TWM288923U - Heat exchange device for liquid - Google Patents

Heat exchange device for liquid Download PDF

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Publication number
TWM288923U
TWM288923U TW94219097U TW94219097U TWM288923U TW M288923 U TWM288923 U TW M288923U TW 94219097 U TW94219097 U TW 94219097U TW 94219097 U TW94219097 U TW 94219097U TW M288923 U TWM288923 U TW M288923U
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Taiwan
Prior art keywords
tube
liquid
heat exchange
exchange device
refrigerant
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TW94219097U
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Chinese (zh)
Inventor
Mao-Hsin Huang
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Mao-Hsin Huang
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Priority to TW94219097U priority Critical patent/TWM288923U/en
Publication of TWM288923U publication Critical patent/TWM288923U/en

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Description

M288923 八、新型說明: 【新型所屬之技術領域】 本= 作係關於-種㈣之熱交換裝置,特別是關於利用 熱包覆基材包覆連接至少二管路,以提升管路間 =讀效率及聽管路破料相互㈣之㈣之熱交換 【先前技術】 習用液體之熱交換裝置,如第2 mr輸入接頭2一輸出接頭3。該二““ 交2 ’另一端接合該輪出接頭3。該熱 ^ ^ ·Γ 1 P㈣12 ’該内管12設於該 CU 形成該熱交換管1。該外管11之材質 之用以導引—冷媒產生熱交換效應,·該 3。背人;^ :獨鋼,用以輪送—液體至該輸出接頭 丨:輸入接頭2具有一冷媒入口21及一液體入口 22,該 冷媒入口 21連接該外瞢】] 該外管心内管二二t端,其™ 之間的通道;該液體入口 22連接該内 :之-端’其用以將該液體導入該内管12。該輸出接 m:冷媒回收口31及—液體出口32,該冷媒回收 外接5 ^該〜冷媒^1口 21連接該外管11之另一端,其用以 m a [、%機之官路(未繪示),使該冷媒經該壓縮機壓 =5,至該冷媒人° 21猶環使用。該液體出口 32 ==口 22連接該内管12之另-端,其用以排出 凡成熱父換後之液體,以供取用。 C:\Linda\PK Pat\PK9927.doc 05/11/04/10:53 Λ M288923 該習用液體之熱交換裝置常設於一冷飲機或冰酒機〔未 繪示〕等飲料裝置,該液體之熱交換裝置於使用時,首先 將該冷媒及液體經由該冷媒入口 21及液體入口 22分別先 後加入該外管11及内管12。在該熱交換管路1内,該冷 媒藉由傳導之熱交換方式相對吸收該液體之熱能,以降低 該液體之溫度。接著,該液體出口 32排出該低溫之液體, 以供飲用,該冷媒回收口 31則相對導引該冷媒經該管路回 流至壓縮機’以循環使用該冷媒。 然而,在實際使用上,該熱交換管路1常需預先捲曲成 適當形狀容設於一冷飲機或冰酒機之機殼内,由於該外管 11及内管12之材質〔鋁或銅〕相對於不銹鋼具較佳之可 撓性,使得該内管12不易形成相同於該外管11之曲度, ”:!§容易在一撓曲部產生龜裂之情形。此時,該冷媒會經由 該内管12之龜裂處滲入該内管12污染該液體,使得該液 體變質危害飲用者。另外,該熱交換管路1之内、外管U 、12设计難以與該輸入接頭2形成良好之三向接合品質, 其係由於該内管12容置於該外管u内部,使得該外管u 或内管12之一先接合後,接著其另一管將不容易進行緊密 接合,如此一來該冷媒極易由該外管n及内管12之穿接 處形成滲漏污染,甚而造成該冷媒之外洩。基於上述=由 ,其確實有必要進一步改良上述習用液體之熱交換裴置。 有鑑於此,本創作改良上述之缺點,其係在—液體之熱 父換裝置設置-第-管及第二管,藉由該第一管及第二其 相互貼接並容設包覆於-導熱包覆基材内,以增加該^ 一 6 — C:\Linda\PK Pat\PK9927.doc 〇5/11/〇4/1〇:53 M288923 效率、該熱交換管路之結構強度、降低管 随,困難度,並增加熱交齡路之可撓曲堆疊 。有致提升液體之熱交換效率、使用安全性及組装 -亨‘ 【新型内容】 本創作主要目的係提供一種液體之熱交換豆 由設置一導埶甘u ^ /、你猎M288923 VIII. New description: [New technical field] This is a heat exchange device for the type (4), especially for the use of a heat-coated substrate to cover at least two pipes to improve the inter-line = read Efficiency and listening to pipeline breaking materials (4) (4) Heat exchange [Prior Art] Conventional liquid heat exchange device, such as 2 m m input connector 2 - output connector 3. The other end of the "" 2" joint engages the wheel joint 3. The heat ^ ^ · Γ 1 P (four) 12 ' is disposed in the CU to form the heat exchange tube 1. The material of the outer tube 11 is used to guide the heat exchange effect of the refrigerant. Back: ^: single steel, used to rotate - liquid to the output joint 丨: the input joint 2 has a refrigerant inlet 21 and a liquid inlet 22, the refrigerant inlet 21 is connected to the outer casing]] the outer tube inner tube The two-t-th end, the passage between the TMs; the liquid inlet 22 is connected to the inner:-end' which is used to introduce the liquid into the inner tube 12. The output is connected to m: a refrigerant recovery port 31 and a liquid outlet 32. The refrigerant is recovered from the external 5^. The refrigerant 1 port 21 is connected to the other end of the outer tube 11, and is used for the ma [, the machine of the machine (not It is shown that the refrigerant is pressed by the compressor = 5 until the refrigerant is used. The liquid outlet 32 == port 22 is connected to the other end of the inner tube 12 for discharging the liquid which has been replaced by the hot parent for access. C:\Linda\PK Pat\PK9927.doc 05/11/04/10:53 Λ M288923 The heat exchange device for the conventional liquid is standing on a beverage device such as a cold drink machine or a ice wine machine (not shown), the heat of the liquid When the exchange device is in use, the refrigerant and the liquid are first introduced into the outer tube 11 and the inner tube 12 through the refrigerant inlet 21 and the liquid inlet 22, respectively. In the heat exchange line 1, the refrigerant relatively absorbs the heat energy of the liquid by conduction heat exchange to lower the temperature of the liquid. Next, the liquid outlet 32 discharges the low temperature liquid for drinking, and the refrigerant recovery port 31 relatively guides the refrigerant back to the compressor through the line to recycle the refrigerant. However, in actual use, the heat exchange line 1 often needs to be pre-curled into a suitable shape to be accommodated in the casing of a cold drink machine or ice wine machine, due to the material of the outer tube 11 and the inner tube 12 [aluminum or copper] The inner tube 12 is less likely to form the same curvature as the outer tube 11 with respect to the stainless steel, and the inner tube 12 is less likely to be cracked in a curved portion. At this time, the refrigerant is passed through. The crack in the inner tube 12 penetrates into the inner tube 12 to contaminate the liquid, so that the liquid deterioration is harmful to the drinker. In addition, the inner and outer tubes U and 12 of the heat exchange tube 1 are difficult to form well with the input joint 2. The three-way joint quality is because the inner tube 12 is housed inside the outer tube u such that one of the outer tube u or the inner tube 12 is first joined, and then the other tube will not be easily joined tightly. In the first place, the refrigerant is easily leaked from the joint between the outer tube n and the inner tube 12, and even the refrigerant is leaked out. Based on the above, it is necessary to further improve the heat exchange of the conventional liquid. In view of this, this creation improves the above shortcomings. The first tube and the second tube are attached to each other and covered by the heat-conductive coating substrate to increase the A 6 — C:\Linda\PK Pat\PK9927.doc 〇5/11/〇4/1〇: 53 M288923 Efficiency, structural strength of the heat exchange line, reduced tube compliance, difficulty, and increased thermal age The flexible stacking of the road. The heat exchange efficiency, safety and assembly of the liquid are improved. [New content] The main purpose of this creation is to provide a liquid heat exchange bean by setting a guide u u ^ /, You hunting

至小二:、、、包祕材,其包覆容置至少二管路,以供該 •進行熱交換,並避免任一管路破裂時相互污染 ^本劊作具有提升液體熱交換效率及管路結構強度之 功效。 又 本遣】作-人要目的係提供一種液體之熱交換裝置,其係一 第ΐ及第一官相互貼接的容設於一導熱包覆基材内, f得該第_熱料方式_第二管進行熱交換,使 得本創作具有提升組裝效率及使用安全性之功效。 本創作另一目的係提供一種液體之熱交換裝置,其中— 導熱包覆基材包覆容置至少二管路,且該導熱包覆基材選 自矩形、方形等易於堆疊之形狀,使得本創作具有提升組 裝便利性之功效。 根據本創作之液體之熱交換裝置,其包含_第一管、一 弟笞及‘熱包覆基材。該第一管相對貼接於該第二管 之外緣’其用以循環—冷媒;該第二管用以輸送一液體。 該導熱包覆基材用以包覆該第-管及第二管。藉此,該導 熱包覆基材以熱傳導方式促使該第一管之冷媒及第二管之 液體進行熱交換。 C:\Linda\PK Pat\PK9927.docTo the second:,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, The effectiveness of the structural strength of the pipeline. In addition, the purpose of the person is to provide a liquid heat exchange device, which is attached to a heat-conducting coating substrate by a first cymbal and a first official, and the _th hot material method is obtained. _ The second tube performs heat exchange, which makes the creation have the effect of improving assembly efficiency and safety of use. Another object of the present invention is to provide a liquid heat exchange device, wherein - the heat conductive coating substrate is covered with at least two pipelines, and the heat conductive coating substrate is selected from the group consisting of rectangular, square, etc., which are easy to stack, so that Creation has the effect of improving assembly convenience. The liquid heat exchange device according to the present invention comprises a first tube, a first tube, and a 'thermal coated substrate. The first tube is relatively attached to the outer edge of the second tube for recycling - the refrigerant; the second tube is for conveying a liquid. The thermally conductive coated substrate is used to coat the first tube and the second tube. Thereby, the heat-conductive covering substrate thermally exchanges heat between the refrigerant of the first tube and the liquid of the second tube. C:\Linda\PK Pat\PK9927.doc

05/11/04/10:53 AN —7 — -M288923 【實施方式】 的、特徵、優點能更明顯 施例,並配合所附圖式, 易 作 為讓本創作之上述及其他目 懂,下文特舉本創作之較佳實 詳細說明如下: 請參照第2圖戶斤示,太春丨# ^ Q所不本創作第一實施例之液體之熱交換 =係^設置於—冷飲機或―冰酒機等飲料裝置之内部 =於Γ村應祕其他流體熱交換機構,其作動方式相05/11/04/10:53 AN —7 — -M288923 [Embodiment] The features, advantages and advantages of the application can be more obvious, and in conjunction with the drawings, it is easy to make the above and other purposes of this creation, below The specific details of this creation are as follows: Please refer to the 2nd figure, the household note, Taichun 丨# ^Q, not the first embodiment of the liquid heat exchange = system ^ set in - cold drink machine or - The inside of the beverage device such as ice wine machine = other fluid heat exchange mechanism in Yucun Village, the mode of operation

再料細贅述。該液體之熱交換裝置係包含一 路t之,4、—輸人接頭5及—輸出接頭6,該熱交換管 :二卞端則,接 導熱包覆基# 0 / Μ、一弟一官42、一 置另 2 ’該第―管41之—端連接該輸人接頭5,及 八 、連接該輸出接頭6,其可供一冷媒於該第一管41 之管_流動。依產品絲,1=及第% 入像貝係砥擇銅、鋁及铜鋁合金等延展性及導熱性佳 導^ ㈣第—f 41於細部㈣及具備良好熱傳 連接該軸雜人制5 ’另一端則 „ .. 、,其可仏一液體於該第二管42之管内空 二生及管训才質係選擇不錄鋼等不娜、不 ν ^ Γ彳土之金屬,以避免該液體產生變質。藉由 :义+ 第一官41及第二管42,避免該第一管41之冷 女、卷^洩日可,該外洩之冷媒直接與該液體相互混合,藉 C:\Linda\PK Pat\PK9927.doc —8——Let me repeat it. The liquid heat exchange device comprises a road t, 4, an input joint 5 and an output joint 6. The heat exchange tube: the second end is connected to the heat conductive coating base # 0 / Μ, one brother and one official 42 And the other end of the first tube 41 is connected to the input connector 5, and eight is connected to the output connector 6, which can supply a refrigerant to the tube _ of the first tube 41. According to the product wire, 1 = and the first % into the shell, choose the ductility and thermal conductivity of copper, aluminum and copper and aluminum alloys. ^ (4) - f 41 in detail (four) and have a good heat transfer connection 5 'The other end is „..,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, The liquid is prevented from being deteriorated. By means: the first officer 41 and the second tube 42, the cold tube of the first tube 41 is avoided, and the leaked refrigerant is directly mixed with the liquid. C:\Linda\PK Pat\PK9927.doc —8——

05/11/04/10:53 AM M288923 此降低後續飲用液體之危險性。 ^再參照第2及3圖所示,該導熱包覆基材43之材質 ^係選自1態導熱包覆基材’特別是選自銅、減銅 卜 $ ^等,展性佳及導熱性佳之金屬,其緊密貼覆該第- S 1及第—官42之外緣表面’用以增加熱交換面積及強 =官路構造。該導熱包覆基材43之形狀係選擇矩形、方形 ^易於堆疊之形狀,域交換管路4藉由—錢堆疊方式 • ☆置於⑽人料I置(未繪不)之内部空間,例如螺旋堆疊 成中空橢圓柱形,以便增加該第_管41及第二管42之接 觸面積’有效提升該第—管41及第二管42之熱交換效率 。該隔^材料44相㈣設於該導熱包覆基材43之外侧, ' ^^丨其車乂彳❻自泡棉’其用以減低外部溫度相對影響該熱交換 、…、1路4之熱交換效率及避免外力碰撞或賴造成該熱交換 管路4之損害。 請再參照第2圖所示,該輪人接頭5設有—冷媒入口 51 • 及一液體入口 52,該冷媒入口 51連接該第-管41之一端 j用=將該冷媒導入該第-管41。該㈣人口 ”連接 该第一官42之-端,其用以將該液體導入該第二管& 該輸出接頭6設有-冷媒回收σ 61及—液體出口 Q,該 冷媒时口 61相對該冷狀口 5丨連接該第—f 41之另_ 端,其用以外接一壓縮機之管路(未緣示),將該冷媒經該 壓縮機壓縮後再導引回該冷媒入口 5循環使用。該液體出 口 62相對該液體入口 52連接該第二管42之另一端,並用 以排出完成熱交換後之液體,以供取用或飲用。 、 C:\Linda\PK Pat\PK9927.doc 05/11/04/10:53 m M288923 請再參胛筮? 液體之熱絲騎;I,_賴作帛—實施例之 冷媒入口 μ導1二’ 冷媒經由該輪人接頭5之 至該細铜6 輸送 :::::^氯~〕等。 體亦經由該液體入口 52導入該第 體流動:二=嶋熱交換後之該液體。在該液 、 —g 42的過程中,由於該第_管41 、人 ’因此該冷媒及液體經由該導^包 =、(、、、料方式逐漸達成—熱平衡狀態,該冷 之=體之熱能,使得該液體之溫度逐漸下降接近^冷媒 、如第2及3圖所示,由於該第一管4卜該第 導熱包覆基材43均為—導熱性極佳之金屬組 交換管路…-姉衛㈣。另外, =^41以包覆__管41及第二管42,提=第 ^…及弟—官42之管路結構強度,以減少該第一管41 及第二管42位於撓曲部發生龜裂之_,且料熱包覆基 =43利輯钱彎延方式,有效增加該第-管41及第1 官42之熱交換長度,進而有效提升熱交換效率,且便於將 該液體之熱交換裝置岐集堆Φ方式容置於额料裝置( 未繪不)之内部空間。再者,該隔熱材料44相對環設於該 導熱包覆基材43之外侧,其減低外部溫度影響熱交換效率 C:\Linda\PK Pat\PK9927. doc05/11/04/10:53 AM M288923 This reduces the risk of subsequent drinking of liquids. ^ Referring again to Figures 2 and 3, the material of the thermally conductive coated substrate 43 is selected from the group consisting of a 1-state thermally conductive coated substrate, particularly selected from the group consisting of copper, copper-reducing, and the like. A good metal that closely adheres to the outer surface of the first - S 1 and the first - 42 to increase the heat exchange area and the strong = official structure. The shape of the heat-conducting coated substrate 43 is selected from a rectangular shape, a square shape, and an easy-to-stack shape. The domain exchange pipe 4 is placed in a space of (10) human I (not drawn), for example, by a stacking method. The spirals are stacked in a hollow elliptical cylinder to increase the contact area of the first tube 41 and the second tube 42 to effectively increase the heat exchange efficiency of the first tube 41 and the second tube 42. The phase (44) of the spacer material 44 is disposed on the outer side of the thermally conductive coated substrate 43, and '^^丨's rutting from the foam' is used to reduce the external temperature and relatively affect the heat exchange, ..., 1 way 4 The heat exchange efficiency and the avoidance of external force collisions or damage to the heat exchange line 4 are caused. Referring to FIG. 2 again, the wheel connector 5 is provided with a refrigerant inlet 51 and a liquid inlet 52. The refrigerant inlet 51 is connected to one end j of the first pipe 41. The refrigerant is introduced into the first pipe. 41. The (four) population is connected to the end of the first official 42 for introducing the liquid into the second tube & the output connector 6 is provided with a refrigerant recovery σ 61 and a liquid outlet Q, the refrigerant port 61 being relatively The cold port 5 is connected to the other end of the first f-41, which is connected to a compressor (not shown), and the refrigerant is compressed by the compressor and then guided back to the refrigerant inlet 5. The liquid outlet 62 is connected to the other end of the second tube 42 with respect to the liquid inlet 52, and is used for discharging the liquid after the heat exchange is completed for use or drinking. C:\Linda\PK Pat\PK9927. Doc 05/11/04/10:53 m M288923 Please refer to it again? Liquid hot wire ride; I, _ _ _ 帛 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 实施 冷 冷 冷 冷 冷 冷 冷 冷The fine copper 6 is transported:::::^chloro~], etc. The body is also introduced into the first body flow through the liquid inlet 52: the liquid after the heat exchange, in the process of the liquid, the -g 42 Because the first tube 41, the person's refrigerant and liquid are gradually reached through the guide package =, (,,, material mode - heat balance state, the cold = The thermal energy causes the temperature of the liquid to gradually decrease to be close to the refrigerant, as shown in Figures 2 and 3, since the first tube 4 and the first thermally conductive coated substrate 43 are both metal-exchange tubes having excellent thermal conductivity. Road...-defend (4). In addition, =^41 to cover the __tube 41 and the second tube 42, the height of the pipe structure of the ^^ and the brother-offer 42 to reduce the first pipe 41 and the first The second tube 42 is located at the flexure portion, and the heat-coated layer is 43%, which effectively increases the heat exchange length of the first tube 41 and the first member 42, thereby effectively improving heat exchange. The efficiency is convenient for the liquid heat exchange device to be placed in the inner space of the fore-aft device (not shown). Further, the heat insulating material 44 is oppositely disposed on the thermally conductive coated substrate 43. On the outside, it reduces the external temperature and affects the heat exchange efficiency C:\Linda\PK Pat\PK9927. doc

05/11/04/10:53 AM —10 — M288923 » * 及,:卜力碰撞或震動造成損害。另-方面,該第一管41 及第^ 42相互獨立’其方便與該輸人接頭5〔及輸出接 頭6〕^/成良好接合品質,因此相對減少冷媒或液體由接 合處滲漏之機率。 .杯㈣4圖料,其細補作帛二實關之液體之 =裝 =較於第一實施例,第二實施例係在該第一 每斤^ : 42相互貼接處,進一步設置一阻絕層45, 該弟一官41及第二管42分別貼接於該阻絕| 45上下兩側 ^阻^ 45之剖㈣呈—具適當厚度之長條狀,其係選 ΪΓ非合金等延展性及導熱性佳之金屬,但亦可 μ 稭此在该弟一官41或第2管42之任 :二冷體外⑽,可有效防止該外浅之液體滲 k,至心-官41或第二管42,之另—管,減少該外紅冷 :使=:混合之情形,有效提升該液體之熱交換裝置 明參照第5及6圖所示,其揭示本 體之熱交換裝置。相較Μ 乍弟一 ^例之液 換管路7設有—第;之熱交 73及一 p埶;7」 一 & 72、一導熱包覆基材 I、、、材枓74。該導熱包覆基材 導熱包覆基材,特別H ^佳係邊自液悲 如乙醇或水等。廷自熱性較佳之工作流體,例 成尺專該隔熱材料74係於内部形成一空 示〕,以供注入該導熱包覆基材 = 材73能緊密包覆該第 敦曰=熱包復基 性良好之液態介質 S ,亚提供一導熱 U而進一步有效提升該第一管71及第 M288923 一管72之熱交換效率。 再者,該隔熱材料74之二端可選 該導熱包覆基材73 ’而僅由二端拉二成:::封, 該輪入接頭5及輸出接頭6。觀該^二 復基材73之設計不致影響該第一管7ι、:匕 接頭5及輸出接頭6之接合品質。 s 别入 如上所述’相較於第1圖之習用液體之熱交換裝置利用 • 該外管U Θ置該内管12,而產生管路易於撓曲部龜裂、 接頭部分組裝困難及無法避免該㈣冷媒渗入混合該液體 等缺點’第二®之本創作藉由設置該導熱包覆基材43,以 包覆容置該第-41及第二管42 ’其確實相對增加該熱 -胸}交換管路4之熱交換效率及結構強度、降低管路與接頭^ 裝之因難度及避免該冷媒及液體相互滲入混合,並有效提 升液體之熱交換效率、組裝效率及使用安全性。 雖然本創作已利用上述較佳實施例揭示,然其並非用以 限定本創作,任何熟習此技藝者,在不脫離本創作之精神 和範圍之内,當可作各種更動與修改,因此本創作之保護 範圍當視後附之申請專利範圍所界定者為準。 C:\Linda\PK Pat\PK9927.doc —12 —05/11/04/10:53 AM —10 — M288923 » * and,: Damage caused by collision or vibration. On the other hand, the first tube 41 and the 42th portion are independent of each other, which facilitates good bonding quality with the input connector 5 [and the output connector 6], thereby relatively reducing the probability of leakage of the refrigerant or liquid from the joint. . . Cup (4) 4 drawing material, which is finely compensated for the liquid of the second real thing. = Mounting = Compared with the first embodiment, the second embodiment is further provided with a resisting layer at the first bonding point of the first: 45, the brother's first officer 41 and the second tube 42 respectively attached to the resistance | 45 upper and lower sides ^ resistance ^ 45 section (four) is - a strip of appropriate thickness, which is selected for non-alloy and other ductility A metal with good thermal conductivity, but it can also be used as the stem of the brother's one official 41 or the second tube 42: two cold outside the body (10), can effectively prevent the shallow liquid from seeping, to the heart - official 41 or the second tube 42. Another tube, reducing the outer red cold: making =: mixing, the heat exchange device for effectively raising the liquid, as shown in Figures 5 and 6, reveals the heat exchange device of the body. Compared with the 乍 乍 一 一 一 换 换 换 换 换 换 换 换 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路 管路The thermally conductive coated substrate is thermally conductively coated with a substrate, in particular, the H ^ good side is self-liquid such as ethanol or water. The working fluid is preferably self-heating, and the insulating material 74 is formed in the interior to form an empty space for injecting the thermally conductive coated substrate. The material 73 can tightly coat the first layer 热 = heat-packing base The liquid medium S with good properties provides a heat transfer U to further effectively improve the heat exchange efficiency of the first tube 71 and the M288923 tube 72. Furthermore, the two ends of the heat insulating material 74 may be selected from the heat-conductive covering substrate 73' and pulled only by two ends:::, the wheel-in joint 5 and the output joint 6. The design of the composite substrate 73 does not affect the bonding quality of the first tube 7i, the 接头 joint 5 and the output joint 6. s is not used as described above. The heat exchanger is used in comparison with the conventional liquid of Fig. 1. The outer tube U is placed on the inner tube 12, and the tube is easily deflected, the joint portion is difficult to assemble, and the joint portion is difficult to assemble. Avoiding the disadvantages of the (4) refrigerant infiltrating the liquid mixture, etc. The second creation of the second layer is provided by the heat-conducting coating substrate 43 to cover and accommodate the first and second tubes 42' which do increase the heat relatively Chest} exchange heat exchange efficiency and structural strength of the pipeline 4, reduce the difficulty of piping and joints, and avoid the infiltration and mixing of the refrigerant and liquid, and effectively improve the heat exchange efficiency, assembly efficiency and safety of the liquid. Although the present invention has been disclosed in the above-described preferred embodiments, it is not intended to limit the present invention, and any person skilled in the art can make various changes and modifications without departing from the spirit and scope of the present invention. The scope of protection is subject to the definition of the scope of the patent application. C:\Linda\PK Pat\PK9927.doc —12 —

05/11/04/10:53 AM M288923 【圖式簡單說明】 第1圖:習用液體之熱交換裝置之立體圖。 第2圖:本創作第一實施例之液體之熱交換裝置之立體 及局部剖視圖。 第3圖:本創作第一實施例之液體之熱交換裝置之局部 剖視圖。 第4圖:本創作第二實施例之液體之熱交換裝置之局部 剖視圖。 第5圖:本創作第三實施例之液體之熱交換裝置之立體 及局部剖視圖。 第6圖:本創作第三實施例之液體之熱交換裝置之局部 剖視圖。05/11/04/10:53 AM M288923 [Simple description of the drawing] Fig. 1: A perspective view of a heat exchange device for a conventional liquid. Fig. 2 is a perspective and partial cross-sectional view showing the liquid heat exchange device of the first embodiment of the present invention. Fig. 3 is a partial cross-sectional view showing the liquid heat exchange device of the first embodiment of the present invention. Fig. 4 is a partial cross-sectional view showing the liquid heat exchange device of the second embodiment of the present invention. Fig. 5 is a perspective and partial cross-sectional view showing the liquid heat exchange device of the third embodiment of the present invention. Fig. 6 is a partial cross-sectional view showing the liquid heat exchange device of the third embodiment of the present invention.

【主要元件符號說明】 1 熱交換管路 11 外管 12 内管 2 輸入接頭 21 冷媒入口 22 液體入口 3 輸出接頭 31 冷媒回收口 32 液體出口 4 熱交換管路 41 第一管 42 第二管 43 導熱包覆基材 44 隔熱材料 45 阻絕層 5 輸入接頭 51 冷媒入口 52 液體入口 6 輸出接頭 61 冷媒回收口 •M288923 62 液體出口 7 熱交換管路 71 第一管 72 第二管 73 導熱包覆基材 74 隔熱材料[Main component symbol description] 1 Heat exchange line 11 Outer tube 12 Inner tube 2 Input joint 21 Refrigerant inlet 22 Liquid inlet 3 Output joint 31 Refrigerant recovery port 32 Liquid outlet 4 Heat exchange line 41 First tube 42 Second tube 43 Thermally conductive coated substrate 44 Thermal insulation material 45 Resistive layer 5 Input connector 51 Refrigerant inlet 52 Liquid inlet 6 Output connector 61 Refrigerant recovery port • M288923 62 Liquid outlet 7 Heat exchange line 71 First tube 72 Second tube 73 Thermally coated Substrate 74 insulation material

C:\Linda\PK Pat\PK9927.doc —14 — 05/11/04/10:53 AMC:\Linda\PK Pat\PK9927.doc —14 — 05/11/04/10:53 AM

Claims (1)

M288923 九、申請專利範圍: 1、 一種液體之熱交換裝置,其包含: 一第一管,其用以循環一冷媒; 一第二管,其用以輸送一液體;及 一導熱包覆基材,其包覆該第一管及第二管,且該導 熱包覆基材以熱傳導方式促使該第一管之冷媒及第二 管之液體進行熱交換。M288923 IX. Patent Application Range: 1. A liquid heat exchange device comprising: a first tube for circulating a refrigerant; a second tube for conveying a liquid; and a thermally conductive coated substrate The first tube and the second tube are coated, and the thermally conductive coated substrate thermally exchanges the liquid of the first tube and the liquid of the second tube. 2、 依申請專利範圍第1項所述之液體之熱交換裝置,其 中另包含一輸入接頭,其設有一冷媒入口及一液體入 口,該冷媒入口連通於該第一管之一端,該液體入口 連通於該第二管之一端。 3、 依申請專利範圍第1項所述之液體之熱交換裝置,其 中另包含一輸出接頭,其設有一冷媒回收口及一液體 出口,該冷媒回收口連通於該第一管之另一端,及該 液體出口連通於該第二管之另一端。 4、 依申請專利範圍第1項所述之液體之熱交換裝置,其 中該第一管相對貼接於該第二管。 5、 依申請專利範圍第1項所述之液體之熱交換裝置,其 中該第一管及第二管係選自相同、不同之高導熱性金 屬管。 6、 依申請專利範圍第1項所述之液體之熱交換裝置,其 中該導熱包覆基材係選自固態導熱包覆基材。 7、 依申請專利範圍第6項所述之液體之熱交換裝置,其 中該固態導熱包覆基材之形狀係選擇為矩形、方形。 C:\Linda\PK Pat\PK9927.doc —15 — 05/11/04/10:53 AM M2889232. The liquid heat exchange device according to claim 1, further comprising an input joint provided with a refrigerant inlet and a liquid inlet, the refrigerant inlet being connected to one end of the first tube, the liquid inlet Connected to one end of the second tube. 3. The liquid heat exchange device according to claim 1, further comprising an output joint having a refrigerant recovery port and a liquid outlet, wherein the refrigerant recovery port is connected to the other end of the first tube, And the liquid outlet is connected to the other end of the second tube. 4. The liquid heat exchange device of claim 1, wherein the first tube is relatively attached to the second tube. 5. The liquid heat exchange device according to claim 1, wherein the first tube and the second tube are selected from the same or different high thermal conductivity metal tubes. 6. The liquid heat exchange device of claim 1, wherein the thermally conductive coated substrate is selected from the group consisting of solid thermally conductive coated substrates. 7. The liquid heat exchange device according to claim 6, wherein the shape of the solid heat conductive coated substrate is selected to be rectangular or square. C:\Linda\PK Pat\PK9927.doc —15 — 05/11/04/10:53 AM M288923 ίοΊο 11 1211 12 13 14 15 依申請專利範圍第1項所述之液體之熱交換裝置,其 中該熱交換管路設有一阻絕層,其貼接於該第一管及 第二管之間,以阻隔該第一管及第二管。 依申請專利範圍第8項所述之液體之熱交換裝置,其 中該阻絕層係選自金屬阻絕層、非金屬阻絕層。 依申請專利範圍第1項所述之液體之熱交換裝置,其 中該導熱包覆基材之外另設有一隔熱材料^以避免外 部溫度影響熱交換效率。 依申請專利範圍第10項所述之液體之熱交換裝置,其 中該隔熱材料係選自泡棉。 一種液體之熱交換裝置,其包含: 一第一管,其用以循環一冷媒; 一第二管,其用以輸送一液體; 一液態導熱包覆基材,其包覆該第一管及第二管;及 一絕熱材料,其容置該第一管、第二管及液態導熱包 覆基材’且該液態導熱包覆基材以熱傳導方式促使該 第一管之冷媒及第二管之液體進行熱交換。 依申請專利範圍第12項所述之液體之熱交換裝置,其 中該第一管相對貼接於該第二管。 依申請專利範圍第12項所述之液體之熱交換裝置,其 中該第一管及第二管係選自相同、不同之高導熱性金 屬管。 依申請專利範圍第12項所述之液體之熱交換裝置,其 中該隔熱材料係選自泡棉。 C:\linda\PK Pat\PK9927.doc —16—— 05/11/04/10:53 AMThe heat exchange device of the liquid according to claim 1, wherein the heat exchange tube is provided with a barrier layer which is adhered between the first tube and the second tube to block the first Tube and second tube. The liquid heat exchange device according to claim 8, wherein the barrier layer is selected from the group consisting of a metal barrier layer and a non-metal barrier layer. The liquid heat exchange device according to claim 1, wherein the heat conductive coated substrate is provided with a heat insulating material to prevent the external temperature from affecting the heat exchange efficiency. The liquid heat exchange device according to claim 10, wherein the heat insulating material is selected from the group consisting of foam. A liquid heat exchange device comprising: a first tube for circulating a refrigerant; a second tube for conveying a liquid; a liquid heat conductive covering substrate covering the first tube and a second tube; and a heat insulating material accommodating the first tube, the second tube and the liquid heat conductive covering substrate 'and the liquid heat conductive coating substrate thermally promotes the refrigerant and the second tube of the first tube The liquid is heat exchanged. The liquid heat exchange device according to claim 12, wherein the first tube is relatively attached to the second tube. The liquid heat exchange device according to claim 12, wherein the first tube and the second tube are selected from the same or different high thermal conductivity metal tubes. The liquid heat exchange device according to claim 12, wherein the heat insulating material is selected from the group consisting of foam. C:\linda\PK Pat\PK9927.doc —16 — 05/11/04/10:53 AM
TW94219097U 2005-11-04 2005-11-04 Heat exchange device for liquid TWM288923U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI582369B (en) * 2014-05-12 2017-05-11 林聖梁 Heat exchanging device and water heater using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI582369B (en) * 2014-05-12 2017-05-11 林聖梁 Heat exchanging device and water heater using the same

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