WO2011137798A1 - Method and device for heat dissipation - Google Patents

Method and device for heat dissipation Download PDF

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Publication number
WO2011137798A1
WO2011137798A1 PCT/CN2011/074388 CN2011074388W WO2011137798A1 WO 2011137798 A1 WO2011137798 A1 WO 2011137798A1 CN 2011074388 W CN2011074388 W CN 2011074388W WO 2011137798 A1 WO2011137798 A1 WO 2011137798A1
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WO
WIPO (PCT)
Prior art keywords
working medium
heat
exchange module
heat exchange
generating device
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PCT/CN2011/074388
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French (fr)
Chinese (zh)
Inventor
罗朝霞
冯踏青
唐文飞
赵钧
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华为技术有限公司
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Publication of WO2011137798A1 publication Critical patent/WO2011137798A1/en

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    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K7/00Constructional details common to different types of electric apparatus
    • H05K7/20Modifications to facilitate cooling, ventilating, or heating
    • H05K7/2029Modifications to facilitate cooling, ventilating, or heating using a liquid coolant with phase change in electronic enclosures
    • H05K7/20336Heat pipes, e.g. wicks or capillary pumps
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05KPRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K7/00Constructional details common to different types of electric apparatus
    • H05K7/20Modifications to facilitate cooling, ventilating, or heating
    • H05K7/2029Modifications to facilitate cooling, ventilating, or heating using a liquid coolant with phase change in electronic enclosures

Definitions

  • the present invention relates to the field of heat dissipation technologies, and in particular, to a heat dissipation method and device.
  • ASHRAE TC9.9 one of the global computer room thermal management organizations, released the power consumption trend of the equipment room in 2005.
  • the power density of the equipment room increases sharply year by year, the power supply capacity and heat dissipation capacity of the equipment room are difficult to keep up with the power consumption of the equipment. development trend.
  • the design heat dissipation capacity is generally 2 ⁇ 3kW, and the air conditioning utilization efficiency is low due to poor airflow management.
  • the new 8kW or even 20kW high-power equipment enters this traditional equipment room it will bring great challenges to the heat dissipation and power distribution of the equipment room, which may lead to local hot spots or downtime events.
  • the most commonly used liquid cooling system is to control the liquid working medium to absorb the heat of the heat generating equipment between the heating equipment of the machine, and use the driving force to push the liquid working medium that absorbs heat to other places, so that the liquid working medium will dissipate the heat. Go, and then transfer the heat-dissipating liquid working fluid back to the heat generating equipment to absorb the heat, so as to take away the heat of the heat generating equipment.
  • a heat sink comprising:
  • the evaporation end heat exchange module is configured to control the heat generated by the liquid working medium to absorb the heat generated by the heat generating device, and evaporate the liquid working medium into a gas working medium;
  • a condensation end heat exchange module configured to control heat of the cold source absorbing gas working medium, to condense the gas working medium into a liquid working medium;
  • the condensing end heat exchange module is higher in gravity direction than the evaporation end heat exchange module a working fluid circulation loop for introducing the vaporized gaseous working fluid into the condensation end heat exchange module, and recirculating the condensed liquid working fluid into the evaporation end heat exchange module.
  • a method of dissipating heat including:
  • the embodiment of the invention has the following beneficial effects:
  • the heat dissipating device controls the liquid working medium to absorb the heat generated by the heat generating device
  • the liquid working medium is evaporated into a gaseous working medium
  • the gaseous working medium evaporated into the gas is introduced in the direction of gravity.
  • the cold source of the thermal equipment causes the cold source to condense the gaseous working medium into a liquid working medium, and recirculates it into the heat generating device to re-absorb the heat.
  • the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working fluid can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed.
  • the driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
  • FIG. 1 is a schematic structural view of a heat dissipation device according to a first embodiment of the present invention
  • 2 is a schematic structural view of a heat dissipating device according to a second embodiment of the present invention
  • FIG. 3 is a schematic structural view of a heat exchange module of an evaporating end of a heat dissipating device according to a second embodiment of the present invention
  • FIG. 4 is a schematic structural view of a condensation end heat exchange module of a heat dissipation device according to a second embodiment of the present invention.
  • FIG. 5 is a schematic structural view of a heat dissipating device of a second connection mode according to a second embodiment of the present invention.
  • FIG. 6 is a schematic structural view of a heat dissipating device of a third connection mode according to a second embodiment of the present invention.
  • FIG. 7 is a schematic flow chart of a heat dissipation method according to a third embodiment of the present invention.
  • the embodiment of the invention provides a heat dissipating device, which can reduce the heat dissipation of the liquid working medium and the gas working medium between the heat generating device and the cold source, thereby achieving the purpose of dissipating heat of the heat generating device.
  • the corresponding cooling method The details are described below separately.
  • Embodiment 1 is a diagrammatic representation of Embodiment 1:
  • FIG. 1 is a schematic structural diagram of a heat dissipating device according to a first embodiment of the present invention, and the heat dissipating device may include:
  • the evaporation end heat exchange module 11 is used for controlling the heat generated by the liquid working medium to absorb the heat generated by the heat generating device, and evaporating the liquid working medium into a gaseous working medium of the gas.
  • the liquid working medium may be water or other liquid distributed around the heat generating device, and the contact surface of the liquid working medium and the heat generating device is larger, and the faster the heat is absorbed.
  • the condensing end heat exchange module 12 is configured to control the heat of the cold source absorbing gas working medium, and condense the gas working medium into a liquid working medium; wherein the condensing end heat exchange module 12 is higher in the gravity direction than the evaporation end heat exchange module 11 .
  • the cold source is used for cooling and heat absorption, and the heat is automatically turned from the object with high temperature.
  • Objects with low temperature, cold source non-stop cooling to ensure that the temperature is higher than the gas working medium, can absorb the heat of the gas working medium, so that the gas working medium is condensed into a liquid working medium.
  • the cold source may be air conditioner, cold air, chilled water, and the like.
  • Working fluid circulation loop 13 for introducing the vaporized gaseous working fluid into the condensation end heat exchange module 12, and refluxing the condensed liquid working fluid into the evaporation end heat exchange module 11;
  • the working fluid circulation loop 13 is configured to introduce the vaporized gaseous working fluid into the liquid end of the condensation end heat exchange module 12 of the evaporation end heat exchange module 11 in the gravity direction, and to condense the condensation end heat exchange module 12 The mass reflux is introduced into the evaporation end heat exchange module 11 to reabsorb heat.
  • the working fluid circulation loop 13 may be a network of conduits connected between the condensing end heat exchange module 12 and the evaporating end heat exchange module 11.
  • the evaporation end heat exchange module 11 controls the liquid working medium to absorb the heat generated by the heat generating device, and then evaporates the liquid working medium into a gas working medium;
  • the condensation end heat exchange module 12 condenses the gaseous working medium into a liquid working medium and passes through the working medium circulation ring.
  • the road 13 is reflowed and introduced into the heat generating device to re-absorb the heat.
  • the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working medium can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed.
  • the driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
  • Embodiment 2 is a diagrammatic representation of Embodiment 1:
  • FIG. 2 is a schematic diagram of heat dissipation of a machine room according to a second embodiment of the present invention.
  • there are three heat generating devices in the machine room which are a heat generating device 201, a heat generating device 202, and a heat generating device 203.
  • the heat generating device 201, the heat generating device 202, and the heat generating device 203 may be machines that are normally working in the equipment room.
  • the heat sink of the equipment room includes:
  • the evaporation end heat exchange module 21 installed in the heat generating device 201, the evaporation end heat exchange module 22 installed in the heat generating device 202, and the evaporation end heat exchange module 23 installed in the heat generating device 203; wherein, the evaporation end heat exchange module 21 a gas working medium for controlling the liquid medium to absorb the heat generated by the heat generating device 201 and evaporating the liquid working medium into a gas; the evaporation end heat exchange module 22 is for controlling the liquid working medium to absorb the heat generated by the heat generating device 202, and a gas working medium for evaporating a liquid working substance into a gas; an evaporation end heat exchange module 23 The gas working medium for controlling the liquid working medium to absorb the heat generated by the heat generating device 203 and evaporating the liquid working medium into a gas.
  • the heat sink of the equipment room further includes:
  • the condensing end heat exchange module 24 installed in the gravity direction is higher than the evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23.
  • the condensing end heat exchange module 24 is configured to control the heat of the gas working medium generated by the cold source absorption evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23, and condense the gas working medium into a liquid working quality.
  • the cold source may be air conditioner, cold air, chilled water, etc., for cooling and absorbing the heat of the gas working medium to achieve the purpose of condensing gas.
  • the heat sink of the equipment room further includes a working fluid circulation loop 25:
  • the working fluid circulation loop 25 is a pipeline network for the gas working fluid outlet of the evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23 and the gas working fluid inlet of the condensation heat exchange module 24.
  • the gas working medium generated by the evaporation end heat exchange module 21, the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 can be automatically introduced into the condensation heat exchange module 24 for condensation; and, for transferring the evaporation end heat exchange
  • the liquid working medium inlet of the module 21, the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 is connected to the liquid working outlet of the condensing heat exchange module 24, so that the liquid working medium condensed by the condensing heat exchange module 24 is automatically returned to the evaporation.
  • the end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23 re-absorb.
  • the heat sink can also be installed with a common evaporation end heat exchange module for simultaneously controlling the heat generated by the liquid working fluid absorption heat generating device 201, the heat generating device 202, and the heat generating device 203.
  • the liquid working medium is evaporated into a gas working medium of gas, and is introduced into the condensing heat exchange module 24 through the working medium circulation loop 25 for condensation, and the condensed liquid working medium is automatically recirculated and introduced into the common evaporation end heat exchange module, so that the common evaporation end is made.
  • the heat exchange module can control the liquid working medium to re-heat the heat generating device 201, the heat generating device 202, and the heat generating device 203.
  • FIG. 3 is a schematic structural diagram of an evaporation end heat exchange module 21 according to a second embodiment of the present invention.
  • the right side of the evaporation end heat exchange module 21 contacts the heat generating device to absorb heat generated by the heat generating device, and the left side includes a gas working medium outlet and a liquid working medium inlet, and the liquid working medium enters the liquid working medium inlet. After absorbing the heat of the heat generating equipment, it is evaporated into a gas working medium, and the gas working medium is further exported from the gas working medium outlet.
  • the structure diagram of the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 can be similar to the evaporation end heat exchange module 21, which is not repeated in this embodiment.
  • FIG. 4 is a schematic structural diagram of a condensing heat exchange module 24 according to a second embodiment of the present invention.
  • one side of the condensing heat exchange module includes a cold source inlet and a cold source outlet, and the cold source can chill water or cold air, and the cold source circulates from the cold source inlet into the condensing heat exchange module to absorb the gas working medium. The heat flows out of the cold source outlet.
  • the other side of the condensing heat exchange module 24 includes a gas working fluid inlet and a liquid working fluid outlet, and the working fluid circulation loop 24 introduces the gas working fluid generated by the evaporating heat exchange module 21, the evaporating heat exchange module 22, and the evaporating heat exchange module 23.
  • the connection of the road is automatically returned to the evaporative heat exchange module 21, the evaporative heat exchange module 22, and the evaporative heat exchange module 23.
  • Figure 5 is a schematic diagram of the connection of three evaporative heat exchange modules and a condensing heat exchange module; see Figure 6, Figure 6 is a schematic diagram of the connection of three evaporative heat exchange modules and two condensing heat exchange modules.
  • gas working fluid outlet of each evaporating heat exchange module is connected to the gas working fluid inlet of at least one condensing heat exchange module, and at least one liquid working fluid outlet of the condensing heat exchange module is connected to the liquid working medium inlet of the evaporating heat exchange module can.
  • the heat dissipating device of the embodiment controls the liquid working medium to absorb the heat generated by the heat generating device, evaporates the liquid working medium into a gas working substance of the gas, controls the heat of the cold source to absorb the working medium of the gas, and condenses the working medium of the gas into a liquid working medium.
  • the vaporized working fluid is introduced into the cold source with the height difference for condensation, and the condensed liquid working fluid is refluxed and introduced into the low-heating heat generating device, and the gas working fluid is automatically pushed to the high place with the pipeline without the driving force.
  • the condensing equipment, the liquid working medium condensed at a high place does not need driving force, and the height difference can be returned to the heat generating equipment along with the pipeline.
  • the driving process of the driving equipment such as a tribute or a fan is not required in the whole cycle, and the energy consumption is reduced.
  • Embodiment 3 is a diagrammatic representation of Embodiment 3
  • FIG. 7 is a schematic flowchart diagram of a heat dissipation method according to a third embodiment of the present invention.
  • the heat dissipation method may include the following steps: 701. Control a liquid working medium to absorb heat generated by the heat generating device, and evaporate the liquid working medium into a gas working medium of the gas;
  • the gas working medium evaporated in step 701 is introduced into a cold source for condensation, and the position of the cold source is higher than the heat generating device in the direction of gravity;
  • the gaseous working fluid evaporated in step 701 can be introduced through the working fluid circulation loop in a direction of gravity higher than the cold source of the heat generating device.
  • the working cycle can be a pipeline for transporting gaseous working fluid and liquid working fluid; the cold source is air conditioning, chilled water, cold air or refrigerant.
  • step 703 Return the liquid working medium condensed in step 703 to the heat generating device.
  • liquid condensate from step 704 can be recirculated to the heat generating device through a working fluid circulation loop.
  • the liquid working medium is controlled to absorb the heat generated by the heat generating device
  • the liquid working medium is evaporated into a gaseous working medium
  • the gaseous working medium evaporated into the gas is introduced in the direction of gravity.
  • the cold source condenses the gas working medium into a liquid working medium, and returns to the heat generating device to re-absorb the heat.
  • the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working medium can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed.
  • the driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
  • the program may be stored in a computer readable storage medium, and the storage medium may include: U disk, read only memory (ROM), random access memory (RAM), disk or optical disk, etc.

Abstract

A method and device for heat dissipation are provided. The device for heat dissipation includes: an evaporating end heat-exchanging module (11), used for controlling the liquid working medium to absorb the heat generated by a heat-generating device, and for evaporating the liquid working medium to the gas working medium; a condensing end heat-exchanging module (12), higher than the evaporating end heat-exchanging module (11) in the gravity direction, used for controlling a cooling source to absorb the heat of the gas working medium, and for condensing the gas working medium to the liquid working medium; a working medium cycle loop (13), used for introducing the evaporated gas working medium to the condensing end heat-exchanging module (12), and for introducing the condensed liquid working medium to reflux to the evaporating end heat-exchanging module (11). In the present invention, the gas working medium can be introduced to the cooling source for condensing without driving force, and the condensed liquid working medium can also be introduced to reflux to the heat-generating device without driving force. The whole cycle does not need driving force of driving device such as a pump, a fan, and so on, so that the energy consumption for heat dissipation is reduced.

Description

一种散热方法和装置  Heat dissipation method and device
本申请要求于 2010 年 09 月 13 日提交中国专利局、 申请号为 201010281175.6、发明名称为"一种散热方法和装置"的中国专利申请的优先权, 其全部内容通过引用结合在本申请中。  The present application claims priority to Chinese Patent Application No. 2010-10281175.6, entitled "A Heat Dissipation Method and Apparatus", which is incorporated herein by reference.
技术领域 Technical field
本发明涉及散热技术领域, 尤其涉及一种散热方法和装置。  The present invention relates to the field of heat dissipation technologies, and in particular, to a heat dissipation method and device.
背景技术 Background technique
全球机房热管理组织之一 ASHRAE TC9.9曾于 2005年发布了机房的功耗 发展趋势, 随着机房的功耗密度在逐年大幅提升,机房的供电能力和散热能力 难以跟上设备功耗的发展趋势。尤其是传统的存量老机房,设计散热能力一般 也就是单机拒功耗 2 ~ 3kW, 而且由于气流管理不善等原因, 空调利用效率较 低。 当新出现的 8kW甚至 20kW的大功耗设备进入这种传统机房时, 对机房 的散热和配电带来了极大挑战, 可能导致局部热点问题或宕机事件。  ASHRAE TC9.9, one of the global computer room thermal management organizations, released the power consumption trend of the equipment room in 2005. As the power density of the equipment room increases sharply year by year, the power supply capacity and heat dissipation capacity of the equipment room are difficult to keep up with the power consumption of the equipment. development trend. Especially in the traditional storage room, the design heat dissipation capacity is generally 2 ~ 3kW, and the air conditioning utilization efficiency is low due to poor airflow management. When the new 8kW or even 20kW high-power equipment enters this traditional equipment room, it will bring great challenges to the heat dissipation and power distribution of the equipment room, which may lead to local hot spots or downtime events.
近几年伴随云计算的出现, 机房内单机拒功耗成倍数上升至 10KW ~ 30KW, 而且由于云计算本身的特点, 云计算数据中心内常常布置大量的功耗 10KW - 30KW的设备, 也就是机房平均散热能力常常需要达到单机拒 10kW 以上。 这种新的需求催生了新建机房在散热和供电方面的全面升级换代。  In recent years, with the advent of cloud computing, the single-machine power consumption in the equipment room has increased to 10KW ~ 30KW, and due to the characteristics of cloud computing itself, cloud computing data centers often have a large number of devices with power consumption of 10KW - 30KW, that is, The average cooling capacity of the equipment room often needs to reach 10kW or more for a single machine. This new demand has spawned a comprehensive upgrade of the new computer room in terms of heat dissipation and power supply.
除了上述解决散热问题以外,节能减排及经济因素催生机房热管理行业蓬 勃发展的另一个重要原因。 为了解决机房散热问题并实现节能减排的目的,技 术人员提出了液冷, ETNO 2008 年年度报告明确提出了在单机拒功耗大于 10kW或者机房平均功耗大于 10kW时, 应该使用机拒级液冷。  In addition to solving the above-mentioned heat dissipation problems, energy saving and emission reduction and economic factors have another important reason for the booming development of the computer room heat management industry. In order to solve the problem of heat dissipation in the equipment room and achieve energy saving and emission reduction, the technicians proposed liquid cooling. The ETNO 2008 annual report clearly stated that when the single machine rejection power consumption is greater than 10 kW or the average power consumption of the equipment room is greater than 10 kW, the machine rejection liquid should be used. cold.
目前最常用的液冷散热系统为,控制液体工质在机房产热设备间吸收产热 设备的热量, 并利用驱动力将吸收热量的液体工质推送到其他地方,使得液体 工质将热量散去, 又将散去热量的液体工质循环推送回到产热设备来吸收热 量, 从而带走产热设备的热量。  At present, the most commonly used liquid cooling system is to control the liquid working medium to absorb the heat of the heat generating equipment between the heating equipment of the machine, and use the driving force to push the liquid working medium that absorbs heat to other places, so that the liquid working medium will dissipate the heat. Go, and then transfer the heat-dissipating liquid working fluid back to the heat generating equipment to absorb the heat, so as to take away the heat of the heat generating equipment.
发明人在实践中发现, 这些液冷系统在推送吸收热量的液体到其他地方 , 以及将散热的液体工质循环至产热设备时,均需要泵或其他驱动力来驱动液体 工质的循环, 克服循环阻力, 增加了散热的能耗。 发明内容 The inventors have found in practice that these liquid cooling systems require a pump or other driving force to drive the circulation of the liquid working medium when pushing the heat-absorbing liquid to other places and circulating the heat-dissipating liquid working medium to the heat generating device. Overcoming the cyclic resistance increases the energy consumption of heat dissipation. Summary of the invention
本发明实施例中提供了一种散热方法和装置, 用于降低散热的能耗。 一种散热装置, 包括:  In the embodiment of the present invention, a heat dissipation method and device are provided for reducing energy consumption of heat dissipation. A heat sink comprising:
蒸发端换热模块, 用于控制液体工质吸收产热设备产生的热量,将所述液 体工质蒸发为气体的气体工质;  The evaporation end heat exchange module is configured to control the heat generated by the liquid working medium to absorb the heat generated by the heat generating device, and evaporate the liquid working medium into a gas working medium;
冷凝端换热模块, 用于控制冷源吸收气体工质的热量,将所述气体工质冷 凝为液体工质; 所述冷凝端换热模块在重力方向上高于所述蒸发端换热模块; 工质循环环路, 用于将蒸发的气体工质导入所述冷凝端换热模块, 并将冷 凝的液体工质回流导入所述蒸发端换热模块。  a condensation end heat exchange module, configured to control heat of the cold source absorbing gas working medium, to condense the gas working medium into a liquid working medium; the condensing end heat exchange module is higher in gravity direction than the evaporation end heat exchange module a working fluid circulation loop for introducing the vaporized gaseous working fluid into the condensation end heat exchange module, and recirculating the condensed liquid working fluid into the evaporation end heat exchange module.
一种散热方法, 包括:  A method of dissipating heat, including:
控制液体工质吸收产热设备产生的热量,将所述液体工质蒸发为气体的气 体工质;  Controlling the liquid medium to absorb the heat generated by the heat generating device, and evaporating the liquid working medium into a gas working medium;
将蒸发的气体工质导入在重力方向上高于产热设备的冷源;  Introducing the vaporized gaseous working medium in a direction of gravity higher than a cold source of the heat generating device;
控制冷源吸收所述气体工质的热量, 将所述气体工质冷凝为液体工质; 将冷凝的所述液体工质回流至产热设备。  Controlling the heat source to absorb the heat of the gas working medium, condensing the gas working medium into a liquid working medium; and refluxing the condensed liquid working medium to the heat generating device.
与现有的技术相比, 本发明实施例具有如下有益效果:  Compared with the prior art, the embodiment of the invention has the following beneficial effects:
本发明实施例中,散热装置控制液体工质吸收产热设备产生的热量后,将 液体工质蒸发为气体的气体工质,并将蒸发为气体的气体工质导入在重力方向 上高于产热设备的冷源,使得冷源将气体工质冷凝为液体工质, 并回流导入产 热设备重新吸收热量。本发明实施例提供的散热装置中, 气体工质在无需驱动 力的情况下可以导入冷源进行冷凝,而冷凝后的液体工质也无需驱动力即可回 流至产热设备, 整个循环过程无需泵或风机等驱动设备的驱动力, 降低了散热 的能耗。  In the embodiment of the present invention, after the heat dissipating device controls the liquid working medium to absorb the heat generated by the heat generating device, the liquid working medium is evaporated into a gaseous working medium, and the gaseous working medium evaporated into the gas is introduced in the direction of gravity. The cold source of the thermal equipment causes the cold source to condense the gaseous working medium into a liquid working medium, and recirculates it into the heat generating device to re-absorb the heat. In the heat dissipating device provided by the embodiment of the invention, the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working fluid can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed. The driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
附图说明 DRAWINGS
为了更清楚地说明本发明实施例的技术方案,下面将对实施例中所需要使 用的附图作筒单地介绍,显而易见地, 下面描述中的附图仅仅是本发明的一些 实施例, 对于本领域普通技术人员来讲, 在不付出创造性劳动性的前提下, 还 可以根据这些附图获得其他的附图。  In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings used in the embodiments will be briefly described below. Obviously, the drawings in the following description are only some embodiments of the present invention, Those skilled in the art can also obtain other drawings based on these drawings without paying creative labor.
图 1是本发明第一实施例提供的一种散热装置的结构示意图; 图 2是本发明第二实施例提供的一种散热装置的结构示意图; 图 3 是本发明第二实施例提供的一种散热装置的蒸发端换热模块的结构 示意图; 1 is a schematic structural view of a heat dissipation device according to a first embodiment of the present invention; 2 is a schematic structural view of a heat dissipating device according to a second embodiment of the present invention; FIG. 3 is a schematic structural view of a heat exchange module of an evaporating end of a heat dissipating device according to a second embodiment of the present invention;
图 4是本发明第二实施例提供的一种散热装置的冷凝端换热模块的结构 示意图;  4 is a schematic structural view of a condensation end heat exchange module of a heat dissipation device according to a second embodiment of the present invention;
图 5 是本发明第二实施例提供的第二种连接方式的散热装置的结构示意 图;  5 is a schematic structural view of a heat dissipating device of a second connection mode according to a second embodiment of the present invention;
图 6是本发明第二实施例提供的第三种连接方式的散热装置的结构示意 图;  6 is a schematic structural view of a heat dissipating device of a third connection mode according to a second embodiment of the present invention;
图 7是本发明第三实施例提供的一种散热方法的流程示意图。  FIG. 7 is a schematic flow chart of a heat dissipation method according to a third embodiment of the present invention.
具体实施方式 detailed description
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清 楚、 完整地描述, 显然, 所描述的实施例仅仅是本发明一部分实施例, 而不是 全部的实施例。基于本发明中的实施例, 本领域普通技术人员在没有做出创造 性劳动前提下所获得的所有其他实施例, 都属于本发明保护的范围。  BRIEF DESCRIPTION OF THE DRAWINGS The technical solutions in the embodiments of the present invention will be described in detail below with reference to the accompanying drawings. All other embodiments obtained by a person of ordinary skill in the art based on the embodiments of the present invention without the creative work are all within the scope of the present invention.
本发明实施例提供一种散热装置,无需驱动可以使得散热的液体工质和气 体工质在产热设备和冷源之间循环利用,从而达到产热设备散热的目的, 本发 明实施例还提供相应的散热方法。 以下分别进行详细说明。  The embodiment of the invention provides a heat dissipating device, which can reduce the heat dissipation of the liquid working medium and the gas working medium between the heat generating device and the cold source, thereby achieving the purpose of dissipating heat of the heat generating device. The corresponding cooling method. The details are described below separately.
实施例一:  Embodiment 1:
请参见图 1 , 图 1是本发明第一实施例的散热装置的结构示意图, 该散热 装置可以包括:  Referring to FIG. 1 , FIG. 1 is a schematic structural diagram of a heat dissipating device according to a first embodiment of the present invention, and the heat dissipating device may include:
蒸发端换热模块 11 , 用于控制液体工质吸收产热设备产生的热量, 将液 体工质蒸发为气体的气体工质。  The evaporation end heat exchange module 11 is used for controlling the heat generated by the liquid working medium to absorb the heat generated by the heat generating device, and evaporating the liquid working medium into a gaseous working medium of the gas.
本发明实施例中,液体工质可以为水或其他液体,分布于产热设备的四周, 液体工质与产热设备的接触面越大, 吸收热量的速度越快。  In the embodiment of the present invention, the liquid working medium may be water or other liquid distributed around the heat generating device, and the contact surface of the liquid working medium and the heat generating device is larger, and the faster the heat is absorbed.
冷凝端换热模块 12, 用于控制冷源吸收气体工质的热量, 将气体工质冷 凝为液体工质; 其中, 冷凝端换热模块 12在重力方向上高于蒸发端换热模块 11。  The condensing end heat exchange module 12 is configured to control the heat of the cold source absorbing gas working medium, and condense the gas working medium into a liquid working medium; wherein the condensing end heat exchange module 12 is higher in the gravity direction than the evaporation end heat exchange module 11 .
本发明实施例中, 冷源用于制冷和吸热, 热量会从温度高的物体自动转向 温度低的物体, 冷源不停的制冷, 保证温度比气体工质高, 就可以吸收气体工 质的热量, 使得气体工质被冷凝成液体工质。 其中, 冷源与气体工质的接触面 越大, 吸热和冷凝的速度越快; 冷源可以是空调、 冷空气、 冷冻水等。 In the embodiment of the invention, the cold source is used for cooling and heat absorption, and the heat is automatically turned from the object with high temperature. Objects with low temperature, cold source non-stop cooling, to ensure that the temperature is higher than the gas working medium, can absorb the heat of the gas working medium, so that the gas working medium is condensed into a liquid working medium. Among them, the larger the contact surface between the cold source and the gas working medium, the faster the heat absorption and condensation speed; the cold source may be air conditioner, cold air, chilled water, and the like.
工质循环环路 13, 用于将蒸发的气体工质导入冷凝端换热模块 12, 并将 冷凝的液体工质回流导入蒸发端换热模块 11;  Working fluid circulation loop 13, for introducing the vaporized gaseous working fluid into the condensation end heat exchange module 12, and refluxing the condensed liquid working fluid into the evaporation end heat exchange module 11;
也就是说, 工质循环环路 13, 用于将蒸发的气体工质导入重力方向高于 蒸发端换热模块 11的冷凝端换热模块 12, 并将冷凝端换热模块 12冷凝的液 体工质回流导入蒸发端换热模块 11重新吸热。  That is, the working fluid circulation loop 13 is configured to introduce the vaporized gaseous working fluid into the liquid end of the condensation end heat exchange module 12 of the evaporation end heat exchange module 11 in the gravity direction, and to condense the condensation end heat exchange module 12 The mass reflux is introduced into the evaporation end heat exchange module 11 to reabsorb heat.
在一个实施例中,工质循环环路 13可以是连接于冷凝端换热模块 12和蒸 发端换热模块 11之间的管道网络。  In one embodiment, the working fluid circulation loop 13 may be a network of conduits connected between the condensing end heat exchange module 12 and the evaporating end heat exchange module 11.
本发明实施例提供的散热装置中, 蒸发端换热模块 11控制液体工质吸收 产热设备产生的热量后, 将液体工质蒸发为气体的气体工质; 工质循环环路 In the heat dissipation device provided by the embodiment of the present invention, the evaporation end heat exchange module 11 controls the liquid working medium to absorb the heat generated by the heat generating device, and then evaporates the liquid working medium into a gas working medium;
13 将蒸发为气体的气体工质导入在重力方向上高于产热设备的冷凝端换热模 块 12, 使得冷凝端换热模块 12将气体工质冷凝为液体工质, 并通过工质循环 环路 13回流导入产热设备重新吸收热量。 本发明实施例提供的散热装置中, 气体工质在无需驱动力的情况下可以导入冷源进行冷凝,而冷凝后的液体工质 也无需驱动力即可回流至产热设备,整个循环过程无需泵或风机等驱动设备的 驱动力, 降低了散热的能耗。 13 introducing a gas working medium evaporated to a gas in a gravity direction higher than a condensation end heat exchange module 12 of the heat generating device, so that the condensation end heat exchange module 12 condenses the gaseous working medium into a liquid working medium and passes through the working medium circulation ring. The road 13 is reflowed and introduced into the heat generating device to re-absorb the heat. In the heat dissipating device provided by the embodiment of the invention, the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working medium can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed. The driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
实施例二:  Embodiment 2:
请参见图 2, 图 2是本发明第二实施例的机房散热示意图, 如图 2所示, 该机房中有三台产热设备, 分别是产热设备 201、 产热设备 202以及产热设备 203。 其中, 产热设备 201、 产热设备 202以及产热设备 203可以是机房中正 常工作的机拒。  Referring to FIG. 2, FIG. 2 is a schematic diagram of heat dissipation of a machine room according to a second embodiment of the present invention. As shown in FIG. 2, there are three heat generating devices in the machine room, which are a heat generating device 201, a heat generating device 202, and a heat generating device 203. . The heat generating device 201, the heat generating device 202, and the heat generating device 203 may be machines that are normally working in the equipment room.
其中, 该机房的散热装置包括:  The heat sink of the equipment room includes:
安装于产热设备 201的蒸发端换热模块 21、 安装于产热设备 202的蒸发 端换热模块 22以及安装于产热设备 203的蒸发端换热模块 23; 其中, 蒸发端 换热模块 21用于控制液体工质吸收产热设备 201产生的热量, 并将液体工质 蒸发为气体的气体工质; 蒸发端换热模块 22用于控制液体工质吸收产热设备 202产生的热量, 并将液体工质蒸发为气体的气体工质; 蒸发端换热模块 23 用于控制液体工质吸收产热设备 203产生的热量,并将液体工质蒸发为气体的 气体工质。 The evaporation end heat exchange module 21 installed in the heat generating device 201, the evaporation end heat exchange module 22 installed in the heat generating device 202, and the evaporation end heat exchange module 23 installed in the heat generating device 203; wherein, the evaporation end heat exchange module 21 a gas working medium for controlling the liquid medium to absorb the heat generated by the heat generating device 201 and evaporating the liquid working medium into a gas; the evaporation end heat exchange module 22 is for controlling the liquid working medium to absorb the heat generated by the heat generating device 202, and a gas working medium for evaporating a liquid working substance into a gas; an evaporation end heat exchange module 23 The gas working medium for controlling the liquid working medium to absorb the heat generated by the heat generating device 203 and evaporating the liquid working medium into a gas.
其中, 该机房的散热装置还包括:  The heat sink of the equipment room further includes:
重力方向上高于蒸发端换热模块 21、 蒸发端换热模块 22以及蒸发端换热 模块 23安装的冷凝端换热模块 24。 其中, 冷凝端换热模块 24用于控制冷源 吸收蒸发端换热模块 21、 蒸发端换热模块 22以及蒸发端换热模块 23产生的 气体工质的热量, 将气体工质冷凝为液体工质。  The condensing end heat exchange module 24 installed in the gravity direction is higher than the evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23. The condensing end heat exchange module 24 is configured to control the heat of the gas working medium generated by the cold source absorption evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23, and condense the gas working medium into a liquid working quality.
其中, 冷源可以是空调、 冷空气、 冷冻水等, 用于制冷并吸收气体工质的 热量以达到冷凝气体的目的。  Among them, the cold source may be air conditioner, cold air, chilled water, etc., for cooling and absorbing the heat of the gas working medium to achieve the purpose of condensing gas.
其中, 该机房的散热装置还包括工质循环环路 25:  The heat sink of the equipment room further includes a working fluid circulation loop 25:
工质循环环路 25是一个管道网络, 用于将蒸发端换热模块 21、 蒸发端换 热模块 22以及蒸发端换热模块 23的气体工质出口与冷凝换热模块 24的气体 工质入口相连接, 使得蒸发端换热模块 21、 蒸发端换热模块 22以及蒸发端换 热模块 23产生的气体工质能够自动导入到冷凝换热模块 24进行冷凝; 以及, 用于将蒸发端换热模块 21、 蒸发端换热模块 22以及蒸发端换热模块 23的液 体工质入口与冷凝换热模块 24的液体工质出口相连接, 使得冷凝换热模块 24 冷凝的液体工质自动回流至蒸发端换热模块 21、 蒸发端换热模块 22以及蒸发 端换热模块 23重新吸热。  The working fluid circulation loop 25 is a pipeline network for the gas working fluid outlet of the evaporation end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23 and the gas working fluid inlet of the condensation heat exchange module 24. Connected, the gas working medium generated by the evaporation end heat exchange module 21, the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 can be automatically introduced into the condensation heat exchange module 24 for condensation; and, for transferring the evaporation end heat exchange The liquid working medium inlet of the module 21, the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 is connected to the liquid working outlet of the condensing heat exchange module 24, so that the liquid working medium condensed by the condensing heat exchange module 24 is automatically returned to the evaporation. The end heat exchange module 21, the evaporation end heat exchange module 22, and the evaporation end heat exchange module 23 re-absorb.
如图 2所示的机房中, 散热装置也可以安装一个公共的蒸发端换热模块, 用于同时控制液体工质吸收产热设备 201、 产热设备 202以及产热设备 203产 生的热量, 将液体工质蒸发为气体的气体工质, 并通过工质循环环路 25导入 冷凝换热模块 24进行冷凝, 冷凝后的液体工质自动回流导入公共的蒸发端换 热模块, 使得公共的蒸发端换热模块可以控制液体工质重新对产热设备 201、 产热设备 202以及产热设备 203进行吸热。  In the equipment room shown in Figure 2, the heat sink can also be installed with a common evaporation end heat exchange module for simultaneously controlling the heat generated by the liquid working fluid absorption heat generating device 201, the heat generating device 202, and the heat generating device 203. The liquid working medium is evaporated into a gas working medium of gas, and is introduced into the condensing heat exchange module 24 through the working medium circulation loop 25 for condensation, and the condensed liquid working medium is automatically recirculated and introduced into the common evaporation end heat exchange module, so that the common evaporation end is made. The heat exchange module can control the liquid working medium to re-heat the heat generating device 201, the heat generating device 202, and the heat generating device 203.
请参见图 3 , 图 3是本发明第二实施例提供的一种蒸发端换热模块 21的 结构示意图。 如图 3所示, 该蒸发端换热模块 21的右边接触产热设备, 吸收 产热设备产生的热量, 左边包括一个气体工质出口和一个液体工质入口, 液体 工质进入液体工质入口, 吸收产热设备的热量后, 蒸发为气体工质, 气体工质 再从气体工质出口导出。 由于有源源不断的液体工质回流至蒸发换热模块, 这 些液体工质不停的被蒸发为气体工质, 气体工质增多, 体积增大, 会自动被压 送到出口, 从而根据循环环路的连接, 无需驱动力到达冷凝换热模块 24。 Referring to FIG. 3, FIG. 3 is a schematic structural diagram of an evaporation end heat exchange module 21 according to a second embodiment of the present invention. As shown in FIG. 3, the right side of the evaporation end heat exchange module 21 contacts the heat generating device to absorb heat generated by the heat generating device, and the left side includes a gas working medium outlet and a liquid working medium inlet, and the liquid working medium enters the liquid working medium inlet. After absorbing the heat of the heat generating equipment, it is evaporated into a gas working medium, and the gas working medium is further exported from the gas working medium outlet. Since the continuous flow of liquid working fluid is returned to the evaporative heat exchange module, this The liquid working fluid is continuously evaporated into a gaseous working medium, the working medium is increased in volume, and the volume is increased, and is automatically pressed to the outlet, so that no driving force is required to reach the condensing heat exchange module 24 according to the connection of the circulation loop.
其中,蒸发端换热模块 22和蒸发端换热模块 23的结构示意图可以类似于 蒸发端换热模块 21 , 本实施例不作复述。  The structure diagram of the evaporation end heat exchange module 22 and the evaporation end heat exchange module 23 can be similar to the evaporation end heat exchange module 21, which is not repeated in this embodiment.
请参见图 4, 图 4是本发明第二实施例提供的一种冷凝换热模块 24的结 构示意图。 如图 4所示, 该冷凝换热模块的一面包括冷源入口和冷源出口, 冷 源可以冷冻水或冷空气, 冷源循环地从冷源入口流入冷凝换热模块, 吸收了气 体工质的热量并从冷源出口流出。 该冷凝换热模块 24的另一面包括气体工质 入口和液体工质出口, 工质循环环路 24将蒸发换热模块 21、 蒸发换热模块 22 以及蒸发换热模块 23产生的气体工质导入冷凝换热模块 24的气体工质入口, 随着冷源将气体工质的热量带走, 气体工质被冷凝为液体工质, 液体工质从液 体工质出口流出, 随着工质循环环路的连接, 自动回流至蒸发换热模块 21、 蒸发换热模块 22以及蒸发换热模块 23。  Referring to FIG. 4, FIG. 4 is a schematic structural diagram of a condensing heat exchange module 24 according to a second embodiment of the present invention. As shown in FIG. 4, one side of the condensing heat exchange module includes a cold source inlet and a cold source outlet, and the cold source can chill water or cold air, and the cold source circulates from the cold source inlet into the condensing heat exchange module to absorb the gas working medium. The heat flows out of the cold source outlet. The other side of the condensing heat exchange module 24 includes a gas working fluid inlet and a liquid working fluid outlet, and the working fluid circulation loop 24 introduces the gas working fluid generated by the evaporating heat exchange module 21, the evaporating heat exchange module 22, and the evaporating heat exchange module 23. The gas working inlet of the condensing heat exchange module 24, with the heat source of the gas working medium taken away, the gas working medium is condensed into a liquid working medium, and the liquid working medium flows out from the liquid working medium outlet, with the working medium circulation ring The connection of the road is automatically returned to the evaporative heat exchange module 21, the evaporative heat exchange module 22, and the evaporative heat exchange module 23.
本实施例中,根据蒸发换热模块和冷凝换热模块的数量不同, 工质循环环 路的管道网络连接也不相同。 请参见图 5 , 图 5是三个蒸发换热模块和一个冷 凝换热模块的连接示意图; 请参见图 6, 图 6是三个蒸发换热模块和两个冷凝 换热模块的连接示意图。只要保证各个蒸发换热模块的气体工质出口连接至少 一个冷凝换热模块的气体工质入口,且至少有一个冷凝换热模块的液体工质出 口连接于蒸发换热模块的液体工质入口即可。  In this embodiment, according to the number of the evaporative heat exchange module and the condensing heat exchange module, the pipeline network connection of the working fluid circulation loop is also different. Referring to Figure 5, Figure 5 is a schematic diagram of the connection of three evaporative heat exchange modules and a condensing heat exchange module; see Figure 6, Figure 6 is a schematic diagram of the connection of three evaporative heat exchange modules and two condensing heat exchange modules. As long as the gas working fluid outlet of each evaporating heat exchange module is connected to the gas working fluid inlet of at least one condensing heat exchange module, and at least one liquid working fluid outlet of the condensing heat exchange module is connected to the liquid working medium inlet of the evaporating heat exchange module can.
本实施例的散热装置控制液体工质吸收产热设备产生的热量,将液体工质 蒸发为气体的气体工质,控制冷源吸收气体工质的热量,将气体工质冷凝为液 体工质,从而实现了将蒸发的气体工质导入具有高度差的冷源进行冷凝, 又将 冷凝的液体工质回流导入高度低的产热设备,气体工质无需驱动力就自动随管 道被推送到高处冷凝设备,在高处冷凝的液体工质无需驱动力, 利用高度差又 可随管道回流至产热设备, 整个循环过程无需贡或风机等驱动设备的驱动力, 降低了能耗。  The heat dissipating device of the embodiment controls the liquid working medium to absorb the heat generated by the heat generating device, evaporates the liquid working medium into a gas working substance of the gas, controls the heat of the cold source to absorb the working medium of the gas, and condenses the working medium of the gas into a liquid working medium. Thereby, the vaporized working fluid is introduced into the cold source with the height difference for condensation, and the condensed liquid working fluid is refluxed and introduced into the low-heating heat generating device, and the gas working fluid is automatically pushed to the high place with the pipeline without the driving force. The condensing equipment, the liquid working medium condensed at a high place does not need driving force, and the height difference can be returned to the heat generating equipment along with the pipeline. The driving process of the driving equipment such as a tribute or a fan is not required in the whole cycle, and the energy consumption is reduced.
实施例三:  Embodiment 3:
请参见图 7,图 7是本发明第三实施例提供的一种散热方法的流程示意图。 其中, 该散热方法可以包括以下步骤: 701、 控制液体工质吸收产热设备产生的热量, 将液体工质蒸发为气体的 气体工质; Referring to FIG. 7, FIG. 7 is a schematic flowchart diagram of a heat dissipation method according to a third embodiment of the present invention. The heat dissipation method may include the following steps: 701. Control a liquid working medium to absorb heat generated by the heat generating device, and evaporate the liquid working medium into a gas working medium of the gas;
702、 将步骤 701蒸发的气体工质导入冷源进行冷凝, 该冷源的位置在重 力方向上高于产热设备;  702. The gas working medium evaporated in step 701 is introduced into a cold source for condensation, and the position of the cold source is higher than the heat generating device in the direction of gravity;
举例来说,可以通过工质循环环路将步骤 701蒸发的气体工质导入在重力 方向上高于产热设备的冷源。其中, 工质循环环路可以是运输气体工质和液体 工质的管道; 冷源为空调、 冷冻水、 冷空气或制冷剂。  For example, the gaseous working fluid evaporated in step 701 can be introduced through the working fluid circulation loop in a direction of gravity higher than the cold source of the heat generating device. Wherein, the working cycle can be a pipeline for transporting gaseous working fluid and liquid working fluid; the cold source is air conditioning, chilled water, cold air or refrigerant.
703、 控制冷源吸收气体工质的热量, 将气体工质冷凝为液体工质; 703. Control the heat of the cold source to absorb the working fluid of the gas, and condense the gaseous working medium into a liquid working medium;
704、 将步骤 703冷凝的液体工质回流至产热设备。 704. Return the liquid working medium condensed in step 703 to the heat generating device.
举例来说,可以通过工质循环环路将步骤 704冷凝的液体工质回流至产热 设备。  For example, the liquid condensate from step 704 can be recirculated to the heat generating device through a working fluid circulation loop.
本实施例三提供的散热方法中, 控制液体工质吸收产热设备产生的热量 后,将液体工质蒸发为气体的气体工质, 并将蒸发为气体的气体工质导入在重 力方向上高于产热设备的冷源,使得冷源将气体工质冷凝为液体工质, 并回流 导入产热设备重新吸收热量。本发明实施例提供的散热方法中, 气体工质在无 需驱动力的情况下可以导入冷源进行冷凝,而冷凝后的液体工质也无需驱动力 即可回流至产热设备, 整个循环过程无需泵或风机等驱动设备的驱动力, 降低 了散热的能耗。  In the heat dissipation method provided in the third embodiment, after the liquid working medium is controlled to absorb the heat generated by the heat generating device, the liquid working medium is evaporated into a gaseous working medium, and the gaseous working medium evaporated into the gas is introduced in the direction of gravity. In the cold source of the heat generating equipment, the cold source condenses the gas working medium into a liquid working medium, and returns to the heat generating device to re-absorb the heat. In the heat dissipation method provided by the embodiment of the invention, the gas working medium can be introduced into the cold source for condensation without the driving force, and the condensed liquid working medium can be returned to the heat generating device without the driving force, and the whole cycle process does not need to be performed. The driving force of driving equipment such as pumps or fans reduces the energy consumption of heat dissipation.
本领域普通技术人员可以理解上述实施例的各种方法中的全部或部分步 骤是可以通过程序来指令相关的硬件来完成,该程序可以存储于一计算机可读 存储介质中, 存储介质可以包括: U盘、 只读存储器(ROM )、 随机存取器 ( RAM )、 磁盘或光盘等。  A person skilled in the art may understand that all or part of the various steps of the foregoing embodiments may be completed by a program instructing related hardware. The program may be stored in a computer readable storage medium, and the storage medium may include: U disk, read only memory (ROM), random access memory (RAM), disk or optical disk, etc.
以上对本发明实施例所提供的一种散热方法和装置进行了详细介绍,本文 中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明 只是用于帮助理解本发明的方法及其核心思想; 同时,对于本领域的一般技术 人员, 依据本发明的思想, 在具体实施方式及应用范围上均会有改变之处, 综 上, 本说明书内容不应理解为对本发明的限制。  The heat dissipation method and device provided by the embodiments of the present invention are described in detail above. The principles and embodiments of the present invention are described in the following. The description of the above embodiments is only for helping to understand the present invention. The method and its core idea; at the same time, those skilled in the art, according to the idea of the present invention, there will be changes in the specific embodiments and application scope. In summary, the content of the specification should not be construed as being limit.

Claims

权 利 要 求 Rights request
1、 一种散热装置, 其特征在于, 包括:  A heat dissipation device, comprising:
蒸发端换热模块,用于控制液体工质吸收产热设备产生的热量,将所述液 体工质蒸发为气体的气体工质;  The evaporation end heat exchange module is configured to control the heat generated by the liquid working medium to absorb the heat generated by the heat generating device, and evaporate the liquid working medium into a gas working medium;
冷凝端换热模块,用于控制冷源吸收气体工质的热量,将所述气体工质冷 凝为液体工质; 所述冷凝端换热模块在重力方向上高于所述蒸发端换热模块; 工质循环环路, 用于将蒸发的气体工质导入所述冷凝端换热模块, 并将冷 凝的液体工质回流导入所述蒸发端换热模块。  a condensation end heat exchange module, configured to control heat of the cold source absorbing gas working medium, to condense the gas working medium into a liquid working medium; the condensing end heat exchange module is higher in gravity direction than the evaporation end heat exchange module a working fluid circulation loop for introducing the vaporized gaseous working fluid into the condensation end heat exchange module, and recirculating the condensed liquid working fluid into the evaporation end heat exchange module.
2、如权利要求 1所述的散热装置,其特征在于,所述冷源为空调、冷冻水、 冷空气或制冷剂。  The heat sink according to claim 1, wherein the cold source is an air conditioner, chilled water, cold air or a refrigerant.
3、 如权利要求 1所述的散热装置, 其特征在于, 所述蒸发端换热模块中的 液体工质分布于散热装置的四周。  3. The heat dissipation device according to claim 1, wherein the liquid working medium in the evaporation end heat exchange module is distributed around the heat dissipation device.
4、 如权利要求 1所述的散热装置, 其特征在于, 所述工质循环环路是运输 气体工质和液体工质的管道。  4. The heat sink according to claim 1, wherein the working fluid circulation loop is a conduit for transporting a gaseous working fluid and a liquid working fluid.
5、 一种散热方法, 其特征在于, 包括:  5. A method of dissipating heat, characterized in that it comprises:
控制液体工质吸收产热设备产生的热量,将所述液体工质蒸发为气体的气 体工质;  Controlling the liquid medium to absorb the heat generated by the heat generating device, and evaporating the liquid working medium into a gas working medium;
将蒸发的气体工质导入在重力方向上高于产热设备的冷源;  Introducing the vaporized gaseous working medium in a direction of gravity higher than a cold source of the heat generating device;
控制冷源吸收所述气体工质的热量, 将所述气体工质冷凝为液体工质; 将冷凝的所述液体工质回流至产热设备。  Controlling the heat source to absorb the heat of the gas working medium, condensing the gas working medium into a liquid working medium; and refluxing the condensed liquid working medium to the heat generating device.
6、 如权利要求 5所述的散热方法, 其特征在于, 所述将蒸发的气体工质导 入在重力方向上高于产热设备的冷源包括:  The heat dissipation method according to claim 5, wherein the introducing the vaporized gaseous working medium into the cold source in the direction of gravity higher than the heat generating device comprises:
通过工质循环环路将蒸发的气体工质导入在重力方向上高于产热设备的 冷源。  The vaporized gaseous working fluid is introduced into the cold source of the heat generating device by the working medium circulation loop in the direction of gravity.
7、 如权利要求 5所述的散热方法, 其特征在于, 所述将冷凝的所述液体工 质回流至产热设备包括:  7. The heat dissipation method according to claim 5, wherein the returning the condensed liquid working material to the heat generating device comprises:
通过工质循环环路将冷凝的所述液体工质回流至产热设备。  The condensed liquid working fluid is returned to the heat generating device through a working fluid circulation loop.
8、 如权利要求 5~7任意一项所述的散热方法, 其特征在于, 所述冷源为 空调、 冷冻水、 冷空气或制冷剂。  The heat dissipation method according to any one of claims 5 to 7, wherein the cold source is an air conditioner, chilled water, cold air or a refrigerant.
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