JPH09138086A - Heat transfer tube for absorption refrigerator - Google Patents

Heat transfer tube for absorption refrigerator

Info

Publication number
JPH09138086A
JPH09138086A JP7298418A JP29841895A JPH09138086A JP H09138086 A JPH09138086 A JP H09138086A JP 7298418 A JP7298418 A JP 7298418A JP 29841895 A JP29841895 A JP 29841895A JP H09138086 A JPH09138086 A JP H09138086A
Authority
JP
Japan
Prior art keywords
heat transfer
tube
transfer tube
absorption
ridges
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
JP7298418A
Other languages
Japanese (ja)
Inventor
Takeshi Nakai
剛 中井
Tadao Otani
忠男 大谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable Ltd
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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP7298418A priority Critical patent/JPH09138086A/en
Publication of JPH09138086A publication Critical patent/JPH09138086A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

(57)【要約】 【課題】 吸収能力を高めようとすると構造が複雑にな
った。 【解決手段】 伝熱管の管外表面管軸長手方向に6条の
凸条部を形成するとともに、この凸条部は管軸に対して
0.18度/mm以上0.72度/mm以下の比捻り角
をもってスパイラルに配置した吸収冷凍機用伝熱管。
(57) [Abstract] [Problem] The structure became complicated when trying to increase the absorption capacity. SOLUTION: Six ridges are formed in the longitudinal direction of the tube surface on the outer surface of the heat transfer tube, and the ridges are 0.18 degrees / mm or more and 0.72 degrees / mm or less with respect to the tube axis. A heat transfer tube for an absorption refrigerator, which is spirally arranged with a specific twist angle.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、吸収冷凍機、吸収
冷温水器あるいは吸収ヒートポンプ等の吸収冷凍サイク
ルを用いる熱交換機に用いられる伝熱管に関し、特に性
能を向上させた吸収冷凍機用伝熱管に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat transfer tube used in a heat exchanger using an absorption refrigeration cycle such as an absorption refrigerator, an absorption chiller-heater, or an absorption heat pump, and more particularly to a heat transfer tube for an absorption refrigerator having improved performance. It is about.

【0002】[0002]

【従来の技術】吸収冷凍機、吸収冷温水機、吸収ヒート
ポンプなどの吸収冷凍サイクルを用いる機器に使用され
る吸収器は、密閉容器内に水平あるいは垂直に多数の伝
熱管を多数配置して構成される。この場合、吸収剤−冷
媒としてわが国で最も多く使用されているリチウムブロ
マイド(LiBr)一水系を用いるものにおいては、伝
熱管外面に上部から高濃度のLiBr水溶液を薄膜状に
流下し、蒸発器で発生した冷媒の水蒸気を当該吸収液で
吸収すると同時に吸収時の潜熱を管内を流れる冷却水に
より取り去るように動作させるのが通常である。
2. Description of the Related Art An absorber used in equipment using an absorption refrigeration cycle, such as an absorption refrigerator, an absorption chiller-heater, and an absorption heat pump, is constructed by arranging a large number of heat transfer tubes horizontally or vertically in a closed container. To be done. In this case, in the case of using the lithium bromide (LiBr) monoaqueous system which is most often used in Japan as the absorbent-refrigerant, a high-concentration LiBr aqueous solution is made to flow down from the upper part to the outer surface of the heat transfer tube, and then the film is formed in the evaporator. It is usual that the generated water vapor of the refrigerant is absorbed by the absorption liquid and at the same time, the latent heat at the time of absorption is removed by the cooling water flowing in the pipe.

【0003】吸収は、蒸発器での蒸発圧力と伝熱管表面
に流下される吸収液の飽和蒸気圧との圧力差によって生
じ、この圧力差が大きければ吸収能力は向上する。ま
た、吸収液は温度が低いほど、あるいは濃度が高いほど
飽和蒸気圧が低く、圧力差が大きくなって吸収能力の向
上に寄与する。一方、伝熱管の外表面における挙動を見
ると、吸収液内へ凝縮した水が拡散する物質移動と、熱
の発生並びにこれの除去のための熱移動とが混在し、き
わめて複雑な様相を呈しており、その現象については未
だ十分な解明に至つていないのが現状である。つまり、
伝熱管の性能を向上せしめるには、前記物質移動と熱移
動の両面での向上が要求されるが、吸収能力の面から判
断すれば、熱移動の向上もさることながら、物質移動の
性能向上がより重要である。ところが、物質移動の向上
を目的とした伝熱管は性能の割りにはコストが高く、吸
収器用伝熱管は平滑管が主流となっている。パソコン、
機器に関する産業において、多ピンへの適用も十分考え
られる。
Absorption is caused by a pressure difference between the evaporation pressure in the evaporator and the saturated vapor pressure of the absorbing liquid flowing down on the surface of the heat transfer tube. If this pressure difference is large, the absorption capacity is improved. Further, the lower the temperature or the higher the concentration of the absorbing liquid, the lower the saturated vapor pressure and the larger the pressure difference, which contributes to the improvement of the absorbing capacity. On the other hand, looking at the behavior on the outer surface of the heat transfer tube, the mass transfer in which the condensed water diffuses into the absorbing liquid and the heat transfer for the generation and removal of heat coexist, showing a very complicated aspect. However, the current situation is that the phenomenon has not been fully clarified yet. That is,
In order to improve the performance of the heat transfer tube, it is necessary to improve both of the above-mentioned mass transfer and heat transfer, but from the viewpoint of the absorption capacity, the heat transfer is improved and the mass transfer performance is improved. Is more important. However, the heat transfer tube for improving the mass transfer is expensive for its performance, and the heat transfer tube for the absorber is mainly a smooth tube. computer,
In the equipment industry, application to a large number of pins can be considered.

【0004】一方、従来の吸収器または伝熱パイプとし
ては、伝熱管の外表面に波形となるよう15゜〜45゜
の傾斜角を有する多数の螺旋溝を刻設した吸収器(実公
昭64−4051号)、管の外面に3度以上の捩れ角を
有する複数の山部と谷部を交互にらせん状に位置させ形
成した伝熱管(特開平2−71062号)、管体の中心
軸に向かう谷部と、伝熱管の外表面の長手管軸方向15
度以下の捩れ角を有する複数の突条を形成した伝熱管
(特開平3−236561号)、管体の中心軸に向かう
谷部と、中心軸の放射方向に隆起する山部とを、周方向
に交互に設けて成る複数のひだを有する伝熱パイプ(特
開平5−39990号)が知られているが、いずれも特
性面で未だ満足する性能を満たすには至っていない状況
にある。
On the other hand, as a conventional absorber or heat transfer pipe, an absorber in which a large number of spiral grooves having an inclination angle of 15 ° to 45 ° are engraved on the outer surface of the heat transfer pipe (Actual Publication 64). -4051), a heat transfer tube formed by alternately arranging a plurality of peaks and valleys having a twist angle of 3 degrees or more on the outer surface of the tube in a spiral shape (JP-A-2-71062), the central axis of the tube body. Direction of the heat transfer tube and the longitudinal tube axial direction 15
A heat transfer tube having a plurality of ridges having a twist angle of not more than 3 degrees (Japanese Patent Application Laid-Open No. H3-236565), a valley portion toward the central axis of the tubular body, and a mountain portion protruding in the radial direction of the central axis are surrounded. A heat transfer pipe having a plurality of pleats alternately provided in the direction (Japanese Patent Laid-Open No. 5-39990) is known, but none of them has yet reached the satisfactory performance in terms of characteristics.

【0005】[0005]

【発明が解決しようとする課題】従来の伝熱管における
技術的課題について述べると、現状の溶液流下方式は薄
膜状に溶液を流す方式であり、さらに伝熱抵抗を減少さ
せ機器の効率向上を図るため、よりー層薄膜化しようと
いう傾向に進みつつある。また、先に述べたように吸収
能力向上に対しては、伝熱を促進させることよりも物質
移動の促進を図ることが先決であるが、それらを目的と
し、またはそれらの問題を解消させようとする伝熱管は
どうしてもその構造が複雑になるため、製造時の加工コ
ストが高くなり実用化には至っていないのが現状であ
る。特にnーオクチルアルコールやジエチルヘキサノー
ル等の界面活性剤を徽量添加することにより、吸収時に
溶液中においていわゆるマランゴニ効果に基く激しい界
面撹乱を生じさせ、吸収能力を向上させようとする方法
もあるが、この場合の伝熱管の構造も工業的には未だ満
足する状態に至っておらず、この面からの伝熱管の構造
改善が強く要望されている現状にある。
The technical problems in the conventional heat transfer tube will be described. The current solution flow-down method is a method of flowing a solution in the form of a thin film, and the heat transfer resistance is further reduced to improve the efficiency of the equipment. For this reason, there is a trend toward more thin layers. In addition, as mentioned above, in order to improve the absorption capacity, it is a priori decided to promote mass transfer rather than heat transfer, but for that purpose, let's solve those problems. Since the structure of the heat transfer tube is inevitably complicated, the processing cost at the time of manufacturing is high and it is not yet in practical use. In particular, there is also a method in which a large amount of a surfactant such as n-octyl alcohol or diethylhexanol is added to cause severe interfacial disturbance based on the so-called Marangoni effect in the solution at the time of absorption to improve the absorption capacity. In this case, the structure of the heat transfer tube has not yet been industrially satisfied, and there is a strong demand for structural improvement of the heat transfer tube from this aspect.

【0006】それ故、本発明の目的は、吸収現象特有の
熱移動と物質移動とをより効果的に進展させることので
きる吸収冷凍機用伝熱管を提供することにある。
Therefore, it is an object of the present invention to provide a heat transfer tube for an absorption refrigerator, which can more effectively develop heat transfer and mass transfer peculiar to the absorption phenomenon.

【0007】本発明の目的は、熱移動と物質移動と言う
二つの現象を著しく向上させ、吸収能力を飛躍的に向上
させた吸収冷凍機用伝熱管を提供することにある。
An object of the present invention is to provide a heat transfer tube for an absorption chiller in which two phenomena, heat transfer and mass transfer, are remarkably improved and the absorption capacity is dramatically improved.

【0008】また、本発明の目的は、構造が簡単で、熱
移動と物質移動とをより効果的に進展させ、吸収能力を
向上させた吸収冷凍機用伝熱管を安価に提供することに
ある。
Another object of the present invention is to provide at low cost a heat transfer tube for an absorption refrigerating machine having a simple structure, more effectively promoting heat transfer and mass transfer, and having improved absorption capacity. .

【0009】また、本発明の目的は、構造が簡単で、製
造時の加工も容易であり、しかも吸収冷凍機用伝熱管の
管外面管軸長手方向における吸収現象特有の熱移動と物
質移動と言う二つの現象を向上させた伝熱管を経済的に
安価に提供することにある。
Another object of the present invention is that the structure is simple, the manufacturing process is easy, and the heat transfer and mass transfer peculiar to the absorption phenomenon in the tube outer surface tube longitudinal direction of the heat transfer tube for the absorption refrigerator. It is to provide a heat transfer tube that improves the above two phenomena economically and inexpensively.

【0010】[0010]

【課題を解決するための手段】本発明は、上記の目的を
達成するために、伝熱管の管外表面に吸収液を滴下また
は散布して、該管外表面に吸収液の液膜を形成し、その
液膜を通して熱移動を行なわせる吸収冷凍機用の伝熱管
において、管外表面管軸長手方向に非変形部を間に設け
て6条の凸条部を形成するとともに、この凸条部は管軸
に対して0.18度/mm以上、0.72度/mm以下
の比捻り角をもってスパイラルに配置されていることを
特徴とする吸収冷凍機用伝熱管を提供する。
In order to achieve the above-mentioned object, the present invention forms a liquid film of the absorbing liquid on the outer surface of the pipe by dropping or spraying the absorbing liquid on the outer surface of the heat transfer pipe. In a heat transfer tube for an absorption refrigerating machine that transfers heat through the liquid film, a non-deformable portion is provided in the longitudinal direction of the outer surface of the tube to form six ridges. Provided is a heat transfer tube for an absorption refrigerating machine, wherein the parts are spirally arranged with a specific twist angle of 0.18 degrees / mm or more and 0.72 degrees / mm or less with respect to the tube axis.

【0011】伝熱管の管外表面に吸収液を滴下または散
布して、該管外表面に吸収液の液膜を形成し、その液膜
を通して熱移動を行なわせる吸収冷凍機用の伝熱管にお
いて、管外表面管軸長手方向に6条の凸条部を形成する
とともに、この凸条部は管軸に対して0.18度/mm
以上、0.72度/mm以下の比捻り角をもってスパイ
ラルに配置して吸収冷凍機用伝熱管を構成することによ
り、伝熱管における吸収現象特有の熱移動と物質移動と
言う二つの現象をともに向上させることができるように
している。
In a heat transfer tube for an absorption refrigerator in which an absorbing liquid is dropped or sprayed on the outer surface of the heat transfer tube to form a liquid film of the absorbing liquid on the outer surface of the heat transfer tube and heat is transferred through the liquid film. The outer surface of the pipe has six ridges formed in the longitudinal direction of the pipe axis, and these ridges are 0.18 degrees / mm with respect to the pipe axis.
As described above, by arranging spirally with a specific twist angle of 0.72 degrees / mm or less to form a heat transfer tube for an absorption refrigerator, both heat transfer and mass transfer peculiar to the absorption phenomenon in the heat transfer tube can be performed. I am trying to improve it.

【0012】また、前記吸収冷凍機用伝熱管の管外面管
軸長手方向にスパイラルに配置され形成された6条の凸
条部は、管内面では凹条に形成されるように構成するこ
とにより、管外表面に吸収液の液膜と管内面での熱移動
を効率よく行なわれるようにしている。
Further, the six convex ridges arranged spirally in the longitudinal direction of the tube outer surface of the heat transfer tube for the absorption chiller are formed to be concave on the inner surface of the tube. The liquid film of the absorbing liquid on the outer surface of the tube and the heat transfer on the inner surface of the tube are efficiently performed.

【0013】さらに、前記吸収冷凍機用伝熱管の管外面
管軸長手方向の管軸に対して0.18度/mm以上0.
72度/mm以下の比捻り角をもってスパイラルに配置
し形成された6条の凸条部を有する伝熱管は、銅または
銅合金のような金属から構成されている。銅としては電
気銅または無酸素銅などがあり、銅合金としては、例え
ば、銅と錫、銅とジルコニウム、銅と銀などが挙げられ
る。これにより管外表面に吸収液の液膜と管内面での熱
移動を極めて効率よく行なわれるように構成している。
Furthermore, the outer surface of the heat transfer tube for the absorption refrigerator is 0.18 degrees / mm or more with respect to the tube axis in the tube axis longitudinal direction.
The heat transfer tube having six ridges arranged spirally with a specific twist angle of 72 degrees / mm or less is made of metal such as copper or copper alloy. Examples of copper include electrolytic copper and oxygen-free copper, and examples of copper alloys include copper and tin, copper and zirconium, and copper and silver. Thereby, the liquid film of the absorbing liquid on the outer surface of the tube and the heat transfer on the inner surface of the tube are configured to be performed very efficiently.

【0014】また、吸収冷凍機用伝熱管の管外面管軸長
手方向の管軸に対してスパイラルに配置され形成された
6条の凸条部は、0.18度/mm以下の比捻り角であ
ると、吸収液は横方向へ広がるが、凸条部を乗り越える
ことができず、吸収液が凸条部間で厚膜となり熱伝達の
妨げとなり、吸収性能の向上は期待できない。一方、
0.72度/mm以上の比捻れ角であると吸収液は円周
方向へと流れ落ちてしまい吸収液の撹拌効果が望めず吸
収性能の向上は期待できない。従って本発明では管軸に
対してスパイラルに配置され形成された6条の凸条部
は、0.18度/mm以上〜0.72度/mm以下の比
捻り角が伝熱管における吸収現象特有の熱移動と物質移
動と言う二つの現象をともに向上させるのに最も適正な
領域である。
The outer surface of the heat transfer tube for an absorption refrigerating machine has six ridges arranged spirally with respect to the tube axis in the longitudinal direction of the tube axis, and the specific twist angle is 0.18 degrees / mm or less. In such a case, the absorbing liquid spreads in the lateral direction, but cannot pass over the ridges, and the absorbing liquid forms a thick film between the ridges, which hinders heat transfer, and improvement in absorption performance cannot be expected. on the other hand,
When the specific twist angle is 0.72 degrees / mm or more, the absorbing liquid flows down in the circumferential direction, the stirring effect of the absorbing liquid cannot be expected, and improvement in absorption performance cannot be expected. Therefore, in the present invention, the six ridges formed spirally with respect to the tube axis have a specific twist angle of 0.18 degrees / mm to 0.72 degrees / mm, which is characteristic of the absorption phenomenon in the heat transfer tube. This is the most appropriate area to improve both the two phenomena of heat transfer and mass transfer.

【0015】[0015]

【発明の実施の形態】図1は本発明伝熱管の実施の形態
であって、伝熱管の横断面図、図2は本発明伝熱管の実
施の形態であって、伝熱管の外観図、図3は本発明に係
る伝熱管の製造法の一例を示す説明図、図4は本発明に
よる伝熱管を製造時に使用する加工ダイスの正面図、図
5は本発明伝熱管の他の実施の形態であって、伝熱管の
外観図である。本発明伝熱管の実施の形態を示す図1に
おいて、伝熱管本体10の外面に所定のピッチと捻れ角
からなる凸条部12を設けてある。11は平滑部であ
る。具体的には凸条部12は伝熱管本体10の周囲上に
6条形成されており、しかも凸条部12は伝熱管本体1
0の管外面管軸長手方向の管軸に対して比捻り角0.3
6度/mmとやや緩やかな捻りにより配置されている。
この図1の実施の形態の伝熱管では凸条部12を形成し
た伝熱管本体10の内部には凹条部13が形成されてい
る。
1 is a cross-sectional view of a heat transfer tube according to an embodiment of the present invention, and FIG. 2 is an external view of the heat transfer tube according to an embodiment of the present invention. FIG. 3 is an explanatory view showing an example of a method for manufacturing the heat transfer tube according to the present invention, FIG. 4 is a front view of a processing die used for manufacturing the heat transfer tube according to the present invention, and FIG. 5 is another embodiment of the heat transfer tube according to the present invention. It is a form and is an external view of a heat transfer tube. 1, which shows an embodiment of the heat transfer tube of the present invention, a ridge 12 having a predetermined pitch and a twist angle is provided on the outer surface of the heat transfer tube body 10. 11 is a smooth part. Specifically, the ridges 12 are formed in six rows on the periphery of the heat transfer tube body 10, and the ridges 12 are formed on the heat transfer tube body 1
No. 0 outer surface of the tube relative to the longitudinal axis of the tube relative twist angle 0.3
It is arranged with a slight twist of 6 degrees / mm.
In the heat transfer tube according to the embodiment shown in FIG. 1, a concave streak portion 13 is formed inside the heat transfer tube main body 10 in which the convex streak portion 12 is formed.

【0016】この図1に示す本発明実施の形態の伝熱管
の凸条部12は、管外面では上部から滴下または散布さ
れる吸収液を、伝熱管表面で特に管軸方向に広げるよう
に作用する。その結果、吸収液は、薄い液膜となり伝熱
管表面を覆い熱伝達率が大きくなるとともに、管軸方向
流れで吸収現象特有の物質移動の向上を図ることがで
き、吸収性能を向上させるものである。一方上記凸条部
12の管内面では凹条部13となる。この凹条部13に
より管内を流れる冷却水は乱され、その結果伝熱管の管
内側伝熱性能も向上し、伝熱管全体としての伝熱性能の
向上が図られる。
The ridge portion 12 of the heat transfer tube according to the embodiment of the present invention shown in FIG. 1 acts to spread the absorbing liquid dropped or sprinkled from the upper portion on the outer surface of the tube, particularly on the surface of the heat transfer tube in the axial direction of the tube. To do. As a result, the absorbing liquid becomes a thin liquid film and covers the surface of the heat transfer tube to increase the heat transfer coefficient, and at the same time, it is possible to improve the mass transfer characteristic of the absorption phenomenon by the flow in the tube axial direction, thereby improving the absorption performance. is there. On the other hand, the inner surface of the tube of the ridge 12 is a ridge 13. The cooling water flowing in the pipe is disturbed by the recessed portion 13, and as a result, the heat transfer performance inside the heat transfer tube is improved, and the heat transfer performance of the heat transfer tube as a whole is improved.

【0017】図2の伝熱管の実施の形態においては、伝
熱管本体20の外面に所定のピッチと捻れ角からなる凸
条部22を設けてある。21は平滑部である。具体的に
は凸条部22は伝熱管本体20の周囲上に6条形成され
ており、しかも凸条部22は伝熱管本体20の管外面管
軸長手方向の管軸に対して比捻り角0.28度/mmと
緩やかな捻りにより配置されている。この図2の伝熱管
の実施の形態においても、凸条部22は管外面では、上
部から滴下または散布される吸収液を、伝熱管表面で特
に管軸方向に広げるように作用する。その結果吸収液
は、薄い液膜となり伝熱管表面を覆い熱伝達率が大きく
なるとともに、管軸方向流れで吸収現象特有の物質移動
の向上を図り、吸収性能を向上させるものである。
In the embodiment of the heat transfer tube shown in FIG. 2, the outer surface of the heat transfer tube body 20 is provided with the ridge portion 22 having a predetermined pitch and a twist angle. 21 is a smooth part. Specifically, the ridges 22 are formed in six rows on the periphery of the heat transfer tube body 20, and the ridges 22 have a specific twist angle with respect to the tube axis in the tube outer surface tube axis longitudinal direction of the heat transfer tube body 20. It is arranged with a gentle twist of 0.28 degrees / mm. Also in the embodiment of the heat transfer tube shown in FIG. 2, the ridge portion 22 acts on the outer surface of the tube so as to spread the absorbing liquid dropped or sprinkled from the upper part particularly on the surface of the heat transfer tube in the tube axial direction. As a result, the absorbing liquid becomes a thin liquid film and covers the surface of the heat transfer tube to increase the heat transfer coefficient, and at the same time, the mass transfer characteristic of the absorption phenomenon is improved by the flow in the tube axial direction to improve the absorption performance.

【0018】図3は、本発明伝熱管の製造方法の一実施
の形態を示す概略図である。加工ダイス32は、図4に
示すダイス本体41の内面に所定のピッチ、高さからな
る突起42が12条設けられている。前記加工ダイス3
2は、図3の外部に位置する回転装置33に固定され回
転可能なように取り付けられている。吸収式用伝熱管は
使用圧力はさほど高くないため比較的薄肉の銅管などが
用いられる。薄肉銅管などの断面円形の素管31は、回
転する加工ダイス32を通しながら引抜加工を施すこと
により、管外面に凸条部12または22を形成すること
ができる。この場合、管内面には凹条部13が6条形成
される。
FIG. 3 is a schematic view showing an embodiment of a method for manufacturing a heat transfer tube of the present invention. In the processing die 32, 12 protrusions 42 having a predetermined pitch and height are provided on the inner surface of the die body 41 shown in FIG. The processing die 3
2 is fixed to a rotating device 33 located outside of FIG. 3 and is rotatably attached. Since the heat transfer tube for absorption type is not so high in working pressure, a relatively thin copper tube or the like is used. The convex tube portion 12 or 22 can be formed on the outer surface of the tube 31 having a circular cross-section, such as a thin copper tube, by performing drawing while passing the rotating processing die 32. In this case, six recesses 13 are formed on the inner surface of the pipe.

【0019】図5は、本発明の他の実施の形態による伝
熱管である。この実施の形態では凸条部52の高さに対
して薄肉銅管などの断面円形の素管の径は大きくしてあ
る。伝熱管の管軸に対してスパイラルに配置され形成さ
れた6条の凸条部52は、0.18度/mm以上〜0.
72度/mm以下の比捻り角を有するように形成してあ
る。これは、伝熱管における吸収現象特有の熱移動と物
質移動と言う二つの現象をともに向上させるためであ
る。また、吸収性能を向上させるために、6条の凸条部
52の間の平滑部には管軸方向に直角な溝51を長さ方
向に形成することもできる。さらに伝熱管の肉厚が薄肉
の場合でも、伝熱管の管内面に微細な溝を形成すること
もできる。このような管軸方向に直角な溝51、あるい
は伝熱管の管内面に微細な溝を設けることにより、吸収
液は、薄い液膜となり伝熱管表面を覆う熱伝達率を向上
させる作用があり、この結果、管軸方向流れで吸収現象
特有の物質移動の特性が良好となり、吸収性能の向上が
図れるものである。
FIG. 5 shows a heat transfer tube according to another embodiment of the present invention. In this embodiment, the diameter of the raw pipe having a circular cross section such as a thin copper pipe is made larger than the height of the protruding portion 52. The six ridge portions 52 arranged and formed spirally with respect to the tube axis of the heat transfer tube have a width of 0.18 degrees / mm or more to 0.
It is formed so as to have a specific twist angle of 72 degrees / mm or less. This is to improve both the two phenomena, heat transfer and mass transfer, which are peculiar to the absorption phenomenon in the heat transfer tube. In addition, in order to improve the absorption performance, a groove 51 perpendicular to the tube axis direction may be formed in the lengthwise direction in the smooth portion between the six ridges 52. Furthermore, even if the heat transfer tube has a small thickness, fine grooves can be formed on the inner surface of the heat transfer tube. By providing such grooves 51 perpendicular to the tube axis direction or fine grooves on the inner surface of the heat transfer tube, the absorbing liquid becomes a thin liquid film and has the effect of improving the heat transfer coefficient covering the surface of the heat transfer tube. As a result, the characteristics of mass transfer peculiar to the absorption phenomenon due to the flow in the axial direction of the tube are improved, and the absorption performance can be improved.

【0020】[0020]

【発明の効果】本発明の効果としては、吸収現象特有の
熱移動と物質移動とを効率よく進展させることのできる
吸収冷凍機用伝熱管を提供することが出来る。
As an effect of the present invention, it is possible to provide a heat transfer tube for an absorption refrigerating machine capable of efficiently advancing heat transfer and mass transfer peculiar to an absorption phenomenon.

【0021】本発明の他の効果としては、構造が簡単
で、熱移動と物質移動と言う二つの現象を著しく向上さ
せ、吸収能力を飛躍的に向上させた吸収冷凍機用伝熱管
を提供することが出来る。
Another advantage of the present invention is to provide a heat transfer tube for an absorption refrigerator, which has a simple structure and which remarkably improves two phenomena of heat transfer and mass transfer and has dramatically improved absorption capacity. You can

【0022】また、本発明の効果としては、構造が簡単
で、熱移動と物質移動とを効率よく進展させ、吸収能力
を向上させた吸収冷凍機用伝熱管を経済的に安価に提供
することが出来る。
Further, as an effect of the present invention, it is possible to economically provide a heat transfer tube for an absorption refrigerator, which has a simple structure, efficiently promotes heat transfer and mass transfer, and has improved absorption capacity at low cost. Can be done.

【0023】また、本発明の他の効果としては、構造が
簡単で、製造時の加工も容易であり、しかも吸収冷凍機
用伝熱管の管外面管軸長手方向における吸収現象特有の
熱移動と物質移動と言う二つの現象を向上させた伝熱管
を経済的に安価に提供することが出来る。
Another advantage of the present invention is that the structure is simple, the manufacturing process is easy, and the heat transfer characteristic of the absorption phenomenon in the longitudinal direction of the tube outer surface of the heat transfer tube for the absorption refrigerator is achieved. It is possible to economically and inexpensively provide a heat transfer tube in which two phenomena called mass transfer are improved.

【0024】本発明の他の効果としては、吸収性能の向
上はもとより、特別な装置を必要とせず、一般的な引抜
き製造装置により高速加工することができるため安価に
高性能な吸収冷凍機用伝熱管を提供することが出来る。
Another advantage of the present invention is that, in addition to improving the absorption performance, it does not require a special apparatus and can be processed at high speed by a general drawing manufacturing apparatus, so that it can be used at a low cost for a high-performance absorption refrigerator. A heat transfer tube can be provided.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明伝熱管の実施の形態であって、伝熱管の
横断面図。
FIG. 1 is a cross-sectional view of a heat transfer tube according to an embodiment of the heat transfer tube of the present invention.

【図2】本発明伝熱管の実施の形態であって、伝熱管の
外観図。
FIG. 2 is an external view of a heat transfer tube according to the embodiment of the heat transfer tube of the present invention.

【図3】本発明に係る伝熱管の製造法の一例を示す説明
図。
FIG. 3 is an explanatory view showing an example of a method for manufacturing a heat transfer tube according to the present invention.

【図4】本発明による伝熱管を製造時に使用する加工ダ
イスの正面図。
FIG. 4 is a front view of a processing die used for manufacturing the heat transfer tube according to the present invention.

【図5】本発明伝熱管の他の実施の形態であって、伝熱
管の外観図。
FIG. 5 is an external view of a heat transfer tube according to another embodiment of the heat transfer tube of the present invention.

【符号の説明】[Explanation of symbols]

10 伝熱管本体 11 平滑部 12 凸条部 13 凹条部 20 伝熱管本体 21 平滑部 22 凸条部 31 素管 32 加工ダイス 33 回転装置 41 ダイス本体 42 突起 51 溝 52 凸条部 10 heat transfer tube main body 11 smooth section 12 convex streak section 13 concave streak section 20 heat transfer tube main body 21 smooth section 22 convex streak section 31 element pipe 32 processing die 33 rotating device 41 die body 42 projection 51 groove 52 convex streak section

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】伝熱管の管外表面に吸収液を滴下または散
布して、該管外表面に吸収液の液膜を形成し、その液膜
を通して熱移動を行なわせる吸収冷凍機用の伝熱管にお
いて、 管外表面管軸長手方向に非変形部を間に設けて6条の凸
条部を形成するとともに、この凸条部は管軸に対して
0.18度/mm以上、0.72度/mm以下の比捻り
角をもってスパイラルに配置されていることを特徴とす
る吸収冷凍機用伝熱管。
Claim: What is claimed is: 1. A transfer for an absorption refrigerating machine, wherein an absorbing liquid is dropped or sprinkled on the outer surface of a heat transfer pipe to form a liquid film of the absorbing liquid on the outer surface of the heat transfer pipe, and heat is transferred through the liquid film. In the heat pipe, a non-deformable portion is provided in the longitudinal direction of the outer surface of the tube to form six ridges, and the ridges are 0.18 degrees / mm or more with respect to the tube axis, and are 0. A heat transfer tube for an absorption refrigerator, which is spirally arranged with a specific twist angle of 72 degrees / mm or less.
【請求項2】前記6条の凸条部は、管内面では凹条に形
成されていることを特徴とする請求項1記載の吸収冷凍
機用伝熱管。
2. The heat transfer tube for an absorption refrigerating machine according to claim 1, wherein the six ridges are formed in a concave shape on the inner surface of the tube.
JP7298418A 1995-11-16 1995-11-16 Heat transfer tube for absorption refrigerator Pending JPH09138086A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7298418A JPH09138086A (en) 1995-11-16 1995-11-16 Heat transfer tube for absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7298418A JPH09138086A (en) 1995-11-16 1995-11-16 Heat transfer tube for absorption refrigerator

Publications (1)

Publication Number Publication Date
JPH09138086A true JPH09138086A (en) 1997-05-27

Family

ID=17859454

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7298418A Pending JPH09138086A (en) 1995-11-16 1995-11-16 Heat transfer tube for absorption refrigerator

Country Status (1)

Country Link
JP (1) JPH09138086A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100468397B1 (en) * 2001-12-26 2005-01-27 엘지전선 주식회사 A Falling Film Enhanced Tub

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100468397B1 (en) * 2001-12-26 2005-01-27 엘지전선 주식회사 A Falling Film Enhanced Tub

Similar Documents

Publication Publication Date Title
JP3315785B2 (en) Heat transfer tube for absorber
JPH10267460A (en) Heat transfer pipe of absorbing device
JPH07111287B2 (en) Heat transfer tube for absorber
JPH09138086A (en) Heat transfer tube for absorption refrigerator
JP2960828B2 (en) Heat transfer tube for absorber
JP3587599B2 (en) Heat transfer tube for absorber
JP2000346579A (en) Heat transfer tube
KR200150457Y1 (en) Heat pipe
CN208312500U (en) Heat exchanger for refrigerating hood and refrigerating hood having the same
JP3019699B2 (en) Heat transfer tube for absorption in pipe
JPS636364A (en) Heat transfer tube for absorber
JP4587545B2 (en) Heat exchanger tube for absorber
JPH06159862A (en) Absorber for freezer
JPH11270980A (en) Heat transfer tube for evaporator
JPH11118382A (en) Heat transfer tube for evaporator and method of manufacturing the same
JPH02176378A (en) Heat transfer tube for absorber
JP3297457B2 (en) Refrigerant pipe
KR100205977B1 (en) Heaa pipe
JP3391170B2 (en) Heat transfer tube and absorber for absorber
KR100205978B1 (en) Heat transfer tube of absorption type refrigerator
JPH1078268A (en) Heat transfer tube
JPH09145279A (en) Heat transfer tube for absorber
JP2934160B2 (en) Heat transfer tubes for absorbers and regenerators
JPH0972628A (en) Absorber heat transfer tube and manufacturing method thereof
JPH058424Y2 (en)