CN1192202C - Flat-plate loop heat pipe (1) - Google Patents
Flat-plate loop heat pipe (1) Download PDFInfo
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- CN1192202C CN1192202C CNB011311983A CN01131198A CN1192202C CN 1192202 C CN1192202 C CN 1192202C CN B011311983 A CNB011311983 A CN B011311983A CN 01131198 A CN01131198 A CN 01131198A CN 1192202 C CN1192202 C CN 1192202C
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- 239000012530 fluid Substances 0.000 claims abstract description 64
- 239000007788 liquid Substances 0.000 claims abstract description 44
- 238000001704 evaporation Methods 0.000 claims abstract description 39
- 230000008020 evaporation Effects 0.000 claims abstract description 39
- 238000009833 condensation Methods 0.000 claims abstract description 29
- 230000005494 condensation Effects 0.000 claims abstract description 29
- 125000006850 spacer group Chemical group 0.000 claims description 20
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- 239000000835 fiber Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims 1
- 238000012546 transfer Methods 0.000 description 16
- 230000017525 heat dissipation Effects 0.000 description 6
- 238000005192 partition Methods 0.000 description 6
- 238000007872 degassing Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0233—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes the conduits having a particular shape, e.g. non-circular cross-section, annular
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0266—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers
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Abstract
Description
技术领域technical field
本发明属于一种平板式环路型热管,特别是涉及一种热传量大、均温性佳,且对于存在板状热管内的非凝结性气体对回路系统特性影响不大的热交换结构。The invention belongs to a flat plate loop heat pipe, in particular to a heat exchange structure with large heat transfer, good temperature uniformity, and little influence on the characteristics of the loop system for the non-condensable gas existing in the plate heat pipe.
背景技术Background technique
现有的热管,由于具有相当好的热传递性,已被广泛地应用于电子组件的散热组件,通常热管式的散热组件,具有一热管1,于电子组件端设有一导热块11,导热块11与热管1的一端相接,热管1的另一端能经另一导热块与热交换装置相接,或是热管1另一端直接夹设有数个散热鳍片12,在图1中所示的,即是散热鳍片12式的热管。Existing heat pipes have been widely used in heat dissipation components of electronic components due to their relatively good heat transfer properties. Usually, heat pipe-type heat dissipation components have a heat pipe 1 and a heat conducting block 11 at the end of the electronic component. The heat conducting block 11 is connected to one end of the heat pipe 1, and the other end of the heat pipe 1 can be connected to the heat exchange device through another heat conduction block, or the other end of the heat pipe 1 is directly sandwiched with several cooling fins 12, as shown in Fig. 1 , that is, the heat pipe of the radiating fin 12 formula.
热管的制造,有相当高的一部份成本是用于热管内的清洁与除气的步骤,也就是热管内进行洁净与抽真空的作业,洁净度与真空度越高,所能完成的传热作用效果越好,越能确保热传导的稳定性,但是,通道中仍存在微量的非凝结性气体(non-condensing gas),非凝结性气体在热管内的通道中,会产生积聚,其积聚的区域与受热端的蒸发区温差很大,便影响到热管作用的顺畅性。其中非凝结性气体易于累积在冷凝区通道处的末端,而使其均温性与热传功能大幅下降。In the manufacture of heat pipes, a relatively high part of the cost is used for the cleaning and degassing steps in the heat pipes, that is, the cleaning and vacuuming operations in the heat pipes. The better the heat effect, the more stable the heat conduction can be ensured. However, there is still a small amount of non-condensing gas in the channel, and the non-condensing gas will accumulate in the channel in the heat pipe. The temperature difference between the heating area and the evaporation area at the heating end is very large, which affects the smoothness of the heat pipe function. Among them, the non-condensable gas is easy to accumulate at the end of the channel in the condensation zone, so that its temperature uniformity and heat transfer function are greatly reduced.
热管1于导热块11为热区的蒸发区提供蒸气流的产生,使蒸气流顺着通道朝另一端为冷区的冷凝区流动,然后在冷区的通道处使蒸气流冷凝形成冷凝液体流,再借助于通道内的毛细组织13快速地将冷凝液体流由冷区朝热区导引流动,用以补充蒸发区液体蒸发成气体的部份,以构成循环的流动。The heat pipe 1 and the heat conduction block 11 provide the generation of vapor flow for the evaporation area of the hot area, so that the vapor flow flows along the channel to the condensation area where the other end is the cold area, and then condenses the vapor flow at the channel of the cold area to form a condensed liquid flow , and then quickly guide the condensed liquid flow from the cold area to the hot area by means of the capillary structure 13 in the channel to supplement the part of the liquid evaporated into gas in the evaporation area to form a circulating flow.
当热管1一端受热而使热管内的液体蒸发,蒸气朝冷凝区流动,并冷凝成液体,经毛细组织使液体回流至蒸发区,由于热管的流体往返回路为设置在同一通道内,会使蒸气流与液体流的流动方向在该通道中相互冲突,而使热传量降低,且通道中残存的非凝结性气体积存于冷凝区,形成温差大的区域,降低了均温性,热传性因而也大幅降低,故传统上对热管的制造条件与保持皆严格要求,因此使成本大幅提高,售价上升,相当不符合经济性,为了提供更符合实际需求的物品,发明人乃进行研发,以解决现有热管其热传性不佳的问题。When one end of the heat pipe 1 is heated and the liquid in the heat pipe evaporates, the vapor flows toward the condensation area and condenses into a liquid, and the liquid returns to the evaporation area through the capillary tissue. Since the fluid return circuit of the heat pipe is set in the same channel, the vapor will The flow directions of the liquid flow and the liquid flow conflict with each other in the channel, which reduces the heat transfer, and the remaining non-condensable gas in the channel is stored in the condensation area, forming an area with a large temperature difference, which reduces the temperature uniformity and heat transfer performance. Therefore, it is also greatly reduced. Therefore, traditionally, the manufacturing conditions and maintenance of heat pipes are strictly required, so the cost is greatly increased, and the selling price is increased, which is quite uneconomical. In order to solve the problem of poor heat transfer performance of the existing heat pipe.
发明内容Contents of the invention
本发明所要解决的技术问题是在于提供一种平板式环路型热管,在板状热管中形成多层式且多通道与多回路式的结构,将蒸发区、蒸气通道、冷凝区、流体返回通道依序串联成一回路,其中蒸气通道可能单一通道或两通道以上相互并联设置,流体返回通道也能以单一通道或两通道以上相互并联设置,便形成单回路式的串、并联组合的架构,即组成更有效率的热交换装置,回路主要是利用通道流阻不同的导引作用,即蒸气通道的流阻小于流体返回通道,让回路中的流体自动产生循环性且稳定的单方向且相同方向的流动。从而使板状热管几乎不会有烧干现象发生,故能产生很好的热传递性,在有限空间下可有极大的热传量。通道中所形成蒸气流与冷凝的液体流皆为顺着同一方向流动而不相互冲突:而且同一平面上的各回路能形成不均匀配置状态,以适应实际需求。The technical problem to be solved by the present invention is to provide a flat plate loop heat pipe, in which a multi-layer, multi-channel and multi-circuit structure is formed in the plate heat pipe, and the evaporation area, steam channel, condensation area, and fluid return The channels are connected in series to form a circuit, in which the steam channel may be arranged in a single channel or more than two channels in parallel with each other, and the fluid return channel may also be arranged in a single channel or more than two channels in parallel with each other to form a single-circuit serial and parallel combination structure. That is to form a more efficient heat exchange device. The loop mainly uses the guiding effect of the different flow resistance of the channel, that is, the flow resistance of the steam channel is smaller than that of the fluid return channel, so that the fluid in the loop automatically generates a cyclical and stable one-way and the same direction of flow. As a result, the plate-shaped heat pipe will almost never dry out, so it can produce good heat transfer, and can have a great heat transfer in a limited space. The vapor flow and the condensed liquid flow formed in the channel all flow in the same direction without conflicting with each other; and the circuits on the same plane can form a non-uniform configuration state to meet actual needs.
本发明另一目的在于提供一种上述的平板式环路型热管,在于以经济性的考虑的前题下,能以低成本进行板状热管的制造,但仍维持有板状热管的热传递功能,而且能产生更快速的引导,运用回路内通道热流不对称的现象与回路结构上的导引,使热交换中的蒸气通道、冷凝区、流体返回通道、蒸发区所依序串联回路成为循环状的通道,即能使壳体内所存在的非凝结性气体无法固定积聚在通道的冷凝区,而让非凝结性气体顺着通道依据设计方向不断地循环流动,大幅提高板状热管的均温性,故板状热管的壳体内即使有非凝结性气体,对板状热管的功能特性均影响不大,并能延长板状热管的使用寿命。Another object of the present invention is to provide a kind of above-mentioned flat loop type heat pipe, under the premise of economical consideration, the manufacture of the plate-shaped heat pipe can be carried out at low cost, but the heat transfer of the plate-shaped heat pipe is still maintained. function, and can produce faster guidance, using the phenomenon of asymmetrical heat flow in the circuit and the guidance of the circuit structure, the steam channel, condensation area, fluid return channel, and evaporation area in the heat exchange are sequentially connected in series. The circular channel can prevent the non-condensable gas existing in the shell from accumulating in the condensation area of the channel, and allow the non-condensable gas to circulate continuously along the channel according to the design direction, greatly improving the uniformity of the plate heat pipe. Therefore, even if there is non-condensable gas in the shell of the plate-shaped heat pipe, it has little effect on the functional characteristics of the plate-shaped heat pipe, and can prolong the service life of the plate-shaped heat pipe.
为达到上述目的,本发明结构为:包括一壳体与数环状回路板,以至少一环状回路板设置于中空壳体内,让环状回路板具有至少一回路,回路形成为依序串联的蒸发区、蒸气通道、冷凝区、流体返回通道,且在壳体中充填有适量液体,流体返回通道与蒸气通道是各自有其独立而不相共享的通道,且于环状回路板盖设有板状毛细组织,并使蒸气通道的流阻小于流体返回通道,当蒸发区受热,冷凝区散热,使回路内所有的流体皆朝同一方向稳定流动不相冲突,且所有流体皆可流经回路各处,故回路内存在的非凝结性气体对回路的均温性影响不大,且顺着回路流动,而使回路热板成为均温性佳,且热传量极大的热交换装置。其中蒸气通道能以二通道以上并联设置,流体返回通道能以二通道以上并联设置。In order to achieve the above object, the structure of the present invention is as follows: comprising a housing and several ring-shaped circuit boards, at least one ring-shaped circuit board is arranged in the hollow housing, so that the ring-shaped circuit board has at least one loop, and the loops are formed sequentially The evaporation zone, steam channel, condensation zone, and fluid return channel are connected in series, and the shell is filled with an appropriate amount of liquid. The fluid return channel and the vapor channel are independent and not shared channels, and are placed on the ring circuit board cover It is equipped with a plate-like capillary structure, and the flow resistance of the vapor channel is smaller than that of the fluid return channel. When the evaporation area is heated, the condensation area dissipates heat, so that all the fluids in the circuit flow stably in the same direction without conflict, and all fluids can flow Passing through all parts of the circuit, the non-condensable gas in the circuit has little effect on the temperature uniformity of the circuit, and flows along the circuit, so that the circuit hot plate becomes a heat exchange device with good temperature uniformity and large heat transfer. Among them, the vapor channel can be arranged in parallel with more than two channels, and the fluid return channel can be arranged in parallel with more than two channels.
为更好地解释本发明为达到预定目的所采取的技术、手段及效果,下面结合附图详细描述的本发明的实施例,相信本发明的目的、特征与优点,可由此得以深入且具体的了解。In order to better explain the technology, means and effects that the present invention adopts to achieve the intended purpose, the following embodiments of the present invention are described in detail in conjunction with the accompanying drawings. It is believed that the purpose, characteristics and advantages of the present invention can be deeply and specifically explained learn.
附图说明Description of drawings
图1为现有技术方案的剖视图;Fig. 1 is the sectional view of prior art scheme;
图2为本发明的立体分解图;Fig. 2 is the three-dimensional exploded view of the present invention;
图3为图2中第一环状回路板翻面后的上视立体图;Fig. 3 is a top perspective view of the first annular circuit board turned over in Fig. 2;
图4为图2中第一环状回路板未翻面的上视立体图;Fig. 4 is an unturned top perspective view of the first annular circuit board in Fig. 2;
图5为图2中第二环状回路板的上视图;Fig. 5 is the top view of the second annular circuit board in Fig. 2;
图6为图2中本发明组合后的剖视图;Fig. 6 is a cross-sectional view of the present invention combined in Fig. 2;
图7为图2中第一环状回路流体的流动示意图;Fig. 7 is a flow schematic diagram of the first annular circuit fluid in Fig. 2;
具体实施例specific embodiment
在图2、3、4、5、6和图7中,本发明的一个实施例为一种环路型热管,具有一壳体3,壳体3其为中空封闭体,并于壳体3内充填有适量液体。液体的充填量,是指填满壳体内的毛细组织及回路内第一环状回路板各回路内通路的容积的80-90%的填入液体的容量。In Fig. 2, 3, 4, 5, 6 and Fig. 7, one embodiment of the present invention is a kind of loop type heat pipe, has a
具有至少一个呈娄空状的第一环状回路板5与至少一个呈娄空状的第二环状回路4,各环状回路板4、5是接设于壳体3内,并以环状回路板4在壳体3内形成具有至少一回路2,回路2是以娄空形成各通道,其中的壳体3是由顶壳31与底壳32所组成,以顶壳31的周缘与底壳32的周缘相接后密闭形成壳体3。其中环状回路板可以仅设其中的一块,或是设置成两块相叠状,可以将图3与图4所示的状态,直接相叠组成另一组合。There is at least one hollow first
其中壳体3可具有另一种型式,壳体是为由一圆管压平成扁平管,且两端封闭者。Wherein the
在第一环状回路板5与第二环状回路板4上开设有突起或凹陷的通道,在图3、4、图5中,该通道的设置能满足形成回路的需求;其中第一环状回路板与第二环状回路板的设置方式近似。On the first
在图2中的第一环状回路板5和第二环状回路板4为呈方形,而且于其中分别形成四等分的使用状态,也就是以十字区分成四区,各区均形成一回路,是由各二条不相交且呈角状平行侧的区隔条50a、40a及垂直侧的区隔条50b、40b与二条角状相交的边缘条57、47相连组成,于该对角状相按的区隔条50a、50b或40a、40b间各形成一中心缺口58、48。In Fig. 2, the first
在一对区隔条40a及40b与一对边缘条47,或是一对区隔条50a及50b与一对边缘条57所框围的空间内,分别以四条的第一隔条41、42、43、44、51、52、53、54与区隔条40a、40b、50a、50b并列形成四条宽通道,再以一第二隔条45、55两侧分别与第一隔条44、54、平行侧的边缘条47、57并列形成二条次宽通道,在另一侧垂直侧的区隔条47、57并列有一底隔条46、56间区隔成一条较窄通道,且使底隔条46、56与第一隔条44、54相接。In the space enclosed by a pair of
在图3、图4中,第一环状回路板5的平行侧区隔条50a、第一、第二隔条51、52、53、54、55分别与相垂直相接的边缘条57处各设有一阶状凹槽59f、59a、59b、59c、59d、59e,各凹槽59设在近宽通道与次宽通道的外端,并形成宽、次宽通道横向相交的状态,以使各凹槽59成为蒸气移动的通道终点,即使第一环状回路板5的蒸气,经由第一环状回路板5宽通道的靠边部份的冷却通路,且呈左右两半间相连通的状态。In Fig. 3 and Fig. 4, the
在图5中,第二环状回路板4的平行侧区隔条40、第一、第二隔条41、42、43、44、45分别与相垂直相接的边缘条47处各设有一贯穿横槽49,形成宽、次宽通道间为平行设置;其需经由第二板状毛细组织7的传递,如图6所示。In Fig. 5, the
各回路板4、5上的各回路形成由宽通道、次宽通道、较窄通道的连通形状。但上述的结构仅为一较佳实施例。其中以宽通道形成蒸气通道22,以较窄通道形成液体返回通道24,中心缺口48处为蒸发区21,以次宽通道所在的板边缘处为冷凝区23,充填于壳体3内的液体其流向在图7中所示。且宽通道靠冷凝区部份已具有为冷凝区的功能和作用。Each circuit on each
回路2由依序串联的蒸发区21、蒸气通道22、冷凝区23、流体返回通道24所组成,在回路2中充填有适量的液体,液体的充填量是指由填满毛细组织至填满回路内的90%的体积。其中流体返回通道24与蒸气通道22是不相共享的通道,也就是蒸气通道22是一独立的通道,流体返回通道24也是一独立的通道,这是不同于现有传统热管的蒸气通道与流体返回通道共享同一通道的结构。
本发明的回路2的区域,在上、下方各形成两组回路2,且上分或下方的一对回路为左右对称设置,即形成中间的蒸发区21与周边的冷凝区23,使蒸气进入四条宽通道所并联组成的蒸气通道22,然后进入冷凝区23的次宽通道,冷凝成的液体顺着较窄通道所形成的流体返回通道24回到蒸发区21,便完成一次的循环动作,而回路的形状能配合需求设置,图中是将蒸发区设置在中心位置,也能为偏心的状态,或是在角落处,均可应用本发明的方式,形成多种的形状。In the region of the
另外,在图2中是形成各自独立的四组并朕式的单一回路设置,仅使液体于中心缺口处汇流,若有需要亦能在环状回路板上形成串联式的数回路组合,以使本发明能顺序地以不同接点接触热源,形成另一种型态的热管结构。In addition, in Fig. 2, four independent sets of single loops are formed in parallel, which only allow the liquid to converge at the center gap. If necessary, a serial number loop combination can also be formed on the annular circuit board, so as to This enables the present invention to sequentially contact the heat source with different contact points to form another type of heat pipe structure.
且本发明使在流体返回通道24内的流阻大于蒸气通道22,此是刻意造成壳体通道内热流的不平衡,以形成壳体3通道内流体流动的不对称结构,使由蒸发区21形成的蒸气很容易且自然稳定地单方向朝冷凝区23流动,并在冷徽区23冷凝形成冷凝液体流,让冷凝的液体流与非凝结性气体,连同未冷凝的蒸气流,在回路的流阻不同作用下与通道结构的引导下,一齐朝向流体返回通道24稳定地单方向流动,且经流体返回通道24回流至蒸发区21。And the present invention makes the flow resistance in the
本发明所指的蒸发区21就是回路2受热位置部份,其能以一热源8,如图6中所示,与壳体3的至少一端面(底面)中心处相接,而热源是指电子组件的易发热表面,通常是指中央处理器,但不局限于该组件。所以,蒸发区与欲散热的热交换装置相接,欲散热的热交换装置可为热源的传热块、受热鳍片组、受热水套或如本发明另一组回路的冷凝区,其中的另一组回路是指本发明两回路的串接型式。The
此外,本发明冷凝区23就是回路散热的位置,此部份为主要的散热区域,当然通道的本身也是良好的散热结构,能使冷凝区与一热交换装置9相接,如图6所示,也就是冷凝区23的至少另一端面(顶面)与作为散热的热交换装置相接,热交换装置为一体式的散热器、散热鳍片组、冷却水塔或本发明另一组回路的蒸发区。所以,壳体能以至少一端面的的蒸发区更与一热源相接,以进行热交换,壳体其余端面的局部至全部再与一热交换装置相接,以进行散热。In addition, the condensing
另外,在图2中所示的蒸气通道22为多个通道,也就是说能设有一或两条以上相互并联的蒸气通道22,以使各蒸气通道的流阻总和小于流体返回通道,其中的流阻控制为改变回路总截面积或总长度或其组合,以形成蒸气通道内的流阻小、流速大的状态,而流体返回通道内的流阻大、流速小的状态,使回路中刻意形成的热流不对称,促使流动方向的确定;且,流体返回通道24在图2中为多个通道,但也能设有两条以上相互并联的流体返回通道,只要符合前述的具有较大流阻条件,并且使冷凝液体只能经过流体返回通道返回蒸发区,即自然产生回路的导引流动,且此种流动的现象为稳定的单方向流动,且被刻意限制的,仅能朝设计的方向流动,不会发生违反设计的随意流动。In addition, the
或让流体返回通道中充满液体以形成液封,其能干流体返回通道中完全置满一毛细组织以形成,亦能缩小气体通过空间以达成上述的液封效果,其中的液封是指流道断面缩小或以毛细组织封闭流道,即以增加流阻的不对称性的方式所形成,而使流体循环更稳定朝设计方向流动,但此时因液体返回通道会影响非凝结气体的通过性,使该实施的均温性较差,可以透过对回路的除气程序,以消除非凝结气体,提高均温性。Or let the fluid return channel be filled with liquid to form a liquid seal, which can completely fill the fluid return channel with a capillary tissue to form, and can also reduce the space through which the gas passes to achieve the above-mentioned liquid seal effect. The liquid seal refers to the flow channel The cross-section is reduced or the flow channel is closed by capillary tissue, which is formed by increasing the asymmetry of the flow resistance, so that the fluid circulation is more stable and flows in the design direction, but at this time, the passage of non-condensable gas will be affected by the return channel of the liquid , so that the temperature uniformity of this implementation is poor, and the non-condensable gas can be eliminated through the degassing process of the circuit to improve the temperature uniformity.
由于回路2已被设置成串联式,且有顺序的单方向循环流动,使存在于回路的非凝结性气体没有积聚停留的空间与时间,只能顺着蒸气流流动或冷凝液体流在回路中流动,所以,本发明在回路内可以形成蒸气通道空间内含有大部份蒸气流的气体与少部份冷凝后液体流的液体与非凝结性气体,而流体返回通道空间内大部份为冷凝的液体与少部份蒸气流的气体与非凝结性气体,构成快速地单方向循环流动。使热管内所有流体皆朝向同一方向流动,不相冲突,且所有流体任何时间都能通过系统内任何通道,故热传性佳,热传量大,且温差小。Since the
本发明在相叠的第一环状回路板5、第二环状回路板4之外分别贴置有一第一板状毛细组织6、一第二板状毛细组织7,板状毛细组织6、7,其长宽约与环状回路板4、5等大,但板状毛细组织上仅相对于宽通道的位置设有沟槽61、71,且沟槽比宽通道为短,沟槽处为允许蒸气流通的区域,于是前述的横槽49即是透过毛细组织7与流体返回通道相接,运用毛细组织将冷凝的液体吸引并引导至流体返回通道。在图2中,为同大覆盖式的毛细组织,其能以至少一板状毛细组织设于单独一块的环状回路板的一面或两面,以形成堆栈状的结构。而板状毛细组织亦比与环状回路板小,或是设置在两环状回路板间。In the present invention, a first plate-shaped
由于毛细组织为多孔性,很容易成为液体的过道,使毛细组织不仅设置及于冷凝液体流所在的流体返回通道的长度,使其内通道变小且流阻变大,或单独延伸至蒸发区或单独延伸至冷凝区,或同时延伸至蒸发区及冷凝区,或更能在整个回路内设有毛细组织,但要符合蒸气通道的流阻小于流体返回通道。其中毛细组织为陶瓷、烧结粉末、发泡金属、编织网、烧结网、沟槽状板、纤维束或螺旋线。其中流体返回通道更要设有空间让蒸气与非凝结性气体通过。且毛细组织能为条状置于通道中或由板状毛细组织上突出伸出至通道通,板状毛细组织不大于环状回路板。如在第一环状回路板的阶状凹槽嵌有一毛细组织,以毛细组织形成流体返回通道与蒸气通道间的连通。Because the capillary is porous, it is easy to become a channel for liquid, so that the capillary is not only set up to the length of the fluid return channel where the condensed liquid flow is located, so that the inner channel becomes smaller and the flow resistance becomes larger, or it extends to the evaporation area alone Either extend to the condensation area alone, or extend to the evaporation area and the condensation area at the same time, or more capillary structures can be provided in the entire circuit, but the flow resistance of the steam channel is smaller than that of the fluid return channel. Among them, the capillary structure is ceramics, sintered powder, foamed metal, woven net, sintered net, grooved plate, fiber bundle or spiral wire. Among them, the fluid return channel should be provided with a space for steam and non-condensable gas to pass through. Moreover, the capillary tissue can be placed in the channel in the form of strips or protrude from the plate-shaped capillary tissue to the channel, and the plate-shaped capillary tissue is not larger than the annular circuit board. For example, a capillary tissue is embedded in the stepped groove of the first annular circuit board, and the communication between the fluid return channel and the steam channel is formed by the capillary tissue.
在图7中,更圈设有各作用区域的标示,中间为凝结液蒸发区21,在蒸气通道22靠内半部通道为蒸发流的蒸发区,即是广义的蒸发区域25,且于蒸气通道22靠外半部通道为蒸气流冷凝区,也与原冷凝区23组合成广义的冷凝区域27,其两侧各为凝结液流与非凝结气流返回区,又在蒸气通道22与流体返回通道24间设有连通的通道,但广义而言,为设有一连接区域26,含有前述连通的通道、阶状凹槽、贯穿横槽等的冷凝区23,也就是使连接区域界于蒸发区域25与冷凝区域27间。In Fig. 7, the mark of each action area is arranged on the circle, the
综上所述的结构,本发明运用独立的分流机构,并构成蒸气通道与流体返回通道间流阻不相等的架构,配合所产生的热流不平衡、毛细现象等的原理,形成串联式的顺序单方向流体循环结构,而且蒸气通道与流体返回通道也能各自形成多通道并联式的结构,只要在流体返回通道24内的流阻大于蒸气通道22的大前题下,便能产生连通环状回路,如此,本发明于制作过程中,不需经过除气的程序,亦能操作传热,若壳体内回路经除气程序后,则热传导性更佳,且操作温度范围更广;如此,使回路更容易组成,在实际使用上与现有热管相比较,其热传导流动的速度快于现有的热管,热均温性高,热传递性佳,则热传量更大、更快,故本发明不需除气制程,且清洗的洁净制程亦不重要,使其制程简单,则成本低,售价亦能降低,具有更好的经济性,且功能特性更佳,所以本发明能提供很好的使用性,本发明与现有热管为完全不同的机构。To sum up the structure described above, the present invention uses an independent flow diversion mechanism, and constitutes a structure with unequal flow resistance between the steam channel and the fluid return channel, and cooperates with the generated heat flow imbalance, capillary phenomenon, etc., to form a serial sequence One-way fluid circulation structure, and the steam channel and the fluid return channel can also form a multi-channel parallel structure, as long as the flow resistance in the
以上所述为本发明的较佳实施例的详细说明与图附,并非用来限制本发明,本发明的所有范围应以专利权利书要求保护的范围为准,凡与本发明的设计思想及其类似变化的实施例、近似结构,都应包含于本发明的专利保护范围之中。The above is a detailed description and drawings of preferred embodiments of the present invention, and is not intended to limit the present invention. All scopes of the present invention should be based on the scope of protection claimed by the patent claims. Its embodiments with similar changes and similar structures should all be included in the patent protection scope of the present invention.
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|---|---|---|---|---|
| TWI846840B (en) * | 2019-03-11 | 2024-07-01 | 日商大日本印刷股份有限公司 | Vapor chamber, electronic device, and sheet for vapor chamber |
Families Citing this family (19)
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| CN111426225A (en) * | 2020-03-04 | 2020-07-17 | 奇鋐科技股份有限公司 | Loop Heat Pipe Structure |
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-
2001
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Cited By (2)
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| TWI846840B (en) * | 2019-03-11 | 2024-07-01 | 日商大日本印刷股份有限公司 | Vapor chamber, electronic device, and sheet for vapor chamber |
| TWI897457B (en) * | 2019-03-11 | 2025-09-11 | 日商大日本印刷股份有限公司 | Vapor chamber, electronic device, and sheet for vapor chamber |
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