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CN109458864B - Capillary pump loop heat pipe with outer space working capacity and working method - Google Patents

Capillary pump loop heat pipe with outer space working capacity and working method Download PDF

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CN109458864B
CN109458864B CN201811260261.1A CN201811260261A CN109458864B CN 109458864 B CN109458864 B CN 109458864B CN 201811260261 A CN201811260261 A CN 201811260261A CN 109458864 B CN109458864 B CN 109458864B
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evaporator
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steam
capillary
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CN109458864A (en
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赵舒然
张丹
刘继平
严俊杰
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Xian Jiaotong 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
    • F28D15/04Heat-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 tubes having a capillary structure
    • F28D15/043Heat-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 tubes having a capillary structure forming loops, e.g. capillary pumped loops

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  • Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)

Abstract

The invention discloses a capillary pump loop heat pipe with outer space working capacity and a working method, wherein the heat pipe comprises a main evaporator, a main radiation heat dissipation plate, a steam pipeline, a liquid phase pipeline, a liquid storage chamber, a regulating chamber, an auxiliary evaporator, an auxiliary radiation heat dissipation plate, a main liquid phase pipeline valve, a main steam valve and an auxiliary steam valve; the main evaporator comprises different areas such as a liquid phase channel area, a liquid absorption core area, a steam channel area, an outer pipe wall and the like; the liquid absorption core comprises an evaporation liquid absorption core and a heat insulation liquid absorption core which are made of different materials and have equivalent pore diameters; the auxiliary evaporator optimizes the starting through the displacement effect of steam before starting, and the auxiliary radiation heat dissipation plate and the auxiliary evaporator lead out the gas-bubble-containing liquid-phase working medium in the main evaporator and eliminate bubbles, so that the heat leakage problem in the stable operation stage is solved, and the operation stability of the heat pipe is improved; the liquid storage chamber separates the liquid storage area from the adjusting area, so that the adjusting sensitivity is improved and the energy consumption is reduced; the heat pipe structure has wide practical prospect in the field of external space heat dissipation.

Description

一种具备外空间工作能力的毛细泵回路热管及工作方法A capillary pump loop heat pipe capable of working in outer space and its working method

技术领域technical field

本发明涉及一种空间冷却技术,适用于失重且无空气等气体介质参与的外空间环境下的传热,具体涉及一种具备外空间工作能力的毛细泵回路热管及工作方法。The invention relates to a space cooling technology, which is suitable for heat transfer in an outer space environment where weightlessness and no gas medium such as air participate, in particular to a capillary pump loop heat pipe with outer space working capability and a working method.

背景技术Background technique

随着空间技术的发展,对于在太空中工作的装置能耗趋于高功率,工作时间趋于长期化,与之伴随的是更大的能源需求,而无论何种形式的能量最终都不得不以热量的形式离开空间装置,如果热量不能及时散出,必然导致产热原件及其周围温度上升,对工作原件造成不可逆的破坏。由于太空中没有空气对流也没有外界物质导热,唯一的散热方式仅有热辐射。实现大功率的辐射散热必然需要较大的散热面积,矛盾的是:大面积的辐射板必然无法直接安装在产热原件附近。因此空间技术需要大功率、小体积、长距离、具备零重力条件下工作能力的高效传热系统,实现热量的导出和散失。With the development of space technology, the energy consumption of devices working in space tends to be high, and the working time tends to be long-term, which is accompanied by greater energy demand, and no matter what form of energy eventually has to be Leaving the space device in the form of heat, if the heat cannot be dissipated in time, it will inevitably lead to an increase in the temperature of the heat-generating element and its surroundings, causing irreversible damage to the working element. Since there is no air convection and no heat conduction by external materials in space, the only way to dissipate heat is thermal radiation. To achieve high-power radiation heat dissipation, a large heat dissipation area is necessary. The contradiction is that a large-area radiant plate cannot be directly installed near the heat-generating components. Therefore, space technology requires a high-power, small-volume, long-distance, and efficient heat transfer system with the ability to work under zero-gravity conditions to achieve heat export and dissipation.

毛细泵回路热管是实现上述功能需求的有效途径之一。毛细泵回路热管是一种回路闭合环型热管,本质上是一种相变换热装置。一般由蒸发器、冷凝器、储液器以及蒸气管线和液体管线构成。毛细泵热管工作原理是:工质在蒸发器处汽化吸热,蒸汽离开从蒸发器时带走热量,蒸汽通过蒸汽管道到达辐射板,在辐射板位置冷凝液化,辐射板通过辐射散热散失热量,冷凝后的工质从液相管道回流至蒸发器。The capillary pump loop heat pipe is one of the effective ways to achieve the above functional requirements. The capillary pump loop heat pipe is a closed loop type heat pipe, which is essentially a phase change heat pipe. It generally consists of an evaporator, a condenser, a liquid accumulator, and a vapor line and a liquid line. The working principle of the capillary pump heat pipe is: the working medium vaporizes and absorbs heat at the evaporator, the steam takes away heat when it leaves the evaporator, the steam reaches the radiant panel through the steam pipe, condenses and liquefies at the position of the radiant panel, and the radiant panel dissipates heat through radiation heat dissipation, The condensed working medium is refluxed from the liquid phase line to the evaporator.

与传统热管相比,毛细泵回路热管主要特点在于液相工质与气相工质的通道相互独立,而吸液芯仅仅存在于蒸发器内。对应的优点有:1.降低了工质的沿程压降,提高了热管的传质能力,进而提高了热管的传热能力。2.气相和液相管道布置路径更加灵活,传输距离也更远。3.由毛细泵提供循环动力,可以在无重力、无外界机械功输入的情况下持续工作,适合外太空的失重条件。Compared with the traditional heat pipe, the main feature of the capillary pump loop heat pipe is that the channels of the liquid working medium and the gaseous working medium are independent of each other, and the liquid wick only exists in the evaporator. The corresponding advantages are as follows: 1. The pressure drop along the working fluid is reduced, the mass transfer capacity of the heat pipe is improved, and the heat transfer capacity of the heat pipe is further improved. 2. The gas phase and liquid phase pipelines are arranged more flexible and the transmission distance is longer. 3. The circulating power is provided by the capillary pump, which can work continuously without gravity and without external mechanical power input, which is suitable for the weightless conditions of outer space.

毛细泵回路热管的吸液芯作为关键组件需要满足以下需求:低导热系数,这是为了防止发生漏热,即防止液相通道内发生汽化;高渗透率,这是为了减少液相工质在吸液芯内传输时的压损;小的当量孔径,这是为了提供更高的毛细力,而矛盾之处在于减小当量孔径的同时往往伴随渗透率的下降。As a key component, the liquid wick of the capillary pump loop heat pipe needs to meet the following requirements: low thermal conductivity, which is to prevent heat leakage, that is, to prevent vaporization in the liquid phase channel; high permeability, which is to reduce the liquid phase working medium in Pressure loss during transport in the wick; small equivalent pore size, which is intended to provide higher capillary force, paradoxically, decreasing the equivalent pore size is often accompanied by a decrease in permeability.

毛细泵回路热管具有诸多优点,但是传统的毛细泵热管仍然存在缺陷:蒸发器热泄露导致传热能力下降甚至导致传热恶化的问题;高毛细力与高渗透率对孔径要求的矛盾;启动过程伴随明显的过热。因此,这就迫切需要开发一种能够克服以上缺陷的新型毛细泵回路热管。The capillary pump loop heat pipe has many advantages, but the traditional capillary pump heat pipe still has defects: the heat leakage of the evaporator leads to the decrease of heat transfer capacity and even the deterioration of heat transfer; the contradiction between high capillary force and high permeability on pore size requirements; the startup process with marked overheating. Therefore, there is an urgent need to develop a new capillary pump loop heat pipe that can overcome the above shortcomings.

发明内容SUMMARY OF THE INVENTION

为克服上述现有技术存在的问题,本发明的目的在于提供一种具备外空间工作能力的毛细泵回路热管及工作方法,包括新的吸液芯结构,新的布局方式以及相应的启动操作流程,从而能够实现外空间环境下稳定的启动和工作,提供高效的传热性能。In order to overcome the problems existing in the above-mentioned prior art, the purpose of the present invention is to provide a capillary pump loop heat pipe with outer space working capability and a working method, including a new wick structure, a new layout and a corresponding start-up operation process. , so as to realize stable startup and work in the outer space environment, and provide efficient heat transfer performance.

为了达到上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:

一种具备外空间工作能力的毛细泵回路热管,包括主蒸发器1、主辐射散热板2、蒸汽管道3、液相管道4、辅助蒸发器5、辅助辐射散热板6、储液室7、调节室8、绝热隔板9、限位环10、主液相管道阀门11、主蒸汽阀门12和辅助蒸汽阀门13;具体连接方式如下:主蒸发器1为一个或多个,为多个时,相互并联,一个或多个主蒸发器1侧面开孔,并连通蒸汽管道3,蒸汽管道3另一端接入外空间中的主辐射散热板2入口;主辐射散热板2出口连接液相管道4;液相管道4从一个或多个主蒸发器1一端接入主蒸发器液相通道,一个或多个主蒸发器1另一端再次通过液相管道4依次连接辅助辐射散热板6、辅助蒸发器5、储液室7和调节室8;辅助蒸发器5靠近辅助辐射散热板6一端的出口安装主液相管道阀门11;储液室7和调节室8共用一个刚性容器,两者中间用绝热隔板9作为两者的分界线,限位环10固定安装在储液室7和调节室8的容器壁上,绝热隔板9的活动范围受到限位环10的限制;辅助蒸发器5的侧面开孔连接辅助蒸汽阀门13,最终接入主蒸发器1和主辐射散热板2之间的蒸汽管道3。A capillary pump loop heat pipe capable of working in outer space, comprising a main evaporator 1, a main radiant heat sink 2, a steam pipeline 3, a liquid phase pipeline 4, an auxiliary evaporator 5, an auxiliary radiant heat sink 6, a liquid storage chamber 7, Adjustment chamber 8, insulation baffle 9, limit ring 10, main liquid phase pipeline valve 11, main steam valve 12 and auxiliary steam valve 13; the specific connection method is as follows: the main evaporator 1 is one or more, and when there are more than one , in parallel with each other, one or more main evaporators 1 have holes on the side and are connected to the steam pipe 3, and the other end of the steam pipe 3 is connected to the inlet of the main radiant heat sink 2 in the outer space; the outlet of the main radiant heat sink 2 is connected to the liquid phase pipeline 4; The liquid phase pipeline 4 is connected to the liquid phase channel of the main evaporator from one end of the one or more main evaporators 1, and the other end of the one or more main evaporators 1 is connected to the auxiliary radiant heat dissipation plate 6, the auxiliary The evaporator 5, the liquid storage chamber 7 and the adjustment chamber 8; the auxiliary evaporator 5 is installed with the main liquid phase pipeline valve 11 at the outlet of one end of the auxiliary radiant heat dissipation plate 6; the liquid storage chamber 7 and the adjustment chamber 8 share a rigid container, and the middle of the two The insulating baffle 9 is used as the boundary between the two, and the limit ring 10 is fixedly installed on the container walls of the liquid storage chamber 7 and the adjustment chamber 8. The movable range of the insulating baffle 9 is limited by the limit ring 10; the auxiliary evaporator The side opening of 5 is connected to the auxiliary steam valve 13, and finally connected to the steam pipeline 3 between the main evaporator 1 and the main radiant heat sink 2.

所述主蒸发器1包括主蒸发器液相通道1.1、隔热毛细吸液芯1.2、蒸发毛细吸液芯1.3、周向蒸汽通道1.4、轴向蒸汽通道1.5和外管壁1.6;所述外管壁1.6、蒸发毛细吸液芯1.3和隔热毛细吸液芯1.2两两间均保持过盈配合,主蒸发器液相通道1.1被隔热毛细吸液芯1.2环绕;周向蒸汽通道1.4是外管壁1.6内侧长方形截面的交替分布的环状槽道,轴向蒸汽通道1.5为外管壁1.6和蒸发毛细吸液芯1.3之间的轴向通道,外管壁1.6侧面开孔使得轴向蒸汽通道1.5连通蒸汽管道3;蒸发毛细吸液芯1.3的横截面并不呈现标准的圆环形状,其靠近轴向蒸汽通道1.5的一侧,沿着轴向蒸汽通道1.5在外管壁1.6横截面圆上的两侧端点之间的连线进行切削,以提供更大的轴向蒸汽通流面积。The main evaporator 1 includes a main evaporator liquid phase channel 1.1, an insulating capillary wick 1.2, an evaporative capillary wick 1.3, a circumferential steam channel 1.4, an axial steam channel 1.5 and an outer tube wall 1.6; the outer tube wall 1.6. The tube wall 1.6, the evaporative capillary wick 1.3 and the insulating capillary wick 1.2 all maintain an interference fit, and the main evaporator liquid phase channel 1.1 is surrounded by the insulating capillary wick 1.2; the circumferential steam channel 1.4 is Alternately distributed annular channels with rectangular sections inside the outer tube wall 1.6, the axial steam channel 1.5 is the axial channel between the outer tube wall 1.6 and the evaporative capillary wick 1.3, and the side openings of the outer tube wall 1.6 make the axial The steam channel 1.5 is connected to the steam channel 3; the cross section of the evaporative capillary wick 1.3 does not present a standard annular shape, it is close to one side of the axial steam channel 1.5, and the cross section of the outer tube wall 1.6 along the axial steam channel 1.5 The connecting line between the two end points on the circle is cut to provide a larger axial steam flow area.

所述主蒸发器1的毛细吸液芯采用分层结构,体现在吸液芯材料上不同,蒸发毛细吸液芯1.3采用铜或铝或镍导热性好的的材料的粉末烧结金属或者泡沫金属结构,隔热毛细吸液芯1.2采用导热性差的陶瓷颗粒或者塑料颗粒的烧结吸液芯。The capillary wick of the main evaporator 1 adopts a layered structure, which is reflected in the different wick materials. The evaporation capillary wick 1.3 is made of powder sintered metal or foamed metal of materials with good thermal conductivity of copper, aluminum or nickel. Structure, heat-insulating capillary wick 1.2 adopts sintered wick of ceramic particles or plastic particles with poor thermal conductivity.

所述主蒸发器1的毛细吸液芯采用分层结构,体现在吸液芯当量孔径上不同,蒸发毛细吸液芯1.3的当量孔径在1~100微米范围内,隔热毛细吸液芯1.2的当量孔径等于或者大于蒸发吸液芯结构,且蒸发毛细吸液芯1.3当量孔径必须满足:The capillary wick of the main evaporator 1 adopts a layered structure, which is reflected in the difference in the equivalent pore size of the wick. The equivalent pore size of the evaporative wick is equal to or greater than that of the evaporative wick structure, and the 1.3 equivalent pore size of the evaporative capillary wick must meet:

Figure BDA0001843733290000041
Figure BDA0001843733290000041

Δp表示设计传热功率下的全程管道压损,σ表示液相工质在工作温度下的表面张力,d表示蒸发吸液芯的当量孔径。Δp represents the entire pipeline pressure loss under the design heat transfer power, σ represents the surface tension of the liquid working medium at the working temperature, and d represents the equivalent pore diameter of the evaporative wick.

所述辅助蒸发器5采用单一种类的毛细吸液芯,该毛细吸液芯由导热性差的陶瓷颗粒或者耐高温塑料颗粒烧结而成,辅助蒸发器5的毛细吸液芯的当量孔径小于或等于主蒸发器1的蒸发毛细吸液芯1.3的当量孔径。The auxiliary evaporator 5 adopts a single type of capillary wick, which is sintered from ceramic particles with poor thermal conductivity or high temperature resistant plastic particles, and the equivalent aperture of the capillary wick of the auxiliary evaporator 5 is less than or equal to Equivalent aperture of the evaporation capillary wick 1.3 of the main evaporator 1.

所述主辐射散热板2的材料选择铝、钛等金属,其外表面进行进行刷漆和镀层,以达到设定工作温度下的高发射率和对太阳能的低吸收比。The material of the main radiation radiating plate 2 is selected from metals such as aluminum and titanium, and its outer surface is painted and plated to achieve high emissivity and low solar energy absorption ratio at the set working temperature.

所述储液室7完全由液相工质充满,并保持一定过冷度。The liquid storage chamber 7 is completely filled with liquid-phase working medium and maintains a certain degree of subcooling.

所述调节室8内的工质始终保持两相共存的状态,其内安装主动控温装置,通过热量输入控制调节室8的压强和体积,从而控制储液室7中液相工质的体积,进而控制工作回路中的工质质量和工作压强,对整个回路的工况起到调节作用。The working medium in the adjustment chamber 8 always maintains the state of two-phase coexistence, and an active temperature control device is installed in it to control the pressure and volume of the adjustment chamber 8 through heat input, thereby controlling the volume of the liquid-phase working medium in the liquid storage chamber 7 , and then control the working medium quality and working pressure in the working loop, and play a regulating role on the working conditions of the entire loop.

所述蒸汽通道3和液相通道4均为内壁光滑的圆形截面管道,具体直径根据需要进行调整The steam passage 3 and the liquid phase passage 4 are both circular-section pipes with smooth inner walls, and the specific diameters can be adjusted as required.

所述具备外空间工作能力的毛细泵回路热管的工作方法:启动之初,打开主液相管道阀门11,调节室8输入热量,体积膨胀,推动绝热隔板9向储液室7端移动,推动液相工质进入辅助蒸发器5和液相通道4,工质注入的体积量使液相工质能够充满整个主蒸发器1和液相通道4;注液完成后,打开主蒸汽阀门12和辅助蒸汽阀门13,并向辅助蒸发器5输入热量,稳定运行预设时间后,主蒸发器1的周向蒸汽通道1.4和轴向蒸汽通道1.5内的液体会被重新排挤进入液相通道4;之后,再向主蒸发器1内输入热量,这样就能够做到主蒸发器1的稳定启动;The working method of the capillary pump loop heat pipe with the ability to work in outer space: at the beginning of startup, open the valve 11 of the main liquid phase pipeline, input heat into the adjustment chamber 8, expand the volume, and push the insulating baffle 9 to move toward the end of the liquid storage chamber 7, Push the liquid-phase working medium into the auxiliary evaporator 5 and the liquid-phase channel 4, and the volume of the working medium injected enables the liquid-phase working medium to fill the entire main evaporator 1 and the liquid-phase channel 4; after the liquid injection is completed, open the main steam valve 12 and the auxiliary steam valve 13, and input heat to the auxiliary evaporator 5. After stable operation for a preset time, the liquid in the circumferential steam passage 1.4 and the axial steam passage 1.5 of the main evaporator 1 will be re-displaced into the liquid phase passage 4. ; After that, input heat into the main evaporator 1, so that the stable startup of the main evaporator 1 can be achieved;

稳态运行时:液相工质从主蒸发器液相管道1.1进入主蒸发器1,大部分液相工质转化成蒸汽并带走大量热量,蒸汽通过周向蒸汽通道1.4汇集于轴向蒸汽通道1.5,最终从主蒸发器1的侧面进入蒸汽管道3;蒸汽由蒸汽管道3到达布置在外空间中的主辐射散热板2,在前进过程中逐渐冷凝并将汽化潜热释放,在最终离开主辐射散热板2并进入液相管道4时保持一定程度的过冷;由于辅助蒸发器5内毛细吸液芯的抽吸作用,进入主蒸发器1的另一小部分液相工质将裹挟着主蒸发器1漏热产生的气泡进入辅助辐射散热板6,在这里蒸汽将重新转变成纯液相状态。During steady state operation: the liquid-phase working medium enters the main evaporator 1 from the liquid-phase pipeline 1.1 of the main evaporator, most of the liquid-phase working medium is converted into steam and takes away a lot of heat, and the steam is collected in the axial steam through the circumferential steam channel 1.4. Passage 1.5, and finally enters the steam pipe 3 from the side of the main evaporator 1; the steam reaches the main radiant heat sink 2 arranged in the outer space from the steam pipe 3, gradually condenses and releases the latent heat of vaporization in the process of advancing, and finally leaves the main radiant When the cooling plate 2 enters the liquid phase pipeline 4, it maintains a certain degree of subcooling; due to the suction effect of the capillary wick in the auxiliary evaporator 5, another small part of the liquid phase working medium entering the main evaporator 1 will be wrapped around the main evaporator. The air bubbles generated by the heat leakage of the evaporator 1 enter the auxiliary radiation radiating plate 6, where the steam will be transformed into a pure liquid phase again.

本发明中所提出的毛细泵热管结构的突出优点在于:The outstanding advantages of the capillary pump heat pipe structure proposed in the present invention are:

1.动力上,采用毛细吸液芯作为克服流动阻力的动力来源,可以不借助重力和外部机械力,因此适用于外空间的失重环境。能量上,采用主辐射散热板2作为散热原件,适用于外空间的无空气环境。两者相互搭配,使本结构具备外空间工作能力。1. In terms of power, the capillary wick is used as the power source to overcome the flow resistance, which can not rely on gravity and external mechanical force, so it is suitable for the weightless environment of outer space. In terms of energy, the main radiation heat dissipation plate 2 is used as the heat dissipation element, which is suitable for the airless environment of the outer space. The combination of the two makes the structure have the ability to work in outer space.

2.对主蒸发器1的毛细吸液芯进行分层,从而同时满足毛细吸液芯对导热,隔热,提供高毛细力,保持高渗透率这几种功能性要求。进一步体现在两方面:一方面是材料的不同,一方面是当量孔径不同。蒸发毛细吸液芯1.3,采用高导热性的金属材料和小孔隙率孔径,目的在于扩大有效蒸发范围,降低导热热阻,提供高毛细力。隔热毛细吸液芯1.2,采用低导热性非金属材料和较大孔隙率孔径,目的在于防止热量渗透到液相通道,防止主蒸发器液相通道1.1内的工质发生汽化,并降低液体流动阻力,保持高渗透率。2. Layer the capillary wick of the main evaporator 1 to meet the functional requirements of the capillary wick for heat conduction, heat insulation, providing high capillary force and maintaining high permeability. It is further reflected in two aspects: on the one hand, the material is different, and on the other hand, the equivalent pore size is different. Evaporation capillary wick 1.3 adopts metal material with high thermal conductivity and small porosity aperture, the purpose is to expand the effective evaporation range, reduce the thermal resistance of heat conduction, and provide high capillary force. The heat-insulating capillary wick 1.2 is made of non-metallic materials with low thermal conductivity and large porosity. The purpose is to prevent heat from penetrating into the liquid phase channel, prevent the vaporization of the working fluid in the liquid phase channel 1.1 of the main evaporator, and reduce the liquid Flow resistance to maintain high permeability.

3.通过辅助蒸发器5和辅助辐射散热板6解决漏热问题。主蒸发器1的没有成为液相工质路径的终点,后面跟着设立了辅助辐射散热板6和辅助蒸发器5,即便主蒸发器1内的液相通道1.1发生漏热,产生气泡,由于辅助蒸发器5的抽吸作用,气泡不会堆积在主蒸发器1内,而会进一步前进到达辅助辐射散热板6,重新凝结,最终进入辅助蒸发器5。3. Solve the problem of heat leakage through the auxiliary evaporator 5 and the auxiliary radiant heat dissipation plate 6 . The main evaporator 1 does not become the end point of the liquid phase working medium path, and is followed by an auxiliary radiation heat sink 6 and an auxiliary evaporator 5. Even if the liquid phase channel 1.1 in the main evaporator 1 leaks heat and generates bubbles, due to the auxiliary Due to the suction effect of the evaporator 5 , the air bubbles will not accumulate in the main evaporator 1 , but will further advance to the auxiliary radiant heat sink 6 , re-condensed, and finally enter the auxiliary evaporator 5 .

4.通过辅助蒸发器5优化了启动性能。在启动之初,辅助蒸发器5先进行工作,产生蒸汽,由于主蒸发器1和辅助蒸发器5的蒸汽管道3相通,辅助蒸发器5产生的蒸汽能够起到排挤作用,从而将主蒸发器1的周向蒸汽通道和1.4轴向蒸汽通道1.5内的液相工质清除,有利于实现主蒸发器1的平稳启动。4. The start-up performance is optimized by the auxiliary evaporator 5. At the beginning of the startup, the auxiliary evaporator 5 works first to generate steam. Since the main evaporator 1 and the steam pipeline 3 of the auxiliary evaporator 5 are connected, the steam generated by the auxiliary evaporator 5 can play a displacement role, so that the main evaporator The liquid-phase working medium in the circumferential steam passage of 1.4 and the axial steam passage 1.5 of 1.4 is removed, which is beneficial to realize the smooth start of the main evaporator 1.

5.将传统的储液室分为了储液室7和调节室8,中间用绝热隔板9隔断,提高了调节的灵敏度并降低了能耗。5. The traditional liquid storage chamber is divided into a liquid storage chamber 7 and an adjustment chamber 8, and the middle is separated by an insulating partition 9, which improves the sensitivity of adjustment and reduces energy consumption.

附图说明Description of drawings

图1为本发明具有空间工作能力的毛细泵回路热管的整体结构图。FIG. 1 is an overall structural diagram of a capillary pump loop heat pipe with space working capability according to the present invention.

图2为本发明中毛细泵回路热管主蒸发器的垂直于轴向方向的截面图。2 is a cross-sectional view perpendicular to the axial direction of the main evaporator of the capillary pump loop heat pipe in the present invention.

图3为本发明中毛细泵回路热管主蒸发器的轴向截面图。3 is an axial cross-sectional view of the main evaporator of the capillary pump loop heat pipe in the present invention.

附图说明:1-主蒸发器,2-主辐射散热板,3-蒸汽管道,4-液相管道,5-辅助蒸发器,6-辅助辐射散热板,7-储液室,8-调节室,9-绝热隔板,10-限位环,11-主液相管道阀们,12-主蒸汽阀门,13-辅助蒸汽阀门。Description of drawings: 1-main evaporator, 2-main radiant heat sink, 3-steam pipeline, 4-liquid phase pipeline, 5-auxiliary evaporator, 6-auxiliary radiant heat sink, 7-liquid storage chamber, 8-adjustment Chamber, 9-insulation baffle, 10-limit ring, 11-main liquid phase pipeline valves, 12-main steam valve, 13-auxiliary steam valve.

1.1-主蒸发器液相通道,1.2-隔热毛细吸液芯,1.3-蒸发毛细吸液芯,1.4-周向蒸汽通道,1.5-轴向蒸汽通道,1.6-外管壁。1.1-Main evaporator liquid phase channel, 1.2-Insulation capillary wick, 1.3-Evaporation capillary wick, 1.4-Circumferential steam channel, 1.5-Axial steam channel, 1.6-Outer tube wall.

具体实施方式Detailed ways

下面结合附图和具体实施方式对本发明作进一步详细说明。The present invention will be further described in detail below with reference to the accompanying drawings and specific embodiments.

如图1所示的该毛细泵回路热管整体结构图;图2所示的主蒸发器的垂直于轴向方向的截面图,图3所示的主蒸发器轴向截面图。Figure 1 shows the overall structure of the capillary pump loop heat pipe; Figure 2 is a cross-sectional view of the main evaporator perpendicular to the axial direction, and Figure 3 is an axial cross-sectional view of the main evaporator.

在图1中,液相工质从主蒸发器液相管道1.1进入主蒸发器1,大部分液相工质转化成蒸汽并带走大量热量,蒸汽通过周向蒸汽通道1.4汇集于轴向蒸汽通道1.5,最终从主蒸发器1的侧面进入蒸汽管道3。蒸汽由蒸汽管道3到达布置在外空间中的主辐射散热板2,在前进过程中逐渐冷凝并将汽化潜热释放,在最终离开主辐射散热板2并进入液相管道4时保持一定程度的过冷。由于辅助蒸发器5内毛细芯的抽吸作用,进入主蒸发器1的另一小部分液相工质将裹挟着主蒸发器1漏热产生的气泡进入辅助辐射散热板6,在这里蒸汽将重新转变成纯液相状态。而传统设计中由于主蒸发器就是液相工质的终点,主蒸发器1漏热产生的气泡会淤积在主蒸发器1的液相通道1.1内,导致传热能力下降,工况不再稳定。In Figure 1, the liquid-phase working medium enters the main evaporator 1 from the liquid-phase pipeline 1.1 of the main evaporator, most of the liquid-phase working medium is converted into steam and takes away a lot of heat, and the steam is collected in the axial steam through the circumferential steam channel 1.4 Channel 1.5, which finally enters the steam pipe 3 from the side of the main evaporator 1. The steam reaches the main radiant heat dissipation plate 2 arranged in the outer space from the steam pipe 3, gradually condenses and releases the latent heat of vaporization in the process of advancing, and maintains a certain degree of subcooling when it finally leaves the main radiation heat dissipation plate 2 and enters the liquid phase pipe 4. . Due to the suction effect of the capillary wick in the auxiliary evaporator 5, another small part of the liquid-phase working medium entering the main evaporator 1 will entrain the air bubbles generated by the heat leakage of the main evaporator 1 and enter the auxiliary radiation radiating plate 6, where the steam will back to the pure liquid phase. In the traditional design, since the main evaporator is the end point of the liquid phase working medium, the bubbles generated by the heat leakage of the main evaporator 1 will accumulate in the liquid phase channel 1.1 of the main evaporator 1, resulting in a decrease in the heat transfer capacity, and the working condition is no longer stable. .

在图1中,启动之初,先打开主液相管道阀门11,调节室8输入热量,调节室内的两相工质体积膨胀,推动绝热隔板9向储液室7端移动,推动液相工质进入辅助蒸发器5和液相通道4,工质注入的体积量使液相工质能够充满整个主蒸发器1和液相通道4。注液完成后,打开主蒸汽阀门12和辅助蒸汽阀门13,并向辅助蒸发器5输入热量,稳定运行一段时间后,主蒸发器1的周向蒸汽通道1.4和轴向蒸汽通道1.5内的液体会被重新排挤进入液相通道4。之后,再向主蒸发器1内输入热量,这样就可以做到主蒸发器1的稳定启动。In Fig. 1, at the beginning of the startup, the valve 11 of the main liquid phase pipeline is opened first, the heat is input to the adjustment chamber 8, the volume of the two-phase working medium in the adjustment chamber expands, the insulating baffle 9 is pushed to the end of the liquid storage chamber 7, and the liquid phase is pushed. The working medium enters the auxiliary evaporator 5 and the liquid phase channel 4 , and the volume of the working medium injected enables the liquid-phase working medium to fill the entire main evaporator 1 and the liquid phase channel 4 . After the liquid injection is completed, open the main steam valve 12 and the auxiliary steam valve 13, and input heat to the auxiliary evaporator 5. After a period of stable operation, the liquid in the circumferential steam passage 1.4 and the axial steam passage 1.5 of the main evaporator 1 will be re-displaced into the liquid phase channel 4 . After that, heat is input into the main evaporator 1, so that the stable startup of the main evaporator 1 can be achieved.

在图1中的辅助蒸发器5,结构上不再要求和主蒸发器一样采用双层毛细吸液芯结构,只采用单层毛细吸液芯结构,在满足毛细抽吸力的前提下材料上优先考虑隔热性能,设计功率上远小于主蒸发器1。In the auxiliary evaporator 5 in Fig. 1, the structure of the auxiliary evaporator 5 is no longer required to adopt the double-layer capillary wick structure as the main evaporator, but only the single-layer capillary wick structure. On the premise of satisfying the capillary suction force Priority is given to thermal insulation performance, and the design power is much smaller than that of the main evaporator 1.

在图2和图3中为主蒸发器1的两个方向的剖面图,液相工质从主蒸发器液相管道1.1进入隔热毛细吸液芯1.2和蒸发毛细吸液芯1.3,在蒸发毛细吸液芯1.3内部汽化,蒸汽进入外管壁1.6上的周向蒸汽通道1.4并汇集于轴向蒸汽通道1.5。蒸发毛细吸液芯1.3采用导热性好的材料,是为了扩大有效蒸发面积,进而降低热阻。之所以采用小当量孔径使因为,毛细抽吸力产生的位置是气相和液相的交界面,当量孔径满足:In Figures 2 and 3, the cross-sectional views of the main evaporator 1 in two directions, the liquid phase working medium enters the insulating capillary wick 1.2 and the evaporation capillary wick 1.3 from the liquid phase pipeline 1.1 of the main evaporator. The inside of the capillary wick 1.3 is vaporized, and the vapor enters the circumferential vapor channel 1.4 on the outer tube wall 1.6 and collects in the axial vapor channel 1.5. Evaporation capillary wick 1.3 is made of materials with good thermal conductivity, in order to expand the effective evaporation area, thereby reducing thermal resistance. The reason why a small equivalent pore size is used is that the position where the capillary suction force is generated is the interface between the gas phase and the liquid phase, and the equivalent pore size satisfies:

Figure BDA0001843733290000091
Figure BDA0001843733290000091

Δp表示设计传热功率下的全程管道压损,σ表示液相工质在工作温度下的表面张力,d表示气液交界面处吸液芯的当量孔径。隔热毛细吸液芯1.2的作用是防止吸液芯向主蒸发器液相通道1.1内导热,一旦隔热毛细吸液芯1.2内侧温度达到主蒸发器液相通道1.1压强下对应的饱和温度,就有可能导致液相工质汽化,即漏热发生,因此需要隔热毛细吸液芯1.2要求良好的隔热性能以减少漏热量。Δp represents the entire pipeline pressure loss under the design heat transfer power, σ represents the surface tension of the liquid working fluid at the working temperature, and d represents the equivalent pore diameter of the liquid-absorbing wick at the gas-liquid interface. The function of the insulating capillary wick 1.2 is to prevent the wick from conducting heat into the liquid phase channel 1.1 of the main evaporator. Once the temperature inside the insulating capillary wick 1.2 reaches the corresponding saturation temperature under the pressure of the liquid channel 1.1 of the main evaporator, It may lead to the vaporization of the liquid phase working medium, that is, heat leakage occurs. Therefore, the heat-insulating capillary wick 1.2 is required to have good heat-insulating properties to reduce heat leakage.

Claims (8)

1. A capillary pump loop heat pipe with outer space working capacity is characterized in that: the system comprises a main evaporator (1), a main radiation heat dissipation plate (2), a steam pipeline (3), a liquid phase pipeline (4), an auxiliary evaporator (5), an auxiliary radiation heat dissipation plate (6), a liquid storage chamber (7), a regulating chamber (8), a heat insulation partition plate (9), a limiting ring (10), a main liquid phase pipeline valve (11), a main steam valve (12) and an auxiliary steam valve (13); the specific connection mode is as follows: one or more main evaporators (1) are connected in parallel when a plurality of main evaporators are used, the side surfaces of one or more main evaporators (1) are provided with holes and are communicated with a steam pipeline (3), a main steam valve (12) is arranged on the steam pipeline close to the side surface hole end of the main evaporator (1), and the other end of the steam pipeline (3) is connected to an inlet of a main radiation heat dissipation plate (2) in an outer space; the outlet of the main radiation heat dissipation plate (2) is connected with a liquid phase pipeline (4); the liquid phase pipeline (4) is connected into a liquid phase channel of the main evaporator from one end of one or more main evaporators (1), and the other end of one or more main evaporators (1) is sequentially connected with the auxiliary radiation heat dissipation plate (6), the auxiliary evaporator (5), the liquid storage chamber (7) and the adjusting chamber (8) through the liquid phase pipeline (4) again; a main liquid phase pipeline valve (11) is arranged at an outlet of one end of the auxiliary evaporator (5) close to the auxiliary radiation cooling plate (6); the liquid storage chamber (7) and the adjusting chamber (8) share one rigid container, a heat insulation partition plate (9) is used as a boundary between the liquid storage chamber (7) and the adjusting chamber (8), a limiting ring (10) is fixedly arranged on the container wall of the liquid storage chamber (7) and the adjusting chamber (8), and the moving range of the heat insulation partition plate (9) is limited by the limiting ring (10); the side opening of the auxiliary evaporator (5) is connected with an auxiliary steam valve (13) and is finally connected into a steam pipeline (3) between the main evaporator (1) and the main radiation heat dissipation plate (2);
the main evaporator (1) comprises a main evaporator liquid phase channel (1.1), a heat insulation capillary liquid absorption core (1.2), an evaporation capillary liquid absorption core (1.3), a circumferential steam channel (1.4), an axial steam channel (1.5) and an outer pipe wall (1.6); interference fit is kept between the outer pipe wall (1.6) and the evaporation capillary wick (1.3), and between the evaporation capillary wick (1.3) and the heat insulation capillary wick (1.2), and the main evaporator liquid phase channel (1.1) is surrounded by the heat insulation capillary wick (1.2); the circumferential steam channel (1.4) is a plurality of annular channels which are arranged on the inner side of the outer pipe wall (1.6) and are axially spaced and uniformly distributed along the main evaporator, two ends of each annular channel are respectively communicated with the axial steam channel (1.5), and the cross section of each annular channel in the axial direction of the main evaporator is rectangular; the axial steam channel (1.5) is an axial channel between the outer tube wall (1.6) and the evaporation capillary wick (1.3), and the lateral surface of the outer tube wall (1.6) is provided with a hole so that the axial steam channel (1.5) is communicated with the steam pipeline (3); the cross section of the evaporation capillary wick (1.3) does not present a standard circular ring shape, one side of the evaporation capillary wick, which is close to the axial steam channel (1.5), is cut along a connecting line between two side end points of the axial steam channel (1.5) on the cross section circle of the outer pipe wall (1.6) so as to provide a larger axial steam through-flow area;
at the beginning of starting, a main liquid phase pipeline valve (11) is opened, heat is input into an adjusting chamber (8), the volume is expanded, a heat insulation partition plate (9) is pushed to move towards the end of a liquid storage chamber (7), liquid phase working media are pushed to enter an auxiliary evaporator (5) and a liquid phase pipeline (4), and the liquid phase working media can fill the whole main evaporator (1) and the whole liquid phase pipeline (4) by the injected volume of the working media; after liquid injection is finished, opening a main steam valve (12) and an auxiliary steam valve (13), inputting heat to an auxiliary evaporator (5), and after stable operation is carried out for a preset time, liquid in a circumferential steam channel (1.4) and an axial steam channel (1.5) of the main evaporator (1) is squeezed again to enter a liquid phase pipeline (4); then, heat is input into the main evaporator (1), so that the stable starting of the main evaporator (1) can be realized.
2. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the capillary liquid absorption cores of the main evaporator (1) are of a layered structure and are different on a liquid absorption core material, the evaporation capillary liquid absorption cores (1.3) are of a powder sintered metal or foam metal structure made of a material with good heat conductivity of copper, aluminum or nickel, and the heat insulation capillary liquid absorption cores (1.2) are made of sintered liquid absorption cores made of ceramic particles or plastic particles with poor heat conductivity.
3. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the capillary wick of main evaporator (1) adopts layered structure, embodies different on imbibition equivalent aperture, and the equivalent aperture of evaporation capillary wick (1.3) is in 1 ~ 100 micron within range, and the equivalent aperture of thermal-insulated capillary wick (1.2) equals or is greater than the equivalent aperture of evaporation capillary wick (1.3), and evaporation capillary wick (1.3) equivalent aperture must satisfy:
Figure FDA0002494521260000031
Δ p represents the whole-process pipeline pressure loss under the designed heat transfer power, σ represents the surface tension of the liquid phase working medium at the working temperature, and d represents the equivalent pore diameter of the evaporation capillary wick (1.3).
4. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the auxiliary evaporator (5) adopts a single capillary liquid absorbing core, the capillary liquid absorbing core is formed by sintering ceramic particles with poor heat conductivity or high-temperature resistant plastic particles, and the equivalent aperture of the capillary liquid absorbing core of the auxiliary evaporator (5) is smaller than or equal to that of the evaporation capillary liquid absorbing core (1.3) of the main evaporator (1).
5. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the main radiation heat dissipation plate (2) is made of aluminum and titanium, and the outer surface of the main radiation heat dissipation plate is painted and coated to achieve high emissivity and low absorption ratio of solar energy at a set working temperature.
6. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the liquid storage chamber (7) is completely filled with a liquid phase working medium and keeps a certain supercooling degree; the working medium in the adjusting chamber (8) is always kept in a two-phase coexistence state, an active temperature control device is arranged in the adjusting chamber, and the pressure and the volume of the adjusting chamber (8) are controlled through heat input, so that the volume of the liquid-phase working medium in the liquid storage chamber (7) is controlled, the quality and the working pressure of the working medium in the working circuit are further controlled, and the working condition of the whole circuit is adjusted.
7. A capillary-pumped loop heat pipe with external space working capability according to claim 1, wherein: the steam pipeline (3) and the liquid phase pipeline (4) are both circular-section pipelines with smooth inner walls, and the specific diameters are adjusted as required.
8. The method of any one of claims 1 to 7 for operating a capillary pump loop heat pipe with external space operation capability:
and (3) steady-state operation: liquid phase working medium enters the main evaporator (1) from a liquid phase channel (1.1) of the main evaporator, most of the liquid phase working medium is converted into steam and takes away a large amount of heat, the steam is collected in an axial steam channel (1.5) through a circumferential steam channel (1.4), and finally enters a steam pipeline (3) from the side surface of the main evaporator (1); the steam reaches a main radiation heat dissipation plate (2) arranged in the outer space from a steam pipeline (3), is gradually condensed and releases latent heat of vaporization in the advancing process, and keeps certain supercooling when finally leaving the main radiation heat dissipation plate (2) and entering a liquid phase pipeline (4); due to the suction effect of the capillary liquid absorption core in the auxiliary evaporator (5), the other small part of liquid-phase working medium entering the main evaporator (1) wraps the bubbles generated by heat leakage of the main evaporator (1) and enters the auxiliary radiation heat dissipation plate (6), and steam is converted into a pure liquid-phase state again.
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CN115507685B (en) * 2022-09-02 2025-05-16 上海格熵航天科技有限公司 A "positive meniscus" capillary wick for high heat flux loop heat pipes

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