TWM336675U - Gravity type capillary pumped loop (CLP) two-phase flow heat-dissipating device - Google Patents

Gravity type capillary pumped loop (CLP) two-phase flow heat-dissipating device Download PDF

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TWM336675U
TWM336675U TW97202732U TW97202732U TWM336675U TW M336675 U TWM336675 U TW M336675U TW 97202732 U TW97202732 U TW 97202732U TW 97202732 U TW97202732 U TW 97202732U TW M336675 U TWM336675 U TW M336675U
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capillary
liquid
cpl
heat
gravity
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TW97202732U
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Chinese (zh)
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Ming Li
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Arbor Technology Corp
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M336675 (一) 本案指定代表圖為:圖(13)。 (二) 本代表圖之元件符號間早說明· CPL雙相流散熱裝置2 蒸發部(evaporator) 10 頭侧面12 液體頭(Liquid head ) 13 尾侧面14 蒸汽頭(vapor head) 15 毛細體部(porous wick part ) 16 開口槽161 凸緣162 蒸汽導槽 (vapor groove ) 17 室腔18 環狀通道20 八、新型說明: 【新型所屬之技術領域】 力式毛·及壤路(cpl )雙相 机政歸置,尤指-種可應用於高能量密度 才 品如車用數位錄影系統(mdVR )上, 冓裝產 MDVR要求在寬溫-30 u6〇〇c之控:滿足系統如 【先前技術】 “皿要求者。 隨著半導體科技的發展,微影與其他 的情況下,使得電子元件的尺寸大幅 技術進步下 晶體被放入積體電路(IC)中,換言之,單^來越多的電 晶體數目急遽增加,再加上ic的運算速度增 積内的電 ㈢σ,導致1C在 3 M336675 運作時產生非常大的熱功率,以目前個人電腦内的中央處 理器(CPU )而言,發熱量從pentium的20W到Pentium Π的 30W甚至43W,而Pentiumiv估計約在150W以上,CPU 的接面溫度(junction temperature)更可高達150 °C,若不能有 效且迅速的移除CPU所產生的熱量,將使得CPU因熱量累 積溫度甚高而導致當機甚至損壞。目前,為了避免電子元 件因高熱高溫而影響其工作性能甚至損毁,通常都於其上 加裝一散熱鰭片(fm),並以一轴流風扇強制空氣對流而 增加其熱移除能力,此為傳統電子元件散熱器之架構。一 般而言,單相空氣強制對流熱傳係數與熱傳表面積增加而 提高。因此,為增加熱傳率,通常都以增加散熱鰭片面積 或使用空氣流量較大的風扇來達成,但增加表面積及空氣 流量所帶來的缺點為體積增大,振動噪音等問題。除了使 用政熱鰭片與風扇來作為散熱裝置以外,尚有空氣衝擊节 冷部與熱管兩種散熱方式。使用空氣衝擊流冷卻的方式= 作為電子元件的散熱之用,其平均熱對流係數可達二Λ 〇W/m _〇甚至更咼,雖然此方式可以較一般空冷方 更佳的熱對流係數,但缺點在於需提供一高壓空教x 右一般空冷方式僅需要一風扇來驅動空氣流動即可。另 外,目前最常使用的熱管是一種高熱傳導性的裝置, 效熱傳係數可大於KKKJW/A t,它能傳送大量的熱能寻 利?液體吸收熱量產生相變化而變成蒸氣,將熱量由;埶 的區域傳送至低溫的區域,工作流體在熱管中不斷循環、、 不需外加任何動力驅使工作流體流動,僅管如此,熱 仍只是一種傳送熱量的裝置,而非散熱的工具。綜 4 M336675 =散:方式,皆有ί致命的缺點,雖然可以滿足目前 =子元件散熱上的要求,值將無法符合未來電子元件在 空間、熱移除能力以及與Ic封裝整合的要求。因 =易式熱管式之散熱器亦無法滿足其散熱之需求,而必 其他之散熱方式才能達到最佳之熱 的 方法為將液、汽傳送通道分離,並藉由特殊設的分離器 (»r),使工作流體產生單方向流動。當熱源⑽ 和熱沈(heatsink )部分因為外在環境所處的相 對位置不同時,則熱流現象即熱傳機構便有所不同。一般 =言’若熱_位置較低、熱沈位置較高時,舰路循環 的驅動力主要為液體因受熱形成密度差的浮力為主。若執 源和熱沈相對位置呈水平狀態或環路處於微重力環境時, =循環的驅動力便不能依-般地面上液體因密度的變化所 產^的額外浮力(buoyancy)作為驅動力(drivingf〇rce)。因 此當加熱於蒸發器時,該液體通道中的工作流體必須藉由 毛細力(capillaryforce)作用吸附而流入蒸發器,並於此吸熱 而篇發成為蒸汽,再經由蒸發器内的蒸汽導槽導入氣體通 道,由蒸汽頭(vaporhead)而流入冷凝器釋放出潛熱,再經 由液體頭流入蒸發器内受熱蒸發,完成自然循環”(natural emulation)的移熱作用。而依此概念所發展出來的機構, 右以多孔性物質的毛細吸力作為環路的驅動力,則稱之為 毛細菜吸環路(Capillary Pumped Loop),縮寫為“cpl”。雙 相流毛細泵吸環路(CPL)是一種藉由工作流體液、汽兩相 之間相變化的潛熱來傳遞熱量,而且不需要外加任何機械 栗浦。工作流體的作動完全靠内部毛細結構物質的毛細 5 M336675 力,作單方向的循環來移熱。由於是靠工作流體之潛熱來 移熱’因此如果經由CPL之設計,能輕易由熱源(cpu)傳 送至筆記型電腦之外殼附近,再利用箱型風扇(Case Fan )便可移走超高量的熱,而遠遠超過常見單相散熱 (如風扇、散熱鰭片)的方式所能達到的效果。此質輕、 構造簡單、熱傳距離遠且不受重力約束、無須任何外加動 力的裝置最適用在一般高價值之電子構裝散熱或人造衛星 上,CPL於1986年應用於挑戰號太空梭更是有其卓越之成 就。以毛細作用力之雙相流環路能有效將熱移除,亦能在 自然冷凝對流狀況下可移除25W之熱量且保持cpu在90 °C 左右。根據此一原理,如果採取強制對流將可有效的將熱 量由箱型風扇(CaseFan )移走。毛細泵吸之雙相流高效 率熱移系統CPL(Capillary Pumped Loop)主要之四大組件包 含·蒸發器、蒸發頭、冷凝器與冷凝頭。另外,由於必須 利用箱型風扇(CaseFan )作為熱沈散熱之工具,因此舉 凡軸流風扇之風量、系統之阻抗等之影響都必須充分考 慮。CPL系統之熱測試則可由cpu熱模擬測試系統測得, 但如何設計一個更高效率之CPL環路已帶走15〇w以上之 熱1則有賴於毛細結構包括毛細半徑(Wick Radius) 、毛細 滲透度(Permeability)、冷凝部規格之再改善,此多有賴於 理論模式之建立。傳統對於電子元件的散熱關與管理, 往往都是被軸於整個㈣程序的最後_環,也就是說電 子元件在製造、封裝測試完成之後,才考慮到散熱的問 題,以及如何將散熱裝置與電子元件結合。對於一個要求 不嚴格的應料合’這樣的規财式可以有較低的成本及 6 M336675 不錯的散熱效 能 但是當面臨封裝尺寸需更加緊緻縮小、 性能導致高發熱量以及電子元件處在-高溫惡 ^^〗見時,舊有的觀念與方式將無法滿足電子元件 ίϋ:要求。因此’便需要-個新的散熱方式與裝置 來解決即將遭遇的問題。 又2001年9月u曰美國九--事件、2002年10月12 二:^二:島恐怖攻擊、2_年3月11曰西班牙火車爆炸 案及2005年7 7 αmM336675 (I) The representative representative of the case is: Figure (13). (2) Early description of the component symbols in this representative figure · CPL dual-phase flow heat sink 2 Evaporator 10 head side 12 Liquid head 13 tail side 14 vapor head 15 Capillary body ( Porous wick part ) 16 open groove 161 flange 162 steam groove 17 chamber 18 annular channel 20 VIII, new description: [new technical field] force type hair and soil road (cpl) dual camera Registration, especially - can be applied to high-energy density products such as digital video recording system (mdVR), armored production MDVR requires control at wide temperature -30 u6〇〇c: meet the system such as [previous technology 】 "Carryer requirements. With the development of semiconductor technology, lithography and other circumstances, the size of electronic components has been greatly improved, the crystal is placed in the integrated circuit (IC), in other words, the more The number of transistors increases sharply, and the electric (3) σ in the accumulative speed of ic increases the 1C to generate very large thermal power when operating at 3 M336675. In the current central processing unit (CPU) in a personal computer, the heat is generated. Amount from the pentium 20W to Pentium Π 30W or even 43W, while Pentiumiv is estimated to be above 150W, CPU junction temperature can be as high as 150 °C, if you can not effectively and quickly remove the heat generated by the CPU, it will make the CPU Due to the high heat accumulation temperature, the machine is even damaged. At present, in order to prevent the electronic components from affecting their working performance or even being damaged due to high heat and high temperature, a heat dissipating fin (fm) is usually added thereto and flowed in one axial flow. The fan forces air convection to increase its heat removal capability, which is the structure of the conventional electronic component heat sink. Generally, the single-phase air forced convection heat transfer coefficient and heat transfer surface area increase and increase. Therefore, in order to increase the heat transfer rate, It is usually achieved by increasing the fin area or using a fan with a large air flow. However, the disadvantages of increased surface area and air flow are volume increase, vibration noise, etc. In addition to using thermal fins and fans. In addition to the heat sink, there are two ways to dissipate the air-cooling section and the heat pipe. The method of using air impingement cooling = heat dissipation as an electronic component For its use, its average thermal convection coefficient can reach ΛW/m _〇 or even more 咼, although this method can have better thermal convection coefficient than the general air cooling, but the disadvantage is that it needs to provide a high pressure air teaching x right general air cooling method. Only one fan is needed to drive the air flow. In addition, the most commonly used heat pipe is a high thermal conductivity device. The heat transfer coefficient can be greater than KKKJW/A t, which can transfer a large amount of heat energy. Producing a phase change and turning into a vapor, transferring heat from the area of the crucible to a low temperature area, the working fluid continuously circulates in the heat pipe, and no additional power is required to drive the working fluid to flow. However, the heat is still only a kind of heat transfer. Device, not a tool for cooling. Comprehensive 4 M336675 = scatter: mode, all have fatal shortcomings, although it can meet the current requirements of sub-component heat dissipation, the value will not meet the requirements of future electronic components in space, heat removal and integration with Ic package. Because the = heat pipe type radiator can not meet the heat dissipation requirements, and other heat dissipation methods to achieve the best heat method is to separate the liquid and steam transfer channels, and by a special separator (» r), causing the working fluid to flow in one direction. When the heat source (10) and the heat sink (inks) are in different positions due to the external environment, the heat transfer mechanism is different. In general, if the heat _ position is low and the heat sink position is high, the driving force of the ship circulation is mainly the buoyancy of the liquid due to the density difference formed by heat. If the relative position of the source and the heat sink is horizontal or the loop is in a microgravity environment, the driving force of the cycle cannot be used as the driving force by the additional buoyancy of the liquid on the ground due to the change in density ( Drivingf〇rce). Therefore, when heated in the evaporator, the working fluid in the liquid passage must be adsorbed by the capillary force to flow into the evaporator, and the heat is absorbed into the steam, and then introduced into the steam guide through the evaporator. The gas passage, which flows from the vapor head into the condenser, releases latent heat, and then flows into the evaporator through the liquid head to be heated and evaporated to complete the natural emulation. The mechanism developed according to this concept Right, the capillary suction of the porous material is used as the driving force of the loop, which is called the Capillary Pumped Loop, abbreviated as “cpl.” The two-phase capillary pumping loop (CPL) is a kind The heat is transferred by the latent heat of the phase change between the working fluid and the vapor phase, and no mechanical pump is required. The working fluid is completely circulated by the capillary of the internal capillary structure 5 M336675. Heat transfer. Because it relies on the latent heat of the working fluid to transfer heat, so if it is designed by CPL, it can be easily transferred from the heat source (cpu) to the notebook. Near the outer casing, the Case Fan can be used to remove a very high amount of heat, far more than the usual single-phase heat dissipation (such as fans and fins). The device with simple structure, long heat transfer distance and no gravity constraint, and no need for any external power is most suitable for general high-value electronic assembly heat dissipation or artificial satellite. CPL was applied to the Challenge Space Shuttle in 1986. Excellent achievement. The double-phase flow loop with capillary force can effectively remove heat, and can remove 25W heat and maintain cpu at 90 °C under natural condensation convection. According to this principle, if The forced convection will effectively remove the heat from the box fan (CaseFan). The capillary pumping two-phase flow high efficiency heat transfer system CPL (Capillary Pumped Loop) four main components include · evaporator, evaporation head, Condenser and condenser head. In addition, since the box fan (CaseFan) must be used as a tool for heat sinking, the influence of the airflow of the axial fan and the impedance of the system must be fully considered. The thermal test can be measured by the cpu thermal simulation test system, but how to design a higher efficiency CPL loop has taken away more than 15 〇w of heat 1 depends on the capillary structure including the capillary radius (Wick Radius), capillary penetration Permeability and the improvement of the specifications of the condensing section depend on the establishment of the theoretical model. The traditional heat dissipation and management of electronic components are often the last _ ring of the whole (4) program, that is, electronic components. After the manufacturing and packaging tests are completed, the heat dissipation problem is considered and how the heat sink is combined with the electronic components. For a less demanding application, such a financial formula can have lower cost and 6 M336675 good heat dissipation performance, but when the package size is required to be more compact, the performance leads to high heat generation and the electronic components are at - high temperature Evil ^^〗 When you see, the old ideas and methods will not be able to meet the electronic components. Therefore, a new cooling method and device are needed to solve the problems that will be encountered. Also in September 2001, u 曰 US Nine--Event, October 12, 2002: ^2: Island Terrorist Attack, March 11th, 2nd, Spanish Train Explosion and 7 7 αm in 2005

墼審株,日央國倫敦地鐵及巴士爆炸案等恐怖攻 m u使歐美危機意識不斷提高,透過安全監控設備可 & >’’阻犯罪與**集相關證據,因此在恐佈攻擊不斷, 預防,罪與H集證據需求持續提升情形下 ,安全監控產品 寺縯成長。監視用的數位錄影系統DVR ( Digital vide〇 Reeonlei· ’或稱為數位影像錄放影機)如車用數位錄影系 統(MDVR ’ Mobile Digital Video Recorder,Mobile dvr )就是一種裝置於車上的小型電腦監控安全系統, 其裝設在國外大型巴士或各小學、高中等之校車上尤其普 遍,其系統共做沿途廣告、說明、警示、播放、網路、衛 星導航等等’是一種安全裝置也是一種服務裝置,因此愈 來愈受國外大型巴士獲校車之重視。而由於在MobileDVR 如此緊密之空間内,為了能克服較大之阻抗,本創作因此 針對高能量密度電子機構產品例如MobileDVR等,提出一 種重力式毛細泵吸環路之散熱裝置(CPLCooler ),以達 到在無扇下之最大熱傳量之效果。 【新型内容】 本創作主要目的在於提供一種重力式毛細果吸環路 7 M3 3 6675 (CPL )雙相流散熱裝置,供應用於高能量密度之電子構 裝產品上如車用數位錄影系統(MDVR);該毛細泵吸環 路(CPL )主要包含:至少一個蒸發部(evaporator ),其 外部底面係對應密貼於一熱源部份如系統主機板之中央處 理器(CPU )上,其頭、尾二侧面上各設一液體頭 (Liquid head )及一蒸汽頭(vapor head)分別供工作液體之The squad, the Japanese central London subway and bus bombings and other terrorist attacks have increased the awareness of the European and American crisis. Through security monitoring equipment, it can be used to prevent crimes and rumors. In the case of prevention, sin and H-set evidence needs to continue to improve, the security monitoring product temple grew. Digital video recording system DVR (Digital vide〇Reeonlei· or digital video recorder), such as the digital video recording system (MDVR 'Mobile Digital Video Recorder, Mobile dvr), is a small computer monitor installed in the car. The safety system is especially popular in large foreign buses or school buses of all primary and high schools. The system is mainly used for advertising, description, warning, broadcasting, internet, satellite navigation, etc. Service devices are increasingly attracting the attention of large foreign buses. In order to overcome the large impedance in the space where MobileDVR is so tight, this work proposes a gravity-type capillary pumping loop heat sink (CPLCooler) for high-energy-density electronic components such as MobileDVR. The effect of maximum heat transfer without a fan. [New content] The main purpose of this creation is to provide a gravity-type capillary drip loop 7 M3 3 6675 (CPL) dual-phase flow heat sink for high-density electronic components such as digital video recording systems for vehicles ( MDVR); the capillary pumping loop (CPL) mainly comprises: at least one evaporator, the external bottom surface corresponding to a heat source part such as a central processing unit (CPU) of the system motherboard, the head a liquid head and a vapor head are respectively provided on the side of the tail two for the working liquid

液相流入及汽相流出,其内部設有一毛細體部(porous wick part )及複數條蒸汽導槽(vapor groove)設在毛細體 部之外圍;一環狀通道,其佈設且連接在蒸汽頭與液體頭 之間;及一冷凝部,其可包含環狀通道並可配合散熱鰭片 或連接至外殼以形成熱沈部份(heat sink );再於環路中 填入工作流體(workingfluid)如氟氣烧(Freon );藉 此,液相工作流體可自液體頭流入蒸發部,再藉由毛細體 部之毛細力作用吸附並同時於此吸熱而蒸發成為汽相,再 藉複數條蒸汽導槽匯流導入蒸汽頭而由蒸發部流出至環狀 通道中流動,再藉由冷凝部釋放出潛熱而回復為液相,再 經由液體頭流入蒸發部内再受熱蒸發,完成一加強其毛細 作用推力之重力式自然循環的移熱作肖,藉以達成在無扇 下之最大熱傳量的散熱效果,並有效克服習知水泵浦環路 之笨重、體積龐大且無法解*高瓦數及無法滿足寬溫 -30 C至60 C )之控溫的問題。 本創作再-目的在於提供一重力式毛細果吸環路雙相 流散熱裝置,其中該毛細泵吸環路(CPL) 戈 以上之蒸發部,且鱗蒸發部係採賴聯排料式設置= 環狀通道上,使錢發部之㈣較連錢彳目同之環狀通 8 M336675 可同時由各液體 道上,使藉由冷凝部凝結之液相工作流 頭進入各蒸發部内。 本創作又一目的在於提供一重力 '=裝置,其進-步可先將毛細系 再真入工作韻,藉以增進散熱效果, 溫要=,要求在寬溫^至控The liquid phase flows in and the vapor phase flows out, and a porous wick part and a plurality of vapor grooves are disposed at the periphery of the capillary portion; an annular passage is arranged and connected to the steam head And a liquid head; and a condensation portion, which may include an annular passage and may be coupled with a heat sink fin or connected to the outer casing to form a heat sink; and a working fluid may be filled in the loop. For example, the fluorine gas is burned (Freon); thereby, the liquid phase working fluid can flow from the liquid head into the evaporation portion, and then adsorbed by the capillary force of the capillary portion and simultaneously evaporates into a vapor phase by the endothermic heat, and then borrows a plurality of steam. The guide trough is introduced into the steam head and flows out from the evaporation portion to the annular passage, and then the latent heat is released by the condensation portion to return to the liquid phase, and then flows into the evaporation portion through the liquid head to be evaporated by heat, thereby completing a capillary action to enhance the capillary action. The gravity-type natural circulation heat transfer function is used to achieve the heat dissipation effect of the maximum heat transfer without the fan, and effectively overcome the cumbersome, bulky and unsolvable *high wattage of the conventional pump circuit. Unable to meet the problem of wide temperature range -30 C to 60 C) of the temperature control. This creation is again aimed at providing a gravity-type capillary drip loop two-phase flow heat sink, wherein the capillary pumping loop (CPL) is above the evaporation section, and the scale evaporation section is based on the joint discharge type setting = On the annular passage, the money-generating part (4) is more connected to the ring. 8 M336675 can simultaneously enter the evaporation sections by the liquid-phase working head condensed by the condensation section from each liquid channel. Another purpose of this creation is to provide a gravity '= device, which can first enter the working system into the rhyme, so as to enhance the heat dissipation effect, and the temperature is required to be controlled at a wide temperature.

流散提供—4力式毛細泵吸環路雙相 却认、、、1置’其進—步可在毛細杲吸環路(CPL )之落發 3外部底面上先貼附一散播用導熱片W),“ =、貼於熱源部份如中央處理器(cpu)上,藉以增進散 “、、效。果’而可滿足系統之控溫要求如歸⑽要求在寬溫 -30 °C至6〇°C之控溫要求。 、本創作又另一目的在於提供一重力式毛細泵吸環路雙 相流散熱裝置,其進一步可在毛細泵吸環路(cpL )之冷 1部,蒸發部之液體頭之間增設一工作流體之儲槽,藉以 曰進政熱效果’而可滿足系統之控溫要求如MDVR要求在 寬溫-30 °C至60°C之控溫要求。 【實施方式】 以下結合附圖’對本創作上述的和另外的技術特徵和 優點作更詳細的說明: 參照圖1、2、3所示,其分別係本創作一實施例 (設具一蒸發部)之基本架構及其蒸發部例内部結構之上 視及橫向斷面示意圖。本創作係一種重力式毛細泵吸環路 C Capillary Pumped Loop,簡寫為CPL )雙相流散熱裝置 9 .M3.36675 1 ,雙相流移熱方式遠比單相移熱效率高,其特點為利用 工作流體(workingfluid)雙相之間潛熱變化迅速移走大量的 熱源(heatsource),可應用於高能量密度之電子構裝產品上 如車用數位錄影系統(MDVR,Mobile Digital Video Recorder,MobileDVR )等,用以移除系統之熱源部分如 系統主機板之中央處理器(CPU)所產生之熱;又在液相 與汽相共存的狀態,兩相間幾無溫度差存在,依熱能吸收 或放出的方向而從液相變回汽相或從汽相變回液相,前者 籲為蒸發過程,後者為凝結過程,而依此概念所發展出來的 熱輸送裝置,稱之為毛細果吸環路(CPL)。本創作重力式 CPL雙相流散熱裝置1主要包含··至少一蒸發部 (evaporator) 10、一環狀通道20及一冷凝部3〇,且藉由蒸 發部10、環狀通道20及冷凝部3〇構成一毛細泵吸環路 (CPL ) ’而環路中則填入工作流體(w〇rking仇邱)如氟 氯烧(Freon )。 該蒸發部(evaporator) 10可為一方形殼體,以具良妤 ❿導熱效果之金屬如鋁合金製成,其外部底面η作為傳熱 面,供可對應密貼於一熱源部份如系統主機板之中央處理 器CPU (圖未示)上以藉熱傳導而移除該中央處理器 (cpu )因作業所產生之熱至蒸發部(evap〇rator) 上; 其頭侧面12上設一液體頭(Liquid head ) 13供液相工作液 體40a流入蒸發部10内,其尾侧面14上設一蒸汽頭(vapor head) 15供蒸發後之汽相工作液體4〇b流出蒸發部1〇。該 ?泰發部之内部設有至少一毛細體部(porous wick part) 16 及複數條蒸汽導槽(vaporgroove) 17,該毛細體部16内部 M336675 具有毛細結構及作用功能,可由高密度且具渗透度之聚乙 烯或燒結銅粉(sinter powder)組成,其毛細孔徑可為 1·05χ10·5ιη,而其參透度為6xl(T1()m2。該複數條蒸汽導槽 (vaporgroove) 17係設在毛細體部16之外圍,設計理念上 對於如何增加整體毛細泵吸環路(CPL )的驅動力,必須 由增加毛細壓差及減少整個環路壓降兩方面來考量,一方 面為了需要較小的毛細孔徑(porous radius)來吸附冷凝之液 相工作液體40a到達蒸發器1〇上内表面加熱,一方面亦須 籲考慮因採用較小孔徑所造成工作流體在蒸發器10内部多孔 毛細體部16内流動所造成的流阻(fl〇w resistance)增大等問 題,因此便採用了複數條蒸汽導槽17的設計,使其可傳送 因吸收熱量而蒸發的汽相工作液體40b,且汽相工作液體 40b在複數條蒸汽導槽17之末端被收集而由蒸發器1〇之尾 侧面14上之蒸汽頭(vapor head) 15排出。 該環狀通道20係佈設在蒸發器10之外部且連接在蒸汽 頭15與液體頭13之間,其佈局方式不拘,可隨所應用高能 •量密度之電子構裝產品如車用數位錄影系統(MDVR)之 内部空間而改變佈局方式。 該冷凝部30主要係設在環狀通道2〇上,也就是環狀通 道20可當作冷凝管,而其主要功能係用以移除由蒸發器川 之蒸汽頭15排出之汽松工作液體4〇b的熱量,使該汽相工 作液體40b再變相(凝結)成液相工作液體4〇&並經由液 體頭13流入蒸發部10内。該冷凝部3〇可隨所應用高能量密 度之電子構裝產品如車用數位錄影系統(MDVR)之内部 空間而改變佈局方式,該冷凝部3〇可利用傳導體3ι包覆在 11 M336675Dispersion provides - 4 force capillary pumping loop, but the phase is recognized, and 1 is set to 'advance step'. Attach a diffusing heat spreader on the outer bottom surface of the capillary sucking loop (CPL). W), " =, attached to the heat source part such as the central processing unit (cpu), in order to enhance the dispersion, and efficiency. It can meet the temperature control requirements of the system. (10) requires temperature control at a wide temperature of -30 °C to 6 °C. Another object of the present invention is to provide a gravity-type capillary pumping loop two-phase flow heat dissipating device, which can further add a work between the cold portion of the capillary pumping loop (cpL) and the liquid head of the evaporation portion. The fluid storage tank can be used to meet the temperature control requirements of the system, such as MDVR requirements for temperature control from -30 °C to 60 °C. [Embodiment] The above and other technical features and advantages of the present invention will be described in more detail below with reference to the accompanying drawings. Referring to Figures 1, 2, and 3, respectively, an embodiment of the present invention is provided. The basic structure and the schematic view of the internal structure of the evaporation section and the transverse section. This creation is a gravity-type capillary pumping loop C Capillary Pumped Loop, abbreviated as CPL) two-phase flow heat sink 9. M3.36675 1 , the two-phase flow heat transfer method is far more efficient than single-phase heat transfer, and its characteristics are utilized Workfluid The latent heat change between two phases quickly removes a large number of heat sources, which can be applied to high-energy-density electronic components such as MDVR (Mobile Digital Video Recorder, MobileDVR). For removing the heat source part of the system, such as the heat generated by the central processing unit (CPU) of the system motherboard; and in the state where the liquid phase and the vapor phase coexist, there is no temperature difference between the two phases, and the heat energy is absorbed or released. The direction changes from the liquid phase back to the vapor phase or from the vapor phase back to the liquid phase. The former is called the evaporation process, the latter is the condensation process, and the heat transfer device developed according to this concept is called the capillary sucking loop ( CPL). The creation gravity CPL dual-phase flow heat dissipation device 1 mainly comprises at least one evaporator 10, an annular passage 20 and a condensation portion 3, and is provided by the evaporation portion 10, the annular passage 20 and the condensation portion. 3〇 constitutes a capillary pumping loop (CPL)' and the working fluid (w〇rking Qiuqiu) such as Freon is filled in the loop. The evaporator 10 can be a square casing made of a metal having a good heat conduction effect, such as an aluminum alloy, and the outer bottom surface η serves as a heat transfer surface for being closely attached to a heat source portion such as a system. The central processing unit CPU (not shown) of the motherboard removes the heat generated by the operation of the central processing unit (cpu) by the heat transfer to the evaporator; the liquid is disposed on the head side 12 A liquid head liquid 13a flows into the evaporation portion 10, and a vapor head 15 is disposed on the tail side 14 for the vaporized working liquid 4〇b after evaporation to flow out of the evaporation portion 1〇. The interior of the Taifa Department is provided with at least one porous wick part 16 and a plurality of vapor grooves. The inside of the capillary portion 16 has a capillary structure and a function, and can be high-density and The permeability of polyethylene or sintered copper powder (sinter powder), the capillary diameter of which may be 1·05χ10·5ιη, and the penetration degree is 6xl (T1() m2. The plurality of vapor grids (vaporgroove) 17 series On the periphery of the capillary portion 16, the design concept of how to increase the driving force of the overall capillary pumping loop (CPL) must be considered by increasing the capillary pressure difference and reducing the entire loop pressure drop. A small capillary radius is used to adsorb the condensed liquid phase working liquid 40a to reach the inner surface of the evaporator 1 加热. On the one hand, it is also necessary to consider the porous capillary of the working fluid inside the evaporator 10 due to the use of a smaller aperture. The problem of increased flow resistance (fl〇w resistance) caused by the flow in the portion 16 is such that a plurality of steam channels 17 are designed to transmit vapor phase working fluid which evaporates due to heat absorption. The body 40b, and the vapor phase working liquid 40b is collected at the end of the plurality of steam channels 17, and is discharged from the vapor head 15 on the tail side 14 of the evaporator 1 . The annular channel 20 is arranged to evaporate. The outside of the device 10 is connected between the steam head 15 and the liquid head 13, and the layout thereof is not limited, and the layout can be changed according to the internal space of the electronic component product such as the digital video recording system (MDVR) of high energy and quantity density applied. The condensing portion 30 is mainly disposed on the annular passage 2, that is, the annular passage 20 can be used as a condensing pipe, and its main function is to remove the squid discharged from the steam head 15 of the evaporator. The heat of the working liquid 4〇b causes the vapor phase working liquid 40b to be disguised (condensed) into a liquid phase working liquid 4〇& and flows into the evaporation portion 10 via the liquid head 13. The condensation portion 3〇 can be applied as applied The energy density of the electronic component product, such as the interior space of the digital video recording system (MDVR), changes the layout. The condensation section 3 can be covered with a conductor 3ι at 11 M336675

環狀通道20之全部(如圖18所示)或一局部(如圖9所 示)上,並可配合散熱鰭片32 (如圖9、18所示)或使傳 導體31及/或散熱鰭片32連接至MDVR之外殼體(圖未 示)上,藉以形成熱沈部份(heatsink )以有效移除環狀 通道20内汽相工作液體40b之熱量;換言之,冷凝部30之 結構便較簡單,為了減少流阻,所有環狀通道2〇可當作冷 凝管,且皆為平滑且導熱性極佳之設計。又冷凝部30亦可 利用mobileDVR現有之外殼以鋁擠型成為中空之鋁殼,設 汁的主要考量為有足夠的能力將由蒸發器1〇所產生的蒸汽 元全的冷凝下來。 藉上述結構,液相工作流體4〇a可自液體頭13流入蒸 發部10内部,再藉由毛細體部16之毛細力作用吸附並同時 於此吸熱而蒸發成為汽相工作流體40b,再藉複數條蒸汽 導槽17匯抓導人蒸汽頭15排出並流至環狀通道2()中流動, 再藉由冷凝部30釋放出潛熱而回復為液相工作流體4〇a, =經由液體頭13流人蒸發部_再受熱蒸發,完成一加強 二毛細作用推力之重力式自然循環的移熱作用,藉以達成 無扇下之最大熱傳量的散熱效果,並有效克服習知水果 j環路之笨重、體祕A且無法解決高瓦數及無法滿足寬 他(如_30。(:至60。(:)之控溫的問題。 敎梦L ί創作之重力式毛細心及環路(CPL )雙相流散 财慮真空問題,因為真空度不佳會造成非凝 加’也會影響冷凝部3〇與蒸發部咖熱傳性 =以及整體環路之控制溫度,因㈣於系统真空度要求 便特別嚴格,環路設計上須減少閥門的使用、,以減少不必 12 M336675 要的浪漏,一般設計真空度的規格為lxl〇_5t〇rr (陶爾 力單位,相當於1厘米汞枉商cm-Hg柱高),亦即在壓 填入工作流體40之前,本創作之毛細果吸環路(; 部壓力以能夠降低至lxl0_5 torr (陶爾)為佳,而—, 壓為760 torr (陶爾)。 氣 又蒸發部(evaporator) 10設計成一方形殼體,乃b、 配合電子發熱元件(如CPU)的幾何形狀,而其尺寸 為50mmx50mmx20mm以合乎Intel公司之pen^jm π时 叹All of the annular passages 20 (as shown in FIG. 18) or a portion (as shown in FIG. 9) may be combined with the heat dissipation fins 32 (as shown in FIGS. 9 and 18) or the conductors 31 and/or heat dissipation. The fins 32 are connected to an outer casing (not shown) of the MDVR to form a heat sink to effectively remove heat from the vapor phase working liquid 40b in the annular passage 20; in other words, the structure of the condensation portion 30 is formed. Simpler, in order to reduce flow resistance, all annular channels 2 can be used as condenser tubes, and both are smooth and thermally conductive. The condensing section 30 can also be made into a hollow aluminum shell by using the existing outer casing of the mobile DVR. The main consideration of the juice is that it has sufficient capacity to condense the steam element generated by the evaporator 1 全. With the above structure, the liquid phase working fluid 4〇a can flow from the liquid head 13 into the interior of the evaporation portion 10, and is adsorbed by the capillary force of the capillary portion 16 and simultaneously evaporates into the vapor phase working fluid 40b by the heat absorption, and then borrows A plurality of steam guiding grooves 17 are taken out to guide the steam head 15 to be discharged and flow to the annular passage 2 (), and then released to the liquid phase working fluid 4〇a by the latent heat released by the condensation portion 30, = via the liquid head The 13-person evaporating part _ is further heated and evaporated to complete the heat transfer effect of a gravity-type natural circulation that strengthens the two-capillary action thrust, thereby achieving the heat dissipation effect of the maximum heat transfer without the fan, and effectively overcoming the conventional fruit j-loop It's cumbersome, secret A and can't solve high wattage and can't satisfy wide (such as _30. (: to 60. (:) temperature control problem. Nightmare L ί creation of gravity capillary and loop ( CPL) Two-phase flow is a vacuum problem, because the vacuum will cause non-condensation, which will also affect the heat transfer of the condensing part 3〇 and the evaporation part, and the control temperature of the overall loop, because (4) the system vacuum The requirements are particularly strict, and the loop design must reduce the valve The use of, in order to reduce the need for 12 M336675 to the leakage, the general design of the vacuum specification is lxl〇_5t〇rr (Taoer force unit, equivalent to 1 cm mercury quotient cm-Hg column height), that is, Before the pressure of the working fluid 40, the capillary of the present invention is sucked (the pressure is reduced to lxl0_5 torr (Taul), and the pressure is 760 torr (Taur). Evaporator 10 is designed as a square housing, b, with the geometry of electronic heating elements (such as CPU), and its size is 50mmx50mmx20mm to meet Intel's pen^jm π sigh

v早晶片 C single chip ),或設為 105 mmx 162 mmx 24 mm 以合伞 CPU之需求。 、’雙 參照圖4_8所示,其分別係本創作之蒸發部另一 例内部結構之上視、橫向斷面、正視斷面、及所使用 體部及組裝毛細體部後之示意圖(且標示參考用尺寸)、 本實施例之蒸發部(evaporator) 1〇之内部設有至少一毛系 體部(porouswickpart) 16及複數條蒸汽導槽(vap〇r 、、田 groove ) 17,而毛細體部16及複數條蒸汽導槽口之間的妹 構型悲並不特別限制,其中該蒸發部(evap〇rat〇r ) 之私 體内部之上、下面可分別設置複數條蒸汽導槽(vap〇r叹 groove ) 17如圖4、5所示,並在上、下面兩排複數條 ,導槽17之間形成_室腔18供設置—相對應形狀之毛細= I516如圖7所示,使該毛細體部π可夾設在上、下兩排複 數條蒸汽導槽17之間如圖8所示;而毛細體部16上設有一 朝向液體頭13之開口槽161,供液相工作流體4〇a可由液 體碩13流入蒸發部10内部並經由開口槽161而流入毛細體 部16内部(請同時參照圖4-8所示),俾可藉由毛細體部 13 M336675 16之毛細力作用吸附並同時於此吸熱而蒸發成為汽相工作 流體働,再藉複數條蒸汽導槽n匯流導入蒸汽頭㈣ 出;又毛細體部16在開口槽161之開口端處設有擂止用凸 緣162,藉以擋止液相工作流體4加因毛細體部16之毛細 力作用吸附而回流向液體頭13。 參照圖9、10、11所示,其分別係本創作另-實施例 (設具二蒸發部)以及其蒸發部之局部透視及分解之示意 圖。本實_之重力式毛細I吸環路(CPL)之雙相流散 熱裝置Μ具二蒸發部1G以對應於二電子發熱元件如cpu (圖未不)、,且該二蒸發部1〇相對於環狀通道如係採用並 聯^列方式,也就是二蒸發部1G之液體是連接至相同 之環狀通道20 ’使藉由冷凝部3G凝結之液相工作流體40a 可同時由各液體頭13進入各蒸發部1〇内。又本實施例之冷 凝邛30並不限制如圖9所示之局部結構,該冷凝部可利 用傳導體31包覆在環狀通道2〇之全部如圖18所示,並可配 合散熱鰭片32 (如圖9、18所示)或使傳導體31及/或散 熱鰭片32連接至MDVR之外殼體(圖未示)上。又,本實 施例之蒸發部10之内部設有至少一毛細體部(p〇r〇uswick part ) 16及複數條蒸汽導槽(vaporgr〇〇ve) 17,而毛細體 部16及複數條蒸汽導槽17之間的結構型態並不特別限制, 其中該蒸發部(evaporator) 10之殼體内部之下緣面可佈設 複數條蒸汽導槽(vapor groove ) 17如圖1〇、π所示,並在 下緣面之複數條蒸汽導槽17之上方形成一室腔18供設置一 相對應形狀之毛細體部16如圖11所示,使該毛細體部16可 嵌設在複數條蒸汽導槽17上方;而毛細體部16上設有一朝 M336675 向液體頭13之開口槽161,供液相工作流體4加可由液體 頭13流入蒸發部10内部並經由開口槽161而流入毛細體部 16内部(請同時參照圖所示),俾可藉由毛細體部 16之毛細力作用吸附並同時於此吸熱而蒸發成為汽相工作 流體働,再藉複數條蒸汽導槽17匯流導入蒸汽頭15排 出;又毛細體部16在開口槽161之開口端處設有擔止用凸 緣162,藉以擂止液相工作流體4〇a因毛細體部16之毛細 力作用吸附而回流向液體頭13。 •參照圖12-15所示,其分別係圖9之蒸發部另一實施 例之局部透視、分解、局部立體及分解示意圖。本實施例 之重力式毛細泵吸環路(CPL )之雙相流散熱裝置2設具 二蒸發部10以對應於二電子發熱元件如CPU (圖未示), 其與圖9所示雙相流散熱裝置2之間的主要不同係在於蒸 發部10之内部結構;本實施例之蒸發部1〇之内部設有一毛 細體部(porouswickpart) 16及複數條蒸汽導槽(vapor groove ) 17,其中該蒸發部(evaporator) 10之殼體(可為 _ 一鋁擠型體)内部之下緣面可形成圓弧形並佈設複數條蒸 汽導槽(vaporgroove) 17如圖13-15所示,使圓弧形下緣 面之複數條蒸汽導槽17上方形成一室腔18供設置一相對應 形狀之毛細體部16如圖13_15所示,使該毛細體部16可嵌 設在複數條蒸汽導槽17上方;而毛細體部16上設有一朝向 液體頭13之開口槽161,供液相工作流體40a可由液體頭 13流入蒸發部1〇内部並經由開口槽161而流入毛細體部16 内部,俾可藉由毛細體部16之毛細力作用吸附並同時於此 吸熱而蒸發成為汽相工作流體40b,再藉複數條蒸汽導槽 15 M336675 17匯流導入蒸汽頭15排出;又毛細體部16在開口槽161之 開口端處設有擋止用凸緣162,藉以擋止液相工作流體 40a因毛細體部16之毛細力作用吸附而回流向液體頭13。 參照圖16所示,其係圖9中二蒸發部採串聯排列時形 成一蒸發部之局部立體示意圖。本實施例之重力式毛細泵 吸裱路(CPL )之雙相流散熱裝置係設具一長度較大之蒸 毛邛’也就疋其毛細體部(P〇r〇USwiekpart) 16及複數條蒸 汽導槽(vaporgroove) 17的長度較大,使該蒸發部相對於 環狀通道20可呈串聯排列方式以對應於二電子發熱元件如 CPU (圖未示),也就是該蒸發部相對於環狀通道如只具 有-液體頭(13)及-蒸汽頭(15),而該蒸發部之外部 底面係以其長度較大的長度向同時對應密貼於二電子發熱 元件如CPUJi (圖未示),以藉熱傳導而移除該二電子發 熱元件如CPU因作業所產生之熱至同—蒸發部,也就是二 電子發熱元件如CPU之位置相對於環狀通道_形成串聯 排列^式,此與圖9中二蒸發部採並聯排列方式不同;經 實體實驗得知,蒸發部採用串聯排列方式崎應於子 發熱元件其對熱源之移除效果比並聯排列方式差。一 a ,參照圖17所示,其係本創作蒸發部之外部底面上設〆 二播用導熱片(spreader)作為傳熱面之橫向斷面示音:。 本創作之重力式毛細泵吸環路(CPL ) 二 丨”進一步可在其蒸心 導熱片(-)50,再對應㈣於熱源部份如 推2 機板6G之中央處理器(CPU) 61上,藉以增 政♦、、、效果,而可滿足系統之控溫要求如娜呢要求在^ M336675 溫-30 C至60 C之控溫要求。 參照圖18所示,其係圖9所示實施例之冷凝部另一實 施例立體示意圖。本實施例重力式毛細泵吸環路(CPL ) 之雙相流散熱裝置之規格如下: 1、 CPL 之材料:|呂(Aluminum )或銅(Copper ) 2、 蒸發部:45X45X23.5 mm3 & 45X45X23.5 mm3 3、 冷凝部:8ψ 4、 蒸汽頭:8mm Φ 5、液體頭:8 mm 6、 毛細體部·具渗透度之聚乙婦(Porous Polyethylene ) 7、 毛細有效孔徑(Porous Effect Radius ) : ΙΟ·4 m〜10-5 m 8、 滲透度(Porous Permeability ) : 6X10_1Gm2 9、 工作流體(WorkingFluid ):氟氯烷(Freon ) 10、 環路真空度(System Vacuum ) : 10-4 〜l〇_5Torrv early chip C single chip ), or set to 105 mmx 162 mmx 24 mm to meet the needs of the umbrella CPU. , 'Double reference to Figure 4_8, which is a schematic view of the internal structure of the other part of the evaporation section of the present invention, the transverse section, the front section, and the body and the assembly of the capillary part (and the reference In the inside of the evaporator of the present embodiment, at least one hairy body part 16 and a plurality of steam guiding grooves (vap〇r, 谷 groove) 17 are provided, and the capillary portion is provided. The sister configuration between the 16 and the plurality of steam guiding slots is not particularly limited, and a plurality of steam guiding grooves (vap〇) may be respectively disposed above and below the private portion of the evaporation portion (evap〇rat〇r). r sing groove] 17 as shown in Figures 4 and 5, and in the upper and lower rows of a plurality of rows, between the channel 17 forming a chamber 18 for the setting - the corresponding shape of the capillary = I516 as shown in Figure 7, The capillary portion π can be sandwiched between the upper and lower rows of the plurality of steam guiding grooves 17 as shown in FIG. 8; and the capillary portion 16 is provided with an opening groove 161 facing the liquid head 13 for the liquid working fluid. 4〇a may flow into the interior of the evaporation portion 10 from the liquid stalk 13 and flow into the capillary via the open groove 161 Inside the part 16 (please refer to FIG. 4-8 at the same time), the crucible can be adsorbed by the capillary force of the capillary portion 13 M336675 16 and simultaneously evaporates into a vapor phase working fluid 于此 under the heat absorption, and then borrows a plurality of vapor guides. The trough n is introduced into the steam head (4); and the capillary portion 16 is provided with a quenching flange 162 at the open end of the opening groove 161, thereby blocking the liquid phase working fluid 4 from being adsorbed by the capillary force of the capillary portion 16. And returning to the liquid head 13. Referring to Figures 9, 10 and 11, respectively, they are schematic views of a partial perspective and decomposition of the present embodiment (the two evaporation portions) and the evaporation portion thereof. The two-phase flow heat dissipating device of the gravity type capillary I suction loop (CPL) of the present invention has two evaporation portions 1G corresponding to two electron heating elements such as cpu (not shown), and the two evaporation portions are relatively The annular passages are connected in parallel, that is, the liquid of the two evaporation portions 1G is connected to the same annular passage 20' so that the liquid phase working fluid 40a condensed by the condensation portion 3G can be simultaneously supplied by the respective liquid heads 13 It enters each evaporation part 1〇. The condensation enthalpy 30 of the present embodiment is not limited to the partial structure shown in FIG. 9. The condensing portion can be covered by the conductor 31 in the annular channel 2, as shown in FIG. 18, and can be matched with the heat dissipation fins. 32 (as shown in Figures 9, 18) or to connect the conductor 31 and/or the heat sink fin 32 to an outer casing (not shown) of the MDVR. Further, the inside of the evaporation portion 10 of the present embodiment is provided with at least one capillary portion 16 and a plurality of vapor guides 17, and the capillary portion 16 and the plurality of steams The structural form between the guide grooves 17 is not particularly limited, and a plurality of vapor grooves 17 may be disposed on the lower inner surface of the casing of the evaporator 10 as shown in FIGS. 1 and π. And forming a chamber 18 above the plurality of steam guiding grooves 17 of the lower edge surface for providing a corresponding shape of the capillary portion 16 as shown in FIG. 11, so that the capillary portion 16 can be embedded in the plurality of vapor guides. Above the groove 17, the capillary portion 16 is provided with an opening groove 161 toward the liquid head 13 toward the liquid head 13, and the liquid phase working fluid 4 is supplied from the liquid head 13 into the evaporation portion 10 and flows into the capillary portion 16 through the opening groove 161. Internally (please refer to the figure at the same time), the crucible can be adsorbed by the capillary force of the capillary body portion 16 and simultaneously evaporated to become the vapor phase working fluid crucible by the endothermic heat, and then introduced into the steam head 15 by a plurality of steam guiding channels 17 Discharge; and the capillary portion 16 is opened in the open slot 161 End stop is provided with supporting flanges 162, thereby retaining the liquid working fluid 4〇a beat by capillary force of the capillary member 16 and the back flow of the liquid portion of the adsorption head 13. Referring to Figures 12-15, there are shown, respectively, partial perspective, exploded, partial perspective and exploded views of another embodiment of the evaporation section of Figure 9. The two-phase flow heat dissipating device 2 of the gravity capillary pumping loop (CPL) of the present embodiment is provided with two evaporation portions 10 to correspond to two electronic heating elements such as a CPU (not shown), which is dual-phased as shown in FIG. The main difference between the flow heat sinks 2 is the internal structure of the evaporation portion 10; the interior of the evaporation portion 1 of the present embodiment is provided with a capillary portion 16 and a plurality of vapor grooves 17, of which The lower edge surface of the casing of the evaporator 10 (which may be an aluminum extruded body) may be formed into a circular arc shape and a plurality of vapor grooves (vaporgroove) 17 are arranged as shown in FIG. 13-15. A plurality of chambers 18 are formed above the plurality of steam guiding grooves 17 of the circular arc-shaped lower edge surface for providing a correspondingly shaped capillary portion 16 as shown in FIG. 13-15, so that the capillary portion 16 can be embedded in the plurality of vapor guides. Above the groove 17, the capillary portion 16 is provided with an opening groove 161 facing the liquid head 13, and the liquid phase working fluid 40a can flow from the liquid head 13 into the interior of the evaporation portion 1 and into the inside of the capillary portion 16 via the opening groove 161.俾 can be adsorbed by the capillary force of the capillary portion 16 At this time, it absorbs heat and evaporates into a vapor phase working fluid 40b, and then flows through a plurality of steam channels 15 M336675 17 to be introduced into the steam head 15; and the capillary portion 16 is provided with a stopper flange at the open end of the opening groove 161. 162, in order to prevent the liquid phase working fluid 40a from being adsorbed by the capillary force of the capillary portion 16 and returning to the liquid head 13. Referring to Fig. 16, there is shown a partial perspective view of an evaporation portion when the two evaporation portions are arranged in series in Fig. 9. The two-phase flow heat dissipating device of the gravity type capillary pump suction road (CPL) of the present embodiment is provided with a long-sized steamed broom', which is also a capillary portion (P〇r〇USwiekpart) 16 and a plurality of strips. The length of the vapor groove 17 is relatively large, so that the evaporation portion can be arranged in series with respect to the annular passage 20 to correspond to a two-electron heating element such as a CPU (not shown), that is, the evaporation portion is opposite to the ring. The channel has only a liquid head (13) and a steam head (15), and the outer bottom surface of the evaporation portion is closely attached to the two electronic heating elements such as the CPUJi with a length corresponding to the length of the evaporation portion (not shown) Removing the heat generated by the operation of the two electronic heating elements such as the CPU to the same evaporation portion, that is, the position of the two electronic heating elements such as the CPU is arranged in series with respect to the annular channel. It is different from the parallel arrangement of the two evaporation sections in Fig. 9; it is known from the physical experiment that the evaporation section adopts a series arrangement manner, and the removal effect of the heat source is worse than that of the parallel arrangement. As shown in Fig. 17, the outer surface of the evaporation portion of the present invention is provided with a spreader for the second broadcast as a transverse section of the heat transfer surface: The gravity-type capillary pumping loop (CPL) of the creation is further available in its core (-) 50, and then in the heat source part, such as the central processor (CPU) of the 6G board. On the basis of the increase in government ♦,, and effects, and can meet the temperature control requirements of the system, such as Na, the temperature control requirements of ^ M336675 temperature -30 C to 60 C. Referring to Figure 18, it is shown in Figure 9. A schematic view of another embodiment of the condensation portion of the embodiment. The specifications of the dual-phase flow heat sink of the gravity capillary pumping loop (CPL) of the present embodiment are as follows: 1. Material of CPL: | Lu or Aluminum (Copper) 2) Evaporation section: 45X45X23.5 mm3 & 45X45X23.5 mm3 3. Condensation section: 8ψ 4. Steam head: 8mm Φ 5. Liquid head: 8 mm 6. Capillary body · Polyethylene with permeability ( Porous Polyethylene ) 7. Porous Effect Radius : ΙΟ·4 m~10-5 m 8. Porous Permeability: 6X10_1Gm2 9. Working Fluid (FingerFluid): Fluorine (Freon) 10, Ring Road Vacuum (System Vacuum ) : 10-4 ~l〇_5Torr

11、 最大熱量(Qmax ) : l〇〇W11, the maximum heat (Qmax): l〇〇W

12、 系統熱阻抗(System Thermal Resistance ) : 0.3 °C /W Φ 13、系統作業溫度 Tcpu (System Operation Temperature) : 7012, System Thermal Resistance: 0.3 °C / W Φ 13, system operating temperature Tcpu (System Operation Temperature): 70

°C°C

14、環境溫度(Ambient temperature ) : 40°C 再參照圖19、20所示,其分別係圖18所示實施例另設 具一工作液體儲槽之分解立體及組合立體示意圖。本創作 進一步可在毛細栗吸ί哀路(CPL )之冷凝部(c〇ndenser ) 30及蒸發部(evaporator) 10之液體頭(Liquid head ) 13 之 間增設一工作流體40之儲槽70,藉以增進散熱效果,而可 滿足系統之控溫要求如MDVR要求在寬溫_3〇 t至60 °C之 17 M336675 控溫要求;因此本實施例與圖18所示實施例之不同為本實 施例又加上一個儲槽70以作為環路之控溫用,當蒸汽由蒸 汽頭15進入冷凝部30時,隨即在此釋放出潛熱,完成移熱 的目的,本實施例設計的要點為確保冷凝部30出口為次冷 態(subcooled)。本實施例之規格如下: 1、 CPL 之材料:銘(Aluminum)或銅(Copper ) 2、 蒸發部:45X45X23.5 mm3 & 45X45X23.5 mm3 3、 冷凝部:8ψ _ 4、蒸汽頭:8mm 5、 液體頭:8mm 6、 毛細體部:具滲透度之聚乙烯(Porous Polyethylene ) 7、 毛細有效孔徑(Porous Effect Radius ) : ΚΓ4 m〜10·5 m 8、 滲透度(Porous Permeability ) : 6X10"10 m2 9、 工作流體(WorkingFluid ):氟氣烧(Freon ) 10、 環路真空度(SystemVacuum ) : 10_4〜10-5Torr14. Ambient temperature: 40 ° C Referring again to Figs. 19 and 20, respectively, the embodiment shown in Fig. 18 is further provided with an exploded three-dimensional and combined perspective view of a working liquid storage tank. The creation further includes a storage tank 70 for the working fluid 40 between the condensation portion (c〇ndenser) 30 of the capillary pumping road (CPL) and the liquid head 13 of the evaporation unit 10. In order to improve the heat dissipation effect, it can meet the temperature control requirements of the system, such as MDVR requires 17 M336675 temperature control requirements at a wide temperature _3〇t to 60 °C; therefore, the difference between this embodiment and the embodiment shown in FIG. 18 is the implementation. In addition, a tank 70 is added for temperature control of the loop. When steam enters the condensing unit 30 from the steam head 15, the latent heat is released therefrom to complete the heat transfer. The main point of the design of this embodiment is to ensure The outlet of the condensing section 30 is subcooled. The specifications of this embodiment are as follows: 1. Material of CPL: Aluminum or Copper 2. Evaporation: 45X45X23.5 mm3 & 45X45X23.5 mm3 3. Condensation: 8ψ _ 4. Steam head: 8mm 5. Liquid head: 8mm 6. Capillary part: Porous Polyethylene 7. Porous Effect Radius: ΚΓ4 m~10·5 m 8. Porous Permeability : 6X10&quot ; 10 m2 9, Working Fluid (FingerFluid): Fluorine (Freon) 10, Loop Vacuum (SystemVacuum): 10_4~10-5Torr

11、 最大熱量(Qmax ) : 100W11, the maximum heat (Qmax): 100W

鲁 12、系統熱阻抗(System Thermal Resistance ) : <0.95 °C /W 13、 系統作業溫度 Tcpu (System Operation Temperature) : 70Lu 12, System Thermal Resistance: <0.95 °C /W 13, system operating temperature Tcpu (System Operation Temperature) : 70

°C°C

14、 環境溫度(Ambient temperature ) ·· _25 °C 〜70 °C 15、 儲槽(Reservoir ) ·· 30X30X20mm3 16、 適用:mobile DVR (車用數位錄影系統MDVR ) 以上所示僅為本創作之較佳實施例,對本創作而言僅 是說明性的,而非限制性的。本專業技術人員理解,在本 M336675 J要求所限定的精神和範圍内可對其進行許多改 内。>改’甚至等效變更,但都將落入本創作的保護範圍 【圖式簡單說明】 圖i係本創作—實施例(設具-蒸發部)之基本架構立體 蒸發部(evapomtoO -實施_部結構之14. Ambient temperature ·· _25 °C ~70 °C 15. Reservoir (Reservoir) ·· 30X30X20mm3 16. Applicable: mobile DVR (Digital Video Recording System MDVR) The above is only for this creation. The preferred embodiment is illustrative only and not limiting. It will be understood by those skilled in the art that many modifications can be made within the spirit and scope defined by the requirements of this M336675 J. >Change 'even equivalent change, but will fall within the scope of protection of this creation [Simple description of the schema] Figure i is the basic structure of the creation - the embodiment (set - evaporation section) three-dimensional evaporation department (evapomtoO - implementation _ part structure

上視示意圖。 =3係圖2所示蒸發部之内部結構橫向斷面示意圖。 f搞,本創作之蒸發部另—實施例内部結冑之上視示意圖 示參考収寸但尚未組裝毛細體部)。 圖:係圖4所示蒸發部之内部結構橫向斷面示意圖。(摔 示參考用尺寸) 、 圖=係圖4所不蒸發部之内部結構正面 不參考用尺寸) ^係圖4所示蒸發部之毛細體部立體示意圖。(標示來 亏用尺寸) 乂 圖8係圖4所不蒸發部之内部結構橫向斷面示意圖。(已 組裝毛細體部) 圖9係本創作另—實施例(設具二蒸發部且並聯排列)之 立體不意圖。 圖10係圖9之蒸發部—實施例之局部透視示意圖。 圖11係圖10之蒸發部之分解示意圖。 圖12係圖9之蒸發部另—實施例之局部透視示意圖。 圖13係係®12之蒸發部之分解示意圖。 M336675 圖14係圖13中蒸發部内部結構之局部立體示意圖。(已組 裝毛細體部) 圖15係圖14之分解示意圖。 圖16係圖9中二蒸發部採串聯排列時形成一較長蒸發部之 局部立體示意圖。 圖17係本創作蒸發部之外部底面上設一散播用導熱片 (spreader )作為傳熱面之橫向斷面示意圖。 圖18係圖9所示實施例之冷凝部另一實施例立體示意圖。 • 圖19係圖18所示實施例另設具一工作液體儲槽之分解立體 示意圖。 圖20係圖19所示實施例之組合立體示意圖。 【主要元件符號說明】 CPL雙相流散熱裝置1、2 蒸發部(evaporator ) 10 外部底面11 頭侧面12 ❿ 液體頭(Liquid head ) 13 尾侧面14 蒸汽頭(vapor head) 15 毛細體部(porous wick part ) 16 開口槽161 凸緣162 蒸汽導槽(vaporgroove) 17 室腔18 環狀通道20 M336675 冷凝部30 傳導體31 散熱鰭片32 工作液體40 液相工作液體40a 汽相工作液體40b 散播用導熱片(spreader ) 50 主機板60 _中央處理器(CPU ) 61 儲槽70The top view is schematic. = 3 is a schematic transverse sectional view of the internal structure of the evaporation portion shown in Fig. 2. f Engaged, the evaporation section of this creation is another example. The internal crusting of the embodiment shows the reference but the capillary part has not been assembled. Figure: is a schematic transverse sectional view of the internal structure of the evaporation portion shown in Figure 4. (Folding reference size), Fig. = The internal structure of the non-evaporating portion of Fig. 4 is not referenced.) ^ is a three-dimensional schematic view of the capillary portion of the evaporation portion shown in Fig. 4. (Marking the deficient size) 乂 Figure 8 is a schematic transverse cross-sectional view of the internal structure of the non-evaporating portion of Figure 4. (Mixed body portion has been assembled) Fig. 9 is a perspective view of another embodiment of the present invention (provided with two evaporation portions and arranged in parallel). Figure 10 is a partial perspective schematic view of the evaporation section of the Figure 9 - embodiment. Figure 11 is an exploded perspective view of the evaporation portion of Figure 10. Figure 12 is a partial perspective schematic view of another embodiment of the evaporation section of Figure 9. Figure 13 is an exploded perspective view of the evaporation section of the system 1212. M336675 Figure 14 is a partial perspective view showing the internal structure of the evaporation portion of Figure 13. (The capillary portion has been assembled) Fig. 15 is an exploded perspective view of Fig. 14. Fig. 16 is a partial perspective view showing the formation of a longer evaporation portion when the two evaporation portions are arranged in series in Fig. 9. Fig. 17 is a schematic transverse cross-sectional view showing a spreader for use as a heat transfer surface on the outer bottom surface of the evaporation portion of the present invention. Figure 18 is a perspective view showing another embodiment of the condensing portion of the embodiment shown in Figure 9. Figure 19 is an exploded perspective view of the embodiment of Figure 18 with a working fluid reservoir. Figure 20 is a perspective view showing the combination of the embodiment shown in Figure 19. [Main component symbol description] CPL two-phase flow heat sink 1, 2 Evaporator 10 External bottom surface 11 Head side 12 Li Liquid head 13 Tail side 14 Steam head 15 Capillary part (porous Wick part ) 16 Open groove 161 Flange 162 Vapor guide (ventilation groove) 17 Chamber 18 Annular passage 20 M336675 Condensation 30 Conductor 31 Heat sink fin 32 Working liquid 40 Liquid phase working fluid 40a Vapor phase working fluid 40b Dispersion Heat spreader (spreader) 50 motherboard 60 _ central processing unit (CPU) 61 storage tank 70

21twenty one

Claims (1)

M336675 九、申請專利範圍: 、-種重力式毛細果吸環路(CPL )雙相流散熱裝置, 係應用於高能量密度之電子構裝產品上如車用數位影 像錄影系統(MDVR);其係包含:至少—蒸發部、/ -環狀通道及-冷凝部,藉以構成一毛細泵吸環路 (CPL),而環路中並填入工作流體,其中:M336675 IX. Patent application scope: - A gravity-type capillary drip loop (CPL) dual-phase flow heat sink for high-energy density electronic components such as digital video recording systems for vehicles (MDVR); The system comprises: at least an evaporation portion, an - annular passage and a condensation portion, thereby forming a capillary pumping loop (CPL), and the working fluid is filled in the loop, wherein: 蒸發部’係-以具導熱效果之金屬製成之殼體,其外 部底面作為傳熱面,供可對應密貼於一熱源部份以藉 熱傳導而移除该熱源;其頭側面上設一液體頭供液相 工作液體流人蒸發㈣,其尾侧H蒸汽頭供蒸 發後之八相工作液體流出蒸發部,其内部設有至少一 毛細體部及複數條蒸汽導槽,該毛細體部具有毛細結 構及作用,该複數條蒸汽導槽係設在毛細體部之 圍; 環狀通道,係佈設在蒸發器 液體頭之間; 之外部且連接在蒸汽頭與The evaporating portion is a casing made of a metal having a heat conducting effect, and an outer bottom surface thereof serves as a heat transfer surface for being closely attached to a heat source portion to remove the heat source by heat conduction; The liquid head is supplied to the liquid working liquid to evaporate (4), and the eight-phase working liquid for evaporating from the tail side H steam head flows out of the evaporation portion, and at least one capillary portion and a plurality of steam guiding grooves are disposed inside the capillary portion. Having a capillary structure and function, the plurality of steam channels are arranged around the capillary portion; the annular passage is disposed between the liquid heads of the evaporator; the outside is connected to the steam head and 冷凝部,主要係設在環狀通道上,藉以形成熱沈部 (heatsink )用以移除由蒸發器之蒸汽頭排出之: 工作液體的熱量,使該汽相I作龍可凝結成 作液體並經由液體頭流入蒸發部内; 藉上述結構,液相卫作流體可自液體頭流人蒸發部 部,再藉由毛細體部之毛細力作用吸附並同時於此 熱而蒸發成為汽相J1作流體,再藉複數條蒸汽導槽 流導入蒸汽嬰iH並流至隸通道祕,再藉由^ 部釋放出潛熱而回復為液相工作流體,再經由液;頭 22 M336675 流入蒸發部内再受熱蒸發,完成一自然循環的移孰作 用。 ”、、 2、 如申請專利範圍第i項所述之重力式毛細泵吸環路 (CPL )雙相〃IL散熱裝置,其中該毛細杲吸環路可設 具兩個或以上之蒸發部,且該等蒸發部係採用並聯排 列方式設置在環狀通道上,使各蒸發部之液體頭是連 接至相同之環狀通道上,使藉由冷凝部凝結之液相工 作机體可同時由各液體頭進入各蒸發部内。 3、 如申請專利範圍第丨項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該蒸發部可為一方形 殼體。 4、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該蒸發部係以鋁製 成。 5、 如申请專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裴置,其中該毛細體部可利用高 雄、度且具渗透度之聚乙烯或燒結銅粉(sinter powder)組 成。 6、 如申請專利範圍第丨項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該毛細體部之毛細孔 徑可為1·〇5χ1〇5ιη,其滲透度為。 7、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該毛細泵吸環路 (CPL )之真空度以降低至lxl〇_5 t〇fr (陶爾)為 佳0 23 M336675 8、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該工作流體為氟氣烷 (Freon ) 〇 9、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該複數條蒸汽導槽係 佈設在蒸發部之殼體内部的下緣面上。 10、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該複數條蒸汽導槽係 • 佈設在蒸發部之殼體内部的圓弧形下緣面上。 11、 如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該冷凝部可利用熱傳 導體包覆在環狀通道之全部或一局部上,且熱傳導體 上並可設置散熱鰭片。 12、 如申請專利範圍第11項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該熱傳導體可為車用 數位影像錄影系統(MDVR )之外殼。 • 13、如申請專利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該毛細體部上設有一 朝向液體頭之開口槽,供液相工作流體可由液體頭流 入蒸發部内部並經由開口槽而流入毛細體部内部。 14、 如申請專利範圍第13項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其中該毛細體部在開口槽 之開口端處設有擋止用凸緣,藉以擋止液相工作流體 回流向液體頭。 15、 如申請權利範圍第1項所述之重力式毛細泵吸環路 24 M336675 (CPL )雙相流散熱裝置,其進一步可在蒸發部的外 部底面上貼附一散播用導熱片(spreader )。 16、如申請權利範圍第1項所述之重力式毛細泵吸環路 (CPL )雙相流散熱裝置,其進一步可在毛細泵吸環 路(CPL )之冷凝部及蒸發部之液體頭之間設置一工 作流體之儲槽。The condensing portion is mainly disposed on the annular passage to form a heatsink for removing the heat discharged from the steam head of the evaporator: the heat of the working liquid, so that the vapor phase I can be condensed into a liquid And flowing into the evaporation portion through the liquid head; by the above structure, the liquid phase fluid can flow from the liquid head to the evaporation portion of the liquid, and then adsorbed by the capillary force of the capillary portion and simultaneously evaporates into the vapor phase J1 by the heat. The fluid is then introduced into the vapor-inducing tank by a plurality of steam guiding channels and flows to the channel, and then returns to the liquid working fluid by releasing the latent heat through the portion, and then flows through the liquid; the head 22 M336675 flows into the evaporation portion and is then evaporated by the heat. , to complete the movement of a natural cycle. "," 2. For example, the gravity-type capillary pumping loop (CPL) two-phase 〃IL heat sink according to item i of the patent application scope, wherein the capillary sucking loop may be provided with two or more evaporation portions. And the evaporation portions are arranged in a parallel arrangement on the annular passage, so that the liquid heads of the evaporation portions are connected to the same annular passage, so that the liquid phase working body condensed by the condensation portion can be simultaneously The liquid head enters each evaporation portion. 3. The gravity capillary pumping loop (CPL) dual-phase flow heat dissipation device according to the scope of the patent application, wherein the evaporation portion can be a square housing. The gravity-type capillary pumping loop (CPL) dual-phase flow heat dissipating device according to the first aspect of the patent, wherein the evaporating portion is made of aluminum. 5. The gravity type capillary pump according to claim 1 The suction loop (CPL) is a two-phase flow heat dissipating device, wherein the capillary portion can be made of Kaohsiung, permeable and permeable polyethylene or sinter powder. Gravity capillary pumping loop (CPL) a two-phase flow heat dissipating device, wherein the capillary portion of the capillary portion may be 1·〇5χ1〇5ιη, and the permeability thereof is 7. The gravity capillary pumping loop (CPL) as described in claim 1 a two-phase flow heat sink in which the vacuum of the capillary pumping loop (CPL) is reduced to lxl 〇 _5 t 〇fr (Taur) is preferably 0 23 M336675 8 as described in claim 1 Gravity capillary pumping loop (CPL) two-phase flow heat sink, wherein the working fluid is a fluorine gas (Freon) 〇9, the gravity capillary pumping loop (CPL) as described in claim 1 a two-phase flow heat dissipating device, wherein the plurality of steam channels are disposed on a lower edge surface of the interior of the casing of the evaporation portion. 10. The gravity capillary pumping loop (CPL) as described in claim 1 a two-phase flow heat sink, wherein the plurality of steam channels are disposed on a circular arc-shaped lower edge surface inside the casing of the evaporation portion. 11. Gravity capillary pumping as described in claim 1 Loop (CPL) two-phase flow heat sink, wherein the condensation portion can utilize heat conduction The body is coated on all or a part of the annular passage, and the heat transfer body can be provided with heat dissipation fins. 12. The gravity capillary pumping loop (CPL) two-phase flow as described in claim 11 a heat dissipating device, wherein the heat conducting body can be a casing of a digital video recording system (MDVR) for a vehicle. • 13. A gravity-type capillary pumping loop (CPL) dual-phase flow heat dissipating device according to claim 1 of the patent application scope, The capillary portion is provided with an opening groove facing the liquid head, so that the liquid phase working fluid can flow from the liquid head into the interior of the evaporation portion and flow into the inside of the capillary portion through the opening groove. 14. The gravity-type capillary pumping loop (CPL) two-phase flow heat dissipating device according to claim 13, wherein the capillary body portion is provided with a blocking flange at the open end of the opening groove, thereby blocking The liquid phase working fluid is returned to the liquid head. 15. The gravity capillary pumping loop 24 M336675 (CPL) dual-phase flow heat sink according to claim 1, further capable of attaching a spreader for spreading on the outer bottom surface of the evaporation portion. . 16. The gravity-type capillary pumping loop (CPL) two-phase flow heat sink according to claim 1, further capable of being in the condensation portion of the capillary pumping loop (CPL) and the liquid head of the evaporation portion A working fluid reservoir is provided between them.
TW97202732U 2008-02-14 2008-02-14 Gravity type capillary pumped loop (CLP) two-phase flow heat-dissipating device TWM336675U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114916193A (en) * 2022-04-24 2022-08-16 大连保税区金宝至电子有限公司 Method for counter-gravity liquid delivery and heat sink

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114916193A (en) * 2022-04-24 2022-08-16 大连保税区金宝至电子有限公司 Method for counter-gravity liquid delivery and heat sink
CN114916193B (en) * 2022-04-24 2024-01-09 大连保税区金宝至电子有限公司 Method for conveying liquid against gravity and heat dissipating device

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