JPH10176888A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH10176888A
JPH10176888A JP35297396A JP35297396A JPH10176888A JP H10176888 A JPH10176888 A JP H10176888A JP 35297396 A JP35297396 A JP 35297396A JP 35297396 A JP35297396 A JP 35297396A JP H10176888 A JPH10176888 A JP H10176888A
Authority
JP
Japan
Prior art keywords
gas
steam
atmosphere
liquid
liquid separator
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
JP35297396A
Other languages
Japanese (ja)
Inventor
Tomonori Maruta
智則 丸田
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.)
TLV Co Ltd
Original Assignee
TLV 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 TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP35297396A priority Critical patent/JPH10176888A/en
Publication of JPH10176888A publication Critical patent/JPH10176888A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a heat exchanger in which vapor and drain are discharged even when noncondensable gas is contained in the vapor. SOLUTION: A gas/liquid separator 5 is mounted on an atmosphere opening pipe 4 in a heat exchange container 1. On the gas/liquid separator 5 there are provided collision/deflection plates 11, 13 and a turning blade member 12 for colliding, deflecting or turning a mixed fluid of gas and liquid. The mixed fluid of noncondensable gas, drain, and vapor passing through the atmosphere opening pipe 4 is separated in gas and liquid in the gas/liquid separator 5, and the separated liquid drops into the atmosphere open pipe 4, and further the noncondensable gas as the gas is exhausted from an atmosphere communication hole 14.

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、各種蒸気使用装置
で使用され残った蒸気や、高温ドレンから発生した再蒸
発蒸気などを、水などの冷却流体で熱交換して凝縮させ
ることにより、モヤモヤと立ち込める蒸気を無くした
り、あるいは、冷却流体を熱交換して温度上昇した温水
を別途使用して蒸気の保有熱を有効利用するものに関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam generator which heats and condenses remaining steam used in various steam-using devices and re-evaporated steam generated from a high-temperature drain with a cooling fluid such as water. The present invention relates to a method for effectively utilizing the retained heat of steam by eliminating steam that can accumulate therein, or separately using warm water whose temperature has been increased by heat exchange of a cooling fluid.

【0002】[0002]

【従来の技術】従来のこの種の熱交換器としては、例え
ば特開昭60−120186号公報に示されたものがあ
る。これは、蒸気供給口を有する熱回収室に冷却管を内
設し、この熱回収室に大気開放部を連通して、大気開放
部と熱回収室の下部に凝縮液を貯溜させることにより、
熱回収室内へ不凝縮気体、例えば空気等、が流入するこ
とを防止して効率良く熱交換することができるものであ
る。
2. Description of the Related Art A conventional heat exchanger of this type is disclosed, for example, in Japanese Patent Application Laid-Open No. 60-120186. This is achieved by installing a cooling pipe inside a heat recovery chamber having a steam supply port, connecting the air release section to this heat recovery chamber, and storing condensate in the air release section and the lower part of the heat recovery chamber.
It is possible to prevent non-condensable gas, for example, air, from flowing into the heat recovery chamber and efficiently exchange heat.

【0003】[0003]

【発明が解決しようとする課題】上記従来の熱交換器で
は、熱回収室の外部から不凝縮気体が流入してくること
は防止できるが、蒸気供給口から供給される蒸気中に不
凝縮気体が混入していると、その不凝縮気体の流れによ
って蒸気の一部あるいはドレンの一部が大気開放部から
外部へ排出されてしまう問題があった。不凝縮気体と共
に排出される蒸気やドレンは周辺の環境を悪化させるこ
ととなり、極力防止しなければならないのである。
In the above-mentioned conventional heat exchanger, it is possible to prevent the non-condensable gas from flowing in from outside the heat recovery chamber, but the non-condensable gas is contained in the steam supplied from the steam supply port. When mixed with water, there is a problem that a part of the steam or a part of the drain is discharged from the open-to-atmosphere portion to the outside due to the flow of the non-condensable gas. Vapors and drains discharged together with the non-condensable gas deteriorate the surrounding environment and must be prevented as much as possible.

【0004】従って本発明の課題は、供給される蒸気中
に空気等の不凝縮気体が混入している場合であっても、
外部に蒸気やドレンを排出することのない熱交換器を得
ることである。
[0004] Therefore, an object of the present invention is to solve the problem even when non-condensable gas such as air is mixed in supplied steam.
The purpose is to obtain a heat exchanger that does not discharge steam or drain to the outside.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めに講じた手段は、大気開放部を設けた熱交換容器に蒸
気と冷却流体を供給して、蒸気を冷却流体で熱交換する
ことにより凝縮させるものにおいて、大気開放部に流入
した気液を分離する気液分離器を取り付けたものであ
る。
Means taken to solve the above problem is to supply steam and a cooling fluid to a heat exchange container provided with an open-to-atmosphere section, and to perform heat exchange of the steam with the cooling fluid. And a gas-liquid separator for separating gas-liquid flowing into the open-to-atmosphere portion.

【0006】[0006]

【発明の実施の形態】熱交換容器へ供給される蒸気は冷
却流体により熱交換されて凝縮する。供給される蒸気中
に空気等の不凝縮気体が混入していると、不凝縮気体は
冷却流体により凝縮することがないために大気開放部か
ら外部へ排出されるが、その流れによって凝縮すべく蒸
気やドレンの一部が大気開放部へ至る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Steam supplied to a heat exchange container is condensed by heat exchange by a cooling fluid. If non-condensable gas such as air is mixed in the supplied steam, the non-condensable gas is discharged to the outside from the open part to the atmosphere because it is not condensed by the cooling fluid. Part of the steam and drains reach the open air section.

【0007】大気開放部には気液分離器を取り付けたこ
とにより、蒸気とドレンの混合が促進されて蒸気の多く
が凝縮され水滴状になると共に、水滴状の液体は不凝縮
気体から分離され大気開放部内を滴下する。水滴が分離
された不凝縮気体だけが気液分離器から系外へ排出され
る。
By installing a gas-liquid separator in the open-to-atmosphere section, the mixing of steam and drain is promoted, and most of the steam is condensed to form water droplets, and the water-drop liquid is separated from non-condensable gas. Dripping in the open air section. Only the non-condensable gas from which the water droplets have been separated is discharged out of the system from the gas-liquid separator.

【0008】気液分離器としては従来周知のものを用い
ることができるが、蒸気と液体の混合を促進するために
は、流体を旋回させたり、板状部材やフィルタ―部材に
衝突させることのできる気液分離器を用いることが望ま
しい。
As the gas-liquid separator, a well-known gas-liquid separator can be used. However, in order to promote the mixing of the vapor and the liquid, it is necessary to swirl the fluid or impinge on the plate-like member or the filter member. It is desirable to use a gas-liquid separator that can.

【0009】[0009]

【実施例】図1において、熱交換容器1と、凝縮させる
べく蒸気を供給する蒸気供給口2と、蒸気の凝縮したド
レンを排出するオ―バ―フロ―管3と、熱交換容器1の
中央に設けた大気開放部としての大気開放管4と、大気
開放管4の上部に取り付けた気液分離器5で熱交換器を
構成する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS In FIG. 1, a heat exchange vessel 1, a steam supply port 2 for supplying steam to be condensed, an overflow pipe 3 for discharging a drain condensed with steam, and a heat exchange vessel 1 are shown. A heat exchanger is constituted by an open-to-atmosphere pipe 4 provided at the center and serving as an open-to-atmosphere section, and a gas-liquid separator 5 attached to an upper portion of the open-to-atmosphere pipe 4.

【0010】熱交換容器1には、その内部に冷却流体供
給管6と連通した冷却コイル7を大気開放管4の周囲に
配置して、上部を温水排出管8と連通する。熱交換容器
1の上部に設けた蒸気供給口2は、バルブ9を介して図
示しないブロワやシュリンクトンネル等の蒸気使用装置
の出口側や再蒸発タンク等と接続して凝縮すべく蒸気を
熱交換容器1へ供給する。
In the heat exchange vessel 1, a cooling coil 7 communicating with a cooling fluid supply pipe 6 is disposed around the atmosphere opening pipe 4, and an upper part thereof communicates with a hot water discharge pipe 8. The steam supply port 2 provided in the upper part of the heat exchange vessel 1 is connected to an outlet side of a steam-using device (not shown) such as a blower or a shrink tunnel or a re-evaporation tank through a valve 9 to exchange steam for condensation. Supply to container 1.

【0011】熱交換容器1の中央に設けた大気開放管4
の下端部10は、熱交換容器1の下方で開口させ、大気
開放管4の更に中央にオ―バ―フロ―管3を取り付け
る。蒸気供給口2から熱交換容器1内へ供給される蒸気
が冷却コイル7で冷却されて凝縮し熱交換容器1の下部
に溜る。溜ったドレンは、供給される蒸気の圧力により
大気開放管4内を上昇してオ―バ―フロ―管3から外部
へ排除される。
An open-to-atmosphere pipe 4 provided at the center of the heat exchange vessel 1
The lower end 10 is opened below the heat exchange vessel 1, and the overflow tube 3 is attached to the center of the open-to-atmosphere tube 4. The steam supplied from the steam supply port 2 into the heat exchange container 1 is cooled by the cooling coil 7 and condensed, and accumulates in the lower part of the heat exchange container 1. The accumulated drain rises in the atmosphere open pipe 4 due to the pressure of the supplied steam and is discharged to the outside from the overflow pipe 3.

【0012】大気開放管4の上部には気液分離器5を取
り付ける。気液分離器5は、気液の混合流体をフィルタ
を介したり、遠心力や旋回力により、あるいは衝突と付
着現象等により、分離することのできるものであれば従
来周知のどのような型式のものでも用いることができる
が、本実施例においては、衝突と旋回を繰り返して行う
ものを用いた例を示す。即ち、気液分離器5の内部に衝
突偏向板11と旋回羽根部材12と更に衝突偏向板13
を順次に取り付けたもので、その上端に大気連通口14
を設ける。
A gas-liquid separator 5 is mounted on the upper part of the open-to-atmosphere pipe 4. The gas-liquid separator 5 is of any type known in the art as long as it can separate the gas-liquid mixed fluid through a filter, by centrifugal force or swirling force, or by collision and adhesion phenomena. Although this can also be used, in the present embodiment, an example using a device which repeatedly performs collision and turning will be described. That is, the collision deflector 11, the revolving blade member 12 and the collision deflector 13 are provided inside the gas-liquid separator 5.
Are sequentially attached, and the air communication port 14 is provided at the upper end thereof.
Is provided.

【0013】蒸気供給口2から熱交換容器1へ供給され
る蒸気中に多量の不凝縮気体例えば空気等を含んでいる
場合、熱交換容器1内に溜った気体は大気開放管4の下
端部10から大気開放管4へ至る間にドレンや蒸気の一
部を巻込んで大気開放管4内から気液分離器5へ至る。
不凝縮気体とドレンと蒸気の混合流体は、まず気液分離
器5内の衝突偏向板11に衝突して一部の気液が分離さ
れると共にその流れが中央の旋回羽根部材12に偏向さ
れる。この場合一部分離した液体は大気開放管4内を自
重で滴下する。旋回羽根部材12に至った混合流体は旋
回され、蒸気とドレンの混合が促進されて蒸気が凝縮す
る。旋回羽根部材12を経た混合流体は更に衝突偏向板
13に衝突して気液の分離を行い、質量の小さな不凝縮
気体だけが上部の大気連通口14から外部へ排出され
る。
When a large amount of non-condensable gas, such as air, is contained in the steam supplied from the steam supply port 2 to the heat exchange vessel 1, the gas accumulated in the heat exchange vessel 1 is discharged from the lower end of the atmosphere opening pipe 4. A part of the drain or the steam is entrained from 10 to the open-to-atmosphere pipe 4 to reach the gas-liquid separator 5 from the inside of the open-to-atmosphere pipe 4.
The mixed fluid of the non-condensable gas, the drain, and the vapor first collides with the collision deflecting plate 11 in the gas-liquid separator 5 to separate a part of the gas and liquid, and the flow is deflected to the central rotating blade member 12. You. In this case, the liquid that has been partially separated drops in the open-to-atmosphere tube 4 by its own weight. The mixed fluid that has reached the swirling blade member 12 is swirled, and the mixing of the steam and the drain is promoted, and the steam condenses. The mixed fluid that has passed through the swirling blade member 12 further collides with the collision deflecting plate 13 to separate gas and liquid, and only the non-condensable gas having a small mass is discharged from the upper air communication port 14 to the outside.

【0014】[0014]

【発明の効果】本発明によれば、供給される蒸気中に空
気等の不凝縮気体を含む場合であっても、大気開放部に
気液分離器を取り付けて、不凝縮気体に混入してきた蒸
気やドレンを分離し、不凝縮気体だけを外部へ排出する
ことができ、周辺の環境の悪化を防止することができ
る。
According to the present invention, even when an uncondensed gas such as air is contained in the supplied steam, a gas-liquid separator is attached to the open-to-atmosphere portion and mixed into the non-condensable gas. Steam and drain can be separated, and only non-condensable gas can be discharged to the outside, so that deterioration of the surrounding environment can be prevented.

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

【図1】本発明の熱交換器の実施例を示す断面構成図で
ある。
FIG. 1 is a sectional view showing an embodiment of a heat exchanger according to the present invention.

【符号の説明】[Explanation of symbols]

1 熱交換容器 2 蒸気供給口 3 オ―バ―フロ―管 4 大気開放管 5 気液分離器 6 冷却流体供給管 7 冷却コイル 11 衝突偏向板 12 旋回羽根部材 13 衝突偏向板 14 大気連通口 DESCRIPTION OF SYMBOLS 1 Heat exchange container 2 Steam supply port 3 Overflow pipe 4 Open-to-atmosphere pipe 5 Gas-liquid separator 6 Cooling fluid supply pipe 7 Cooling coil 11 Colliding deflecting plate 12 Rotating blade member 13 Colliding deflecting plate 14 Atmospheric communication port

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 大気開放部を設けた熱交換容器に蒸気と
冷却流体を供給して、蒸気を冷却流体で熱交換すること
により凝縮させるものにおいて、大気開放部に流入した
気液を分離する気液分離器を取り付けたことを特徴とす
る熱交換器。
1. A method for supplying steam and a cooling fluid to a heat exchange container provided with an open-to-atmosphere portion and condensing the steam by exchanging heat with the cooling fluid to separate gas and liquid flowing into the open-to-atmosphere portion. A heat exchanger equipped with a gas-liquid separator.
JP35297396A 1996-12-13 1996-12-13 Heat exchanger Pending JPH10176888A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35297396A JPH10176888A (en) 1996-12-13 1996-12-13 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35297396A JPH10176888A (en) 1996-12-13 1996-12-13 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH10176888A true JPH10176888A (en) 1998-06-30

Family

ID=18427720

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35297396A Pending JPH10176888A (en) 1996-12-13 1996-12-13 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH10176888A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101893394A (en) * 2010-07-28 2010-11-24 郭心岭 Thread aluminum pipe heat exchanger
JP2016109374A (en) * 2014-12-09 2016-06-20 株式会社テイエルブイ Heat exchanger
JP2020030008A (en) * 2018-08-23 2020-02-27 株式会社テイエルブイ Steam suppression system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101893394A (en) * 2010-07-28 2010-11-24 郭心岭 Thread aluminum pipe heat exchanger
JP2016109374A (en) * 2014-12-09 2016-06-20 株式会社テイエルブイ Heat exchanger
JP2020030008A (en) * 2018-08-23 2020-02-27 株式会社テイエルブイ Steam suppression system

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