JPS5946466A - Liquid disperser - Google Patents

Liquid disperser

Info

Publication number
JPS5946466A
JPS5946466A JP15788982A JP15788982A JPS5946466A JP S5946466 A JPS5946466 A JP S5946466A JP 15788982 A JP15788982 A JP 15788982A JP 15788982 A JP15788982 A JP 15788982A JP S5946466 A JPS5946466 A JP S5946466A
Authority
JP
Japan
Prior art keywords
liquid
distribution device
heat exchanger
liquid distribution
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.)
Pending
Application number
JP15788982A
Other languages
Japanese (ja)
Inventor
益征 橋本
敏男 中山
真下 克之
健 金井
増田 照夫
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
Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co 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, Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP15788982A priority Critical patent/JPS5946466A/en
Publication of JPS5946466A publication Critical patent/JPS5946466A/en
Pending legal-status Critical Current

Links

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】 (イ)発明の分野 本発明は吸収冷凍機や吸収ヒートポンプ、吸収冷温水機
などの吸収冷熱器に使用される吸収液および/または冷
媒液(以下冷熱液という)を機内の熱交換器上に均等に
分散するための液分散装置に関する。
Detailed Description of the Invention (a) Field of the Invention The present invention relates to an absorption liquid and/or a refrigerant liquid (hereinafter referred to as a cooling liquid) used in an absorption chiller such as an absorption chiller, an absorption heat pump, or an absorption chiller/heater. This invention relates to a liquid dispersion device for uniformly dispersing liquid on an in-machine heat exchanger.

(ロ)従来技術 吸収冷熱機の液分散装置にはポンプにより生じる液圧を
利用したスプレ一式のものと重力による自然落下のもの
どがあり、後者には、第1図乃至第3図に示″′1−よ
うにザイホン式(特公昭43−18501)、フィンチ
ー−ブ式(特公昭7+8−33665)、エプロン式(
4′、′[公明52−243925)などの方式がある
(b) Conventional technology There are two types of liquid dispersion devices for absorption chillers: one is a spray set that uses liquid pressure generated by a pump, and the other is a spray device that uses gravity to naturally fall. ``'1-like the Zaihon type (Special Publication No. 43-18501), Finchieve type (Special Publication No. 7+8-33665), Apron type (Special Publication No. 7+8-33665)
There are methods such as 4',' [Kobei No. 52-243925].

(ハ)従来技術の問題点 しかし、スプレ一式のものはポンプ動力が必要とされる
ため、機器が余分に必要となって小型の吸収冷熱機には
不向きなものであり、後者の方式においても、最上方に
ある第1の冷熱液分配装置(1)によって液分配の性能
が実質的に決ってしまう欠点を有していた。すなわち、
ザイホン式(第1図)、フィンテー−ブ式(第2図)、
エプロン式(第3図)のいずれの液分散装置においても
、第1の液分配装置(1)から偏った液の流下が行なわ
れると、下方の熱交換装置(2)では、この偏りを是正
する機能は殆ど有していなかった。
(c) Problems with the conventional technology However, since the spray set requires pump power, extra equipment is required, making it unsuitable for small-sized absorption chillers. However, the liquid distribution performance was substantially determined by the first cold/hot liquid distribution device (1) located at the top. That is,
Zaihon type (Figure 1), Fin tab type (Figure 2),
In any apron type (Figure 3) liquid dispersion device, if the liquid flows down from the first liquid distribution device (1) in a biased manner, the lower heat exchange device (2) corrects this bias. It had almost no functionality.

特にサイホン(3)の場合には個々のサイホンな均−に
形成することはbくめてφ1Fかしく、エプロン(4)
の場合には該エプロン部の傾斜の影メ;・7を強く受け
る欠点、又、フィン(5)の場合には、第1の液分配装
置(1)からの液の流下の偏りがそのまま下方島液分散
となって吸収器や蒸発器を4?・“I成する熱交換器(
6)(7)上に伝わイ)傾向の強いものであった。
Especially in the case of siphon (3), it is important to form each siphon uniformly, and the apron (4)
In the case of the fin (5), the influence of the inclination of the apron part is strongly affected by the influence of Island liquid dispersion and absorber and evaporator 4?・“I heat exchanger (
6) (7) It was transmitted a) with a strong tendency.

に)発明の目的 このような点に鑑みなされた本発明は、吸収冷熱(式の
吸収器や蒸発器などのよつ1(熱交換器の管内の液体と
8(交1突器に散布される液体とを熱交換させる場合に
、咳熱へ一1ニジ暑°;の伝φ・j〜管を充分にR3ら
1−に必決な液−Fll、を糾持しながら液部下の均一
化をはかることを目的としたものである。
Purpose of the Invention The present invention was made in view of the above points. When exchanging heat with a liquid, it is necessary to thoroughly hold the essential liquid -Fll from R3 to 1- through the pipe φ・j~, which transfers heat to cough fever, and to ensure uniformity under the liquid. The purpose is to increase the

(ホ)発明の要点 このような目的を連成1ろために本発明はれ゛1シ交t
1器の上部に第1の液分配装置を設け、かつ、この液分
配装置の下方における熱交換器の上部又は中間部に針状
フィンを有する帯利を芯利に巻回した第2の液分配装置
を配設したものであり、以下に図7G]に従い本発明の
説ツ1なする。
(E) Key Points of the Invention In order to combine these objects, the present invention combines two parts.
A first liquid distribution device is provided in the upper part of the first liquid distribution device, and a second liquid is prepared by winding a belt having needle-shaped fins around the core in the upper or middle part of the heat exchanger below the liquid distribution device. A dispensing device is disposed therein, and part 1 of the present invention will be described below in accordance with FIG. 7G].

(へ)発明の実施例 第4図において、(8)は加熱装置(9)を有し、冷媒
を吸収して冷媒濃度の増した吸収液(以下濃液という)
を加熱沸騰させることにより吸収液から冷媒をガス化し
て分離するようにした再生器、(10)は再生器(8)
から流入する冷媒ガスを冷却液化する凝縮器、旧)はブ
ライン熱交換器(7)を有し、凝縮器(10)で液化さ
れた冷媒を低圧条件下で気化させることにより熱交換器
(力中のプラインの熱を気化潜熱として機内にとり込む
ようにした蒸発器、(1湯は蒸発器01)で気化した冷
媒を吸収させ、蒸発器Ql)における冷媒の気化機能が
維持できるようにした吸収器であり、蒸発器(11)及
び吸収器θ2)には夫々、冷媒液及び吸収液を熱交換器
(力(6)上に散布するための液分散装置(1,1+0
4)を有しており、吸収器(12)において冷媒を吸収
した濃液は再生器(8)に還流されて再び冷媒分離が行
1よりれる。
(f) Embodiment of the invention In FIG. 4, (8) has a heating device (9), and absorbs a refrigerant to increase the refrigerant concentration (hereinafter referred to as concentrated liquid).
A regenerator (10) is a regenerator (8) that gasifies and separates the refrigerant from the absorption liquid by heating and boiling the refrigerant.
The condenser (formerly) has a brine heat exchanger (7) that cools and liquefies the refrigerant gas flowing in from the condenser (10), and vaporizes the refrigerant liquefied in the condenser (10) under low pressure conditions. The evaporator is designed to take the heat of the internal prine into the machine as latent heat of vaporization, and the vaporized refrigerant is absorbed in the evaporator 01 (1 hot water is evaporator 01), so that the refrigerant vaporization function in the evaporator Ql) can be maintained. The evaporator (11) and absorber θ2) each have a liquid dispersion device (1,1+0
4), and the concentrated liquid that has absorbed the refrigerant in the absorber (12) is refluxed to the regenerator (8), where the refrigerant is separated again through line 1.

斯る構成において、蒸発器の熱交換器(7区流れる液体
は冷却され、吸収器の熱交換器(6)に流れる液体は加
熱されるため、蒸発器(7)側で冷却温度を調節して負
荷に接続するときは吸収冷凍機、吸収器(6)側で加熱
される液体温度を調節して負荷に接続するときは吸収加
熱機として利用できるものである。
In such a configuration, the liquid flowing through the evaporator heat exchanger (section 7) is cooled, and the liquid flowing into the absorber heat exchanger (6) is heated, so the cooling temperature is adjusted on the evaporator (7) side. It can be used as an absorption refrigerator when connected to a load, and as an absorption heater when connected to a load by adjusting the temperature of the liquid heated on the absorber (6) side.

而して、これらの蒸発器(II)及び吸収器02)に使
用される液分散装置は、第5図及び第6図に示すように
、熱交換器の伝熱管(15)の上部に第1の液分配装f
ft、(16)と第2の液分配装置(17)との二つの
液分配装置を設け、第1の液分配装置(16)で大略の
分散が行なわれた冷媒(又は吸収)液を第2の液分配装
置a力で再分散し、熱交換器の伝熱管(19の表面に均
一な液流下を行なわせるようにしたものである。
As shown in FIGS. 5 and 6, the liquid dispersion device used in these evaporators (II) and absorbers 02) is equipped with a tube located above the heat exchanger tube (15) of the heat exchanger. 1 liquid distribution system f
ft, (16) and a second liquid distribution device (17) are provided, and the refrigerant (or absorption) liquid that has been roughly dispersed in the first liquid distribution device (16) is transferred to the first liquid distribution device (16) and a second liquid distribution device (17). The liquid is redispersed by the force of the liquid distribution device 2, and the liquid is made to flow uniformly down the surface of the heat exchanger tube (19) of the heat exchanger.

すなわち、第1の液分散装置間は、第2の分散装置(1
7)上の全体にわたって適当な間隔でおおまかに分けて
液を流下させる構造ならサイホン式、エプロン式、その
他特別な形式を要求しない。
That is, between the first liquid dispersion device, the second dispersion device (1
7) A siphon type, apron type, or other special type is not required as long as the structure allows the liquid to flow down roughly at appropriate intervals over the entire area.

一方、第2の液分散装置0ηは第7図に一例を示すよう
に、約01’rnm厚、1mm巾のアルミニウムの帯材
の両側から7乃至10mm毎に切り込みを入て切り起し
、このようにしてできた針状フィン(18)を有′1−
る帯材(1旬を芯材(20)に巻回した構成を有するも
のであり、伝熱管(+5)に沿って配設されている。
On the other hand, as an example of the second liquid dispersion device 0η is shown in FIG. The needle-like fin (18) made in this way is
The core material (20) has a structure in which a strip material (one piece) is wound around a core material (20), and is arranged along the heat exchanger tube (+5).

尚、針状フィン(18)の形成は、必ずしも、第7図の
構成に駆足されろものではなく、帯材(l動に別体のフ
ィンを多数本植設したものを芯材(20)に巻回しても
良い。
It should be noted that the formation of the needle-like fins (18) is not necessarily driven by the configuration shown in FIG. ).

(ト)発明の効果 このような第1と第2の液分配装置を組み合わせて構成
された本発明の液分散装置は、第1の液分配装置によっ
て全面にわたって大略の滴下が行なわれた液が、第2の
分配装置のフィンとの衝突、分流、液の表面張力の働き
などによって芯利の軸方向に広がり、巻回されたフィン
群毎に液滴として懸垂滴下されろ。
(G) Effects of the Invention The liquid dispersing device of the present invention, which is constructed by combining the first and second liquid distributing devices as described above, is capable of dispersing liquid that has been roughly dropped over the entire surface by the first liquid distributing device. The liquid spreads in the axial direction of the core due to collision with the fins of the second distribution device, branching, and the action of surface tension of the liquid, and is suspended as droplets from each group of wound fins.

而して、第2の液分配装置は、第5図乃至第7図に示し
たように帯材を巻回して生じるピッチ毎のフィン群に分
散されて液滴下が行なわれるので、第2分配装置から熱
交換器の伝熱管に滴下する位置の数は、液量にも依るが
、第1分配装置の数倍の数に増えて熱交換器の伝熱管に
滴下させることができイ)。
As shown in FIGS. 5 to 7, the second liquid dispensing device performs droplet dispersion by distributing the liquid to the fin groups at each pitch created by winding the strip material. Although the number of locations at which liquid is dripped from the device to the heat exchanger tubes of the heat exchanger depends on the amount of liquid, it is possible to increase the number of locations several times that of the first distribution device and allow the liquid to be dripped into the heat exchanger tubes of the heat exchanger (b).

又、本発明の液分散装置は、従来の液分敗北[1りと違
って液の滴下位傷゛が増えるように針状フィンの紐状材
が機能するので、多量の液量に対しても滴下液流となっ
て伝熱管表面を語らす一方、紀1分配装置から滴下する
液量に偏りがあったり、或いは、液分散装置・\供給さ
れる液量が少ないときでも、局部的な液滴下の偏在を解
消し、伝熱管の表面を充分に語らすことができろもので
ある。
In addition, the liquid dispersion device of the present invention has a needle-like fin string material that functions to increase damage caused by liquid dripping, unlike the conventional liquid dispersion device. However, if the amount of liquid dripping from the distribution device is uneven, or even when the amount of liquid supplied by the liquid dispersion device is small, local It is possible to eliminate the uneven distribution of droplets and make the surface of the heat exchanger tube fully visible.

更に又、本発明の液分散装置は、吸収冷媒剤として水よ
りも表面張力が小さくかつ比重が大ぎい液、例えば、2
,2.2−トリフルオロ−1−エタノールやN−ブチル
−2−ピロリドン等有機系の冷媒液や吸収液を用いろ場
合において特に効果の太きいものである。
Furthermore, the liquid dispersion device of the present invention uses a liquid having a lower surface tension and a higher specific gravity than water, such as 2
, 2.2-Trifluoro-1-ethanol, N-butyl-2-pyrrolidone, and other organic refrigerant liquids and absorption liquids are particularly effective.

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

成を示す模式図、第5図は本発明による液分散装置の基
本構造を示j横断説明図、第6図は同じくその部分側面
図、第7図は第2の液分配装置の構造の一例を示す斜視
図。 6.7〜熱交換器、  11〜蒸発器、  12〜吸収
器、  16〜第1の液分配装置、  17〜第2の液
分配装置、  18〜針状フイン、  19〜帯拐
5 is a cross-sectional explanatory diagram showing the basic structure of the liquid dispersion device according to the present invention, FIG. 6 is a partial side view thereof, and FIG. 7 is an example of the structure of the second liquid distribution device. FIG. 6.7~heat exchanger, 11~evaporator, 12~absorber, 16~first liquid distribution device, 17~second liquid distribution device, 18~needle fin, 19~band strip

Claims (1)

【特許請求の範囲】[Claims] (1)吸収液および相変化する冷媒の循環サイクルを用
いて熱媒体の冷却や加熱を行なう吸収冷熱機において、
この冷熱機内で液を散布する装置は、吸収器および/ま
たは蒸発器を構成する熱交換器の上部に第1の液分配装
置を有し、かつ、該第1の液分配装置の下方に位置する
前記熱交換器の上部又は中間部に、針状フィンを放射状
に有する帯材を芯材に巻回した第2の液分配装置を配設
したことを特徴とする液分配装置。
(1) In an absorption chiller that cools or heats a heat medium using a circulation cycle of an absorption liquid and a phase-changing refrigerant,
This device for dispersing liquid in a chiller has a first liquid distribution device above a heat exchanger constituting an absorber and/or an evaporator, and is located below the first liquid distribution device. A liquid distribution device characterized in that a second liquid distribution device is disposed in an upper or intermediate portion of the heat exchanger, the second liquid distribution device having a core material wound around a band material having radial needle-like fins.
JP15788982A 1982-09-09 1982-09-09 Liquid disperser Pending JPS5946466A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15788982A JPS5946466A (en) 1982-09-09 1982-09-09 Liquid disperser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15788982A JPS5946466A (en) 1982-09-09 1982-09-09 Liquid disperser

Publications (1)

Publication Number Publication Date
JPS5946466A true JPS5946466A (en) 1984-03-15

Family

ID=15659626

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15788982A Pending JPS5946466A (en) 1982-09-09 1982-09-09 Liquid disperser

Country Status (1)

Country Link
JP (1) JPS5946466A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009295362A (en) * 2008-06-04 2009-12-17 Hitachi Ltd Box type electronic module

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4833665A (en) * 1971-09-04 1973-05-11
JPS55118597A (en) * 1979-03-02 1980-09-11 Venables Herbert J Iii Tubular heat exchanger

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4833665A (en) * 1971-09-04 1973-05-11
JPS55118597A (en) * 1979-03-02 1980-09-11 Venables Herbert J Iii Tubular heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009295362A (en) * 2008-06-04 2009-12-17 Hitachi Ltd Box type electronic module

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