JPS60111859A - Heat transfer pipe for absorption refrigerator - Google Patents

Heat transfer pipe for absorption refrigerator

Info

Publication number
JPS60111859A
JPS60111859A JP21761983A JP21761983A JPS60111859A JP S60111859 A JPS60111859 A JP S60111859A JP 21761983 A JP21761983 A JP 21761983A JP 21761983 A JP21761983 A JP 21761983A JP S60111859 A JPS60111859 A JP S60111859A
Authority
JP
Japan
Prior art keywords
tube
heat transfer
liquid
heat exchanger
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.)
Granted
Application number
JP21761983A
Other languages
Japanese (ja)
Other versions
JPH059707B2 (en
Inventor
佐藤 巧行
礒崎 昭夫
江崎 秀司
宮城 龍雄
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.)
Tokyo Sanyo Electric Co Ltd
Kobe Steel Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Kobe Steel Ltd
Sanyo Electric Co Ltd
Sanyo Denki Co 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 Tokyo Sanyo Electric Co Ltd, Kobe Steel Ltd, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP21761983A priority Critical patent/JPS60111859A/en
Publication of JPS60111859A publication Critical patent/JPS60111859A/en
Publication of JPH059707B2 publication Critical patent/JPH059707B2/ja
Granted legal-status Critical Current

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は吸収冷温水機及び吸収ヒートポンプなどの(火
器用となる液滴滴下方式又はスプレー方式の燕発器、吸
収器、光牛器その他の熱交換器に用いられる伝熱管に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is applicable to absorption chiller-heating machines, absorption heat pumps, etc. (droplet type or spray type swallow generators, absorbers, light pumps, and other heat exchangers for firearms). This relates to heat exchanger tubes.

一般に、伝熱管を横に配した液滴滴下方式又はスプレー
方式の吸収冷温水機及び吸収ヒートポンプなどの蒸発器
、吸収器並びに発生器において、この伝熱管に液を分散
させて液滴滴下又は散布し、該伝熱管上に液膜を均一に
形成させることは、それら熱交換器の伝熱性能を保持す
る上に不可欠なことである。
In general, in evaporators, absorbers, and generators such as absorption chiller-heating machines and absorption heat pumps that use droplet-dropping or spray-type absorption heat pumps that have heat transfer tubes placed next to them, liquid is dispersed in the heat transfer tubes and then dripped or sprayed. However, it is essential to uniformly form a liquid film on the heat exchanger tubes in order to maintain the heat transfer performance of these heat exchangers.

従来、この液を均一に分散さ1士るために、例えば液滴
の滴下装置くI−レー)に各種工夫がなされ伝熱管の管
群の上段部にあっては均一な液膜形成がなされている。
Conventionally, in order to disperse this liquid uniformly, various improvements have been made to the droplet dropping device (I-ray), for example, to form a uniform liquid film on the upper part of the tube group of heat transfer tubes. ing.

しかし、下段に向うにしたがって冷媒の場合は蒸発によ
る液滴滴下流量が減少し、更には液の物性あるいは滴下
速度などの影響によって管軸方向への液の分散が充分に
行なわれず、液の分布に偏りが生ずるものである(第3
図において、無模様部分参照)。
However, as the refrigerant moves toward the bottom, the droplet flow rate decreases due to evaporation, and furthermore, due to the influence of the physical properties of the liquid or the dropping speed, the liquid is not sufficiently dispersed in the tube axis direction, resulting in liquid distribution. (Third point)
(See the non-patterned area in the figure).

従って、液の分布が不十分となると伝熱管上に液が触れ
ない部分く乾いた部分)が生じ、伝熱管の伝熱性111
8が低下する欠点を有している。
Therefore, if the distribution of the liquid is insufficient, there will be dry areas (where the liquid does not touch) on the heat exchanger tube, and the heat transfer properties of the heat exchanger tube will decrease.
8 has the disadvantage of decreasing.

本発明は」−記実情に鑑み、液の偏りを防ぎ、伝熱管の
上段から下段までほぼ均一に液を分布させ、液膜を均一
に形成ざぜることを目的とした伝熱管を提供するしので
ある。
The present invention has been made in view of the above-mentioned circumstances, and provides a heat exchanger tube whose purpose is to prevent the liquid from being unevenly distributed, distribute the liquid almost uniformly from the upper stage to the lower stage of the heat exchanger tube, and form a liquid film uniformly. It is.

即ち、本発明は1云熱管自体の形状を3角形。That is, in the present invention, the shape of the heat tube itself is triangular.

5角形、7角形等の奇数角をもつ多角形状とし、該包の
表面にローフイン加工あるいはその他の特殊加工を施し
、11つ該管の多角形の一辺を上面に位置づるよう設置
する4i^成どしている。このよう<r伝熱管を液滴滴
下装置の下方に適宜本数配設ηれば、該管の」二面の一
辺には滴下された液滴の軸方向への拡がりが従来の円管
よりも大ぎくとることができ、伝熱管上に均一な液膜を
形成しやすい効果をもたばている。また、伝熱管の多角
形を奇数角どしたことににっで、−辺を上面どづれば真
下情買に必ず一角(尖部)が来るものどなり、次段の伝
熱管への液滴の滴下を(イ「実にするものである。
A polygonal shape with an odd number of angles such as a pentagon or a heptagon, and the surface of the package is processed with a loaf-in process or other special process, and the 11 tubes are installed so that one side of the polygon is positioned on the top surface. What's wrong? By arranging an appropriate number of heat transfer tubes below the droplet dripping device in this way, the droplet spreads in the axial direction on one side of the two surfaces of the tube more than in a conventional circular tube. It has the effect of easily forming a uniform liquid film on the heat transfer tube. Also, because the polygon of the heat transfer tube has an odd number of angles, if the - side is placed on the top side, one corner (apex) will always be located directly below the tube. (a) It is something that brings to fruition.

以下、本発明を実施例の図面に基づ゛いて説明すれ(:
11次の通りである。
The present invention will be explained below based on the drawings of the embodiments (:
The 11th order is as follows.

第1図、第2図は伝熱管を5角形4fa成どしたもので
ある。1は管形状を5角形とした伝熱管本体で、該伝熱
管本体1の表面にローフイン加工を6って形成したフィ
ン部2を全域に配し多角形状の伝熱管3としたものであ
る。
Figures 1 and 2 show the heat exchanger tubes having a pentagonal shape of 4fa. 1 is a heat exchanger tube body having a pentagonal tube shape, and fin portions 2 formed by loaf-in processing on the surface of the heat exchanger tube body 1 are arranged over the entire area to form a polygonal heat exchanger tube 3.

いよこの作用を説明すると、先ず吸収冷凍機の伝熱管と
して使用するに際し、適宜本数の伝熱管3を第2図に示
づ如く一定間隔(をもって多段に配列し、この最上位置
の伝熱管3の真上部に、吸収器、蒸発器及び発生器(図
示せず)への液ン9人用配管4と液滴散布用となる1−
レー5を設置するものである。この場合、各段の伝熱管
3は平坦部3aどなる一辺を上面とし一角となる尖部3
bを下面として配し、最上位置の伝熱管3の平坦部3a
の真−にに散布用トレー5に設けだ液滴散布用小穴6を
臨まけてなる。即ち、多段どなる伝熱管3群は、多角形
の一角となる尖部3bの真下位置に下段の一辺となる平
坦部3aが配されるl!Iff成となる。
To explain the function of heat exchanger tubes, first, when used as heat exchanger tubes in an absorption refrigerator, an appropriate number of heat exchanger tubes 3 are arranged in multiple stages at regular intervals as shown in FIG. Immediately above there are pipes 4 for 9 liquids to the absorber, evaporator and generator (not shown) and 1- for liquid droplet dispersion.
This is where the relay 5 is installed. In this case, the heat exchanger tubes 3 at each stage have one side that is the flat part 3a as the upper surface, and the peak part 3 that forms one corner.
flat part 3a of the heat exchanger tube 3 in the uppermost position, with b as the lower surface
A small hole 6 for dispersing liquid droplets provided in the dispersing tray 5 is facing directly in the middle. That is, in the 3 groups of multi-stage heat exchanger tubes, the flat part 3a, which is one side of the lower stage, is arranged directly below the peak part 3b, which is one corner of the polygon. If is completed.

ここにおいて、液滴滴下装置となる1−レー5の液滴散
布用小穴6より滴下する吸収液あるいは冷媒の液aは、
伝熱管3の平+n部3aへ滴下するものとなるが、この
液滴の滴下面が平らであることから、従来の丸型伝熱管
に比べて管軸方向への液の広がりが大ぎく、伝熱管3を
均一に濡らず−しのどイ乍る。即ち、伝熱管3を多段に
配した管群は、従来の丸型伝熱管3′では管軸方向への
液の広がりが小さいため、液の物性あるいは蒸発による
滴下速度の減少等と相俟って滴下間隔が小さく、管軸方
向への液の分布が均一でなくなり、伝熱管」二に液が触
れない部分が生じ、伝熱性能の悪化がみられる(第3図
の無模様部分参照)。まlζ、この様な液膜の均一化が
計れない理由として、滴下流mににつでは液滴落下のI
iu性力に、につて第4図に示J如きに次段の管の真上
に滴下し4yい現象)〕(生ずる。
Here, the absorption liquid or refrigerant liquid a dripping from the droplet dispersion small holes 6 of the 1-ray 5, which is the droplet dropping device, is
The liquid drops onto the flat+n portion 3a of the heat exchanger tube 3, but since the dropping surface of the droplet is flat, the liquid spreads much more in the tube axis direction than in conventional round heat exchanger tubes. The heat exchanger tubes 3 are not evenly wetted. In other words, in a tube group in which heat transfer tubes 3 are arranged in multiple stages, since the spread of the liquid in the tube axis direction is small in the conventional round heat transfer tubes 3', this is combined with a decrease in the dropping rate due to the physical properties of the liquid or evaporation. As a result, the intervals between drops are small, and the distribution of the liquid in the tube axis direction is not uniform, resulting in parts of the heat transfer tube where the liquid does not touch, resulting in a deterioration of heat transfer performance (see the non-patterned area in Figure 3). . However, the reason why such a uniform liquid film cannot be measured is that the I of the droplet falls in the droplet stream m.
Due to the physical force, the liquid drops directly above the next stage pipe as shown in Fig. 4 (4y phenomenon)].

この点、本発明の伝熱管3は前1本したように管軸方向
への液の広がりの効果をもたけており、滴下間l1Ii
lρが大す・<なってもその広がりの大きざにJ:って
管を均一に月つ薄く濡らずことが可能となる(第2図に
あって、模様部分参照)。
In this respect, the heat exchanger tube 3 of the present invention has the effect of spreading the liquid in the tube axis direction like the previous one, and the dropping interval l1Ii
Even if lρ becomes large, it becomes possible to wet the tube evenly and thinly due to the size of its spread (see the pattern in Figure 2).

また、多角形管形状でその尖部3bを下方ぎにl!Ii
!’I−ることかう、伝熱管下端にa′3(プる液滴の
慣性力の方向が、円管の水平方向に比べて垂直一方向に
近いことがら液滴の分散(液滴の飛び敗り)をi成牛さ
せることも兼ねる。
Also, it has a polygonal tube shape with its apex 3b pointing downward! Ii
! The fact that the direction of the inertial force of the droplet is closer to the vertical direction than the horizontal direction of the tube is that the dispersion of the droplet (the flying of the droplet) It also serves as a way to make the defeated cow become an adult.

上述の様に、本発明の吸収冷凍機用伝熱管は、管外表面
をローフイン加工あるいはその他の特殊加工を施Jと」
ξに、管白体を奇数角の多角形とした構成としたことに
より、冷媒及び吸収液の滴下状態を丸型の伝熱管に比べ
良好な滴下el能及び濡れ旧市を1qるものである。従
って、蒸発器の伝熱性能及び吸収器の吸収性能と伝熱性
能が向上し、月つ装置のコンパクト化及びそれに伴う装
置のコストダウン化が計れる効果を秦する。
As mentioned above, the heat exchanger tube for an absorption refrigerator of the present invention has the outer surface of the tube subjected to a loaf-in process or other special process.
By configuring the tube white body to be a polygon with odd angles in ξ, the dripping state of the refrigerant and absorption liquid is improved by 1q compared to a round heat transfer tube. . Therefore, the heat transfer performance of the evaporator and the absorption performance and heat transfer performance of the absorber are improved, thereby achieving the effect of making the device more compact and reducing the cost of the device accordingly.

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

図面は本発明の実施例を示ずもので、第1図は伝熱性・
の側面図、第2図は使用状態の側面図、第3図は円管と
なる従来型の使用状態の側面図、第4図は同円管の滴下
状態の説明図である。 1・・・伝熱管本体、2・・・フィン部、3・・・伝熱
管、3a・・・平坦部、3b・・・尖部。 特許出願人 株式金相 神戸製鋼所 面 三洋電(幾株式会ネl 同 東京三洋電機株式会社 代 理 人 尾 股 行 k、1[ 同 荒 木 友之助 第2図 第3図 第4図
The drawings do not show the embodiments of the present invention, and FIG.
2 is a side view of the conventional type in use, FIG. 3 is a side view of the conventional circular tube in use, and FIG. 4 is an explanatory view of the same circular tube in a dripping state. DESCRIPTION OF SYMBOLS 1... Heat exchanger tube main body, 2... Fin part, 3... Heat exchanger tube, 3a... Flat part, 3b... Apex part. Patent Applicant: Kobe Steel, Ltd., Sanyo Electric Co., Ltd. Tokyo Sanyo Electric Co., Ltd. Agent: Omata Yuki K, 1

Claims (1)

【特許請求の範囲】 1、伝熱管の管外に吸収液あるいは冷媒を滴下又は散布
し、該管外表面に吸収液あるいは冷媒の液膜を形成し、
その液膜を通して熱移動を行なわしめる吸収冷凍(幾の
伝熱管において、管外表面にローフイン加工あるいはそ
の他の特殊加工をもってフィン部を配し、月つ伝熱管自
体を多角形の形状としたことを特徴とJる吸収冷凍機用
伝熱色。 2、伝熱管の多角形が、3角形、5角形、7角形等の奇
数角形である特許請求の範囲第1項記載の吸収冷凍機用
伝熱色・。
[Claims] 1. Dropping or scattering an absorption liquid or refrigerant outside the heat transfer tube to form a liquid film of the absorption liquid or refrigerant on the outside surface of the tube,
Absorption refrigeration, in which heat transfers through the liquid film 2. Heat transfer for an absorption refrigerator according to claim 1, wherein the polygon of the heat transfer tube is an odd polygon such as a triangle, a pentagon, or a heptagon. color·.
JP21761983A 1983-11-18 1983-11-18 Heat transfer pipe for absorption refrigerator Granted JPS60111859A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21761983A JPS60111859A (en) 1983-11-18 1983-11-18 Heat transfer pipe for absorption refrigerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21761983A JPS60111859A (en) 1983-11-18 1983-11-18 Heat transfer pipe for absorption refrigerator

Publications (2)

Publication Number Publication Date
JPS60111859A true JPS60111859A (en) 1985-06-18
JPH059707B2 JPH059707B2 (en) 1993-02-05

Family

ID=16707126

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21761983A Granted JPS60111859A (en) 1983-11-18 1983-11-18 Heat transfer pipe for absorption refrigerator

Country Status (1)

Country Link
JP (1) JPS60111859A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS636364A (en) * 1986-06-25 1988-01-12 東京瓦斯株式会社 Heat transfer tube for absorber

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5217414B2 (en) * 2007-12-21 2013-06-19 東京電力株式会社 Evaporator

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS47394U (en) * 1971-01-26 1972-08-01
JPS5565893A (en) * 1978-11-06 1980-05-17 Akzo Nv Heat transmitter using hollow filaments
JPS55153553U (en) * 1979-04-23 1980-11-05

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS47394U (en) * 1971-01-26 1972-08-01
JPS5565893A (en) * 1978-11-06 1980-05-17 Akzo Nv Heat transmitter using hollow filaments
JPS55153553U (en) * 1979-04-23 1980-11-05

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS636364A (en) * 1986-06-25 1988-01-12 東京瓦斯株式会社 Heat transfer tube for absorber

Also Published As

Publication number Publication date
JPH059707B2 (en) 1993-02-05

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