CN107356016A - A kind of evaporator and the changeable heat exchange unit of loop circuit heat pipe - Google Patents

A kind of evaporator and the changeable heat exchange unit of loop circuit heat pipe Download PDF

Info

Publication number
CN107356016A
CN107356016A CN201710437653.XA CN201710437653A CN107356016A CN 107356016 A CN107356016 A CN 107356016A CN 201710437653 A CN201710437653 A CN 201710437653A CN 107356016 A CN107356016 A CN 107356016A
Authority
CN
China
Prior art keywords
heat exchanger
heat
refrigerant
evaporator
mouths
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.)
Granted
Application number
CN201710437653.XA
Other languages
Chinese (zh)
Other versions
CN107356016B (en
Inventor
张春路
刘洪鑫
曹祥
邵亮亮
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.)
Tongji University
Original Assignee
Tongji University
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 Tongji University filed Critical Tongji University
Priority to CN201710437653.XA priority Critical patent/CN107356016B/en
Publication of CN107356016A publication Critical patent/CN107356016A/en
Application granted granted Critical
Publication of CN107356016B publication Critical patent/CN107356016B/en
Expired - Fee Related 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
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • 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
    • F25B39/00Evaporators; Condensers

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

本发明涉及一种蒸发器与环路热管可切换的换热单元,包括主换热器、预冷换热器和再热换热器,所述预冷换热器、主换热器和再热换热器的换热流体通道依次串联,所述预冷换热器、主换热器和再热换热器的制冷剂换热通道通过制冷剂连接管联通,并通过制冷剂管路切换形成独立蒸发器模式或蒸发器加环路热管组合模式。与现有技术相比,本发明可以通过四个三通阀来实现不同情况下独立蒸发器模式及蒸发器加环路热管组合模式的转换,从而减少系统不必要的能量损失。

The invention relates to a switchable heat exchange unit between an evaporator and a loop heat pipe, comprising a main heat exchanger, a precooling heat exchanger and a reheating heat exchanger, the precooling heat exchanger, the main heat exchanger and the reheating heat exchanger The heat exchange fluid passages of the heat exchanger are connected in series in sequence, and the refrigerant heat exchange passages of the precooling heat exchanger, the main heat exchanger and the reheat heat exchanger are connected through refrigerant connecting pipes, and are switched through refrigerant pipelines. Form independent evaporator mode or combined mode of evaporator plus loop heat pipe. Compared with the prior art, the present invention can realize the conversion of the independent evaporator mode and the combined mode of the evaporator plus loop heat pipe under different conditions through four three-way valves, thereby reducing unnecessary energy loss of the system.

Description

一种蒸发器与环路热管可切换的换热单元A heat exchange unit with switchable evaporator and loop heat pipe

技术领域technical field

本发明涉及一种换热单元,具体涉及一种蒸发器与环路热管可切换的换热单元。The invention relates to a heat exchange unit, in particular to a heat exchange unit in which an evaporator and a loop heat pipe can be switched.

背景技术Background technique

热管是一种新型的传热元件,主要原理是利用介质在热端蒸发后在冷端冷凝的相变过程(即利用液体的蒸发潜热和凝结潜热),使热量快速传导,其导热能力超过任何已知金属的导热能力。环路热管是一种高效的相变传热装置,它由蒸发器、冷凝器组成,通过气液传输管路连接成回路,利用工质的蒸发和冷凝来传递热量,能够在小温差,长距离的情况下传递大量的热量。环路热管目前已成为航空热控制系统的首选传热元件,在地面电子设备的冷却系统中也正发挥着越来越重要的作用。The heat pipe is a new type of heat transfer element. The main principle is to use the phase change process of the medium condensing at the cold end after evaporating at the hot end (that is, using the latent heat of evaporation and latent heat of condensation of the liquid) to conduct heat quickly, and its heat conduction capacity exceeds any The thermal conductivity of metals is known. The loop heat pipe is a high-efficiency phase change heat transfer device. It is composed of an evaporator and a condenser. It is connected into a loop through a gas-liquid transmission pipeline. It uses the evaporation and condensation of the working fluid to transfer heat. A large amount of heat is transferred over a long distance. Loop heat pipes have become the heat transfer element of choice in aviation thermal control systems and are playing an increasingly important role in cooling systems for ground electronics.

在蒸汽压缩制冷装置中,蒸发器利用制冷剂低压蒸发,形成低温,实现对换热流体降温。蒸发器面积越大,制冷系统的蒸发压力越高,制冷循环的效率越高。当使用蒸发器对空气进行热湿处理时,不仅可以实现空气降温,当蒸发器表面温度低于露点温度时还可以使空气中的水分凝结,实现除湿功能,且蒸发温度越低,凝水效果越显著。In the vapor compression refrigeration device, the evaporator utilizes the low-pressure evaporation of the refrigerant to form a low temperature to cool the heat exchange fluid. The larger the area of the evaporator, the higher the evaporation pressure of the refrigeration system and the higher the efficiency of the refrigeration cycle. When the evaporator is used for heat and humidity treatment of the air, it can not only reduce the temperature of the air, but also condense the moisture in the air when the surface temperature of the evaporator is lower than the dew point temperature, so as to realize the dehumidification function, and the lower the evaporation temperature, the better the condensation effect more significant.

在实际应用过程中,某些情况下需要将所有换热面积都作为蒸发器,尽可能提高蒸发温度,提高循环效率;在除湿再热的条件下,又需要利用低蒸发温度增加凝水效率,通过再热实现热回收。例如,在热泵干衣机的热泵循环中,为了使除湿效果更好,蒸发温度一般较低,而且空气先经过降温除湿然再进行加热,带来不必要的能量损失。In the actual application process, in some cases, it is necessary to use all the heat exchange area as an evaporator to increase the evaporation temperature as much as possible and improve the cycle efficiency; under the condition of dehumidification and reheating, it is necessary to use the low evaporation temperature to increase the condensation efficiency. Heat recovery is achieved by reheating. For example, in the heat pump cycle of a heat pump dryer, in order to make the dehumidification effect better, the evaporation temperature is generally lower, and the air is first cooled and dehumidified before being heated, which brings unnecessary energy loss.

发明内容Contents of the invention

本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种可以在独立蒸发器和蒸发器加环路热管组合之间相互转换的换热单元。The object of the present invention is to provide a heat exchange unit that can be switched between an independent evaporator and a combination of an evaporator plus a loop heat pipe in order to overcome the above-mentioned defects in the prior art.

本发明的目的可以通过以下技术方案来实现:一种蒸发器与环路热管可切换的换热单元,该换热单元包括主换热器、预冷换热器和再热换热器,所述预冷换热器、主换热器和再热换热器的换热流体通道依次串联,所述预冷换热器、主换热器和再热换热器的制冷剂换热通道通过制冷剂连接管联通,并通过制冷剂管路切换形成独立蒸发器模式或蒸发器加环路热管组合模式。The purpose of the present invention can be achieved through the following technical solutions: a heat exchange unit with switchable evaporator and loop heat pipe, the heat exchange unit includes a main heat exchanger, a precooling heat exchanger and a reheating heat exchanger, the The heat exchange fluid passages of the pre-cooling heat exchanger, the main heat exchanger and the reheat heat exchanger are connected in series in sequence, and the refrigerant heat exchange passages of the pre-cooling heat exchanger, the main heat exchanger and the reheat heat exchanger pass through The refrigerant connection pipes are connected, and the independent evaporator mode or the combination mode of the evaporator plus the loop heat pipe is formed through the switching of the refrigerant pipeline.

优选的,所述的换热流体通道的进口设置在预冷换热器上,换热流体通道的出口设置在再热换热器上。Preferably, the inlet of the heat exchange fluid passage is arranged on the precooling heat exchanger, and the outlet of the heat exchange fluid passage is arranged on the reheat heat exchanger.

所述的换热流体通道中流动的流体为空气,通过风机将空气从换热流体通道的进口输送至换热流体通道的出口。The fluid flowing in the heat exchange fluid channel is air, and the air is transported from the inlet of the heat exchange fluid channel to the outlet of the heat exchange fluid channel by the fan.

所述制冷剂换热通道连接顺序如下:一号三通阀的三号口与主换热器的制冷剂通道的a端连接;一号三通阀的二号口分别与预冷换热器的制冷剂通道的a端及三号三通阀的三号口连接;预冷换热器的制冷剂通道的b端与二号三通阀的一号口连接,所述二号三通阀的二号口与主换热器的制冷剂通道的a端连接,所述主换热器的制冷剂通道的b端分别与三号三通阀的一号口及四号三通阀的三号口连接,所述三号三通阀的二号口与再热换热器的制冷剂通道的a端连接,所述再热换热器的制冷剂通道的b端分别与二号三通阀的三号口及四号三通阀的一号进口连接。The connection sequence of the refrigerant heat exchange channels is as follows: port No. 3 of the No. 1 three-way valve is connected to end a of the refrigerant channel of the main heat exchanger; No. 2 port of the No. 1 three-way valve is connected to the pre-cooling heat exchanger The a end of the refrigerant passage of the refrigerant channel is connected with the third port of the third three-way valve; the b end of the refrigerant passage of the pre-cooling heat exchanger is connected with the first port of the second three-way valve, and the second three-way valve The No. 2 port of the main heat exchanger is connected to the a end of the refrigerant channel of the main heat exchanger, and the b end of the refrigerant channel of the main heat exchanger is respectively connected to the No. 1 port of the No. 3 three-way valve and the third port of the No. 4 three-way valve. The No. 2 port of the No. 3 three-way valve is connected to the a-end of the refrigerant passage of the reheat heat exchanger, and the b-end of the refrigerant passage of the reheat heat exchanger is respectively connected to the No. 2 tee The No. 3 port of the valve and the No. 1 inlet of the No. 4 three-way valve are connected.

所述再热换热器的制冷剂通道的b端与二号三通阀的三号口的连接管路上设有制冷剂泵。A refrigerant pump is provided on the connecting pipeline between end b of the refrigerant channel of the reheat heat exchanger and port No. 3 of the No. 2 three-way valve.

独立蒸发器模式下,所述一号三通阀的三号口、二号三通阀的三号口、三号三通阀的三号口及四号三通阀的三号口关闭。In the independent evaporator mode, the No. 3 port of the No. 1 three-way valve, No. 3 port of the No. 2 three-way valve, No. 3 port of the No. 3 three-way valve and No. 3 port of the No. 4 three-way valve are closed.

蒸发器加环路热管组合模式下,所述一号三通阀的二号口、二号三通阀的二号口、三号三通阀的一号口及四号三通阀的一号口关闭。In the combination mode of the evaporator plus the loop heat pipe, the No. 2 port of the No. 1 three-way valve, the No. 2 port of the No. 2 three-way valve, the No. 1 port of the No. 3 three-way valve, and the No. 1 port of the No. 4 three-way valve Mouth closed.

所述制冷剂换热通道的进口与一号三通阀一号口连接,制冷剂换热通道的出口与四号三通阀的二号口连接,此种连接方式下,制冷剂换热通道中的流体流动与换热流体通道中的空气流动呈顺流。The inlet of the refrigerant heat exchange channel is connected to the No. 1 port of the No. 1 three-way valve, and the outlet of the refrigerant heat exchange channel is connected to the No. 2 port of the No. 4 three-way valve. In this connection mode, the refrigerant heat exchange channel The fluid flow in the heat exchange fluid channel is co-current with the air flow in the heat exchange fluid channel.

所述制冷剂换热通道的进口与四号三通阀的二号口连接,制冷剂换热通道的出口与一号三通阀一号口连接。此种连接方式下,制冷剂换热通道中的流体流动与换热流体通道中的空气流动呈逆流。The inlet of the refrigerant heat exchange channel is connected to the No. 2 port of the No. 4 three-way valve, and the outlet of the refrigerant heat exchange channel is connected to the No. 1 port of the No. 1 three-way valve. In this connection mode, the fluid flow in the refrigerant heat exchange channel and the air flow in the heat exchange fluid channel are countercurrent.

所述预冷换热器、主换热器和再热换热器的类型包括翅片管换热器,微通道换热器,板式换热器,管壳式换热器,降膜式换热器,套管式换热器。The types of the precooling heat exchanger, main heat exchanger and reheat heat exchanger include finned tube heat exchangers, microchannel heat exchangers, plate heat exchangers, shell and tube heat exchangers, falling film heat exchangers Heater, casing heat exchanger.

该换热单元有以下两种工作模式:The heat exchange unit has the following two working modes:

1.独立蒸发器模式:换热单元进口,预冷换热器、主换热器和再热换热器的制冷剂通道,换热单元出口通过连接管和三通阀顺序连接在一起,组成独立蒸发器。换热流体依次经过预冷换热器、主换热器和再热换热器。1. Independent evaporator mode: the inlet of the heat exchange unit, the refrigerant passages of the pre-cooling heat exchanger, the main heat exchanger and the reheat heat exchanger, and the outlet of the heat exchange unit are connected together sequentially through connecting pipes and three-way valves to form a Independent evaporator. The heat exchange fluid passes through the pre-cooling heat exchanger, the main heat exchanger and the reheat heat exchanger in sequence.

2.蒸发器加环路热管组合模式:主换热器单独作为蒸发器,其制冷剂通道通过连接管和三通阀与换热单元的进出口相连;预冷换热器、再热换热器和制冷剂泵通过连接管和三通阀直接相连组成环路热管,制冷剂在预冷换热器内蒸发进入再热换热器,在再热换热器中冷凝为液态,通过制冷剂泵将液态制冷剂再输送到预冷换热器。换热流体依次经过预冷换热器、主换热器和再热换热器。2. Combined mode of evaporator plus loop heat pipe: the main heat exchanger acts as an evaporator alone, and its refrigerant channel is connected to the inlet and outlet of the heat exchange unit through connecting pipes and three-way valves; pre-cooling heat exchanger, reheating heat exchange The refrigerant pump and the refrigerant pump are directly connected through a connecting pipe and a three-way valve to form a loop heat pipe. The refrigerant evaporates in the pre-cooling heat exchanger and enters the reheating heat exchanger. The pump re-delivers the liquid refrigerant to the pre-cooling heat exchanger. The heat exchange fluid passes through the pre-cooling heat exchanger, the main heat exchanger and the reheat heat exchanger in sequence.

与现有技术相比,本发明的有益效果体现在:Compared with the prior art, the beneficial effects of the present invention are reflected in:

通过制冷剂管路切换来实现独立蒸发器和蒸发器加环路热管两种模式的转换。其中,独立蒸发器模式的作用在于可以将所有换热面积都作为蒸发器,尽可能提高蒸发温度,提高循环效率;蒸发器加环路热管组合模式的作用在于在除湿再热的条件下,利用低蒸发温度增加凝水效率,通过环路热管组合实现蒸发器前后的预冷和再热,从而减少系统不必要的能量损失。The conversion between the independent evaporator mode and the evaporator plus loop heat pipe mode is realized by switching the refrigerant pipeline. Among them, the role of the independent evaporator mode is that all heat transfer areas can be used as evaporators to increase the evaporation temperature as much as possible and improve cycle efficiency; the role of the evaporator plus loop heat pipe combination mode is to use the The low evaporating temperature increases the condensation efficiency, and realizes precooling and reheating before and after the evaporator through the combination of loop heat pipes, thereby reducing unnecessary energy loss of the system.

附图说明Description of drawings

图1为实施例1的连接示意图;Fig. 1 is the connection schematic diagram of embodiment 1;

图2为实施例1中独立蒸发器模式的原理示意图;Fig. 2 is the schematic diagram of the principle of independent evaporator mode in embodiment 1;

图3为实施例1中蒸发器加环路热管组合模式的原理示意图;Fig. 3 is the schematic diagram of the principle of the combination mode of evaporator plus loop heat pipe in embodiment 1;

图4为实施例2的连接示意图。FIG. 4 is a schematic connection diagram of Embodiment 2.

其中,1为预冷换热器,11为预冷换热器的制冷剂通道的a端;12为预冷换热器的制冷剂通道的b端;2为主换热器,21为主换热器的制冷剂通道的a端,22为主换热器的制冷剂通道的b端,3为再热换热器,31为再热热器的制冷剂通道的a端,32为再热换热器的制冷剂通道的b端,4为一号三通阀,41为一号三通阀的一号口,42为一号三通阀的二号口,43为一号三通阀的三号口,5为二号三通阀,51为二号三通阀的一号口,52为二号三通阀的二号口,53为二号三通阀的三号口,6为三号三通阀,61为三号三通阀的一号口,62为三号三通阀的二号口,63为三号三通阀的三号口,7为四号三通阀,71为四号三通阀的一号口,72为四号三通阀的二号口,73为四号三通阀的三号口,8为换热流体通道,81为风机,9为制冷剂泵,101为制冷剂换热通道的进口,102为制冷剂换热通道的出口。Among them, 1 is the pre-cooling heat exchanger, 11 is the a end of the refrigerant passage of the pre-cooling heat exchanger; 12 is the b end of the refrigerant passage of the pre-cooling heat exchanger; 2 is the main heat exchanger, and 21 is the main End a of the refrigerant channel of the heat exchanger, 22 is the end b of the refrigerant channel of the main heat exchanger, 3 is the reheat heat exchanger, 31 is the a end of the refrigerant channel of the reheater, and 32 is the reheater The b end of the refrigerant channel of the heat exchanger, 4 is the No. 1 three-way valve, 41 is the No. 1 port of the No. 1 three-way valve, 42 is the No. 2 port of the No. 1 three-way valve, and 43 is the No. 1 three-way valve The No. 3 port of the valve, 5 is the No. 2 three-way valve, 51 is the No. 1 port of the No. 2 three-way valve, 52 is the No. 2 port of the No. 2 three-way valve, and 53 is the No. 3 port of the No. 2 three-way valve. 6 is No. 3 three-way valve, 61 is No. 1 port of No. 3 three-way valve, 62 is No. 2 port of No. 3 three-way valve, 63 is No. 3 port of No. 3 three-way valve, and 7 is No. 4 three-way valve Valve, 71 is the No. 1 port of the No. 4 three-way valve, 72 is the No. 2 port of the No. 4 three-way valve, 73 is the No. 3 port of the No. 4 three-way valve, 8 is the heat exchange fluid channel, 81 is the fan, 9 101 is the inlet of the refrigerant heat exchange channel, and 102 is the outlet of the refrigerant heat exchange channel.

具体实施方式detailed description

下面对本发明的实施例作详细说明,本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The following is a detailed description of the embodiments of the present invention. This embodiment is implemented on the premise of the technical solution of the present invention, and detailed implementation methods and specific operating procedures are provided, but the protection scope of the present invention is not limited to the following implementation example.

实施例1Example 1

一种蒸发器与环路热管可切换的换热单元,其结构如图1所示,包括主换热器2、预冷换热器1和再热换热器3,预冷换热器1、主换热器2和再热换热器3的换热流体通道8依次连接,预冷换热器1、主换热器2和再热换热器3的制冷剂换热通道形成独立蒸发器模式或蒸发器加环路热管组合模式,其中,预冷换热器1、主换热器2和再热换热器3的类型为翅片管换热器。A heat exchange unit with switchable evaporator and loop heat pipe, its structure is shown in Figure 1, including main heat exchanger 2, pre-cooling heat exchanger 1 and reheating heat exchanger 3, pre-cooling heat exchanger 1 , the heat exchange fluid passages 8 of the main heat exchanger 2 and the reheat heat exchanger 3 are connected in sequence, and the refrigerant heat exchange passages of the precooling heat exchanger 1, the main heat exchanger 2 and the reheat heat exchanger 3 form independent evaporation The heat exchanger mode or the combination mode of the evaporator and the loop heat pipe, wherein the type of the precooling heat exchanger 1, the main heat exchanger 2 and the reheating heat exchanger 3 are finned tube heat exchangers.

换热流体通道8的进口设置在预冷换热器1上,换热流体通道8的出口设置在再热换热器3上。换热流体通道8中流动的流体为空气,通过风机81将空气从换热流体通道8的进口输送至换热流体通道8的出口。The inlet of the heat exchange fluid passage 8 is arranged on the precooling heat exchanger 1 , and the outlet of the heat exchange fluid passage 8 is arranged on the reheat heat exchanger 3 . The fluid flowing in the heat exchange fluid channel 8 is air, and the fan 81 transports the air from the inlet of the heat exchange fluid channel 8 to the outlet of the heat exchange fluid channel 8 .

制冷剂换热通道连接顺序如下:制冷剂换热通道的进口101与一号三通阀的一号口41连接,制冷剂换热通道的出口102与四号三通阀的二号口72连接,此种连接方式下,制冷剂换热通道中的流体流动与换热流体通道8中的空气流动呈顺流。一号三通阀的三号口43与主换热器的制冷剂通道的a端21连接;一号三通阀的二号口42分别与预冷换热器的制冷剂通道的a端11及三号三通阀的三号口63连接;预冷换热器的制冷剂通道的b端12与二号三通阀的一号口51连接,二号三通阀的二号口52与主换热器的制冷剂通道的a端21连接,主换热器的制冷剂通道的b端22分别与三号三通阀的一号口61及四号三通阀的三号口73连接,三号三通阀的二号口62与再热换热器的制冷剂通道的a端31连接,再热换热器的制冷剂通道的b端32分别与二号三通阀的三号口53及四号三通阀7的一号进口连接。再热换热器的制冷剂通道的b端32与二号三通阀的三号口53的连接管路上设有制冷剂泵9。The connection sequence of the refrigerant heat exchange channels is as follows: the inlet 101 of the refrigerant heat exchange channel is connected to the No. 1 port 41 of the No. 1 three-way valve, and the outlet 102 of the refrigerant heat exchange channel is connected to the No. 2 port 72 of the No. 4 three-way valve. , in this connection mode, the fluid flow in the refrigerant heat exchange channel and the air flow in the heat exchange fluid channel 8 are co-current. The No. 3 port 43 of the No. 1 three-way valve is connected to the a-end 21 of the refrigerant passage of the main heat exchanger; the No. 2 port 42 of the No. 1 three-way valve is respectively connected to the a-end 11 of the refrigerant passage of the pre-cooling heat exchanger. and the No. 3 port 63 of the No. 3 three-way valve; the b-end 12 of the refrigerant channel of the precooling heat exchanger is connected with the No. 1 port 51 of the No. 2 three-way valve, and the No. 2 port 52 of the No. 2 three-way valve is connected with The a-end 21 of the refrigerant channel of the main heat exchanger is connected, and the b-end 22 of the refrigerant channel of the main heat exchanger is respectively connected with the No. 1 port 61 of the No. 3 three-way valve and the No. 3 port 73 of the No. 4 three-way valve , the No. 2 port 62 of the No. 3 three-way valve is connected to the a-end 31 of the refrigerant passage of the reheat heat exchanger, and the b-end 32 of the refrigerant passage of the reheat heat exchanger is respectively connected to the No. 3 port of the No. 2 three-way valve. Port 53 and No. 1 inlet of No. 4 three-way valve 7 are connected. A refrigerant pump 9 is provided on the connecting pipeline between the b-end 32 of the refrigerant channel of the reheat heat exchanger and the third port 53 of the second three-way valve.

本实施例的独立蒸发器模式原理如图2所示,其中,一号三通阀的三号口43、二号三通阀的三号口53、三号三通阀的三号口63及四号三通阀的三号口73关闭。此时,换热流体依次经过预冷换热器1、主换热器2和再热换热器3,换热面积大,可以尽可能提高蒸发温度,提高循环效率。The principle of the independent evaporator mode of this embodiment is shown in Figure 2, wherein the No. 3 port 43 of the No. 1 three-way valve, the No. 3 port 53 of the No. 2 three-way valve, the No. 3 port 63 of the No. 3 three-way valve and No. 3 port 73 of No. 4 three-way valve is closed. At this time, the heat exchange fluid passes through the pre-cooling heat exchanger 1, the main heat exchanger 2 and the reheat heat exchanger 3 in sequence, and the heat exchange area is large, which can increase the evaporation temperature as much as possible and improve the cycle efficiency.

本实施例的蒸发器加环路热管组合模式原理如图3所示,一号三通阀的二号口42、二号三通阀的二号口52、三号三通阀的一号口61及四号三通阀的一号口71关闭。一号三通阀4使制冷剂换热通道的进口101只与主换热器的制冷剂通道的a端21相连,二号三通阀5使预冷换热器的制冷剂通道的b端12通过制冷剂泵9只与再热换热器的制冷剂通道的b端32连通,三号三通阀6使再热换热器的制冷剂通道的a端31只与预冷换热器的制冷剂通道的a端11连通,四号三通阀7使制冷剂换热通道的出口102只与主换热器的制冷剂通道的b端22连通。制冷剂从冷剂换热通道的进口101进入换热单元,经过一号三通阀4后直接进入主换热器10,然后经过四号三通阀7直接从制冷剂换热通道的出口102流出该换热单元。此时,主换热器单独作为系统的蒸发器使用。与此同时,预冷换热器1和再热换热器3通过连接管和二号三通阀5和三号三通阀6直接相连组成环路热管。预冷换热器1作为环路热管的蒸发端,再热换热器3作为环路热管的冷凝端,液态的换热流体在预冷换热器1吸热变为气态,在热扩散的动力下进入再热换热器3,冷凝释放出热量,液态的换热流体再经制冷剂泵9输送回预冷换热器1,完成环路热管的循环。此时,换热流体先经过预冷换热器1,实现蒸发器前的预冷,再经过主换热器2,实现进一步的降温除湿,最后经过再热换热器3实现再热,从而减少系统不必要的能量损失。The principle of the evaporator plus loop heat pipe combination mode of this embodiment is shown in Figure 3, No. 2 port 42 of No. 1 three-way valve, No. 2 port 52 of No. 2 three-way valve, and No. 1 port of No. 3 three-way valve No. 1 port 71 of No. 61 and No. four three-way valves is closed. The No. 1 three-way valve 4 connects the inlet 101 of the refrigerant heat exchange channel to the a-end 21 of the refrigerant channel of the main heat exchanger, and the No. 2 three-way valve 5 makes the b-end of the refrigerant channel of the pre-cooling heat exchanger 12 Through the refrigerant pump 9, only the b end 32 of the refrigerant passage of the reheat heat exchanger is connected, and the No. 3 three-way valve 6 makes the a end 31 of the refrigerant passage of the reheat heat exchanger only connected with the precooling heat exchanger The a-end 11 of the refrigerant passage of the main heat exchanger communicates with the a-end 11 of the refrigerant passage, and the No. 4 three-way valve 7 makes the outlet 102 of the refrigerant heat exchange passage only communicate with the b-end 22 of the refrigerant passage of the main heat exchanger. The refrigerant enters the heat exchange unit from the inlet 101 of the refrigerant heat exchange channel, directly enters the main heat exchanger 10 after passing through the No. 1 three-way valve 4, and then directly flows from the outlet 102 of the refrigerant heat exchange channel through the No. flow out of the heat exchange unit. At this time, the main heat exchanger is used alone as the evaporator of the system. At the same time, the precooling heat exchanger 1 and the reheating heat exchanger 3 are directly connected to the second three-way valve 5 and the third three-way valve 6 through connecting pipes to form a loop heat pipe. The precooling heat exchanger 1 is used as the evaporation end of the loop heat pipe, and the reheat heat exchanger 3 is used as the condensation end of the loop heat pipe. The liquid heat exchange fluid absorbs heat in the precooling heat exchanger 1 and becomes a gaseous state. Under power, it enters the reheating heat exchanger 3, condenses and releases heat, and the liquid heat exchange fluid is transported back to the precooling heat exchanger 1 through the refrigerant pump 9 to complete the circulation of the loop heat pipe. At this time, the heat exchange fluid first passes through the precooling heat exchanger 1 to realize precooling before the evaporator, then passes through the main heat exchanger 2 to realize further cooling and dehumidification, and finally passes through the reheating heat exchanger 3 to realize reheating, thereby Reduce unnecessary energy loss of the system.

实施例2Example 2

才用于实施例1相同的连接方式,不同点在于:制冷剂换热通道的进口101与四号三通阀的二号口72连接,制冷剂换热通道的出口102与一号三通阀的一号口连接,具体如图4所示。The same connection method is used in Example 1, the difference is: the inlet 101 of the refrigerant heat exchange channel is connected to the second port 72 of the No. 4 three-way valve, and the outlet 102 of the refrigerant heat exchange channel is connected to the No. 1 three-way valve. 1 port connection, as shown in Figure 4.

与实施例1相比,仅预冷换热器1,主换热器2,再热换热器3的制冷剂通道连接顺序发生了变化,功能不变。Compared with Example 1, only the connection sequence of the refrigerant channels of the precooling heat exchanger 1, the main heat exchanger 2, and the reheating heat exchanger 3 has changed, and the functions remain unchanged.

Claims (10)

1. a kind of evaporator and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that the heat exchange unit include main heat exchanger, Precool heat exchanger device and again heat exchanger, the precool heat exchanger device, main heat exchanger and the heat transfer fluid channels of heat exchanger are successively again Series connection, the precool heat exchanger device, main heat exchanger and again the refrigerant heat exchanger passage of heat exchanger by connecting refrigerant lines UNICOM, And switch to form independent evaporator mode or evaporator adds loop circuit heat pipe integrated mode by refrigerant line.
2. a kind of evaporator according to claim 1 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that described The imports of heat transfer fluid channels be arranged on precool heat exchanger device, the outlet of heat transfer fluid channels is arranged on again on heat exchanger.
3. a kind of evaporator according to claim 1 or 2 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that The fluid flowed in described heat transfer fluid channels is air, is delivered to air from the import of heat transfer fluid channels by blower fan The outlet of heat transfer fluid channels.
4. a kind of evaporator according to claim 2 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that described The refrigerant heat exchanger passage order of connection is as follows:The a ends of No. three mouths of No.1 triple valve and the coolant channel of main heat exchanger connect; No. three mouths of No. two mouths of No.1 triple valve respectively with a ends of the coolant channel of precool heat exchanger device and No. three triple valves are connected; The b ends of the coolant channel of precool heat exchanger device are connected with the No.1 mouth of No. two triple valves, No. two mouths of No. two triple valves with The a ends connection of the coolant channel of main heat exchanger, the b ends of the coolant channel of the main heat exchanger respectively with No. three triple valves No. three mouths of No.1 mouth and No. four triple valves connect, the coolant channel of No. two mouths of No. three triple valves and heat exchanger again The connection of a ends, the b ends of the coolant channel of the heat exchanger again No. three mouths and No. four triple valves with No. two triple valves respectively No.1 import connection.
5. a kind of evaporator according to claim 4 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that described The b ends of the coolant channel of heat exchanger and the connecting line of No. three mouths of No. two triple valves are provided with refrigerated medium pump again.
6. a kind of evaporator according to claim 5 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that independent Under evaporator mode, No. three mouths of the No.1 triple valve, No. three mouths of No. two triple valves, No. three mouths and four of No. three triple valves No. three mouths of number triple valve are closed.
7. a kind of evaporator according to claim 5 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that evaporation Device adds under loop circuit heat pipe integrated mode, No. two mouths of the No.1 triple valve, No. two mouths of No. two triple valves, No. three triple valves The No.1 mouth of No.1 mouth and No. four triple valves is closed.
8. a kind of evaporator according to claim 4 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that described The import of refrigerant heat exchanger passage is connected with No.1 triple valve No.1 mouth, outlet and No. four triple valves of refrigerant heat exchanger passage No. two mouth connections.
9. a kind of evaporator according to claim 4 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that described The import of refrigerant heat exchanger passage is connected with No. two mouths of No. four triple valves, outlet and the No.1 triple valve of refrigerant heat exchanger passage No.1 mouth connects.
10. a kind of evaporator according to claim 1 and the changeable heat exchange unit of loop circuit heat pipe, it is characterised in that institute State precool heat exchanger device, main heat exchanger and the type of heat exchanger includes finned tube exchanger, micro-channel heat exchanger, plate-type heat-exchange again Device, shell-and-tube heat exchanger, falling-film heat exchanger or double pipe heat exchanger.
CN201710437653.XA 2017-06-12 2017-06-12 A heat exchange unit with switchable evaporator and loop heat pipe Expired - Fee Related CN107356016B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710437653.XA CN107356016B (en) 2017-06-12 2017-06-12 A heat exchange unit with switchable evaporator and loop heat pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710437653.XA CN107356016B (en) 2017-06-12 2017-06-12 A heat exchange unit with switchable evaporator and loop heat pipe

Publications (2)

Publication Number Publication Date
CN107356016A true CN107356016A (en) 2017-11-17
CN107356016B CN107356016B (en) 2020-06-26

Family

ID=60272644

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710437653.XA Expired - Fee Related CN107356016B (en) 2017-06-12 2017-06-12 A heat exchange unit with switchable evaporator and loop heat pipe

Country Status (1)

Country Link
CN (1) CN107356016B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109990262A (en) * 2018-03-09 2019-07-09 青岛金玉大商贸有限公司 A kind of auxiliary heating steam generator
CN111637618A (en) * 2019-03-01 2020-09-08 米泰克控股公司 Heat exchanger
CN112902708A (en) * 2021-02-08 2021-06-04 南京慧和建筑技术有限公司 Multi-stage temperature control method for humidifying water and humidifying method

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4307372A1 (en) * 1993-03-09 1994-09-15 Licentia Gmbh Programme-controlled laundry drier with heat-pump circuit
US6209223B1 (en) * 1998-12-08 2001-04-03 Advanced Dryer Systems, Inc. Grain drying system with high efficiency dehumidifier and modular drying bin
KR20110024698A (en) * 2009-09-03 2011-03-09 위니아만도 주식회사 Heat pump dryer and heat pump dryer control method
CN102803882A (en) * 2009-06-04 2012-11-28 松下电器产业株式会社 Drying device
EP2468948B1 (en) * 2010-12-21 2013-11-27 Panasonic Corporation Dehumidifying and heating apparatus and clothes drying machine using the same
CN203687197U (en) * 2013-12-27 2014-07-02 湖南大学 Energy-storage fluorine pump heat pipe system
CN104266277A (en) * 2014-10-21 2015-01-07 东南大学 Heat pipe heat recovery all fresh air dehumidification air-conditioning device
CN104776739A (en) * 2014-01-13 2015-07-15 杭州三花研究院有限公司 Heat pipe heat exchanger, evaporator component and heat pump clothes dryer
CN105423457A (en) * 2015-12-18 2016-03-23 珠海格力电器股份有限公司 Air conditioning system
CN105716410A (en) * 2016-03-23 2016-06-29 青岛大学 Haw flake and caked sugar heat pump dryer and drying system
CN106440748A (en) * 2016-10-14 2017-02-22 安徽美乐柯制冷空调设备有限公司 Heat pump type drying device

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4307372A1 (en) * 1993-03-09 1994-09-15 Licentia Gmbh Programme-controlled laundry drier with heat-pump circuit
US6209223B1 (en) * 1998-12-08 2001-04-03 Advanced Dryer Systems, Inc. Grain drying system with high efficiency dehumidifier and modular drying bin
CN102803882A (en) * 2009-06-04 2012-11-28 松下电器产业株式会社 Drying device
KR20110024698A (en) * 2009-09-03 2011-03-09 위니아만도 주식회사 Heat pump dryer and heat pump dryer control method
EP2468948B1 (en) * 2010-12-21 2013-11-27 Panasonic Corporation Dehumidifying and heating apparatus and clothes drying machine using the same
CN203687197U (en) * 2013-12-27 2014-07-02 湖南大学 Energy-storage fluorine pump heat pipe system
CN104776739A (en) * 2014-01-13 2015-07-15 杭州三花研究院有限公司 Heat pipe heat exchanger, evaporator component and heat pump clothes dryer
CN104266277A (en) * 2014-10-21 2015-01-07 东南大学 Heat pipe heat recovery all fresh air dehumidification air-conditioning device
CN105423457A (en) * 2015-12-18 2016-03-23 珠海格力电器股份有限公司 Air conditioning system
CN105716410A (en) * 2016-03-23 2016-06-29 青岛大学 Haw flake and caked sugar heat pump dryer and drying system
CN106440748A (en) * 2016-10-14 2017-02-22 安徽美乐柯制冷空调设备有限公司 Heat pump type drying device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109990262A (en) * 2018-03-09 2019-07-09 青岛金玉大商贸有限公司 A kind of auxiliary heating steam generator
CN110006019A (en) * 2018-03-09 2019-07-12 青岛金玉大商贸有限公司 A kind of hanging structure steam generator
CN111637618A (en) * 2019-03-01 2020-09-08 米泰克控股公司 Heat exchanger
CN112902708A (en) * 2021-02-08 2021-06-04 南京慧和建筑技术有限公司 Multi-stage temperature control method for humidifying water and humidifying method

Also Published As

Publication number Publication date
CN107356016B (en) 2020-06-26

Similar Documents

Publication Publication Date Title
CN101701737B (en) Heat-pump-driven solution dehumidifying air-conditioning device
CN102032705B (en) Two-stage compression heat pump system
CN101846367A (en) Internally-cooled solution dehumidifying fresh air handling unit driven by heat pump
CN106403116A (en) Integrated natural cooling machine room air conditioning system
KR101138970B1 (en) Defrosting system using air cooling refrigerant evaporator and condenser
CN105135729B (en) Vapor compression refrigeration/heat pump of single refrigerant loop, more pressures at expulsion
CN102901261A (en) Two-stage multi-unit single-throttling incomplete-intercooling refrigeration system
CN107356016B (en) A heat exchange unit with switchable evaporator and loop heat pipe
CN104214854A (en) Integrated machine room air conditioning system
CN112050618A (en) Three-effect heat recovery type mixed air heat pump drying system and its application
CN105627470A (en) Air conditioning unit based on supercooling and reheating
CN100458292C (en) Refrigerating unit of air condition by dehumidifying, evaporative cooling solution
CN202993640U (en) Two-stage multi-connection double-throttling incomplete inter-cooling refrigerating system
CN205690729U (en) Variable-flow either simplex matter heat exchangers in parallel overlapping heat pump
CN108613383A (en) A kind of sludge drying heat pump system
CN103743149A (en) Heat pump air conditioning system with one-way valves controlling flow direction of refrigerant in heat regenerator
CN110595106A (en) A heat pump system
CN106352586A (en) Double machine head heat source tower heat pump unit
CN110455070A (en) A multi-working condition heat pump dryer system and its control method
CN110345572A (en) Dehumidification system and air conditioning system
CN206222578U (en) Integrated natural cooling machine room air conditioning system
CN109869942B (en) A flat tube casing type heat recovery type heat pump air conditioning system and its working method
CN210718200U (en) a heat pump system
CN104457010B (en) A kind of double circulation power heat pipe formula central air-conditioning energy-saving system
CN102901278B (en) Two-stage multi-connected primary throttling intermediate complete cooling refrigeration system

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
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200626