JPH05322375A - Film type heat transfer device - Google Patents

Film type heat transfer device

Info

Publication number
JPH05322375A
JPH05322375A JP8051791A JP8051791A JPH05322375A JP H05322375 A JPH05322375 A JP H05322375A JP 8051791 A JP8051791 A JP 8051791A JP 8051791 A JP8051791 A JP 8051791A JP H05322375 A JPH05322375 A JP H05322375A
Authority
JP
Japan
Prior art keywords
heat transfer
tube
heat exchanger
pipe
liquid
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
JP8051791A
Other languages
Japanese (ja)
Inventor
Osayuki Inoue
修行 井上
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP8051791A priority Critical patent/JPH05322375A/en
Publication of JPH05322375A publication Critical patent/JPH05322375A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a film type heat transfer device in which solution is not irregularly located even if a heat transfer unit is inclined. CONSTITUTION:A film type heat transfer device has a plurality of heat transfer tubes having straight tube parts and a liquid sprinkler 3 at an upper part of the tubes, and comprises a plurality of deflectors 4 between the upper and lower tubes. Each deflector 4 has a shape in which a width in contact with the upper tube is wide and a width in contact with the lower tube is smaller than a diameter of the tube.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、伝熱器に係り、特に上
部に液散布装置を有する液膜式伝熱器に関するものであ
る。そして、このような伝熱器は、吸収冷凍機の発生
器、吸収器、蒸発器などに採用されている。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat transfer device, and more particularly to a liquid film type heat transfer device having a liquid spraying device on the upper part thereof. And such a heat exchanger is adopted as a generator, an absorber, an evaporator, etc. of an absorption refrigerator.

【0002】[0002]

【従来の技術】吸収冷凍機が車用に利用される場合など
では、機器が傾斜した状態で使われることが多い。この
ような場合、従来からの通常の吸収冷凍機では、伝熱管
が直管方向に傾斜すると、散布された液は、伝熱器の一
方向に片寄り、所定の伝熱が期待できなくなる。
2. Description of the Related Art When an absorption refrigerating machine is used for a vehicle, the equipment is often used in a tilted state. In such a case, in the conventional ordinary absorption refrigerating machine, when the heat transfer pipe is inclined in the straight pipe direction, the sprayed liquid is biased in one direction of the heat transfer device, and the predetermined heat transfer cannot be expected.

【0003】[0003]

【発明が解決しようとする課題】本発明は、機器が傾斜
した場合でも、散布された液が一方向に片寄ることを防
止することのできる液膜式伝熱器とそれを用いた吸収冷
凍機を提供することを目的とする。
DISCLOSURE OF THE INVENTION The present invention provides a liquid film type heat transfer device capable of preventing the sprayed liquid from deviating in one direction even if the device is tilted, and an absorption refrigerator using the same. The purpose is to provide.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
には、本発明では、直管部を有する複数の伝熱管及びこ
の伝熱管の上部に液散布装置を持った液膜式伝熱器にお
いて、上下関係にある伝熱管と伝熱管との間に、邪魔板
を複数設け、該邪魔板の形状を上側の伝熱管に接する幅
は広くし、下側に接する幅は伝熱管の直径よりも小さく
したことを特徴とする液膜式伝熱器としたものである。
また、上記他の目的を達成するために、本発明では、発
生器、吸収器、蒸発器、凝縮器、溶液熱交換器を主要構
成機器とし、これらを溶液配管、冷媒配管で結んでサイ
クルを構成する吸収冷凍機において、これらに用いる伝
熱機器として前記の液膜式伝熱器を用いて構成した吸収
冷凍機としたものである。
In order to achieve the above object, according to the present invention, a plurality of heat transfer tubes having straight pipe portions and a liquid film type heat transfer device having a liquid spraying device above the heat transfer tubes. In the above, a plurality of baffle plates are provided between the heat transfer tubes which are in a vertical relationship, and the shape of the baffle plate is wide in contact with the upper heat transfer tube, and the width in contact with the lower side is larger than the diameter of the heat transfer tube. It is also a liquid film type heat exchanger characterized by being made smaller.
Further, in order to achieve the above-mentioned other objects, in the present invention, a generator, an absorber, an evaporator, a condenser, a solution heat exchanger as a main component equipment, these are connected by a solution pipe, a refrigerant pipe, a cycle. In the absorption chiller to be configured, the absorption chiller is configured by using the liquid film type heat exchanger as a heat transfer device used for them.

【0005】次に、本発明を詳細に説明する。本発明で
設ける邪魔板は、液の分布を良好に保つため、邪魔板の
うちの下の管に接する部分の幅を管の直径よりも小さ
く、好ましくは、直径の1/2以下にするのがよい。ま
た、邪魔板の数はなるべく多いのがよいが、少なくと
も、管の上下段数よりも多い数を2管の間に設けるのが
よい。邪魔板は、上下の管に接しても、また片一方ある
いは両方が管に接着されていても差し支えない。また管
と一体になっていてもよい。伝熱管は、液が、よく広が
るように、あるいは、伝熱をよくするように、ピン状の
フィン加工などを施したものであって、邪魔板とは、ピ
ンの部分で接するようになっていてもよい。
Next, the present invention will be described in detail. In the baffle plate provided in the present invention, in order to maintain a good liquid distribution, the width of the portion of the baffle plate which is in contact with the lower tube is smaller than the diameter of the tube, and preferably 1/2 or less of the diameter. Is good. The number of baffle plates is preferably as large as possible, but it is preferable that at least a larger number than the upper and lower stages of the tubes be provided between the two tubes. The baffles may be in contact with the upper and lower tubes, or one or both of them may be adhered to the tubes. It may also be integrated with the tube. The heat transfer tube is a pin-shaped fin processed to spread the liquid well or to improve the heat transfer, and the baffle plate is in contact with the pin at the pin portion. May be.

【0006】[0006]

【作用】本発明によれば、伝熱管の間に設けた邪魔板の
下の管に接する部分の幅を小さくしたことにより、上の
管で捕集された液は、下の管の頂上付近に供給され、伝
熱管の表面積を有効に使用することができる。直径より
も大きいと、伝熱管に供給されず、そのまま落下するこ
ともあり伝熱効率を悪くする。
According to the present invention, by reducing the width of the portion of the baffle plate provided between the heat transfer tubes and in contact with the lower tube, the liquid collected in the upper tube is near the top of the lower tube. The surface area of the heat transfer tube can be effectively used. If the diameter is larger than the diameter, it is not supplied to the heat transfer tube and may drop as it is, which deteriorates heat transfer efficiency.

【0007】[0007]

【実施例】以下、本発明を図面を用いて具体的に説明す
るが、本発明はこれらの実施例に限定されるものではな
い。 実施例1 図1に本発明の液膜式伝熱器の一例を示す。図1は正面
断面図であり、2は伝熱管、3は液散布管、4は邪魔板
を表し、伝熱管2の中には流体5が流れており、液散布
管3からの溶液7と熱交換している。図2に図1のA部
拡大図を示し、図3に図2の断面図を示す。このように
邪魔板4は、伝熱管2の上下の間に多数設けられてお
り、その構造は図3に記載のように台形をしており、長
辺が上の伝熱管に接して設けられ、短辺が下の伝熱管に
接して設けられている。
The present invention will be specifically described below with reference to the drawings, but the present invention is not limited to these embodiments. Example 1 FIG. 1 shows an example of the liquid film heat exchanger of the present invention. 1 is a front sectional view, 2 is a heat transfer tube, 3 is a liquid distribution tube, 4 is a baffle plate, a fluid 5 is flowing in the heat transfer tube 2, and a solution 7 from the liquid distribution tube 3 Heat exchange. FIG. 2 shows an enlarged view of part A of FIG. 1, and FIG. 3 shows a sectional view of FIG. As described above, a large number of baffle plates 4 are provided between the upper and lower sides of the heat transfer tube 2, and the structure thereof has a trapezoidal shape as shown in FIG. The short side is provided in contact with the lower heat transfer tube.

【0008】図4、図5に伝熱器が傾斜した場合の液の
流れを示す。図4は伝熱器が伝熱管の左右方向に傾斜し
た場合の液の流れを示し、これによると、液は邪魔板に
よってせき止められて下の伝熱管に流下している。ま
た、図5は、伝熱器が伝熱管の前後方向に傾斜した場合
の液の流れを示しており、液は邪魔板に沿って流れ、伝
熱管の全体に広がっている。また、この邪魔板は断面形
状を波形に加工してもよく、こうすることで横方向の傾
斜に際して、液の分散性を良くすることができる。管と
邪魔板とを別々に製作する場合は、邪魔板にスペーサを
いれて邪魔板どうしを横に連結することもできる。ま
た、邪魔板は、図6,図7に示されるような形状とする
こともできる。図6ではスペーサを兼ねて側板を設け、
横方向に飛ぶ液滴を捕集するようにしており、また、図
7は上下、左右に邪魔板をくっつけて、1枚の形にして
おり、管の長手方向に複数枚設ける。
FIGS. 4 and 5 show the flow of liquid when the heat transfer device is inclined. FIG. 4 shows the flow of the liquid when the heat transfer device is inclined in the left-right direction of the heat transfer pipe. According to this, the liquid is dammed by the baffle plate and flows down to the heat transfer pipe below. FIG. 5 shows the flow of the liquid when the heat transfer device is inclined in the front-back direction of the heat transfer pipe, and the liquid flows along the baffle plate and spreads over the entire heat transfer pipe. Further, this baffle plate may be processed into a corrugated cross-sectional shape, which makes it possible to improve the dispersibility of the liquid at the time of inclining in the lateral direction. When the tube and the baffle plate are manufactured separately, a spacer may be placed in the baffle plate to connect the baffle plates sideways. Further, the baffle plate may have a shape as shown in FIGS. In FIG. 6, a side plate is provided also as a spacer,
Droplets that fly in the lateral direction are collected, and in FIG. 7, baffle plates are attached to the top, bottom, left and right to form a single sheet, and a plurality of sheets are provided in the longitudinal direction of the tube.

【0009】実施例2 図8に、本発明の液膜式伝熱器を吸収冷凍機の発生器に
用いた例を示す。図8は、吸収冷凍機のフロー構成図で
あり、Gは発生器、Aは吸収器、Eは蒸発器、Cは凝縮
器、Hsは溶液熱交換器、Hcは冷媒熱交換器、20,21
はポンプ、管11〜14は溶液通路、管15〜19は冷
媒通路を示している。そして、発生器Gは、上部に溶液
散布管3を有し、伝熱管2とその間に設けられた邪魔板
4とで構成されている。この邪魔板は実施例1で示され
たものを用いた。この装置の冷房運転では、冷媒を吸収
した希溶液は、吸収器Aから管11を通り、ポンプ20
により溶液熱交換器Hsの被加熱側に送られ、熱交換によ
り加温された希溶液は管12を通り、発生器Gの上部の
散布管3より伝熱管2の上に散布される。伝熱管2には
温水5が通っており、伝熱管の外表面を流下する希溶液
を加熱し、冷媒蒸気を発生している。そして、伝熱管に
は上下に渡って邪魔板が設けられているため、発生器G
が傾斜した場合でも溶液は一方に片寄ることがなく伝熱
管全体を流下することができ伝熱効率がよくなってい
る。
Embodiment 2 FIG. 8 shows an example in which the liquid film type heat exchanger of the present invention is used as a generator of an absorption refrigerator. FIG. 8 is a flow configuration diagram of an absorption refrigerator, G is a generator, A is an absorber, E is an evaporator, C is a condenser, Hs is a solution heat exchanger, Hc is a refrigerant heat exchanger, 20, 21
Is a pump, pipes 11 to 14 are solution passages, and pipes 15 to 19 are refrigerant passages. The generator G has a solution spraying pipe 3 on the upper part thereof, and is composed of a heat transfer pipe 2 and a baffle plate 4 provided therebetween. As the baffle plate, the one shown in Example 1 was used. In the cooling operation of this device, the diluted solution that has absorbed the refrigerant passes from the absorber A through the pipe 11 and the pump 20.
The diluted solution, which is sent to the heated side of the solution heat exchanger Hs and heated by the heat exchange, passes through the pipe 12 and is sprayed onto the heat transfer pipe 2 from the spray pipe 3 above the generator G. Hot water 5 passes through the heat transfer tube 2 and heats the dilute solution flowing down the outer surface of the heat transfer tube to generate refrigerant vapor. Further, since the heat transfer tubes are provided with baffle plates vertically, the generator G
Even if is inclined, the solution does not shift to one side and can flow down the entire heat transfer tube, improving heat transfer efficiency.

【0010】冷媒蒸気を発生して濃縮した濃溶液は管1
3から熱交換器Hsの加熱側を通って管14から吸収器A
に導入され、再び冷媒を吸収して希溶液となって管11
から循環するサイクルをとる。一方発生器Gで発生した
冷媒蒸気は管15から凝縮器Cに導入され、凝縮され
て、管16から膨張弁22を通り蒸発器Eに導入され
る。蒸発器Eに導入された冷媒液は、ポンプ21により
管17から冷媒熱交換器Hcの被加熱側を通り、冷風から
熱を奪い加温されて管18から蒸発器Eに至り、冷媒熱
交換器での加温分だけ冷媒を蒸発して、残りは管17か
ら循環する。そして、冷媒蒸気は管19から吸収器Aに
導入されて溶液に吸収されて循環する。この例では、本
発明の液膜式伝熱器を発生器に用いているが、発生器以
外にも吸収器A、蒸発器Eにも使用することができる。
The concentrated solution produced by generating the refrigerant vapor is concentrated in the tube 1.
3 through the heating side of the heat exchanger Hs to pipe 14 to absorber A
Is introduced into the pipe 11 and absorbs the refrigerant again to form a dilute solution.
Take a cycle that circulates from. On the other hand, the refrigerant vapor generated in the generator G is introduced into the condenser C from the pipe 15, condensed, and introduced into the evaporator E from the pipe 16 through the expansion valve 22. The refrigerant liquid introduced into the evaporator E passes from the pipe 17 to the heated side of the refrigerant heat exchanger Hc by the pump 21, takes heat from the cold air and is heated to reach the evaporator E from the pipe 18, and the refrigerant heat exchange is performed. The refrigerant is evaporated by the amount of heating in the vessel, and the rest is circulated from the pipe 17. Then, the refrigerant vapor is introduced from the pipe 19 into the absorber A, absorbed in the solution, and circulated. In this example, the liquid film heat exchanger of the present invention is used for the generator, but it can be used for the absorber A and the evaporator E as well as the generator.

【0011】[0011]

【発明の効果】本発明によれば、伝熱管の間に邪魔板を
設け、この邪魔板の形状を下流側の幅を伝熱管の直径よ
り小さくしたために、伝熱器が左右、前後に傾斜して
も、伝熱管に沿って流れる液は、一方に片寄ることなく
全体に渡って流下し、伝熱効率がよくなった。
According to the present invention, since the baffle plate is provided between the heat transfer tubes and the width of the baffle plate is made smaller than the diameter of the heat transfer tube, the heat transfer device is inclined to the left, right, front and back. Even so, the liquid flowing along the heat transfer tube flowed down over the whole without being biased to one side, and the heat transfer efficiency was improved.

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

【図1】本発明の液膜式伝熱器の正面断面図である。FIG. 1 is a front sectional view of a liquid film type heat exchanger of the present invention.

【図2】図1のA部拡大図である。FIG. 2 is an enlarged view of part A in FIG.

【図3】図2の側断面図である。FIG. 3 is a side sectional view of FIG.

【図4】伝熱器が左右方向に傾斜した場合の液の流れの
説明図である。
FIG. 4 is an explanatory diagram of a liquid flow when the heat transfer device is inclined in the left-right direction.

【図5】伝熱器が前後方向に傾斜した場合の液の流れの
説明図である。
FIG. 5 is an explanatory diagram of a liquid flow when the heat exchanger is inclined in the front-rear direction.

【図6】本発明の一例を示す伝熱器の部分側断面図であ
る。
FIG. 6 is a partial side sectional view of a heat transfer device showing an example of the present invention.

【図7】本発明の一例を示す伝熱器の部分側断面図であ
る。
FIG. 7 is a partial side sectional view of a heat transfer device showing an example of the present invention.

【図8】吸収冷凍機のフロー構成図である。FIG. 8 is a flow configuration diagram of an absorption refrigerator.

【符号の説明】[Explanation of symbols]

1:伝熱器、2:伝熱管、3:液散布管、4:邪魔板、
9:側板、11〜14:溶液配管、15〜19:冷媒配
管、G:発生器、A:吸収器、C:凝縮器、E:蒸発
器、Hs:溶液熱交換器、Hc:冷媒熱交換器
1: Heat transfer device, 2: Heat transfer pipe, 3: Liquid distribution pipe, 4: Baffle plate,
9: Side plate, 11-14: Solution pipe, 15-19: Refrigerant pipe, G: Generator, A: Absorber, C: Condenser, E: Evaporator, Hs: Solution heat exchanger, Hc: Refrigerant heat exchange vessel

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成5年3月26日[Submission date] March 26, 1993

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】図面[Document name to be corrected] Drawing

【補正対象項目名】全図[Correction target item name] All drawings

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図1】 [Figure 1]

【図2】 [Fig. 2]

【図3】 [Figure 3]

【図4】 [Figure 4]

【図5】 [Figure 5]

【図6】 [Figure 6]

【図7】 [Figure 7]

【図8】 [Figure 8]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 直管部を有する複数の伝熱管及びこの伝
熱管の上部に液散布装置を持った液膜式伝熱器におい
て、上下関係にある伝熱管と伝熱管との間に、邪魔板を
複数設け、該邪魔板の形状を上側の伝熱管に接する幅は
広くし、下側に接する幅は伝熱管の直径よりも小さくし
たことを特徴とする液膜式伝熱器。
1. In a liquid film type heat exchanger having a plurality of heat transfer tubes having a straight pipe section and a liquid spraying device above the heat transfer tubes, there is a hindrance between the heat transfer tubes which are vertically arranged. A liquid film heat exchanger characterized in that a plurality of plates are provided, and a shape of the baffle plate has a wide width in contact with the upper heat transfer tube and a width in contact with the lower side is smaller than a diameter of the heat transfer tube.
【請求項2】 前記伝熱管は、表面にピン状のフィンを
有していることを特徴とする請求項1記載の液膜式伝熱
器。
2. The liquid film heat exchanger according to claim 1, wherein the heat transfer tube has pin-shaped fins on its surface.
【請求項3】 発生器、吸収器、蒸発器、凝縮器、溶液
熱交換器を主要構成機器とし、これらを溶液配管、冷媒
配管で結んでサイクルを構成する吸収冷凍機において、
伝熱機器として請求項1記載の液膜式伝熱器を用いたこ
とを特徴とする吸収冷凍機。
3. An absorption refrigerator in which a generator, an absorber, an evaporator, a condenser, and a solution heat exchanger are main components, and these are connected by a solution pipe and a refrigerant pipe to form a cycle,
An absorption refrigerator comprising the liquid film heat exchanger according to claim 1 as a heat transfer device.
JP8051791A 1991-03-20 1991-03-20 Film type heat transfer device Pending JPH05322375A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8051791A JPH05322375A (en) 1991-03-20 1991-03-20 Film type heat transfer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8051791A JPH05322375A (en) 1991-03-20 1991-03-20 Film type heat transfer device

Publications (1)

Publication Number Publication Date
JPH05322375A true JPH05322375A (en) 1993-12-07

Family

ID=13720506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8051791A Pending JPH05322375A (en) 1991-03-20 1991-03-20 Film type heat transfer device

Country Status (1)

Country Link
JP (1) JPH05322375A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998043027A1 (en) * 1997-03-25 1998-10-01 Sanyo Electric Co., Ltd. Absorber of absorption system refrigerator
JP2007532855A (en) * 2004-04-09 2007-11-15 エイアイエル リサーチ インク Thermal mass exchange machine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998043027A1 (en) * 1997-03-25 1998-10-01 Sanyo Electric Co., Ltd. Absorber of absorption system refrigerator
US6192704B1 (en) 1997-03-25 2001-02-27 Sanyo Electric Co., Ltd. Absorber of absorption system refrigerator
JP2007532855A (en) * 2004-04-09 2007-11-15 エイアイエル リサーチ インク Thermal mass exchange machine

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