器23之换热面积S的变化范围为0~W2/q,The variation range of the heat exchange area S of the fin heat exchanger 23 is 0 to W 2 /q,

冷量回收换热器13之换热面积S1的变化范围为0~(W1-W2)/q1The variation range of the heat exchange area S 1 of the cold energy recovery heat exchanger 13 is 0~(W 1 -W 2 )/q 1 ,

其中,机组制热量Q1=W1+Pi,kw;W1为系统制热运行时蒸发器侧的制冷量,kw;Pi为系统制热运行输入功率,kw;W2为制冷回收冷量,kw;S=W2/q为翅片式换热器23的换热面积,m2;q为制热工况下蒸发侧单位换热面积制冷量,kw/m2;S1=(W1-W2)/q1为冷量回收换热器13的换热面积,m2;q1为冷量回收换热器13单位换热面积制冷量,kw/m2Wherein, the unit heating capacity Q 1 =W 1 +P i , kw; W 1 is the cooling capacity of the evaporator side during the system heating operation, kw; P i is the system heating operation input power, kw; W 2 is the refrigeration recovery Cooling capacity, kw; S=W 2 /q is the heat exchange area of the fin heat exchanger 23, m 2 ; q is the cooling capacity per unit heat exchange area on the evaporating side under heating conditions, kw/m 2 ; S 1 =(W 1 -W 2 )/q 1 is the heat exchange area of the cooling capacity recovery heat exchanger 13 , m 2 ; q 1 is the cooling capacity per unit heat exchange area of the cooling capacity recovery heat exchanger 13 , kw/m 2 .

本技术领域中的普通技术人员应当认识到,以上的实施例仅是用来说明本发明的技术方案,而并非用作为对本发明的限定,任何基于本发明的实质精神对以上所述实施例所作的变化、变型,都将落在本发明的权利要求的保护范围内。Those skilled in the art should realize that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than being used to limit the present invention. The changes and modifications will fall within the protection scope of the claims of the present invention.

Claims (2)

1. The utility model provides a binary channels variable capacity heat exchanger for take air source heat pump hot-water heating system of cold volume recovery, air source heat pump hot-water heating system include the first subsystem that first compressor and cold volume recovery heat exchanger constitute, the second subsystem that second compressor and finned heat exchanger constitute, its characterized in that:
the double-channel variable-capacity heat exchanger comprises a shell-and-tube heat exchanger serving as a heat exchanger main body and a control valve group connected to a refrigerant tube pass channel of the shell-and-tube heat exchanger;
the heat exchanger main body is internally provided with a first refrigerant channel and a second refrigerant channel which are mutually independent, and the two refrigerant tube pass channels are arranged in a common shell pass channel; the first subsystem and the second subsystem are connected to two refrigerant tube pass channels through the control valve group to establish a dynamically controllable refrigerant circulation loop;
the refrigerants in the two refrigerant tube pass channels exchange heat with water in the shell pass channel at the same time; a shell pass channel of the heat exchanger main body establishes hydrophily heat supply circulation through a hot water circulation pipeline and a hot water circulation pump;
the control valve group comprises three electromagnetic valves and two one-way valves which are connected with a refrigerant tube pass channel; the electromagnetic valves comprise a first electromagnetic valve connected to the outlet of the first refrigerant channel, a second electromagnetic valve connected between the outlet of the first refrigerant channel and the inlet of the second refrigerant channel, and a third electromagnetic valve connected to the outlet of the second refrigerant channel; the check valve comprises a first check valve connected to the inlet of the second refrigerant channel and a second check valve connected between the outlet of the second refrigerant channel and the outlet of the first electromagnetic valve in parallel;
a refrigerant discharge pipe path of the first compressor is connected to an inlet of the first refrigerant path through a first four-way valve; after the outlet of the first electromagnetic valve and the outlet of the second one-way valve are connected in parallel, the first electromagnetic valve and the second one-way valve are connected to a refrigerant channel of the cold energy recovery heat exchanger through a first expansion valve; a refrigerant discharge pipeline of the second compressor is connected to an inlet of the first check valve through a second four-way valve; an outlet of the third electromagnetic valve is connected to a refrigerant channel of the finned heat exchanger through a second expansion valve;
the air source heat pump hot water system realizes dynamic multi-mode operation of the double-channel variable-capacity heat exchanger by changing the on-off state of the control valve group;
the heat exchanger main body adopts a vertical structure with a shell pass channel communicated up and down, the first refrigerant channel is arranged at the upper part of the shell pass channel, and the second refrigerant channel is arranged at the lower part of the shell pass channel; high-temperature sensible heat of the refrigerant is transferred to water on the upper part of the shell pass channel in the first refrigerant channel to form a high-temperature sensible heat exchange zone; the latent heat of condensation of the refrigerant is transferred to water at the lower part of the shell pass channel in the second refrigerant channel to form a latent heat of condensation heat exchange zone.
2. The two-pass variable capacity heat exchanger of claim 1, wherein the dynamic multi-mode operation includes four modes of operation:
(1) the first subsystem cold and hot equalization mode: the method comprises the following steps that a first compressor is started, a second compressor is stopped, a first electromagnetic valve is opened, a second electromagnetic valve is closed, high-temperature and high-pressure refrigerants discharged by the first compressor circularly enter a first refrigerant channel in the mode, and then enter a cold recovery heat exchanger through the first electromagnetic valve and a first expansion valve to establish a first subsystem refrigerant circulating loop; the refrigerant in the first refrigerant channel exchanges heat with water in the shell pass channel, and heat energy recovered by the cold energy recovery heat exchanger in the cold water preparation process of the first subsystem is transferred to hot water prepared in the shell pass channel of the heat exchanger main body;
(2) the air source hot water mode of the second subsystem is as follows: the first compressor stops, the second compressor starts, the second electromagnetic valve closes, the third electromagnetic valve opens, in this mode, the high-temperature and high-pressure refrigerant discharged by the second compressor enters the second refrigerant channel through the first one-way valve, and then enters the finned heat exchanger through the third electromagnetic valve and the second expansion valve, and a second subsystem refrigerant circulation loop is established; the refrigerant in the second refrigerant channel exchanges heat with water in the shell-side channel, and the heat energy absorbed by the fin-type heat exchanger of the second subsystem from an air source is transferred to hot water prepared in the shell-side channel of the heat exchanger main body;
(3) a dual-system constant-volume cold and hot water mode: the first compressor and the second compressor are started simultaneously, the first electromagnetic valve is opened, the second electromagnetic valve is closed, and the third electromagnetic valve is opened; in the mode, high-temperature and high-pressure refrigerant discharged by the first compressor circularly enters the first refrigerant channel and then enters the cold recovery heat exchanger through the first electromagnetic valve and the first expansion valve to establish a first subsystem refrigerant circulating loop; high-temperature and high-pressure refrigerant discharged by the second compressor enters a second refrigerant channel through the first one-way valve and then enters the finned heat exchanger through a third electromagnetic valve and a second expansion valve to establish a second subsystem refrigerant circulation loop; the refrigerant in the first refrigerant channel exchanges heat with water in the shell pass channel, and the heat energy recovered by the cold energy recovery heat exchanger in the cold water preparation process of the first subsystem is transferred to the hot water prepared in the shell pass channel of the heat exchanger main body; meanwhile, the refrigerant in the second refrigerant channel exchanges heat with water in the shell pass channel, and the heat energy absorbed by the fin type heat exchanger of the second subsystem from an air source is transferred to hot water prepared in the shell pass channel of the heat exchanger main body;
(4) two-channel variable-capacity operation mode: in the mode, high-temperature and high-pressure refrigerant discharged by the first compressor firstly enters a first refrigerant channel, then enters a second refrigerant channel through the second electromagnetic valve and then enters a cold energy recovery heat exchanger through a second one-way valve, so that a two-channel variable-capacity operation refrigerant circulation loop is established; the refrigerant carries out heat exchange with water in the shell pass channel twice through the first refrigerant channel and the second refrigerant channel, and heat energy recovered by the cold energy recovery heat exchanger in the cold water preparation process of the first subsystem is transferred to hot water prepared in the shell pass channel of the heat exchanger main body.
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