[go: up one dir, main page]

CN104197760A - Pipeline type pulse heat pipe heat exchanger - Google Patents

Pipeline type pulse heat pipe heat exchanger Download PDF

Info

Publication number
CN104197760A
CN104197760A CN201410403626.7A CN201410403626A CN104197760A CN 104197760 A CN104197760 A CN 104197760A CN 201410403626 A CN201410403626 A CN 201410403626A CN 104197760 A CN104197760 A CN 104197760A
Authority
CN
China
Prior art keywords
pipe
heat
pipeline
pulsating
section
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.)
Pending
Application number
CN201410403626.7A
Other languages
Chinese (zh)
Inventor
杨洪海
邹晶
方海洲
王欣
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.)
Donghua University
Original Assignee
Donghua 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 Donghua University filed Critical Donghua University
Priority to CN201410403626.7A priority Critical patent/CN104197760A/en
Publication of CN104197760A publication Critical patent/CN104197760A/en
Pending legal-status Critical Current

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

本发明提供了一种管线式脉动热管换热器,其特征在于,包括热媒流动管道,热媒流动管道的前后两侧各设有一个脉动热管,所述的脉动热管包括蒸发段、冷凝段以及位于蒸发段和冷凝段之间的绝热段,所述的热媒流动管道包括入口管路、出口管路和位于入口管路和出口管路之间的中间管路,其中,所述的脉动热管的蒸发段设于热媒流动管道的入口管路的侧面,所述的脉动热管的冷凝段设于热媒流动管道的出口管路的侧面。本发明的脉动热管能够高效传热,在无动力的外界条件下,依靠汽、液两相介质的自我振荡流动来传递热量。在整个过程中,无需消耗外部机械功和电功,在热驱动下实现自我振荡,具有制造容易、成本低廉的特点。The invention provides a pipeline type pulsating heat pipe heat exchanger, which is characterized in that it includes a heat medium flow pipe, and a pulsating heat pipe is respectively arranged on the front and rear sides of the heat medium flow pipe, and the pulsating heat pipe includes an evaporation section and a condensation section and an adiabatic section between the evaporating section and the condensing section, the heat medium flow pipeline includes an inlet pipeline, an outlet pipeline and an intermediate pipeline between the inlet pipeline and the outlet pipeline, wherein the pulsation The evaporation section of the heat pipe is arranged on the side of the inlet pipeline of the heat medium flow pipe, and the condensation section of the pulsating heat pipe is arranged on the side of the outlet pipeline of the heat medium flow pipeline. The pulsating heat pipe of the present invention can transfer heat efficiently, relying on the self-oscillating flow of vapor and liquid two-phase medium to transfer heat under the external condition of no power. During the whole process, no need to consume external mechanical and electric power, self-oscillation is realized under thermal drive, and it has the characteristics of easy manufacture and low cost.

Description

一种管线式脉动热管换热器A pipeline type pulsating heat pipe heat exchanger

技术领域technical field

本发明涉及的是一种利用脉动热管进行增强换热的管线式换热器的一种装置。利用脉动热管相变传热和脉动效应,有效提高换热器的换热效率,形成高效的脉动热管换热器。主要用于船舶、汽车、航天、电子、余热回收以及太阳能与地热利用等场合。具有换热效率高,压力损失少,不易结垢等特点。The invention relates to a device of a line type heat exchanger which utilizes a pulsating heat pipe to enhance heat exchange. Utilizing the phase change heat transfer and pulsation effect of the pulsating heat pipe, the heat exchange efficiency of the heat exchanger is effectively improved, and an efficient pulsating heat pipe heat exchanger is formed. Mainly used in ships, automobiles, aerospace, electronics, waste heat recovery, solar energy and geothermal utilization, etc. It has the characteristics of high heat exchange efficiency, less pressure loss, and not easy to scale.

背景技术Background technique

在交通运输、航空航天以及工业生产过程中,需要在设备系统与周围环境之间或者在同一系统的不同部分之间控制或是强化热量的传递。换热器不仅是保证正常生产生活必不可少的关键设备之一,同时也在节能减排,能源的二次利用之中起到了不可替代的作用。目前换热器的种类很多,技术相对成熟,但是如何高效,节能的提高换热效率依然是换热器面对的难题。In transportation, aerospace and industrial processes, it is necessary to control or enhance the transfer of heat between equipment systems and the surrounding environment or between different parts of the same system. The heat exchanger is not only one of the key equipments necessary to ensure normal production and life, but also plays an irreplaceable role in energy saving, emission reduction and secondary utilization of energy. At present, there are many types of heat exchangers, and the technology is relatively mature, but how to improve heat exchange efficiency with high efficiency and energy saving is still a difficult problem for heat exchangers.

脉动热管是一种新型高效传热设备,运行时主要依靠汽、液两相介质的自我振荡流动来传递热量。其工作原理是:将管内抽成真空后充注一定量的工作介质,由于管径足够小,管内将形成气泡柱和液体柱间隔布置并呈随机分布的状态。在蒸发端,工质吸热产生气泡,迅速膨胀和升压,推动工质流向低温冷凝端,那里,气泡冷却收缩并破裂,压力下降。这样,由于两端间存在压差以及相邻管子之间存在的压力不平衡,使得工质在蒸发段和冷凝段之间振荡流动,从而实现热量的传递。在整个过程中,无需消耗外部机械功和电功,完全是在热驱动下的自我震荡。脉动热管具有结构简单,制造容易,成本低廉的优点,现已成功应用在电力设备及微电子的热处理。结构合理的脉动热管传热系数很大,由不锈钢板制作的板式脉动热管的导热系数约为2000W/m·K,比原不锈钢的导热系数高出120倍,同时保持了不锈钢原有的优点。The pulsating heat pipe is a new type of high-efficiency heat transfer equipment, which mainly relies on the self-oscillating flow of the vapor and liquid two-phase medium to transfer heat during operation. Its working principle is: vacuumize the inside of the tube and fill it with a certain amount of working medium. Because the tube diameter is small enough, bubble columns and liquid columns will be formed in the tube, which are arranged at intervals and randomly distributed. At the evaporating end, the working fluid absorbs heat to generate bubbles, rapidly expands and boosts the pressure, and pushes the working fluid to flow to the low-temperature condensation end, where the bubbles cool, shrink and burst, and the pressure drops. In this way, due to the pressure difference between the two ends and the pressure imbalance between adjacent tubes, the working fluid oscillates and flows between the evaporation section and the condensation section, thereby realizing heat transfer. In the whole process, there is no need to consume external mechanical and electric power, and it is completely self-oscillation driven by heat. The pulsating heat pipe has the advantages of simple structure, easy manufacture and low cost, and has been successfully applied in the heat treatment of power equipment and microelectronics. The heat transfer coefficient of the pulsating heat pipe with reasonable structure is very large. The thermal conductivity of the plate-type pulsating heat pipe made of stainless steel plate is about 2000W/m·K, which is 120 times higher than that of the original stainless steel, while maintaining the original advantages of stainless steel.

发明内容Contents of the invention

本发明所要解决的问题是提供一种具有高效传热性能的管线式脉动热管换热器。The problem to be solved by the present invention is to provide a pipeline type pulsating heat pipe heat exchanger with high heat transfer performance.

为了解决上述技术问题,本发明提供了一种管线式脉动热管换热器,其特征在于,包括热媒流动管道,热媒流动管道的前后两侧各设有一个脉动热管,所述的脉动热管包括蒸发段、冷凝段以及位于蒸发段和冷凝段之间的绝热段,所述的热媒流动管道包括入口管路、出口管路和位于入口管路和出口管路之间的中间管路,其中,所述的脉动热管的蒸发段设于热媒流动管道的入口管路的侧面,所述的脉动热管的冷凝段设于热媒流动管道的出口管路的侧面。In order to solve the above technical problems, the present invention provides a pipeline type pulsating heat pipe heat exchanger, which is characterized in that it includes a heat medium flow pipe, and a pulsating heat pipe is provided on the front and rear sides of the heat medium flow pipe, and the pulsating heat pipe It includes an evaporating section, a condensing section, and an adiabatic section between the evaporating section and the condensing section, and the heat medium flow pipeline includes an inlet pipeline, an outlet pipeline, and an intermediate pipeline between the inlet pipeline and the outlet pipeline, Wherein, the evaporating section of the pulsating heat pipe is arranged on the side of the inlet pipe of the heat medium flow pipe, and the condensation section of the pulsating heat pipe is arranged on the side of the outlet pipe of the heat medium flow pipe.

优选地,所述的脉动热管的蒸发段与热媒流动管道的入口管路之间以及所述的脉动热管的冷凝段与热媒流动管道的出口管路之间设有增强换热管网。Preferably, an enhanced heat exchange pipe network is provided between the evaporation section of the pulsating heat pipe and the inlet pipeline of the heat medium flow pipeline, and between the condensation section of the pulsating heat pipe and the outlet pipeline of the heat medium flow pipeline.

更优选地,所述的增强换热管网和脉动热管分别对称地设于热媒流动管道的两侧。More preferably, the enhanced heat exchange pipe network and the pulsating heat pipes are respectively arranged symmetrically on both sides of the heat medium flow pipe.

优选地,所述的脉动热管为蛇形管,所述的蛇形管的首尾相连形成闭式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有制冷剂。Preferably, the pulsating heat pipe is a serpentine pipe, the serpentine pipes are connected end to end to form a closed circuit pulsating heat pipe, and its cross-sectional shape is circular, and refrigerant is arranged in the serpentine pipe.

优选地,所述的脉动热管为蛇形管,所述的蛇形管的首尾不相连形成开式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有制冷剂。Preferably, the pulsating heat pipe is a serpentine pipe, the end of the serpentine pipe is not connected to form an open loop pulsating heat pipe, and its cross section is circular, and refrigerant is arranged in the serpentine pipe.

更优选地,所述的蛇形管的充液率为55%,所述的制冷剂为R134a、丙酮、酒精、水或氨水。(工质可以依据实际换热量以及成本等综合考虑而定)。More preferably, the liquid filling rate of the serpentine tube is 55%, and the refrigerant is R134a, acetone, alcohol, water or ammonia water. (The working fluid can be determined based on comprehensive considerations such as actual heat transfer and cost).

优选地,所述的热媒流动管道为蛇形管。Preferably, the heat medium flow pipe is a serpentine pipe.

更优选地,所述的蛇形管的弯头部分设于绝热箱体中。More preferably, the elbow part of the serpentine pipe is arranged in the heat insulation box.

优选地,所述的热媒流动管道内设有热媒,热媒流速为0.02kg/s-1.5kg/s。Preferably, the heat medium flow pipe is provided with a heat medium, and the flow rate of the heat medium is 0.02kg/s-1.5kg/s.

优选地,所述的脉动热管竖直安装,其蒸发段位于上侧,冷凝段位于下侧,热媒流动管道中的热媒由高端流向低端。Preferably, the pulsating heat pipe is installed vertically, its evaporating section is located on the upper side, and the condensing section is located on the lower side, and the heat medium in the heat medium flow pipe flows from the high end to the low end.

优选地,所述的脉动热管水平安装,其蒸发段位于绝热段的左侧或右侧,冷凝段位于绝热段的右侧或左侧,脉动热管的弯头数为40个以上。Preferably, the pulsating heat pipe is installed horizontally, the evaporating section is located on the left or right of the adiabatic section, the condensing section is located on the right or left of the adiabatic section, and the number of bends of the pulsating heat pipe is more than 40.

与现有技术相比,本发明的有益效果是:Compared with prior art, the beneficial effect of the present invention is:

1、本发明是通过利用脉动热管内工作液体的相态变化来增强换热的装置。脉动热管能够高效传热,在无动力的外界条件下,依靠汽、液两相介质的自我振荡流动来传递热量。在整个过程中,无需消耗外部机械功和电功,在热驱动下实现自我振荡,具有制造容易、成本低廉的特点。1. The present invention is a device for enhancing heat exchange by using the phase change of the working liquid in the pulsating heat pipe. Pulsating heat pipes can transfer heat efficiently, relying on the self-oscillating flow of vapor and liquid two-phase media to transfer heat under unpowered external conditions. During the whole process, no need to consume external mechanical and electric power, self-oscillation is realized under thermal drive, and it has the characteristics of easy manufacture and low cost.

2、本发明的增强换热管网在热媒流动管道与脉动热管之间安装,这样有利于热媒流体管道与脉动热管之间热量的交换,同时能够使脉动热管受热均匀,更好的提高脉动热管换热器的换热效率。2. The enhanced heat exchange pipe network of the present invention is installed between the heat medium flow pipe and the pulsating heat pipe, which is beneficial to the heat exchange between the heat medium fluid pipe and the pulsating heat pipe, and at the same time can make the pulsating heat pipe evenly heated, better improving Heat transfer efficiency of a pulsating heat pipe heat exchanger.

附图说明Description of drawings

图1a为开式脉动热管结构示意图;Figure 1a is a schematic diagram of the structure of an open pulsating heat pipe;

图1b为闭式脉动热管结构示意图;Figure 1b is a schematic diagram of the structure of a closed pulsating heat pipe;

图2为热媒流动管道结构示意图;Fig. 2 is a structural schematic diagram of a heat medium flow pipeline;

图3为增强换热管网结构示意图;Figure 3 is a schematic diagram of the structure of the enhanced heat exchange pipe network;

图4a为使用开式脉动热管的管线式脉动热管换热器结构示意图;Figure 4a is a schematic structural diagram of a pipeline type pulsating heat pipe heat exchanger using an open pulsating heat pipe;

图4b为使用闭式脉动热管的管线式脉动热管换热器结构示意图;Figure 4b is a schematic structural diagram of a pipeline type pulsating heat pipe heat exchanger using a closed pulsating heat pipe;

图5为管线式脉动热管换热器俯视图。Fig. 5 is a top view of the pipeline type pulsating heat pipe heat exchanger.

具体实施方式Detailed ways

下面结合具体实施例,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。Below in conjunction with specific embodiment, further illustrate the present invention. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.

实施例1Example 1

一种使用开式脉动热管的管线式脉动热管换热器,包括脉动热管1、热媒流动管道2、增强换热管网3和绝热箱体4。A pipeline type pulsating heat pipe heat exchanger using an open pulsating heat pipe, comprising a pulsating heat pipe 1 , a heat medium flow pipe 2 , an enhanced heat exchange pipe network 3 and an adiabatic box 4 .

如图1a所示,所述的脉动热管1为由外径4mm,内径2.7mm的紫铜管弯制而成的蛇形管,弯曲半径为8mm,所述的蛇形管的首尾不相连形成开式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有R134a制冷剂,充液率为55%,真空度达到10-3Pa。工质可以依据实际换热量以及成本等综合考虑而定。所述的脉动热管1包括蒸发段11、冷凝段13以及位于蒸发段11和冷凝段13之间的绝热段12。蒸发段11和冷凝段13的长度、弯头数可以根据实际需求而定。As shown in Figure 1a, the pulsating heat pipe 1 is a serpentine tube bent from a copper tube with an outer diameter of 4 mm and an inner diameter of 2.7 mm, and the bending radius is 8 mm. The ends of the serpentine tube are not connected to each other. The open circuit pulsating heat pipe has a circular cross-section. The serpentine tube is provided with R134a refrigerant, the liquid filling rate is 55%, and the vacuum degree reaches 10 -3 Pa. The working fluid can be determined based on comprehensive considerations such as actual heat transfer and cost. The pulsating heat pipe 1 includes an evaporating section 11 , a condensing section 13 and an adiabatic section 12 between the evaporating section 11 and the condensing section 13 . The length and number of bends of the evaporating section 11 and the condensing section 13 can be determined according to actual needs.

如图2所示,所述的热媒流动管道2由具有高效传热性能的材料紫铜管(紫铜是一种良好的导热材料,在考虑制作成本及传热性能的基础上,建议选择紫铜管作为热媒流动管道)弯制而成,管道呈蛇形,增大了热媒的散热面积,便于热量交换,其包括入口管路21、出口管路22和位于入口管路21和出口管路22之间的中间管路23。所述的蛇形管的弯头部分设于绝热箱体4中,绝热箱体4覆盖在热媒流动管道2的弯头部分,以达到减少热量损失的目的。所述的热媒流动管道内设有热媒,热媒流速为0.02kg/s-1.5kg/s。对管径没有特殊要求,可以依据热媒流速而定。As shown in Figure 2, the heat medium flow pipe 2 is made of a material with high heat transfer performance of copper (copper is a good heat conduction material, on the basis of considering the production cost and heat transfer performance, it is recommended to choose purple The copper tube is bent as the heat medium flow pipe), and the pipe is serpentine, which increases the heat dissipation area of the heat medium and facilitates heat exchange. Intermediate pipeline 23 between pipelines 22 . The elbow part of the serpentine pipe is arranged in the heat insulation box 4, and the heat insulation box 4 covers the elbow part of the heat medium flow pipe 2, so as to reduce heat loss. A heat medium is arranged in the heat medium flowing pipeline, and the flow rate of the heat medium is 0.02kg/s-1.5kg/s. There is no special requirement for the pipe diameter, which can be determined according to the flow rate of the heat medium.

如图3所示,所述的增强换热管网是由直径1mm的紫铜丝编织而成,紫铜丝横竖交织,组成网状结构,目的是为了增大接触面积,采用导热系数高的材料,能够加强换热。增强换热管网的形状,大小依据脉动热管冷热段的长度而定,材料可以依据实际需求而定。其大小正好覆盖脉动热管的冷凝段或蒸发段,在热媒流动管道与脉动热管之间安装,这样有利于热媒流体管道与脉动热管之间热量的交换,同时能够使脉动热管受热均匀,更好的提高脉动热管换热器的换热效率。As shown in Figure 3, the enhanced heat exchange pipe network is braided by copper wires with a diameter of 1 mm, and the copper wires are interwoven horizontally and vertically to form a network structure. The purpose is to increase the contact area and use materials with high thermal conductivity. Can enhance heat transfer. The shape and size of the enhanced heat exchange pipe network are determined according to the length of the hot and cold sections of the pulsating heat pipe, and the material can be determined according to actual needs. Its size just covers the condensation section or evaporation section of the pulsating heat pipe, and it is installed between the heat medium flow pipe and the pulsating heat pipe. It is good to improve the heat exchange efficiency of the pulsating heat pipe heat exchanger.

如图4a所示,热媒流动管道2的前后两侧各设有一个脉动热管1,热媒流动管道2与脉动热管1呈垂直布置。其中,所述的脉动热管1的蒸发段11设于热媒流动管道2的入口管路21的侧面,所述的脉动热管1的冷凝段13设于热媒流动管道2的出口管路22的侧面。所述的脉动热管1的蒸发段11与热媒流动管道2的入口管路21之间以及所述的脉动热管1的冷凝段13与热媒流动管道2的出口管路22之间设有增强换热管网3。如图5所示,所述的增强换热管网3和脉动热管1分别对称地设于热媒流动管道2的两侧。热媒经过入口处进入管道,在管道内呈S形流动,强化了热媒的换热面积。热媒流动管道可以依据实际需求具体布置。安装时,先固定好热媒流动管道2,在热媒流动管道2的两端布置增强换热管网3,尽量减少增强换热管网3与热媒流动管道2之间的间隙,使其紧凑的安装在脉动热管1与热媒流动管道2之间;绝热箱体4安装在热媒流动管道2的弯头处,使其减少热媒在弯头处的热量损失,提高管线式脉动热管换热器的换热效率。As shown in FIG. 4 a , a pulsating heat pipe 1 is provided on the front and rear sides of the heat medium flow pipe 2 , and the heat medium flow pipe 2 and the pulsation heat pipe 1 are vertically arranged. Wherein, the evaporation section 11 of the pulsating heat pipe 1 is arranged on the side of the inlet pipeline 21 of the heat medium flow pipeline 2, and the condensation section 13 of the pulsating heat pipe 1 is arranged on the side of the outlet pipeline 22 of the heat medium flow pipeline 2. side. Between the evaporation section 11 of the pulsating heat pipe 1 and the inlet pipeline 21 of the heat medium flow pipeline 2 and between the condensation section 13 of the pulsating heat pipe 1 and the outlet pipeline 22 of the heat medium flow pipeline 2, reinforcement Heat exchange pipe network 3. As shown in FIG. 5 , the enhanced heat exchange pipe network 3 and the pulsating heat pipe 1 are symmetrically arranged on both sides of the heat medium flow pipe 2 . The heat medium enters the pipe through the entrance, and flows in an S shape in the pipe, which strengthens the heat exchange area of the heat medium. Heat medium flow pipes can be arranged according to actual needs. During installation, fix the heat medium flow pipe 2 first, and arrange the enhanced heat exchange pipe network 3 at both ends of the heat medium flow pipe 2, so as to minimize the gap between the enhanced heat exchange pipe network 3 and the heat medium flow pipe 2, so that Compactly installed between the pulsating heat pipe 1 and the heat medium flow pipe 2; the heat insulation box 4 is installed at the elbow of the heat medium flow pipe 2 to reduce the heat loss of the heat medium at the elbow and improve the performance of the pipeline type pulsating heat pipe. heat transfer efficiency of the heat exchanger.

本发明涉及的管线式脉动热管换热器的部件的长度和结构形式可以根据实际情况而定。管线式脉动热管换热器可以垂直安装也可以水平安装。如图4a所示,当脉动热管1竖直安装时,其蒸发段位于上侧,冷凝段位于下侧,热媒入口设置在高处,热媒流动管道2中的热媒由高端流向低端。脉动热管的弯头数个数没有明确要求。当脉动热管1水平安装时,其蒸发段位于绝热段的左侧或右侧,冷凝段位于绝热段的右侧或左侧,热媒流动入口可以设置在任意端,经过大量实验证明,在以100℃水为热媒,R134a为脉动热管的制冷剂时,随着脉动热管弯头数的增加,换热效率由75%上升至90%,一般情况下弯头数满足40个以上,对换热器的换热效率具有明显促进作用同时能够摆脱脉动热管垂直安装与水平安装的限制。The length and structural form of the parts of the pipeline type pulsating heat pipe heat exchanger involved in the present invention can be determined according to actual conditions. The pipeline type pulsating heat pipe heat exchanger can be installed vertically or horizontally. As shown in Figure 4a, when the pulsating heat pipe 1 is installed vertically, the evaporation section is located on the upper side, the condensation section is located on the lower side, the heat medium inlet is set at a high place, and the heat medium in the heat medium flow pipe 2 flows from the high end to the low end . The number of elbows of the pulsating heat pipe has no specific requirements. When the pulsating heat pipe 1 is installed horizontally, the evaporating section is located on the left or right side of the adiabatic section, the condensing section is located on the right or left side of the adiabatic section, and the heat medium flow inlet can be set at any end. A large number of experiments have proved that in the following When water is the heat medium at 100°C and R134a is the refrigerant of the pulsating heat pipe, the heat transfer efficiency increases from 75% to 90% as the number of elbows of the pulsating heat pipe increases. Generally, the number of elbows meets more than 40. The heat exchanging efficiency of the heater has obvious promoting effect, and at the same time, it can get rid of the limitation of vertical installation and horizontal installation of the pulsating heat pipe.

使用时,高温的热媒经过增强换热管网,给脉动热管的蒸发段供能,脉动热管启动,经过脉动热管的相变传热及脉动效应,热量传递给冷凝段,此时经过换热的低温水经过冷凝段,强化了冷凝段的换热,使热量快速的散发出去,达到强化换热的目的。When in use, the high-temperature heat medium passes through the enhanced heat exchange pipe network to supply energy to the evaporation section of the pulsating heat pipe, the pulsating heat pipe starts, and through the phase change heat transfer and pulsation effect of the pulsating heat pipe, the heat is transferred to the condensation section. The low-temperature water passes through the condensation section, which strengthens the heat exchange in the condensation section, so that the heat can be dissipated quickly, and the purpose of strengthening the heat exchange is achieved.

实施例2Example 2

如图4b所示,为使用闭式脉动热管的管线式脉动热管换热器结构示意图,所述的使用闭式脉动热管的管线式脉动热管换热器,其结构类似于实施例1,区别在于,所述的脉动热管1的结构不同,所述的脉动热管1为蛇形管,所述的蛇形管的首尾相连形成闭式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有制冷剂。As shown in Figure 4b, it is a schematic structural diagram of a pipeline-type pulsating heat pipe heat exchanger using a closed-type pulsating heat pipe. The structure of the pipeline-type pulsating heat-pipe heat exchanger using a closed-type pulsating heat pipe is similar to that of Example 1, the difference is that , the structure of the pulsating heat pipe 1 is different. The pulsating heat pipe 1 is a serpentine pipe. A refrigerant is provided in the tube.

Claims (10)

1.一种管线式脉动热管换热器,其特征在于,包括热媒流动管道(2),热媒流动管道(2)的前后两侧各设有一个脉动热管(1),所述的脉动热管(1)包括蒸发段(11)、冷凝段(13)以及位于蒸发段(11)和冷凝段(13)之间的绝热段(12),所述的热媒流动管道(2)包括入口管路(21)、出口管路(22)和位于入口管路(21)和出口管路(22)之间的中间管路(23),其中,所述的脉动热管(1)的蒸发段(11)设于热媒流动管道(2)的入口管路(21)的侧面,所述的脉动热管(1)的冷凝段(13)设于热媒流动管道(2)的出口管路(22)的侧面。  1. A pipeline type pulsating heat pipe heat exchanger is characterized in that it comprises a heat medium flow pipe (2), and a pulsating heat pipe (1) is respectively provided on the front and rear sides of the heat medium flow pipe (2), and the pulsating heat pipe (1) The heat pipe (1) includes an evaporation section (11), a condensation section (13) and an adiabatic section (12) between the evaporation section (11) and the condensation section (13), and the heat medium flow pipe (2) includes an inlet pipeline (21), outlet pipeline (22) and an intermediate pipeline (23) between the inlet pipeline (21) and the outlet pipeline (22), wherein the evaporation section of the pulsating heat pipe (1) (11) is arranged on the side of the inlet pipeline (21) of the heat medium flow pipeline (2), and the condensation section (13) of the pulsating heat pipe (1) is arranged on the outlet pipeline of the heat medium flow pipeline (2) ( 22) side. the 2.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的脉动热管(1)的蒸发段(11)与热媒流动管道(2)的入口管路(21)之间以及所述的脉动热管(1)的冷凝段(13)与热媒流动管道(2)的出口管路(22)之间设有增强换热管网(3)。  2. The pipeline type pulsating heat pipe heat exchanger according to claim 1, characterized in that, the evaporation section (11) of the pulsating heat pipe (1) and the inlet pipe (21) of the heat medium flow pipe (2) An enhanced heat exchange pipe network (3) is arranged between the condensing section (13) of the pulsating heat pipe (1) and the outlet pipe (22) of the heat medium flow pipe (2). the 3.如权利要求2所述的管线式脉动热管换热器,其特征在于,所述的增强换热管网(3)和脉动热管(1)分别对称地设于热媒流动管道(2)的两侧。  3. The pipeline type pulsating heat pipe heat exchanger according to claim 2, characterized in that, the enhanced heat exchange pipe network (3) and the pulsating heat pipe (1) are respectively symmetrically arranged on the heat medium flow pipe (2) on both sides. the 4.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的脉动热管(1)为蛇形管,所述的蛇形管的首尾相连形成闭式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有制冷剂。  4. The pipeline type pulsating heat pipe heat exchanger according to claim 1, characterized in that, the pulsating heat pipe (1) is a serpentine tube, and the end-to-end connection of the serpentine tubes forms a closed loop pulsating heat pipe, Its section shape is circular, and refrigerant is arranged in the serpentine tube. the 5.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的脉动热管(1)为蛇形管,所述的蛇形管的首尾不相连形成开式回路脉动热管,其断面形状为圆形,所述的蛇形管中设有制冷剂。  5. The pipeline type pulsating heat pipe heat exchanger according to claim 1, characterized in that, the pulsating heat pipe (1) is a serpentine tube, and the ends of the serpentine tubes are not connected to form an open circuit pulsating heat pipe , its cross-sectional shape is circular, and refrigerant is arranged in the serpentine tube. the 6.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的热媒流动管道为蛇形管。  6. The pipeline type pulsating heat pipe heat exchanger according to claim 1, wherein the heat medium flow pipe is a coiled pipe. the 7.如权利要求6所述的管线式脉动热管换热器,其特征在于,所述的蛇形管的弯头部分设于绝热箱体(4)中。  7. The pipeline type pulsating heat pipe heat exchanger according to claim 6, characterized in that, the elbow part of the serpentine pipe is arranged in the heat insulation box (4). the 8.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的热媒流动管道内设有热媒,热媒流速为0.02kg/s-1.5kg/s。  8 . The pipeline type pulsating heat pipe heat exchanger according to claim 1 , wherein a heat medium is arranged in the heat medium flow pipe, and the flow rate of the heat medium is 0.02kg/s-1.5kg/s. the 9.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的脉动热管(1)竖直安装,其蒸发段位于上侧,冷凝段位于下侧,热媒流动管道(2) 中的热媒由高端流向低端。  9. The pipeline type pulsating heat pipe heat exchanger according to claim 1, wherein the pulsating heat pipe (1) is installed vertically, the evaporating section is located on the upper side, the condensing section is located on the lower side, and the heat medium flow pipe (2) The heat medium flows from the high end to the low end. the 10.如权利要求1所述的管线式脉动热管换热器,其特征在于,所述的脉动热管(1)水平安装,其蒸发段位于绝热段的左侧或右侧,冷凝段位于绝热段的右侧或左侧,脉动热管(1)的弯头数为40个以上。  10. The pipeline type pulsating heat pipe heat exchanger according to claim 1, wherein the pulsating heat pipe (1) is installed horizontally, the evaporating section is located on the left or right side of the adiabatic section, and the condensing section is located in the adiabatic section The right or left side of the pulsating heat pipe (1) has more than 40 elbows. the
CN201410403626.7A 2014-08-15 2014-08-15 Pipeline type pulse heat pipe heat exchanger Pending CN104197760A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410403626.7A CN104197760A (en) 2014-08-15 2014-08-15 Pipeline type pulse heat pipe heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410403626.7A CN104197760A (en) 2014-08-15 2014-08-15 Pipeline type pulse heat pipe heat exchanger

Publications (1)

Publication Number Publication Date
CN104197760A true CN104197760A (en) 2014-12-10

Family

ID=52083088

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410403626.7A Pending CN104197760A (en) 2014-08-15 2014-08-15 Pipeline type pulse heat pipe heat exchanger

Country Status (1)

Country Link
CN (1) CN104197760A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104567499A (en) * 2015-01-20 2015-04-29 北京建筑大学 Pulse heat pipe heat radiation device used for electronic device and heat radiation device thereof
CN105157460A (en) * 2015-08-24 2015-12-16 东华大学 Pulsating heat pipe heat exchanger with ammonia water as media and stainless steel as materials
CN105299540A (en) * 2015-11-05 2016-02-03 广州百年光电技术开发有限公司 Self-exciting type loop heat pipe sunflower heat dissipation module and large-power LED tube light
CN105571366A (en) * 2015-12-25 2016-05-11 南昌大学 Pulsating heat pipe with tilt-angle communicating pipe structure
CN107036333A (en) * 2017-04-28 2017-08-11 东南大学 Lithium bromide refrigerator generator
CN107310348A (en) * 2017-06-07 2017-11-03 东南大学 A kind of built-in heat pipe passive cooling system of bottom of car
CN109640576A (en) * 2017-10-09 2019-04-16 周哲明 A kind of water cooling phase-change heat equipment

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002206881A (en) * 2001-01-12 2002-07-26 Ts Heatronics Co Ltd Radiator
US20110067843A1 (en) * 2008-11-14 2011-03-24 Vasiliev Jr Leonid Heat exchange device made of polymeric material
CN102692087A (en) * 2012-06-06 2012-09-26 长春工程学院 Flat plate type solar thermal collector with composite pulsating heat pipe
CN203100223U (en) * 2012-12-14 2013-07-31 华北电力大学 Solar combined heat and power generation system based on pulsating heat pipe
CN203629391U (en) * 2013-12-11 2014-06-04 中国航天空气动力技术研究院 Radiator for performance-enhanced pulsating heat pipe

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002206881A (en) * 2001-01-12 2002-07-26 Ts Heatronics Co Ltd Radiator
US20110067843A1 (en) * 2008-11-14 2011-03-24 Vasiliev Jr Leonid Heat exchange device made of polymeric material
CN102692087A (en) * 2012-06-06 2012-09-26 长春工程学院 Flat plate type solar thermal collector with composite pulsating heat pipe
CN203100223U (en) * 2012-12-14 2013-07-31 华北电力大学 Solar combined heat and power generation system based on pulsating heat pipe
CN203629391U (en) * 2013-12-11 2014-06-04 中国航天空气动力技术研究院 Radiator for performance-enhanced pulsating heat pipe

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
杨洪海等: "脉动热管技术的研究现状及前沿热点", 《东华大学学报(自然科学版)》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104567499A (en) * 2015-01-20 2015-04-29 北京建筑大学 Pulse heat pipe heat radiation device used for electronic device and heat radiation device thereof
CN105157460A (en) * 2015-08-24 2015-12-16 东华大学 Pulsating heat pipe heat exchanger with ammonia water as media and stainless steel as materials
CN105299540A (en) * 2015-11-05 2016-02-03 广州百年光电技术开发有限公司 Self-exciting type loop heat pipe sunflower heat dissipation module and large-power LED tube light
CN105571366A (en) * 2015-12-25 2016-05-11 南昌大学 Pulsating heat pipe with tilt-angle communicating pipe structure
CN107036333A (en) * 2017-04-28 2017-08-11 东南大学 Lithium bromide refrigerator generator
CN107310348A (en) * 2017-06-07 2017-11-03 东南大学 A kind of built-in heat pipe passive cooling system of bottom of car
CN109640576A (en) * 2017-10-09 2019-04-16 周哲明 A kind of water cooling phase-change heat equipment

Similar Documents

Publication Publication Date Title
CN104197760A (en) Pipeline type pulse heat pipe heat exchanger
CN102620587B (en) Tube shell type pulsating heat pipe heat exchanger
CN201177465Y (en) Condensing heat exchanger for gas water heater
CN103512412B (en) U-shaped heat pipe heat exchanging component and the U-shaped heat exchange of heat pipe integrated with electrostatic precipitator
CN102927843A (en) Flue gas waste heat recovery system based on liquid metal heat transfer
CN104596335A (en) Heat storing device and heat circulating method of pulsating heat pipes
CN102121768A (en) Heat exchange apparatus with heat pipe soaking device for refrigeration air conditioning system
CN101520205A (en) Separable heat pipe heating system
CN204665993U (en) A kind of superconducting heat pipe exchanger device
CN105698245A (en) Water floor heating device characterized by utilizing pulsating heat pipe as radiating coil pipe
CN100443850C (en) Heat pipe type solid phase powder heat exchange system
CN202254521U (en) A Microchannel Condenser for Heat Pump Water Heater
CN204574495U (en) A kind of air-source water heater outer disk high-performance heat exchanger water tank
CN204007242U (en) A kind of plate type heat exchanger
CN203231656U (en) Condensation water saver for circulating cooling water system
CN205690946U (en) A kind of gas-liquid pulsating heat pipe heat exchanger
CN204438871U (en) A kind of pulsating heat pipe regenerative apparatus
CN205279807U (en) Compound heat exchanger of three media of worm formula
CN104006683A (en) Plate heat exchanger
CN203657572U (en) Novel smoke hot water boiler heat exchanger
CN201289323Y (en) Fin type heat exchanger for natural convection
CN203100177U (en) Condensing heat exchanger
CN112739142A (en) Water-cooling phase change heat dissipation equipment
CN103644750A (en) Heat exchanger of smoke and hot water boiler
CN205481248U (en) Utilize water floor heating device of pulsation heat pipe as radiating coil pipe

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20141210