CN201032440Y - Snake structure separated heat pipe heat exchange system - Google Patents
Snake structure separated heat pipe heat exchange system Download PDFInfo
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- 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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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-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
- F28D15/02—Heat-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
- F28D15/0266—Heat-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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- 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。
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.
Description
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
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
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
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
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
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
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
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
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.
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Cited By (7)
| 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 |
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2007
- 2007-04-05 CN CNU2007200365716U patent/CN201032440Y/en not_active Expired - Fee Related
Cited By (8)
| 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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