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CN201032440Y - Snake structure separated heat pipe heat exchange system - Google Patents

Snake structure separated heat pipe heat exchange system Download PDF

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Publication number
CN201032440Y
CN201032440Y CNU2007200365716U CN200720036571U CN201032440Y CN 201032440 Y CN201032440 Y CN 201032440Y CN U2007200365716 U CNU2007200365716 U CN U2007200365716U CN 200720036571 U CN200720036571 U CN 200720036571U CN 201032440 Y CN201032440 Y CN 201032440Y
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evaporating
condensation
condensing
heat pipe
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李菊香
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Nanjing Tech University
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Nanjing Tech University
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
    • F28D15/0266Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers

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

Abstract

一种蒸发段和冷凝段分离式蛇形热管换热系统,属于热管换热技术领域,它包括蒸发段(11)和冷凝段(12),热管工质在蒸发段(11)的输出口处通过热管工质上升管路(1)与冷凝段(12)的输入口相连,热管工质在冷凝段(12)的输出口处通过热管工质下降管路(10)与蒸发段(11)的输入口相连,其特征是所述的蒸发段(11)由蒸发段壳体(2)、蒸发管(3)、蒸发段弯管(13)、蒸发段孔板(4)以及蒸发段端盖(5)组成,所述的冷凝段(12)由冷凝段壳体(6)、冷凝管(7)、冷凝段弯管(14)、冷凝段孔板(8)以及冷凝段端盖(9)组成。它解决了现有的分离式热管换热系统存在的体积大、维修不便的问题,具有结构简单,制造安装维护方便,体积小、成本低的优点。

Figure 200720036571

A serpentine heat pipe heat exchange system with separate evaporating section and condensing section, which belongs to the technical field of heat pipe heat exchange, and includes an evaporating section (11) and a condensing section (12), and the working medium of the heat pipe is at the output port of the evaporating section (11) The heat pipe working fluid ascending pipeline (1) is connected to the input port of the condensation section (12), and the heat pipe working fluid passes through the heat pipe working medium descending pipeline (10) and the evaporation section (11) at the output port of the condensation section (12). It is characterized in that the evaporating section (11) is composed of evaporating section shell (2), evaporating pipe (3), evaporating section elbow (13), evaporating section orifice plate (4) and evaporating section end cover (5), and the condensation section (12) is composed of the condensation section housing (6), the condensation pipe (7), the condensation section elbow (14), the condensation section orifice (8) and the condensation section end cover ( 9) Composition. It solves the problems of large volume and inconvenient maintenance existing in the existing separated heat pipe heat exchange system, and has the advantages of simple structure, convenient manufacture, installation and maintenance, small volume and low cost.

Figure 200720036571

Description

蛇形结构分离式热管换热系统 Snake structure separated heat pipe heat exchange system

技术领域 technical field

本实用新型涉及一种换热装置,尤其是一种采用分离式热管技术对热流体冷却加热冷流体以进行换热的系统,具体地说是一种蒸发段和冷凝段均为蛇形结构的分离式热管换热系统。The utility model relates to a heat exchanging device, in particular to a system for cooling and heating a hot fluid and heating a cold fluid for heat exchange by adopting a separated heat pipe technology, in particular to a system in which both the evaporating section and the condensing section are serpentine structures Separate heat pipe heat exchange system.

背景技术 Background technique

目前,分离式热管的管束结构是,通过上、下联箱将传热管焊接连接成管束结构,在上、下联箱上分别有伸出壳体外的短管,短管分别和热管工质的上升管路和下降管路连接,如图1所示。上、下联箱和传热管间的焊接接头型式为角焊缝。角焊缝的焊接质量不易得到保证,而且所有的焊缝都位于流体通道内,容易被磨损、腐蚀,造成泄漏。管束的固定不易控制。上、下联箱的直径比传热管大,增加了设备的重量。At present, the tube bundle structure of the separated heat pipe is that the heat transfer tubes are welded and connected into a tube bundle structure through the upper and lower headers. Pipeline and downpipe connection, as shown in Figure 1. The welded joints between the upper and lower headers and heat transfer tubes are fillet welds. The welding quality of the fillet welds is not easy to guarantee, and all the welds are located in the fluid passages, which are easy to be worn, corroded, and cause leakage. The fixation of the tube bundle is not easy to control. The diameter of the upper and lower headers is larger than that of the heat transfer tubes, which increases the weight of the equipment.

发明内容 Contents of the invention

本实用新型的目的是针对现有的分离式热管换热系统存在的体积大、使用寿命短、维修不便等问题,提供一种结构简单、体积小、维护方便的蒸发段和冷凝段均为蛇形结构的分离式热管换热系统。The purpose of this utility model is to provide a simple structure, small volume, easy maintenance, the evaporating section and the condensing section are snake A separate heat pipe heat exchange system with shaped structure.

本实用新型的技术方案是:The technical scheme of the utility model is:

一种蒸发段和冷凝段均为蛇形结构的分离式热管换热系统,包括蒸发段11和冷凝段12,热管工质在蒸发段11的输出口处通过热管工质上升管路1与冷凝段12的输入口相连,热管工质在冷凝段12的输出口处通过热管工质下降管路10与蒸发段11的输入口相连,其特征是所述的蒸发段11由蒸发段壳体2、蒸发管3、蒸发段弯管13、蒸发段孔板4以及蒸发段端盖5组成,每支蒸发管3都顺着管内热管工质的流动方向有一微小角度的向上倾斜,蒸发管3之间设有热流体通道,它的两端支承在蒸发段孔板4,蒸发段孔板4分别安装在蒸发段壳体2的两端,蒸发段端盖5安装在所述蒸发段壳体2的两端且位于蒸发段孔板4外侧,所述的蒸发段弯管13位于蒸发段端盖5与蒸发段孔板4之间,它的两端分别与相邻蒸发管3的对应端相连并使蒸发管3所有或部分地首尾相连成蛇形结构布置在蒸发段壳体2中;所述的冷凝段12由冷凝段壳体6、冷凝管7、冷凝段弯管14、冷凝段孔板8以及冷凝段端盖9组成,每支冷凝管7都顺着管内热管工质的流动方向有一微小角度的向下倾斜,冷凝管7之间设有冷流体通道,它的两端支承在冷凝段孔板8,冷凝段孔板8分别安装在冷凝段壳体6的两端,冷凝段端盖9安装在所述冷凝段壳体6的两端且位于冷凝段孔板8外侧,所述的冷凝段弯管14位于冷凝段端盖9与冷凝段孔板8之间,它的两端分别与相邻冷凝管7的对应端相连并使冷凝管7所有或部分地首尾相连成蛇形结构布置在冷凝段壳体6中。A separate heat pipe heat exchange system in which both the evaporating section and the condensing section are serpentine structures, including an evaporating section 11 and a condensing section 12, and the heat pipe working fluid passes through the heat pipe working fluid ascending pipeline 1 at the output port of the evaporating section 11 and condenses The input port of the section 12 is connected, and the heat pipe working medium is connected to the input port of the evaporating section 11 through the heat pipe working fluid descending pipeline 10 at the output port of the condensing section 12, and the feature is that the evaporating section 11 is composed of the evaporating section shell , evaporating tube 3, evaporating section elbow 13, evaporating section orifice 4 and evaporating section end cover 5, each evaporating tube 3 is inclined upwards at a slight angle along the flow direction of the heat pipe working medium in the tube, the evaporating tube 3 There is a hot fluid channel between them, and its two ends are supported on the evaporation section orifice plate 4, the evaporation section orifice plate 4 is respectively installed on the two ends of the evaporation section shell 2, and the evaporation section end cover 5 is installed on the evaporation section shell 2 The two ends of the evaporation section are located outside the orifice 4 of the evaporation section. The elbow 13 of the evaporation section is located between the end cover 5 of the evaporation section and the orifice 4 of the evaporation section. Its two ends are respectively connected to the corresponding ends of the adjacent evaporation tubes 3. And all or part of the evaporating tubes 3 are connected end to end to form a serpentine structure and arranged in the evaporating section shell 2; The plate 8 and the end cover 9 of the condensing section are composed. Each condensing tube 7 is inclined downward at a slight angle along the flow direction of the heat pipe working medium in the tube. There is a cold fluid channel between the condensing tubes 7, and its two ends are supported on Condensing section orifice 8, condensing section orifice 8 is respectively installed on the two ends of condensing section shell 6, and condensing section end cover 9 is installed on the two ends of described condensing section shell 6 and is positioned at the outside of condensing section orifice 8, so The condensing section elbow 14 is located between the condensing section end cover 9 and the condensing section orifice 8, and its two ends are respectively connected to the corresponding ends of the adjacent condensing pipes 7 so that all or part of the condensing pipes 7 are connected end to end to form a snake. The shape structure is arranged in the shell 6 of the condensation section.

所述的蒸发段端盖5与蒸发段壳体2间视热流体物理特性为可拆卸式连接结构或焊接连接结构;所述的冷凝段端盖9与冷凝段壳体6间也视冷流体物理特性为可拆卸式连接结构或焊接连接结构。The connection between the end cover 5 of the evaporating section and the shell 2 of the evaporating section is a detachable connection structure or a welded connection structure depending on the physical properties of the hot fluid; The physical characteristic is a detachable connection structure or a welded connection structure.

所述的蒸发段弯管13与蒸发管3之间为焊接连接结构,且焊接点位于蒸发段孔板4和蒸发段端盖5间的空间;所述的冷凝段弯管14与冷凝管7之间也为焊接连接结构,且焊接点位于冷凝段孔板8和冷凝段端盖9间的空间。The elbow 13 of the evaporating section and the evaporating pipe 3 are welded connection structures, and the welding point is located in the space between the orifice 4 of the evaporating section and the end cover 5 of the evaporating section; the elbow 14 of the condensing section and the condensing pipe 7 There is also a welding connection structure between them, and the welding point is located in the space between the orifice plate 8 of the condensation section and the end cover 9 of the condensation section.

本实用新型具有以下优点:The utility model has the following advantages:

1、本实用新型的分离式热管蒸发段和冷凝段管束通过采用蛇形管结构,省去了过程体积大、安装维修不便的上、下联箱结构,不仅使得整体结构简单,而且可以大大降低制造成本。1. The tube bundle of the separated heat pipe evaporating section and condensing section of the utility model adopts a serpentine tube structure, which saves the upper and lower header structures with large process volume and inconvenient installation and maintenance, which not only makes the overall structure simple, but also greatly reduces the manufacturing cost. cost.

2、对热、冷流体进行降温或升温时蒸发段和冷凝段的壳体内分别含有两块孔板,对蛇形管束起到了很好的支撑和固定作用。当冷流体侧为液体蒸发时,冷流体通道就是汽包。2. When the hot and cold fluids are cooled or heated up, the shells of the evaporation section and the condensation section contain two orifice plates respectively, which play a good role in supporting and fixing the serpentine tube bundle. When the liquid evaporates on the cold fluid side, the cold fluid channel is the steam drum.

3、蛇形管束的管与管之间用180°的弯头与其对接焊,焊缝位于流体通道之外,对接焊缝的质量相比于角焊缝更容易检验,焊缝数目比原结构减少,可靠性得到了提高。3. The pipes of the serpentine tube bundle are butt welded with 180° elbows. The welds are located outside the fluid passage. The quality of the butt welds is easier to inspect than the fillet welds, and the number of welds is more than that of the original structure. reduced and improved reliability.

4、壳体两侧为可拆卸的端盖时,可随时对传热管和弯管之间连接处的焊缝质量进行检查。4. When there are detachable end covers on both sides of the shell, the quality of the weld seam at the joint between the heat transfer tube and the elbow can be checked at any time.

5、冷热流体为气体时,传热管管外可扩展翅片等传热面以进一步提高换热效率。5. When the hot and cold fluid is gas, the heat transfer surface such as fins can be expanded outside the heat transfer tube to further improve the heat transfer efficiency.

附图说明 Description of drawings

图1是现有结构的分离式热管换热系统的结构示意图。Fig. 1 is a structural schematic diagram of a separated heat pipe heat exchange system in an existing structure.

图2是本实用新型的结构示意图。Fig. 2 is a schematic structural view of the utility model.

图中:RLT表示热流体,LLT表示冷流体,101为现有的热管工质上升管路,102为现有的蒸发段管束上联箱,103为现有的蒸发段管束,104为现有的蒸发段壳体,105现有的蒸发段管束下联箱,106为现有的冷凝段管束上联箱,107为现有的冷凝段管束,108为现有的冷凝段壳体。109为现有的冷凝段管束下联箱,110为现有的热管工质下降管路。In the figure: RLT means hot fluid, LLT means cold fluid, 101 is the existing heat pipe working fluid ascending pipeline, 102 is the upper header of the existing evaporating section tube bundle, 103 is the existing evaporating section tube bundle, 104 is the existing 105 is the lower header of the tube bundle of the evaporating section, 106 is the upper header of the tube bundle of the condensing section, 107 is the tube bundle of the existing condensing section, and 108 is the shell of the existing condensing section. 109 is the lower header of the tube bundle in the existing condensing section, and 110 is the descending pipeline of the existing heat pipe working medium.

具体实施方式 Detailed ways

下面结构附图和实施例对本实用新型作进一步的说明。The following structural drawings and embodiments further illustrate the utility model.

如图2所示。as shown in picture 2.

一种蒸发段和冷凝段均为蛇形结构的分离式热管换热系统,包括蒸发段11和冷凝段12,热管工质在蒸发段11的输出口处通过热管工质上升管路1与冷凝段12的输入口相连,热管工质在冷凝段12的输出口处通过热管工质下降管路10与蒸发段11的输入口相连,其特征是所述的蒸发段11由蒸发段壳体2、蒸发管3、蒸发段弯管13、蒸发段孔板4以及蒸发段端盖5组成,每支蒸发管3都顺着管内热管工质的流动方向有一微小角度(范围可在0.1-20度之间选取)的向上倾斜,蒸发管3之间设有热流体通道,它的两端支承在蒸发段孔板4,蒸发段孔板4分别安装在蒸发段壳体2的两端,蒸发段端盖5安装在所述蒸发段壳体2的两端且位于蒸发段孔板4外侧,所述的蒸发段弯管13位于蒸发段端盖5与蒸发段孔板4之间,它的两端分别与相邻蒸发管3的对应端相连并使蒸发管3所有或部分地首尾相连成蛇形结构布置在蒸发段壳体2中;所述的冷凝段12由冷凝段壳体6、冷凝管7、冷凝段弯管14、冷凝段孔板8以及冷凝段端盖9组成,每支冷凝管7都顺着管内热管工质的流动方向有一微小角度的向下倾斜,冷凝管7之间设有热流体通道,它的两端支承在冷凝段孔板8,冷凝段孔板8分别安装在冷凝段壳体6的两端,冷凝段端盖9安装在所述冷凝段壳体6的两端且位于冷凝段孔板8外侧,所述的冷凝段弯管14位于冷凝段端盖9与冷凝段孔板8之间,它的两端分别与相邻冷凝管7的对应端相连并使所有冷凝管7首尾相连成蛇形结构布置在冷凝段壳体6中。A separate heat pipe heat exchange system in which both the evaporating section and the condensing section are serpentine structures, including an evaporating section 11 and a condensing section 12, and the heat pipe working fluid passes through the heat pipe working fluid ascending pipeline 1 at the output port of the evaporating section 11 and condenses The input port of the section 12 is connected, and the heat pipe working medium is connected to the input port of the evaporating section 11 through the heat pipe working fluid descending pipeline 10 at the output port of the condensing section 12, and the feature is that the evaporating section 11 is composed of the evaporating section shell , evaporating tube 3, evaporating section elbow 13, evaporating section orifice 4 and evaporating section end cover 5, each evaporating tube 3 has a slight angle along the flow direction of the heat pipe working fluid in the tube (the range can be 0.1-20 degrees (choose between) is inclined upward, and a hot fluid channel is provided between the evaporation tubes 3, and its two ends are supported on the orifice plate 4 of the evaporation section. The end cover 5 is installed on both ends of the evaporation section shell 2 and is located outside the evaporation section orifice 4, and the evaporation section elbow 13 is located between the evaporation section end cover 5 and the evaporation section orifice 4, and its two The ends are respectively connected with the corresponding ends of the adjacent evaporating tubes 3 and all or part of the evaporating tubes 3 are connected end-to-end to form a serpentine structure and arranged in the evaporating section shell 2; the condensing section 12 consists of the condensing section shell 6, the condensing section Tube 7, condensing section elbow 14, condensing section orifice 8 and condensing section end cover 9, each condensing tube 7 has a slight downward slope along the flow direction of the heat pipe working medium in the tube, and the gap between the condensing tubes 7 A thermal fluid channel is provided, and its two ends are supported on the orifice plate 8 of the condensing section, the orifice plate 8 of the condensing section is respectively installed on the two ends of the shell 6 of the condensing section, and the end cover 9 of the condensing section is installed on the side of the shell 6 of the condensing section The two ends are located outside the orifice 8 of the condensation section, and the elbow 14 of the condensation section is located between the end cover 9 of the condensation section and the orifice 8 of the condensation section, and its two ends are respectively connected to the corresponding ends of the adjacent condensation pipe 7 and All the condensation pipes 7 are connected end to end to form a serpentine structure and arranged in the casing 6 of the condensation section.

其中的蒸发段弯管13采用首尾相连的形式将蒸发管3所有或部分地连接成一段或多段的蛇形(或“S”形)结构,整个蒸发段中每小段的第一支的蒸发管3的进口端作为蒸发段11中该小段的工质输入端穿过蒸发段孔板4和蒸发段端盖5后与热管工质下降管路10相连,每小段的最后一支蒸发管3的出口端作为蒸发段11中该小段的输出口穿过蒸发段孔板4和蒸发段端盖5后与热管工质上升管路1相连,每小段中其它蒸发管3的出口与进口均由蒸发段弯管13相连;同样地冷凝段弯管14采用首尾相连的形式将冷凝管7所有或部分地连接成一段或多段的蛇形(或“S”形)结构,整个冷凝段中每小段的第一支冷凝管7的进口端作为冷凝段12中该小段的工质输入端穿过冷凝段孔板8和冷凝段端盖9后与热管工质上升管路1相连,每小段的最后一支冷凝管7的出口端作为冷凝段12中该小段的输出口穿过冷凝段孔板8和冷凝段端盖9后与热管工质下降管路10相连,每小段中其它冷凝管7的出口与进口均由冷凝段弯管14相连。The evaporating section elbow 13 is connected end to end to connect all or part of the evaporating tubes 3 into one or more sections of serpentine (or "S" shape) structure, and the first evaporating tube of each small section in the entire evaporating section The inlet end of 3 is used as the working medium input end of the small section in the evaporating section 11, passes through the orifice plate 4 of the evaporating section and the end cover 5 of the evaporating section, and then connects with the working fluid descending pipeline 10 of the heat pipe, and the last evaporating tube 3 of each small section The outlet end is used as the output port of this small section in the evaporation section 11, and after passing through the orifice plate 4 of the evaporation section and the end cover 5 of the evaporation section, it is connected with the heat pipe working medium ascending pipeline 1, and the outlets and inlets of other evaporation tubes 3 in each small section are all controlled by the evaporation section. The section elbow 13 is connected; the same condensing section elbow 14 adopts the form of end-to-end connection to connect all or part of the condensing pipe 7 into one or more sections of serpentine (or "S" shape) structure, and each small section in the whole condensing section The inlet end of the first condensing pipe 7 passes through the orifice plate 8 of the condensing section and the end cover 9 of the condensing section as the working fluid input end of the subsection in the condensing section 12, and is connected with the heat pipe working fluid rising pipeline 1, and the last section of each subsection The outlet end of branch condensing pipe 7 is used as the output port of this small section in condensing section 12, passes through condensing section orifice 8 and condensing section end cover 9, and is connected with heat pipe working fluid descending pipeline 10, and the outlets of other condensing pipes 7 in each small section Both are connected with the inlet by the condensing section elbow 14.

具体实施时蒸发段端盖5与蒸发段壳体2间视热流体物理特性为可拆卸式连接结构或焊接结构;所述的冷凝段端盖9与冷凝段壳体6也视冷流体物理特性为可拆卸式连接结构或焊接结构。可拆卸式连接结构便于拆开维护。During specific implementation, the physical properties of the thermal fluid between the evaporation section end cover 5 and the evaporation section shell 2 are detachable connection structures or welded structures; It is a detachable connection structure or a welded structure. The detachable connection structure is convenient for disassembly and maintenance.

所述的蒸发段弯管13与蒸发管3之间为焊接连接结构,且焊接点位于蒸发段孔板4和蒸发段端盖5间的空间;所述的冷凝段弯管14与冷凝管7之间也为焊接连接结构,且焊接点位于冷凝段孔板8和冷凝段端盖9间的空间,焊接点不与冷热介质相接触,可大大延长焊接点和整台设备的寿命,提高防腐性能,同时也便于检查和维修。The elbow 13 of the evaporating section and the evaporating pipe 3 are welded connection structures, and the welding point is located in the space between the orifice 4 of the evaporating section and the end cover 5 of the evaporating section; the elbow 14 of the condensing section and the condensing pipe 7 There is also a welding connection structure between them, and the welding point is located in the space between the orifice plate 8 of the condensation section and the end cover 9 of the condensation section. Anti-corrosion performance, but also convenient for inspection and maintenance.

本实用新型未涉及部分均与现有技术相同,或可采用现有技术加以实现。The parts not involved in the utility model are all the same as the prior art, or can be realized by adopting the prior art.

Claims (3)

1.一种蒸发段和冷凝段均为蛇形结构的分离式热管换热系统,包括蒸发段(11)和冷凝段(12),热管工质在蒸发段(11)的输出口处通过热管工质上升管路(1)与冷凝段(12)的输入口相连,热管工质在冷凝段(12)的输出口处通过热管工质下降管路(10)与蒸发段(11)的输入口相连,其特征是所述的蒸发段(11)由蒸发段壳体(2)、蒸发管(3)、蒸发段弯管(13)、蒸发段孔板(4)以及蒸发段端盖(5)组成,每支蒸发管(3)都顺着管内热管工质的流动方向有一微小角度的向上倾斜,蒸发管(3)之间设有热流体通道,它的两端支承在蒸发段孔板(4),蒸发段孔板(4)分别安装在蒸发段壳体(2)的两端,蒸发段端盖(5)安装在所述蒸发段壳体(2)的两端且位于蒸发段孔板(4)的外侧,所述的蒸发段弯管(13)位于蒸发段端盖(5)与蒸发段孔板(4)之间,它的两端分别与相邻蒸发管(3)的对应端相连并使蒸发管(3)所有或部分地首尾相连成蛇形结构布置在蒸发段壳体(2)中;所述的冷凝段(12)由冷凝段壳体(6)、冷凝管(7)、冷凝段弯管(14)、冷凝段孔板(8)以及冷凝段端盖(9)组成,每支冷凝管(7)都顺着管内热管工质的流动方向有一微小角度的向下倾斜,冷凝管(7)之间设有热流体通道,它的两端支承在冷凝段孔板(8),冷凝段孔板(8)分别安装在冷凝段壳体(6)的两端,冷凝段端盖(9)安装在所述冷凝段壳体(6)的两端且位于冷凝段孔板(8)的外侧,所述的冷凝段弯管(14)位于冷凝段端盖(9)与冷凝段孔板(8)之间,它的两端分别与相邻冷凝管(7)的对应端相连并使冷凝管(7)所有或部分地首尾相连成蛇形结构布置在冷凝段壳体(6)中。1. A separate heat pipe heat exchange system in which both the evaporating section and the condensing section are serpentine structures, comprising an evaporating section (11) and a condensing section (12), and the heat pipe working medium passes through the heat pipe at the output port of the evaporating section (11) The working fluid ascending pipeline (1) is connected to the input port of the condensing section (12), and the heat pipe working medium passes through the heat pipe working medium descending pipeline (10) at the output port of the condensing section (12) and the input of the evaporating section (11) It is characterized in that the evaporating section (11) consists of evaporating section shell (2), evaporating tube (3), evaporating section elbow (13), evaporating section orifice (4) and evaporating section end cover ( 5) Composition, each evaporating tube (3) is inclined upward at a slight angle along the flow direction of the heat pipe working medium in the tube, and a thermal fluid channel is provided between the evaporating tubes (3), and its two ends are supported on the evaporating section hole The plate (4), the orifice plate (4) of the evaporating section is respectively installed at both ends of the evaporating section shell (2), and the end cover (5) of the evaporating section is installed at both ends of the evaporating section shell (2) and is located at the The outer side of the section orifice (4), the evaporation section elbow (13) is located between the evaporation section end cover (5) and the evaporation section orifice (4), and its two ends are respectively connected to the adjacent evaporation tube (3 ) are connected to each other and all or part of the evaporation tubes (3) are connected end to end to form a serpentine structure and arranged in the evaporation section shell (2); the condensation section (12) is composed of the condensation section shell (6), Condensation pipe (7), condensation section elbow (14), condensation section orifice (8) and condensation section end cover (9), each condensation pipe (7) has a small The angle is inclined downward, and there is a hot fluid channel between the condensation pipes (7), and its two ends are supported on the orifice plate (8) of the condensation section, and the orifice plate (8) of the condensation section is respectively installed on the casing (6) of the condensation section The two ends of the condensing section end caps (9) are installed on both ends of the condensing section shell (6) and are located outside the orifice plate (8) of the condensing section, and the condensing section elbow (14) is located in the condensing section Between the end cover (9) and the orifice plate (8) of the condensing section, its two ends are respectively connected to the corresponding ends of the adjacent condensing pipes (7) and all or part of the condensing pipes (7) are connected end to end to form a serpentine structure Arranged in the condensation section housing (6). 2.根据权利要求1所述之蒸发段和冷凝段均为蛇形结构的分离式热管换热系统,其特征是所述的蒸发段端盖(5)与蒸发段壳体(2)根据热流体的物理特性为可拆卸式连接结构或焊接结构;所述的冷凝段端盖(9)与冷凝段壳体(6)也可根据冷流体的物理特性为可拆卸式连接结构或焊接结构。2. According to claim 1, the evaporating section and the condensing section are separated heat pipe heat exchange systems with serpentine structures, characterized in that the evaporating section end cover (5) and the evaporating section shell (2) The physical property of the fluid is a detachable connection structure or a welded structure; the condensation section end cover (9) and the condensation section shell (6) can also be a detachable connection structure or a welding structure according to the physical characteristics of the cold fluid. 3.根据权利要求1所述之蒸发段和冷凝段均为蛇形结构的分离式热管换热系统,其特征是所述的蒸发段弯管(13)与蒸发管(3)之间为焊接连接结构,且焊接点位于蒸发段孔板(4)和蒸发段端盖(5)间的空间;所述的冷凝段弯管(14)与冷凝管(7)之间也为焊接连接结构,且焊接点位于冷凝段孔板(8)和冷凝段端盖(9)间的空间。3. According to claim 1, the evaporating section and the condensing section are separated heat pipe heat exchange systems with a serpentine structure, characterized in that the elbow (13) of the evaporating section and the evaporating pipe (3) are welded The connection structure, and the welding point is located in the space between the evaporation section orifice (4) and the evaporation section end cover (5); the condensation section elbow (14) and the condensation pipe (7) are also welded connection structures, And the welding point is located in the space between the orifice plate (8) of the condensation section and the end cover (9) of the condensation section.
CNU2007200365716U 2007-04-05 2007-04-05 Snake structure separated heat pipe heat exchange system Expired - Fee Related CN201032440Y (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101865621A (en) * 2010-07-01 2010-10-20 江苏科圣化工装备工程有限公司 Heat exchanger with cold fluid and hot fluid not leak through with each other
CN102809314A (en) * 2012-08-31 2012-12-05 苏州浩佳节能科技有限公司 Three-dimensional heat-pipe heat exchanger and production method thereof
CN104764338A (en) * 2015-03-19 2015-07-08 南京华电节能环保设备有限公司 Heat pipe type flue gas pulverized coal heating device
CN105758238A (en) * 2016-04-21 2016-07-13 中国科学院工程热物理研究所 U-shaped heat pipe array device and air conditioning system with the same
CN106567773A (en) * 2016-05-31 2017-04-19 贵州大学 Loop heat pipe intercooler and work method thereof
CN111521050A (en) * 2020-04-26 2020-08-11 吉林省电力科学研究院有限公司 Heating system based on waste heat recovery of boiler body
CN116672884A (en) * 2023-07-14 2023-09-01 浙江大学 Catalytic oxidation system and catalytic oxidation method for efficiently converting and removing VOCs in coal chemical industry

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101865621A (en) * 2010-07-01 2010-10-20 江苏科圣化工装备工程有限公司 Heat exchanger with cold fluid and hot fluid not leak through with each other
CN102809314A (en) * 2012-08-31 2012-12-05 苏州浩佳节能科技有限公司 Three-dimensional heat-pipe heat exchanger and production method thereof
CN104764338A (en) * 2015-03-19 2015-07-08 南京华电节能环保设备有限公司 Heat pipe type flue gas pulverized coal heating device
CN105758238A (en) * 2016-04-21 2016-07-13 中国科学院工程热物理研究所 U-shaped heat pipe array device and air conditioning system with the same
CN106567773A (en) * 2016-05-31 2017-04-19 贵州大学 Loop heat pipe intercooler and work method thereof
CN111521050A (en) * 2020-04-26 2020-08-11 吉林省电力科学研究院有限公司 Heating system based on waste heat recovery of boiler body
CN116672884A (en) * 2023-07-14 2023-09-01 浙江大学 Catalytic oxidation system and catalytic oxidation method for efficiently converting and removing VOCs in coal chemical industry
CN116672884B (en) * 2023-07-14 2024-01-16 浙江大学 Catalytic oxidation system and catalytic oxidation method for efficiently converting and removing VOCs in coal chemical industry

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