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JPH0723820B2 - Heat transfer tube for absorber - Google Patents
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JPH0723820B2 - Heat transfer tube for absorber - Google Patents

Heat transfer tube for absorber

Info

Publication number
JPH0723820B2
JPH0723820B2 JP14066587A JP14066587A JPH0723820B2 JP H0723820 B2 JPH0723820 B2 JP H0723820B2 JP 14066587 A JP14066587 A JP 14066587A JP 14066587 A JP14066587 A JP 14066587A JP H0723820 B2 JPH0723820 B2 JP H0723820B2
Authority
JP
Japan
Prior art keywords
heat transfer
transfer tube
absorber
liquid
absorption
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.)
Expired - Fee Related
Application number
JP14066587A
Other languages
Japanese (ja)
Other versions
JPS63306372A (en
Inventor
治 川又
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 JP14066587A priority Critical patent/JPH0723820B2/en
Publication of JPS63306372A publication Critical patent/JPS63306372A/en
Publication of JPH0723820B2 publication Critical patent/JPH0723820B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Non-Disconnectible Joints And Screw-Threaded Joints (AREA)
  • Rigid Pipes And Flexible Pipes (AREA)
  • Pipe Accessories (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は吸収式冷凍機、吸収式ヒートポンプ等の吸収器
に使用される伝熱管に関するものである。
The present invention relates to a heat transfer tube used in an absorber such as an absorption refrigerator and an absorption heat pump.

[従来技術とその問題点] 吸収式冷凍機、吸収式ヒートポンプ等における吸収器
は、密閉容器内に、水平あるいは垂直に多数の伝熱管を
配置して構成される。この場合、伝熱管の外側には吸収
液、例えばLiBr水溶液(濃度約60質量%)が滴下散布さ
れ、蒸発器で発生した水蒸気を吸収させると同時に、吸
収時の熱を管内を流れる冷却水により取去るように作用
する。
[Prior Art and Problems Thereof] An absorber in an absorption refrigerator, an absorption heat pump, or the like is configured by arranging a large number of heat transfer tubes horizontally or vertically in a closed container. In this case, an absorbing liquid, for example, a LiBr aqueous solution (concentration of about 60% by mass) is dropped and sprinkled on the outside of the heat transfer tube to absorb the steam generated in the evaporator, and at the same time, heat at the time of absorption is absorbed by the cooling water flowing in the tube. Acts to remove.

吸収は蒸発器での蒸発圧力と、伝熱管の表面に滴下され
た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。
従って、この種の伝熱管には熱の移動と吸収液内への凝
縮した水が拡散する物質移動の両面の向上が要求され
る。しかし、これまでこの吸収機構については不明な点
が多く、伝熱管としては平滑管が主流となっている。
Absorption is caused by the pressure difference between the evaporation pressure in the evaporator and the saturated vapor pressure of the absorbing liquid dropped on the surface of the heat transfer tube. If this pressure difference is large, the 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.
Therefore, this type of heat transfer tube is required to improve both the heat transfer and the mass transfer of the condensed water into the absorbing liquid. However, there are many unclear points regarding this absorption mechanism, and smooth tubes have been the mainstream as heat transfer tubes.

一方、吸収器では伝熱管が水平に配置され、吸収液が上
方から滴下される方式が主流である。この際、管表面上
を流れる吸収液は薄膜状となり、さらに伝熱抵抗の減
少、機器の効率向上のため、より薄膜化の方向に進んで
いる。しかし、吸収においては熱移動よりも物質移動が
律速となる。従って、現状の薄膜流下方式では伝熱を促
進させることよりも物質移動の促進を図らなければ吸収
性能の飛躍的向上は望めない。そのため最近、伝熱面積
を増加させると同時に吸収液の薄膜化を図る目的で、ロ
ーフィンチューブ等の加工管を使用する試みがなされて
いるが、これでも伝熱管の増加に見合うまでの吸入能力
の向上には至っていない。
On the other hand, in the absorber, the heat transfer tubes are arranged horizontally and the absorption liquid is dripped from above. At this time, the absorbing liquid flowing on the surface of the tube is in the form of a thin film, and further progress is being made toward a thin film in order to reduce the heat transfer resistance and improve the efficiency of the device. However, in absorption, mass transfer is rate limiting rather than heat transfer. Therefore, in the current thin-film flow-through method, it is impossible to expect a dramatic improvement in absorption performance unless the mass transfer is promoted rather than the heat transfer is promoted. Therefore, recently, it has been attempted to use a processing tube such as a low fin tube for the purpose of increasing the heat transfer area and at the same time making the absorption liquid into a thin film. Has not improved.

吸収器は、機器の性能を左右する重要なコンポーネント
であるため、今後機器の小形化、高性能化を図る上で吸
収器を高性能化することが大きな意味をもつ。従って、
伝熱管の高性能化が重要なポイントであり、特に吸収過
程における物質移動の促進を図る必要がある。
Since the absorber is an important component that influences the performance of the equipment, it is important to improve the performance of the absorber in order to make the equipment compact and high performance in the future. Therefore,
Improving the performance of heat transfer tubes is an important point, and it is especially necessary to promote mass transfer during the absorption process.

[発明の目的] 商用の吸収式冷凍機、吸収式ヒートポンプ等の吸収液に
はジエチルヘキサノール等の界面活性剤が加えられてい
る。これは吸収能力を向上させる方法として経験的に知
られている。
[Object of the Invention] Surfactants such as diethylhexanol are added to the absorption liquid of commercial absorption refrigerators, absorption heat pumps and the like. This is empirically known as a method of improving absorption capacity.

本発明では、このような界面活性剤を添加した吸収液を
用いる吸収器であっても飛躍的な性能向上を図ることの
できる新規な伝熱管を提供することにある。
An object of the present invention is to provide a novel heat transfer tube capable of dramatically improving performance even in an absorber using an absorbent containing such a surfactant.

[発明の概要] 発明者等は伝熱性能と共に物質伝熱性能についても研究
・実験を重ねた結果、伝熱管表面上の吸収液膜内で対流
が発生すると、熱と共に、特に物質移動が大幅に促進さ
れることがわかった。伝熱管表面上の溶液は水蒸気と接
する面では水蒸気を吸収して低濃度となるが、深さ方向
への移動は拡散だけではあまり進展しない。そこで対流
が発生すれば液膜内での撹拌が発生し、溶液表面だけが
低濃度となって吸収を抑制することはなくなり性能が向
上する。
[Summary of the Invention] The inventors have conducted research and experiments on heat transfer performance as well as heat transfer performance, and as a result, when convection occurs in the absorbing liquid film on the surface of the heat transfer tube, heat transfer, particularly mass transfer, is significantly increased. It turned out to be promoted to. The solution on the surface of the heat transfer tube absorbs the water vapor on the surface in contact with the water vapor to have a low concentration, but the movement in the depth direction does not progress much by diffusion alone. If convection occurs there, agitation occurs in the liquid film, and only the surface of the solution becomes low in concentration, and absorption is not suppressed, and the performance is improved.

また、一般に対流は界面活性剤の添加による表面張力差
により引き起こされ、溶液の厚さが大きい方が発生しや
すいことが知られている。
Further, it is known that convection is generally caused by a difference in surface tension due to the addition of a surfactant, and tends to occur when the thickness of the solution is large.

本発明では管自体の形状を液の滴下方向に対して広がり
を持たせたことにより管上部で液膜を厚く停留させると
同時に円周方向への液の流れの分配を行ない、管表面全
体を伝熱面として有効に作用させる。それによりフィン
チューブを効果をより有効に発揮させ、熱、物質移動を
大幅に促進されるようにしている。
In the present invention, the shape of the pipe itself is made wider in the dropping direction of the liquid, so that the liquid film is thickly retained at the upper part of the pipe and at the same time, the liquid flow is distributed in the circumferential direction, and the entire pipe surface is covered. It works effectively as a heat transfer surface. As a result, the fin tube is more effectively exerted, and heat and mass transfer are greatly promoted.

[発明の実施例] 第1図及び第2図は、外径19mmの伝熱管用の銅管に、高
さ0.9mm、長手方向のピッチ0.7mmで各々独立した針状の
フィン2を設け、この伝熱管1を一方向にプレスし、長
軸24mm、短軸14mmトラック形状にした場合を示してい
る。
[Embodiment of the Invention] FIGS. 1 and 2 show that a copper tube having an outer diameter of 19 mm for a heat transfer tube is provided with independent fins 2 each having a height of 0.9 mm and a longitudinal pitch of 0.7 mm. The case where the heat transfer tube 1 is pressed in one direction to have a track shape of a long axis 24 mm and a short axis 14 mm is shown.

この伝熱管1について、その短軸側を垂直方向にして第
2図に示すような実験装置3内に多段に組込んで液の流
れを観察した。
Regarding this heat transfer tube 1, the liquid flow was observed by incorporating the heat transfer tube 1 in multiple stages in an experimental apparatus 3 as shown in FIG.

実験は、40℃の吸収液4(濃度58wt%LiBr水溶液)を滴
下する一方、伝熱管1内に28℃の冷却水を流した。
In the experiment, the absorption liquid 4 (concentration 58 wt% LiBr aqueous solution) at 40 ° C. was dropped, while the cooling water at 28 ° C. was flown into the heat transfer tube 1.

この実験の結果、管上部で液4が停留して液膜厚さが厚
く保持されると同時に、円周方向への液4の分配は管表
面のほぼ全体を均一に流れ、第3図に示すような様相を
呈した。
As a result of this experiment, the liquid 4 was retained at the upper part of the pipe and the liquid film thickness was kept thick. The appearance was as shown.

このことから、対流の発生による液の撹拌と伝熱面積の
増加により伝熱管の大幅な伝熱性能の向上が期待できる
ことがわかる。
From this, it can be seen that a significant improvement in heat transfer performance of the heat transfer tube can be expected due to the agitation of the liquid due to the generation of convection and the increase in the heat transfer area.

[発明の効果] 本発明の伝熱管は吸収液の滴下方向に対して幅に広い形
状となっており、管上部で液を停留させて液膜厚さを大
きく保持させて対流を発生させると同時に、円周方向へ
の液の分配を均一にさせて管表面のほぼ全体に液が流れ
るようになり、伝熱面積を大幅に増大させ、フィンチュ
ーブの効果をより有効に発揮させたものであるから、こ
れを用いる吸収式冷凍機、吸収式ヒートポンプ等の吸収
器の性能を向上させ、機器のコンパクト化に大いに貢献
する。
[Effects of the Invention] The heat transfer tube of the present invention has a shape wide in the width direction of the absorbing liquid, and when the liquid is retained at the upper part of the tube to keep the liquid film thickness large and convection is generated. At the same time, the liquid is evenly distributed in the circumferential direction to allow the liquid to flow over almost the entire surface of the tube, greatly increasing the heat transfer area and making the fin tube more effective. Therefore, the performance of an absorber such as an absorption refrigerator or an absorption heat pump using the same is improved, which greatly contributes to downsizing of the equipment.

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

第1図は本発明に係る伝熱管の一実施例を示す横断面
図、第2図はその正面図、第3図は、実施例の伝熱管に
おける液の流れの状態を示す図である。 1:伝熱管、2:針状フィン。
FIG. 1 is a transverse sectional view showing an embodiment of a heat transfer tube according to the present invention, FIG. 2 is a front view thereof, and FIG. 3 is a view showing a state of liquid flow in the heat transfer tube of the embodiment. 1: Heat transfer tube, 2: Needle fin.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】密閉容器内に水平に配置され、外側に吸収
液が滴下され、内側に冷却水が流れる吸収器の伝熱管で
あって、外面にフィンが形成され、かつ伝熱管自体が液
の滴下方向に対して幅に広い楕円形ないし長円形断面を
有することを特徴とする吸収器用伝熱管。
Claim: What is claimed is: 1. A heat transfer tube of an absorber which is horizontally arranged in a closed container, in which an absorbing liquid is dripped on the outside, and cooling water flows on the inside, fins are formed on the outer surface, and the heat transferring tube itself is a liquid A heat transfer tube for an absorber, which has an elliptical or elliptical cross section that is wide in the direction of dripping.
JP14066587A 1987-06-04 1987-06-04 Heat transfer tube for absorber Expired - Fee Related JPH0723820B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14066587A JPH0723820B2 (en) 1987-06-04 1987-06-04 Heat transfer tube for absorber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14066587A JPH0723820B2 (en) 1987-06-04 1987-06-04 Heat transfer tube for absorber

Publications (2)

Publication Number Publication Date
JPS63306372A JPS63306372A (en) 1988-12-14
JPH0723820B2 true JPH0723820B2 (en) 1995-03-15

Family

ID=15273914

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14066587A Expired - Fee Related JPH0723820B2 (en) 1987-06-04 1987-06-04 Heat transfer tube for absorber

Country Status (1)

Country Link
JP (1) JPH0723820B2 (en)

Also Published As

Publication number Publication date
JPS63306372A (en) 1988-12-14

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