TWI291541B - A sprinkling type heat exchanger - Google Patents

A sprinkling type heat exchanger Download PDF

Info

Publication number
TWI291541B
TWI291541B TW094147101A TW94147101A TWI291541B TW I291541 B TWI291541 B TW I291541B TW 094147101 A TW094147101 A TW 094147101A TW 94147101 A TW94147101 A TW 94147101A TW I291541 B TWI291541 B TW I291541B
Authority
TW
Taiwan
Prior art keywords
refrigerant
liquid refrigerant
shower
tube
liquid
Prior art date
Application number
TW094147101A
Other languages
Chinese (zh)
Other versions
TW200724848A (en
Inventor
Jung-Je Liou
Yau-Tzu Hu
Hsi-Tsung Cheng
Original Assignee
Ind Tech Res Inst
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ind Tech Res Inst filed Critical Ind Tech Res Inst
Priority to TW094147101A priority Critical patent/TWI291541B/en
Priority to US11/642,684 priority patent/US20070151279A1/en
Publication of TW200724848A publication Critical patent/TW200724848A/en
Application granted granted Critical
Publication of TWI291541B publication Critical patent/TWI291541B/en
Priority to US12/637,495 priority patent/US8561675B2/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D5/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0017Flooded core heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/02Details of evaporators
    • F25B2339/024Evaporators with refrigerant in a vessel in which is situated a heat exchanger
    • F25B2339/0242Evaporators with refrigerant in a vessel in which is situated a heat exchanger having tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/0071Evaporators

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The sprinkling type heat exchanger exposes the liquid refrigerant uniformly on those heat conducting pipes by sprinkling through the longitudinal distribution pipes and the refrigerant outgates of the refrigerant sprinkling module. By way of the opening of the main body to retrieve the evaporated refrigerant this sprinkling type of heat exchanger not only increases the efficiency of the mechanical refrigerating device to be higher than that of the overflow type of the evaporator but also reduces both the charging quantity over twenty percent of the refrigerant and the material cost at least twenty five per cent of the heat exchanger.

Description

1291541 九、發明說明: 【發明所屬之技術領域】 本發明係有關於一種熱交換裝置,應用於機械式製冷設 備中所使用之冷媒蒸發裝置,特別是一種淋灑式熱交換裂置。 【先前技術】 機械式製冷設備包含有四個主要元件:壓縮機、膨脹裝 置、冷凝裝置與蒸發裝置,其中依據蒸發裝置可大致分為直膨 式、滿溢式與淋灑式等製冷系統。滿溢式與直膨式主要構造都 是屬於外殼内管式熱交換器的一種,直膨式在管内側流動的是 冷媒,而在殼側流動的是目標流體,為防止管内液態冷媒因蒸 ,不完全被吸入壓縮機中造成壓縮機受損,因此在直膨式製^ 系統中需要提高壓縮機入口端過熱度,造成壓縮機的耗功。 士而滿溢式製冷設備管内侧流動的是目標流體冷媒,而在 殼側流動的是冷媒,由於壓縮機入口端不易吸收到液態冷媒, 因此可以降低壓縮機入口端冷媒的過熱度,減低壓縮機的耗 功。但由於滿溢式蒸發裝置是將管子浸泡於殼中之液態冷媒 中,因此需要更多量的液態冷媒來浸泡殼内管子,造成所需要 的冷媒充填量比直膨式多了 一倍以上的量,增加了設備成本與 環境負擔。 淋灑式蒸發器利用淋下的冷媒在殼内管上形成液態薄 二方面义重力或其他力量影響在垂直或與管子平行方向進 =動,同雜由管外騎下的冷媒紐將鋪料目標流體 =置帶走,達賴交換的目的。由於液胁媒在祕管表面 加’加速了液態冷_體在熱傳管表面蒸發成氣態冷媒 值您ii、因此可以增加該熱交換裝置的效能,達到減少殼内熱 b、成本至少25%’同時因為不需要將熱傳管大量浸泡於液 1291541 悲冷媒中,所以也可減低機械製冷設備的冷媒填充量2〇%以 上。但是使用淋灑式蒸發裝置的冷媒流佈控制等許多機制會影 響到淋灑式条發裝置的效能,如果無法有效控制淋灑冷媒的機 構,由於冷媒淋落在熱傳管上分佈不良反將造成製冷設備的耗 能0 【發明内容】 本發明之主要目的是提出一種淋灑式熱交換裝置,係可 均勻控制絲冷制分佈,有效提升製冷效率,耕低材料 根據本發明所揭露之淋灑式熱交換裝置,係包含 ,、熱傳管與分佈冷媒淋灑模、组,本體具有容置空間與 容置空間之開口,而熱傳管設置於本體之容置空間内,分= ,淋灑模組包含有軸向分佈f、液態冷媒人σ與冷媒淋二 軸向分佈管财魏_孔,雜冷媒心設置_ 亡、,可將液態冷媒藉由液態冷媒入口輸入至軸向分佈管,二 怨冷媒通蝴m至冷媒職面職至鱗管,進行施 而轉丄匕為氣態冷媒,並藉由本體之開口流出;#此 將液態冷媒淋灑域傳管上,提升製冷鱗, :: 可降低材料成本。 _早'並 有關本創作之詳細内容及技術,茲就配合圖式說明如 【實施方式】 卜· 根據本發明所揭露之淋灑式熱交換裝置,請參閱「 ^係包含本體10、分佈冷媒淋灑模組20與熱傳管3〇, 體10之橫剖面概略為為容器形狀,内部具有容置 且具有一個開口 12。熱傳管30係可為交錯或是盤繞等形式置 .1291541 於本體10之容置空間11之概略底部的位置。 分佈冷媒淋灑模組20包含有軸向分佈管21,其上具有一 個液態冷媒入口 22,底面具有複數個開孔2U,請參閱/'「第2 圖」,而其底面係為冷媒淋灑面23,具有複數個供液態冷媒淋 灑的淋灑開孔231 (見弟3圖)。且轴向分佈管21可藉由^個 擋板24連接冷媒淋灑面23,並藉由此擋板24提供^止> 飛錢的功能。 7 ' 液態冷媒由分佈冷媒淋灑模組20之液態冷媒入口 22導 入丄而至軸向分佈管21,因為其是長轴向的延伸',故可以將 液態冷媒做長轴向的均勻分佈,接著通過軸向分佈管21底面 的開孔211,而可滴落至冷媒淋灑面23,此時,藉由檀板% 可阻止液悲冷媒滴洛時的贺藏,另一方面,也可以增設有蓉如 為多孔性材料的緩衝材232 (見第3圖),譬如為化學纖維不 織布、植物纖維不織布、海綿或海綿相似物、網隔狀織布、金 屬絨狀物與非金屬絨狀物等,能吸收液態冷媒直接衝擊所產生 f衝擊力,以減低液態冷媒飛濺並阻止液態冷媒迅速從冷媒淋 ,面23之淋灑開口 231上淋灑至熱傳管30,造成液態冷媒淋 灑不,勻。而冷媒淋灑面23之淋灑開口 231除了圖式中所緣 示的圓孔外,也可為任何幾何形狀之孔、溝槽或置入隔柵式^ 道,而可增進液態冷媒於此二維平面的均勻分佈。 淋下的液態冷媒在熱傳管30上形成液態薄膜,一方面受 重力或其他广量影響在垂直或與熱傳管3〇平行方向進行移 動,同,液態冷媒蒸發將熱傳管3〇内目標流體的熱量帶走, 達到熱交換的目的。由於液態冷媒在熱傳管3〇表面流速增 加,加速了液態冷媒流體在熱傳管3〇表面蒸發成氣態冷媒的 速率,因此可以增加該熱交換裝置的效能,達到減少成本至少 25%,同時因為不需要將熱傳管3〇大量浸泡於液態冷媒中, 所以也可減低機械製冷設備的冷媒填充量2〇%以上。 1291541 口 12 父換後蒸發之氣態冷媒,财11由本體10之開 可於開Ϊ ^内’為進—步防止液態冷媒_壓縮機, 續機汗々日·又置液體分離裝置,防止飛濺液體微粒回到壓 、%機、歧触有其鋪式滅猶裝置。 而伟部乂東效果,當然也可以增加液態冷媒的量, 機竹^之”、、傳官3G浸泡於液態冷媒巾。藉此,可有效提高 冷設_效率’節省能源驗f與節省設備製造的費 含 可以使機械式製冷設備的效率比使用滿溢式蒸發器提BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchange device for use in a refrigerant evaporation device used in a mechanical refrigeration device, and more particularly to a shower type heat exchange split. [Prior Art] The mechanical refrigeration equipment includes four main components: a compressor, an expansion device, a condensing device, and an evaporation device, and the evaporation device can be roughly classified into a direct expansion type, a full overflow type, and a shower type. The overflow and direct expansion main structures are all ones of the inner tube type heat exchangers. The direct expansion type flows the refrigerant inside the tube, and the target fluid flows on the shell side to prevent the liquid refrigerant in the tube from being steamed. The compressor is not completely sucked into the compressor and the compressor is damaged. Therefore, in the direct expansion system, it is necessary to increase the superheat of the inlet end of the compressor, resulting in the power consumption of the compressor. The inside of the overflow-type refrigeration equipment tube is the target fluid refrigerant, and the refrigerant flowing on the shell side is not easy to absorb the liquid refrigerant at the inlet end of the compressor, so the superheat of the refrigerant at the inlet end of the compressor can be reduced, and the compression can be reduced. The power consumption of the machine. However, since the overflow evaporating device is for immersing the tube in the liquid refrigerant in the shell, a larger amount of liquid refrigerant is needed to soak the tubes in the shell, resulting in more than twice as much refrigerant filling as the direct expansion type. Quantity increases equipment costs and environmental burden. The shower evaporator uses the chilled refrigerant to form a liquid thin layer on the inner tube of the shell. The gravity or other force influences the vertical or parallel direction of the tube to move, and the refrigerant will be laid by the refrigerant outside the tube. Target fluid = take away, the purpose of the Dalai exchange. Because the liquid damper adds 'in the surface of the secret tube' to accelerate the evaporation of the liquid cold _ body on the surface of the heat transfer tube into a gaseous refrigerant value, you can increase the efficiency of the heat exchange device, reduce the heat in the shell, and cost at least 25%. 'At the same time, because it is not necessary to immerse the heat pipe in a large amount of liquid 1291541, it can also reduce the refrigerant filling capacity of the mechanical refrigeration equipment by more than 2%. However, many mechanisms, such as the use of a shower-type evaporation device, can affect the performance of the shower-type hair-sending device. If the mechanism for showering the refrigerant is not effectively controlled, the poor distribution of the refrigerant on the heat-transfer tube will result in Energy consumption of refrigeration equipment 0 SUMMARY OF THE INVENTION The main object of the present invention is to provide a shower type heat exchange device, which can uniformly control the distribution of the wire cooling system, effectively improve the cooling efficiency, and plough the material according to the invention. The heat exchange device comprises: a heat transfer pipe and a distributed refrigerant shower die, a group, the body has an opening for accommodating space and a accommodating space, and the heat transfer pipe is disposed in the accommodating space of the body, and is divided into The sprinkling module comprises an axial distribution f, a liquid refrigerant σ and a refrigerant immersed in the axial distribution of the tube Wei Wei_ hole, and a miscellaneous refrigerant medium setting _ 死, the liquid refrigerant can be input to the axial distribution tube through the liquid refrigerant inlet The second grievance refrigerant passes through the m to the refrigerant level to the scale tube, and then turns into a gaseous refrigerant, and flows out through the opening of the body; # this will liquid the liquid on the field, improve the refrigeration , :: material cost can be reduced. _Early and related to the details and technology of this creation, please refer to the following description. [Embodiment] Bu · According to the shower type heat exchange device disclosed in the present invention, please refer to "^ contains the body 10, distributed refrigerant The shower module 20 and the heat transfer tube 3 are substantially in the shape of a container, and have an inner receiving portion and an opening 12. The heat transfer tube 30 can be in the form of staggered or coiled. 1291441 The position of the bottom portion of the accommodating space 11 of the main body 10. The distributed refrigerant shower module 20 includes an axial distribution tube 21 having a liquid refrigerant inlet 22 and a plurality of openings 2U on the bottom surface, see /' Fig. 2 is a bottom view of the refrigerant shower surface 23, and has a plurality of shower openings 231 for liquid refrigerant showering (see Figure 3). Further, the axial distribution pipe 21 can be connected to the refrigerant shower surface 23 by means of the baffle 24, and by this means, the baffle 24 can provide the function of flying money. 7 ' The liquid refrigerant is introduced into the axial distribution tube 21 from the liquid refrigerant inlet 22 of the distributed refrigerant shower module 20, because it is a long axial extension, so that the liquid refrigerant can be evenly distributed in the long axial direction. Then, through the opening 211 of the bottom surface of the axial distribution pipe 21, it can be dripped to the cooling shower surface 23. At this time, the sandstone can prevent the liquid stagnation refrigerant from dropping, and on the other hand, it can be added. There is a buffer material 232 (see Figure 3), such as chemical fiber non-woven fabric, vegetable fiber non-woven fabric, sponge or sponge similar material, mesh woven fabric, metal velvet and non-metallic velvet. In addition, it can absorb the f impact force generated by the direct impact of the liquid refrigerant to reduce the splash of the liquid refrigerant and prevent the liquid refrigerant from rapidly leaching from the refrigerant. The shower opening 231 of the surface 23 is sprayed onto the heat transfer pipe 30, causing the liquid refrigerant to drain. ,uniform. The shower opening 231 of the refrigerant spray surface 23 can be any geometric hole, groove or grid type in addition to the circular hole shown in the drawing, and the liquid refrigerant can be promoted here. Uniform distribution of two-dimensional planes. The liquid refrigerant that is dripped forms a liquid film on the heat transfer pipe 30, and is moved vertically or in parallel with the heat transfer pipe 3〇 by gravity or other extensive influence. Similarly, the liquid refrigerant evaporates and heats the heat pipe 3 The heat of the target fluid is carried away to achieve the purpose of heat exchange. Since the flow rate of the liquid refrigerant on the surface of the heat transfer tube 3 increases, the rate at which the liquid refrigerant fluid evaporates into the gaseous refrigerant on the surface of the heat transfer tube 3 is accelerated, so that the efficiency of the heat exchange device can be increased, and the cost can be reduced by at least 25%. Since it is not necessary to immerse the heat transfer tube 3 in a large amount in the liquid refrigerant, the refrigerant charge amount of the mechanical refrigeration equipment can be reduced by 2% or more. 1291541 Port 12 After the father exchanges the vaporized refrigerant, the money 11 is opened by the body 10 and can be opened. ^Into the step - prevent liquid refrigerant_compressor, continue to sweat and set the liquid separation device to prevent splashing The liquid particles return to the pressure, the % machine, and the collisions have their shop-type device. And the effect of the Weibu Jidong, of course, can also increase the amount of liquid refrigerant, machine bamboo ^", and Guanguan 3G soaked in liquid refrigerant towel. This can effectively improve the cold design _ efficiency 'saving energy inspection f and saving equipment The manufacturing cost can make the efficiency of mechanical refrigeration equipment higher than that of using overflow evaporator

n,更可以降低冷媒充填量與熱交換器材料成本。 、^然本發明以前述之較佳實施例揭露如上,然其並非用 ^限定本發明,任何熟習此技藝者,在不脫離本發明之精神和 範,内,當可作些許之更動與潤飾,因此本發明之保護範圍當 視後附之申請專利範圍所界定者為準。n, can reduce the amount of refrigerant filling and heat exchanger material costs. The present invention has been described above with reference to the preferred embodiments thereof. However, the present invention is not limited thereto, and any one skilled in the art can make some modifications and refinements without departing from the spirit and scope of the present invention. Therefore, the scope of the invention is defined by the scope of the appended claims.

【圖式簡單說明】 8 1291541 第1圖係為本發明淋灑式熱交換裝置之示意圖。 第2圖係為本發明淋灑式熱交換裝置之分佈冷媒淋灑模 組示意圖。 第3圖係為本發明分佈冷媒淋灑模組之冷媒淋灑面之變 化例圖。 【主要元件符號說明】 10 本體 11 容置空間 12 開口 20 分佈冷媒淋灑模組 21 轴向分佈管 211 開孔 22 液態冷媒入口 23 冷媒淋灑面 231 淋灑開孔 232 缓衝材 24 擋板 30 熱傳管[Simple description of the drawing] 8 1291541 Fig. 1 is a schematic view of the shower type heat exchange device of the present invention. Fig. 2 is a schematic view showing the distributed refrigerant showering mold set of the shower type heat exchange device of the present invention. Fig. 3 is a view showing a variation of the refrigerant spray surface of the distributed refrigerant shower module of the present invention. [Main component symbol description] 10 Main body 11 accommodating space 12 Opening 20 Distributed refrigerant shower module 21 Axial distribution pipe 211 Opening 22 Liquid refrigerant inlet 23 Refrigerant shower surface 231 Sprinkling opening 232 Buffer material 24 Baffle 30 heat pipe

Claims (1)

1291541 申請專利範圍: 一種淋灑式熱交換裝置,係包含有: -本體,具有-容置空間與-連通該容置 . 一熱傳管,係設置於該本體之容置空間内· Θ用’ —分佈冷媒淋灑模組,係包含有一軸向分佑^ 一 人口與-冷媒淋灑®,該軸向分佈管具 媒 J液態冷媒入口設置於該轴向分佈管1,$二離冷 媒藉由該液態冷媒入口輸入至該軸向寻 J媒通過關减紅鱗聽· 悲 其中該液態冷媒淋灑至該熱傳管,盘嗲埶^:至該”、、傳5 ’ 轉化為一氣態冷媒,並藉由該本進f熱交換而 其中該分佈冷媒淋職组之冷媒频^ ’ 材以減低該液態冷媒飛賤;两上更包含有-緩衝 其中該軸向分佈管係利用-擋板連接於 2· 以防止該液態冷媒飛濺。X γ琛林巍面’亚用 如申請專利範圍第1項所述之鈦、、憩^ , 饰冷媒淋濃模組之冷媒淋灑面传震置’其中該分 3.如申請專利範圍第i項所述之二C孔。 佈冷媒淋濃模組之冷媒淋灑面传且^裝置’其中該分 佈冷媒淋灑模組之冷媒淋灑裝置’其中該分 &如申請專利範圍第5項所式流道。 衝材係為一多孔性材質。 八…、又換裝置,其中該緩 6·如申請專利範圍第6項所述之 孔性材質係選自化學纖維不’麗土:、$換裝置,其中該多 海綿相似物、網隔狀織布、全:彳物纖維不織布、海綿或 群組之-。 屬織狀物與非金屬織狀物所成 7·如申請專利範圍第i項所述 傳管係採交錯位置排列。淋,麗式熱父換農置,其中該熱 1291541 # W 8.如申請專利範圍第1項所述之淋灑式熱交換裝置,其中該熱 傳管係採整齊排列。1291541 Patent application scope: A shower type heat exchange device, comprising: - a body, having a accommodating space and - connecting the accommodating. A heat pipe is disposed in the accommodating space of the body. '—Distribution of the refrigerant shower module, comprising an axial distribution of a population and a refrigerant shower®, the axial distribution of the tube medium J liquid refrigerant inlet is disposed in the axial distribution tube 1, $ two from the refrigerant The liquid refrigerant inlet is input to the axial search medium to reduce the red scale and listen to the sadness. The liquid refrigerant is sprayed onto the heat transfer tube, and the tray 嗲埶^: to the "," and 5' is converted into a a gaseous refrigerant, and by the heat exchange of the refrigerant, wherein the refrigerant is distributed to reduce the liquid refrigerant fly hopper; the two are further included - the buffer is used in the axial distribution pipe system - The baffle is connected to 2· to prevent the liquid refrigerant from splashing. The X γ 琛 巍 ' 亚 亚 亚 亚 亚 亚 亚 亚 亚 亚 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如 如The vibration is set to 'the same. 3. The two C holes as described in item i of the patent application. The refrigerant cooling surface of the cloth cooling concentration module transmits and the device 'the refrigerant spraying device of the distributed cooling shower module' is divided into the flow path of the fifth item of the patent application scope. It is a porous material. Eight..., and the device is replaced, wherein the porous material is selected from the chemical fiber, which is not selected from the chemical fiber, and the device is replaced by a chemical fiber. Sponge similar, mesh woven fabric, full: woven fabric non-woven fabric, sponge or group - woven fabrics and non-metallic woven fabrics. 7 as described in the scope of patent application section i In the case of a staggered position, the hot heat transfer tube is arranged in a neat arrangement, wherein the heat transfer tube is arranged in a neat manner. 1111
TW094147101A 2005-12-29 2005-12-29 A sprinkling type heat exchanger TWI291541B (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
TW094147101A TWI291541B (en) 2005-12-29 2005-12-29 A sprinkling type heat exchanger
US11/642,684 US20070151279A1 (en) 2005-12-29 2006-12-21 Spray type heat-exchanging unit
US12/637,495 US8561675B2 (en) 2005-12-29 2009-12-14 Spray type heat-exchanging unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW094147101A TWI291541B (en) 2005-12-29 2005-12-29 A sprinkling type heat exchanger

Publications (2)

Publication Number Publication Date
TW200724848A TW200724848A (en) 2007-07-01
TWI291541B true TWI291541B (en) 2007-12-21

Family

ID=38222943

Family Applications (1)

Application Number Title Priority Date Filing Date
TW094147101A TWI291541B (en) 2005-12-29 2005-12-29 A sprinkling type heat exchanger

Country Status (2)

Country Link
US (1) US20070151279A1 (en)
TW (1) TWI291541B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI20100249U1 (en) 2010-07-16 2012-01-17 Alfa Laval Corp Ab HEAT EXCHANGE DEVICE WITH REFRIGERANT FLUID DISTRIBUTION SYSTEM
US10267547B2 (en) * 2016-02-18 2019-04-23 Johnson Controls Technology Company Falling-film evaporator suitable for low pressure refrigerant
CN107726886A (en) * 2017-10-12 2018-02-23 江苏万节能科技股份有限公司 A kind of heat exchanger
JP7182622B2 (en) * 2017-10-20 2022-12-02 ジョンソン コントロールズ テクノロジー カンパニー Falling film heat exchanger
CN107673433A (en) * 2017-11-13 2018-02-09 广东港荣水务科技有限公司 A kind of sewage disposal device of high-efficient energy-saving environment friendly
KR102292395B1 (en) * 2020-02-13 2021-08-20 엘지전자 주식회사 Evaporator
KR102292397B1 (en) 2020-02-13 2021-08-20 엘지전자 주식회사 Evaporator
KR102292396B1 (en) 2020-02-13 2021-08-20 엘지전자 주식회사 Evaporator

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1855552A (en) * 1931-04-20 1932-04-26 Alco Products Inc Heat exchanger
US3146609A (en) * 1964-04-27 1964-09-01 Baltimore Aircoil Co Inc Water distribution system
FR1531361A (en) * 1966-09-21 1968-07-05 Evaporator improvements
JPS5993181A (en) * 1982-11-19 1984-05-29 Hitachi Ltd Liquid film vaporization type heat exchanger
DE3709652A1 (en) * 1987-03-24 1988-10-06 Thermo Consulting Heidelberg DEVICE FOR EVAPORATING LIQUIDS OR ABSORBING OR DEGASSING TWO- OR MULTIPLE-MATERIAL SOLUTIONS IN DOWNTUBE CASE FILM DESIGN
US5561987A (en) * 1995-05-25 1996-10-08 American Standard Inc. Falling film evaporator with vapor-liquid separator
US5799621A (en) * 1996-11-26 1998-09-01 Burnham Corporation Boiler assembly
US5910167A (en) * 1997-10-20 1999-06-08 Modine Manufacturing Co. Inlet for an evaporator
US6089312A (en) * 1998-06-05 2000-07-18 Engineers And Fabricators Co. Vertical falling film shell and tube heat exchanger
US6293112B1 (en) * 1999-12-17 2001-09-25 American Standard International Inc. Falling film evaporator for a vapor compression refrigeration chiller
US6830099B2 (en) * 2002-12-13 2004-12-14 American Standard International Inc. Falling film evaporator having an improved two-phase distribution system
US6868695B1 (en) * 2004-04-13 2005-03-22 American Standard International Inc. Flow distributor and baffle system for a falling film evaporator

Also Published As

Publication number Publication date
TW200724848A (en) 2007-07-01
US20070151279A1 (en) 2007-07-05

Similar Documents

Publication Publication Date Title
TWI291541B (en) A sprinkling type heat exchanger
TWI320094B (en) Spray type heat exchang device
US8561675B2 (en) Spray type heat-exchanging unit
Liu et al. Heat transfer optimization of R134a phase change spray cooling in a closed loop system
KR100904363B1 (en) The hot water supply system using heat pump
EP1365199A1 (en) Evaporator with mist eliminator
CN107490212B (en) A kind of Falling Film Evaporator of Horizontal Tube
CN103727707A (en) Full-falling-film evaporator with double refrigerant distribution devices
JP2016054248A (en) Cooling module, cooling module mounting substrate, and electronic device
US20170370654A1 (en) Temperature glide thermosyphon and heat pipe
JP2011011202A (en) Evaporation type seawater desalination apparatus using phase-change medium
KR20180055833A (en) Air conditioner
CN108471693A (en) A kind of vaporation-type cooling system
CN102322751B (en) Spray cooling device for cooling heat source with high heat flux
CN102032825A (en) Heat exchange tube for evaporator and evaporator formed by same
JP2008292106A (en) Cooling tower system
CN202304118U (en) Falling film evaporator
CN108224604A (en) Electrical box cooling system and method and air conditioner
TWI289190B (en) Loop-type heat exchange device
WO2017088772A1 (en) Refrigerant evaporator of no-circulation pump of absorption type refrigeration unit, refrigeration unit and matrix
CN112833590B (en) Evaporative condenser with double precooling systems and embedded foam fin plates and method
WO2018072315A1 (en) Internal heat exchange component of absorption refrigeration unit, and absorption refrigeration unit and matrix
KR20220102963A (en) Condenser and air conditioner includling the same
CN205784031U (en) A kind of structural member for evaporative condenser
Karimi et al. A review on methods of design of condenser for vapour compression system