五、新型說明： 【新型所屬之技術領域】 本創作係有關於一種埶瞢勒上k 提H“ l，、、s熱讀輯造，特別是指可 =二“溫廢氣的降溫效率之熱管熱交換器構造。 【先前技術】 在工業產業領域中有著許多高溫的應用，如金屬冶全 、破璃工業、光電產業等等，隨之即衍生了許多廢液、廢 水及廢氣等相_環保問題。對於高溫的廢氣問題而言， 由於排出的氣體溫度很高，若直接排人大氣中，不僅提升 城中碳濃度，更會對環境產生不良的熱A效應，使空氣 〜蜀、能見度,¾劣；而且’高溫熱能直接排放於大氣之中 也是-種資源浪費。因此’目前對高溫廢氣有—種慣用的 處理方式，疣是在高溫廢氣排放前利用一種熱交換器進行 降溫處理，同時截取熱源再利用。 按，習知應用於處理廢熱氣體之熱交換器，其係利用 —流體迴路，並在該迴路内添加液體媒介（一般為：油）， 該迴路橫跨於高溫流道與低溫流道，二流道之間藉由隔板 分隔，使其形成二獨立之氣體通道。上述熱交換器常將其 應用於工業上煙道廢氣之廢熱回收，於此一操作中，煙道 之鬲溫廢氣係流通於高溫流道，使其藉熱傳導作用輸送至 流體迴路，流體迴路中的液態媒介吸收熱源後氣化，上升 M423819 =路之上半部位(亦即低溫流道中），迴路的管壁内因心 4回復成液態再回流至迴路下方的高溫流道中。惟查 ^述=迴路群屬同一通路，熱油靠熱廢氣釋放熱㈣ 二媒八二壁再吸熱後亦是藉對流熱傳釋熱給熱油，使該液 2媒"在熱傳過程只有溫賴化未作㈣化。因此，該種 咖降溫效率是有改善空間的(總括熱傳係數 ，，’勺為 32kca/m2. hr· 〇C )。另外，羽 4 _ 除了流r迴路㈣杜 父換器系統複雜， ，路的s件之外’油槽、油泵、閥件、輸送系統 專，句構成建置上的固難度與成本，並且複雜的系統亦增 么了故/¥的機率’而流體迴路若有漏油(破損）則必須全部停 =排除故障。爰是’創作一熱管熱交換器以求得解決上述 問喊之需求乃有其必要。 【新型内容】 效率=作之曰目的在於改善習知熱管熱交換器所存在降溫 、数:之問題。遂而提供一種可增加廢熱氣的降溫較率 之熱纟構造。 ，達上述目的’本創作包含框架及若干熱管所構成， ^框^以隔板分隔出-冷空氣流道與一廢熱氣流道，框 :内係痛多數個等距併列之熱管，該多數個熱管均貫穿 IW反熱官的下半部位於廢熱氣流道卜而熱管的上半部 則位於冷空氣流道中；其主要的設計在於，該熱管為 閉之金屬管體，熱f内部形成真空狀並添人適量之水液，· 4 外表面則以輻射狀設置有鰭片者。 糟由上述構造，本案熱管是—種能迅速傳送熱量之金 屬管，當執管之一總為刼 Μ ’ 上并$内之水液即蒸發形成蒸氣而 2熱以端’在該端釋出熱量冷凝為水液後，再回流 =而達到熱交換之目的。本案藉由 古2傳送熱量，水液在真空的密閉熱管内作用，將可提 ν 1專導效率。 【實施方式】 …兹配合圖式將本案實施例詳細說明如下，其所附圖僅 \。方式況明本案之基本結構。因此在該等圖示中僅標 示與本案有關之^件’且所顯示之^件非以實施時之數 目;;形狀、尺找㈣加轉製，其實際㈣時之規格尺 寸貫為一種選擇性之設計，閤先述明。 口月參知第-圖及第二圖所繪示的本案實施例示意圖。 本案：要包含一熱管10結構，該熱管10乃是-種作為傳 遞熱！的管件’其構造係為—封閉之金屬管體，熱管ι〇内 部形成真空狀並添人適量之液態媒介流體，較佳的，該液 態媒介㈣為水液。肖，熱f之外表面以難狀設置有縛 ’藉由轉片11的設置可幫助熱管1〇的導溫效率。熱 官10的上半部為凝結區12，而下半部則為蒸發區13。 請配合參閱第二圖所示，本實施例t更包含有框架 20’並於該框㈣内以隔板21分隔出一冷空氣流道22與 M423819 一廢熱氣流道23。該框架20用以容納多數個等距併列之 熱管10，該多數個熱管10均貫穿隔板21而使該熱管1〇 的下半部之蒸發區13位於廢熱氣流道23中，而熱管的 上半部之凝結區12則位於冷空氣流道22中。上述冷空氣 流道22與廢熱氣流道23係為二獨立之流體通道，冷空氣 流道22係包括隔板21以上之框架2〇及熱管1〇之凝結區 12。卩仞，而廢熱氣流道23則包括隔板21以下之框架 及熱管10之蒸發區13部份。V. New description: 【New technology field】 This creation department is about a kind of heat pump that can be used for the cooling efficiency of warm exhaust gas. Heat exchanger construction. [Prior Art] There are many high-temperature applications in the industrial industry, such as metallurgy, glass-making industry, photovoltaic industry, etc., which has led to many environmental problems such as waste liquid, waste water and waste gas. For high-temperature exhaust gas problems, because the temperature of the exhausted gas is very high, if it is directly discharged into the atmosphere, it will not only increase the carbon concentration in the city, but also cause a bad thermal A effect on the environment, making the air ~ 蜀, visibility, 3⁄4 inferior; Moreover, 'high-temperature heat energy is directly discharged into the atmosphere is also a waste of resources. Therefore, there is a conventional treatment method for high-temperature exhaust gas, which is cooled by a heat exchanger before high-temperature exhaust gas is discharged, and the heat source is intercepted and reused. According to the conventional heat exchanger for treating waste heat gas, the utility model utilizes a fluid circuit, and a liquid medium (generally: oil) is added in the circuit, and the circuit crosses the high temperature flow path and the low temperature flow path, and the second flow The channels are separated by a partition to form two separate gas passages. The above heat exchanger is often applied to waste heat recovery of industrial flue gas. In this operation, the flue gas of the flue is circulated in the high temperature flow path, and is transported to the fluid circuit by heat conduction, in the fluid circuit. The liquid medium absorbs the heat source and then gasifies, rising M423819 = the upper part of the road (ie, in the low temperature flow path), and the inner wall of the circuit returns to a liquid state and then flows back to the high temperature flow path below the circuit. However, the investigation is as follows: the circuit group belongs to the same path, and the hot oil releases heat by the hot exhaust gas. (4) After the second medium and the second wall are absorbed again, the heat is transferred to the hot oil by the convection heat, so that the liquid 2 medium " Only Wen Laihua has not done (four). Therefore, the coffee cooling efficiency has room for improvement (total heat transfer coefficient, 'spoon is 32kca/m2. hr· 〇C). In addition, the feather 4 _ in addition to the flow r circuit (four) Du Fu changer system complex, the road's s outside the 'oil tank, oil pump, valve parts, conveyor system, the sentence constitutes the construction of the difficulty and cost, and complex The system also increases the probability of / / ¥ and the fluid circuit if there is oil leakage (damage) must stop all = troubleshooting. It is necessary to create a heat pipe heat exchanger to solve the above demand. [New content] Efficiency = The purpose of the project is to improve the temperature and number of problems in conventional heat pipe heat exchangers. It provides a enthalpy structure that increases the cooling rate of waste heat. For the above purposes, 'this creation consists of a frame and a number of heat pipes, ^ frame ^ separated by a partition - cold air flow path and a waste hot air flow path, frame: internal pain, most equidistant juxtaposed heat pipes, the majority The heat pipe runs through the waste heat flow channel in the lower half of the IW anti-heating officer, while the upper half of the heat pipe is located in the cold air flow channel; the main design is that the heat pipe is a closed metal pipe body, and the inside of the heat f forms a vacuum. And add a proper amount of water, · 4 The outer surface is set with fins in the radial direction. According to the above configuration, the heat pipe of the present case is a metal pipe capable of rapidly transferring heat, and when one of the pipes is always 刼Μ', the water in the liquid is evaporated to form a vapor and the heat is released at the end. After the heat is condensed into water, it is refluxed to achieve the purpose of heat exchange. In this case, the heat is transmitted by the ancient 2, and the water liquid acts in a closed heat pipe of the vacuum, which can improve the efficiency of the ν 1 . [Embodiment] The embodiment of the present invention will be described in detail below with reference to the drawings, and the drawings thereof are only \. The mode shows the basic structure of the case. Therefore, in the illustrations, only the parts related to the case are marked and the number of parts displayed is not the number of implementations; the shape, the ruler is found (4) plus the conversion system, and the actual (four) specification size is a kind of selectivity. The design is described first. The schematic diagram of the embodiment of the present invention is illustrated in the first and second figures. In this case, a heat pipe 10 structure is included, and the heat pipe 10 is a kind of heat transfer! The pipe fitting 'is constructed as a closed metal pipe body, and the inside of the heat pipe ι is vacuum-formed and an appropriate amount of liquid medium fluid is added. Preferably, the liquid medium (4) is water liquid. Xiao, the surface of the heat f is arranged in a difficult shape. The setting of the rotor 11 can help the temperature control efficiency of the heat pipe 1〇. The upper half of the heat official 10 is the condensation zone 12 and the lower half is the evaporation zone 13. Referring to the second figure, the embodiment t further includes a frame 20' and a cold air flow path 22 and a M423819 waste heat flow path 23 are partitioned by the partition 21 in the frame (4). The frame 20 is configured to accommodate a plurality of equidistant juxtaposed heat pipes 10, each of which extends through the partition 21 such that the evaporation zone 13 of the lower half of the heat pipe 1 is located in the waste heat flow passage 23, and the heat pipe The half of the condensation zone 12 is located in the cold air flow passage 22. The cold air flow passage 22 and the waste heat flow passage 23 are two independent fluid passages, and the cold air flow passage 22 includes a frame 2 of the partition 21 and a condensation zone 12 of the heat pipe 1 . The waste heat flow passage 23 includes a frame below the partition 21 and a portion of the evaporation portion 13 of the heat pipe 10.
5月多閱第二圖所示，藉由上述結構之構成，本案熱? .熱交換II於操作時，該待降溫的熱廢氣係被引流於廢^ 流道23中流過熱flQ之蒸發區13，而冷空氣流道⑺ 輸入冷空氣而流經熱管1〇之凝結區12。藉此，當待降〉、 的f廢氣流經廢熱氣流道23時，熱管1Q之蒸發區13受』 熱氧的向溫影響，使其將熱能藉熱傳導作用輸送至献管^In the second figure, as shown in the second figure, by the above structure, the heat exchange of the case is performed. During the operation, the hot exhaust gas to be cooled is drained to the evaporation zone 13 of the superheated flQ flowing in the waste channel 23. And the cold air flow path (7) inputs cold air and flows through the condensation zone 12 of the heat pipe 1〇. Therefore, when the exhaust gas to be lowered flows through the waste heat flow passage 23, the evaporation zone 13 of the heat pipe 1Q is affected by the temperature of the hot oxygen, so that the heat energy is transferred to the pipe by the heat conduction effect.
^熱管H)中之液態媒介吸收熱能後會產生氣化作用而荐 變為，氣’使蒸氣上升至熱管上半部之凝結區12(亦p 冷空氣流道22中），由於冷空氣流道22中之埶管1〇管々 外的氣體為較低溫之冷空氣，故藉該低溫作用使上升於; 結區12的蒸氣冷凝回復為水液，該水液即延熱管10管, —至下方之蒸發區13(亦即廢熱氣流道23中）。 當廢熱氣通過埶管ΐη— 行熱交換咖時，係與熱管1011 違H的作用，熱f 1G内的液態媒介流體蒸 6 M423819 發成蒸氣上升至凝結區12後，經冷卻而凝結回復成液體沿 熱管10 f壁流下至蒸發㊄13，再被廢熱氣加熱而構成一 反覆的熱交換循環。由此熱傳原理可明顯得知，其熱傳機 制主要是由相變化（兩相）熱傳，兩相熱傳熱管内的液態媒 介流體因吸熱而蒸發，快速流向壓力較低的凝結區，並且 在此釋放出凝結潛熱而液化，該液化水液經由毛細管力及 重f流回原蒸發區完成-次循環，熱f 1Q内的液態媒介流 體藉反覆循環來達到熱傳導之目的。值得一提的是，熱管 10内。係呈真空狀並以水作為卫作液，水在真空的狀態下 將可以有效提高熱傳導效率。 由疋：本案熱熱交換器結構中，每—熱管1G係為獨 的’’、、傳it件’即使發生異常也不影響整體^備運轉，故 =較低’故障排除亦較為簡便。再者，本案熱傳機制主 要疋由兩相熱傳’當可有效提高熱料效率（ 數約為 50kca/m? hr。「、 , .、 …、1 寻货、 上 ..，相較於習知的熱管熱交換器而 5 ’其熱傳效率將提升約4〇百分比。 上述内容係為用以解釋本創作之較佳實施例，並非對 2 = 此’凡有在相同之精神下所作 飾或變更，皆仍應包括在本創作保護料之中 供諸多優點而;=著 ==用性，且其運用之技術手段及其構造特徵，確為 本案創作人所研發而成，嗣本案誠已符合專利之要件，表 7 M423819 依法提出申請，並祈賜專利權為禱。 【圖式fa彳单說明】 第一圖繪示本案熱管的結構圖； 第二圖繪示本案框架與熱管的立體結構圖； 第三圖繪示本案熱管的使用示意圖。 【主要元件符號說明】 10 熱管 11 鰭片 12 凝結區 13 蒸發區 20 框架 21 隔板 22 冷空氣流道. 23 廢熱氣流道^The liquid medium in the heat pipe H) will generate gasification after the absorption of heat energy, and the gas will raise the vapor to the condensation zone 12 of the upper half of the heat pipe (also in the cold air flow channel 22) due to the cold air flow. The gas outside the manifold 1 in the channel 22 is a cold air of lower temperature, so that the low temperature acts to rise; the vapor condensation in the junction region 12 is returned to the water liquid, and the water liquid is the heat pipe 10 tubes, To the evaporation zone 13 below (ie, in the waste heat flow channel 23). When the waste heat gas passes through the ΐ — 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 行 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 热 液态 液态 液态 液态 液态 液态 液态 液态 液态 液态 液态 液态The liquid flows down the wall of the heat pipe 10f to evaporate five 13, and is heated by the waste heat to form a repeated heat exchange cycle. According to the principle of heat transfer, the heat transfer mechanism is mainly caused by phase change (two-phase) heat transfer, and the liquid medium fluid in the two-phase heat transfer tube evaporates due to heat absorption, and rapidly flows to the condensation zone with lower pressure. And the condensed latent heat is released here to liquefy, and the liquefied water liquid is returned to the original evaporation zone via the capillary force and the heavy f to complete the secondary cycle, and the liquid medium fluid in the heat f 1Q is repeatedly circulated to achieve the purpose of heat conduction. It is worth mentioning that the heat pipe 10 is inside. It is vacuum-like and uses water as the vinegar. Water can effectively improve the heat transfer efficiency under vacuum. Since: in the heat exchanger structure of this case, each heat pipe 1G is a unique '', and the relay piece' does not affect the overall operation even if an abnormality occurs, so the lower = troubleshooting is also relatively simple. Furthermore, the heat transfer mechanism of this case is mainly caused by two-phase heat transfer' when it can effectively improve the efficiency of hot materials (the number is about 50kca/m? hr. ", , . , ..., 1 search for goods, upper.., compared to The conventional heat pipe heat exchanger 5' will increase the heat transfer efficiency by about 4%. The above is a preferred embodiment for explaining the present creation, not for 2 = this is done in the same spirit. Decorations or changes should still be included in the creation of protective materials for many advantages; ===use, and the technical means and structural features of the application, which was developed by the creator of the case, Cheng has already met the requirements of the patent, Table 7 M423819 filed according to law, and prayed for the patent right. [Illustration of the fa彳 single] The first picture shows the structure of the heat pipe in this case; the second picture shows the frame and heat pipe of the case The three-dimensional structure diagram; The third diagram shows the use of the heat pipe in this case. [Main component symbol description] 10 Heat pipe 11 Fin 12 Condensation zone 13 Evaporation zone 20 Frame 21 Partition 22 Cold air flow path. 23 Waste heat flow path