JPH10253270A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH10253270A
JPH10253270A JP8196897A JP8196897A JPH10253270A JP H10253270 A JPH10253270 A JP H10253270A JP 8196897 A JP8196897 A JP 8196897A JP 8196897 A JP8196897 A JP 8196897A JP H10253270 A JPH10253270 A JP H10253270A
Authority
JP
Japan
Prior art keywords
ejector
steam
upper chamber
heat exchange
cooling fluid
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
JP8196897A
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 JP8196897A priority Critical patent/JPH10253270A/en
Publication of JPH10253270A publication Critical patent/JPH10253270A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To obtain a heat exchanger, capable of condensing vapor surely with a small amount of cooling fluid. SOLUTION: A heat exchanging vessel 1 is divided into an upper chamber 20 and a lower chamber 21. The upper chamber 20 is communicated with the lower chamber 21 through a communicating pipe 23. An ejector 4 is attached to the inside of the upper chamber 20 and the nozzle unit 7 of the ejector 4 is connected to a cooling fluid supplying pipe 3. The suction port 8 of the ejector 4 is opened in the upper chamber 20. A coil type indirect heat exchanging unit 5 is connected to the diffuser 9 of the ejector 4. The cooling fluid, supplied to the ejector 4, is supplied into the indirect heat exchanging unit 5 while making a part of vapor in the upper chamber 20 through the suction port 8 to effect the heat exchange of vapor in the upper chamber 20 of the heat exchanging vessel 1 furthermore and condense the vapor.

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
で使用されて残った蒸気や、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、熱交換した冷却流体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 The present invention relates to a method for condensing steam remaining in a steam-using device or reevaporated steam generated from a high-temperature drain by exchanging heat with a cooling fluid such as water. The present invention relates to a device that eliminates steam that can accumulate in a steam or uses a cooling fluid that has undergone heat exchange separately to effectively use the retained heat of the steam.

【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 the non-condensable gas 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、蒸気を完全に凝縮させるには大量の冷却水を必要と
する問題があった。すなわち、供給された蒸気は熱回収
室で冷却管と熱交換するだけであるために、蒸気のモヤ
モヤと立ち込める状態を無くしたい場合のように多量の
蒸気を完全に凝縮しなければならない場合には大量の冷
却水を要してしまうのである。
The conventional heat exchanger has a problem that a large amount of cooling water is required to completely condense the steam. In other words, the supplied steam only exchanges heat with the cooling pipe in the heat recovery chamber, so when it is necessary to completely condense a large amount of steam as in the case where it is necessary to eliminate the state in which the steam can be trapped. A large amount of cooling water is required.

【0004】従って本発明の技術的課題は、大量の冷却
流体を要することなく、蒸気を確実に凝縮することので
きる熱交換器を得ることである。
Accordingly, it is an object of the present invention to provide a heat exchanger capable of reliably condensing steam without requiring a large amount of cooling fluid.

【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、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当該蒸気
を凝縮させるものにおいて、熱交換容器を少なくとも上
下2室に分割して、分割したそれぞれの室を連通する連
通管を取り付け、少なくとも上下2室に分割した下室に
凝縮すべく蒸気を供給する蒸気供給管を接続し、上室に
冷却流体供給管とエゼクタを接続して当該エゼクタの吸
引部を上室内に開口すると共に、熱交換容器の上室内で
エゼクタの出口側に間接熱交換部を連設したものであ
る。
Means taken to solve the above problem is to supply steam and a cooling fluid to a heat exchange container, and to condense the steam by exchanging heat with the cooling fluid. In the apparatus, the heat exchange vessel is divided into at least two upper and lower chambers, a communication pipe for communicating the divided chambers is attached, and a steam supply pipe for supplying steam to condense the lower chamber divided into at least two upper and lower chambers. Connected, a cooling fluid supply pipe and an ejector connected to the upper chamber, the suction part of the ejector is opened in the upper chamber, and an indirect heat exchange part is connected to the outlet side of the ejector in the upper chamber of the heat exchange container. It is.

【0006】[0006]

【発明の実施の形態】熱交換容器の下室にある凝縮すべ
く蒸気は連通管を通って上室内に至る。上室には吸引部
を開口したエゼクタが冷却流体供給管と接続されている
ことにより、凝縮すべく蒸気はエゼクタの吸引部に吸引
される。また、吸引された蒸気はエゼクタ内で冷却流体
と混合されて出口側に連設された間接熱交換部へ供給さ
れ、この間接熱交換部で更に上室内の蒸気を凝縮させ
る。
DETAILED DESCRIPTION OF THE INVENTION The vapor to be condensed in the lower chamber of the heat exchange vessel reaches the upper chamber through a communication pipe. In the upper chamber, an ejector having an open suction unit is connected to the cooling fluid supply pipe, so that the vapor is sucked into the suction unit of the ejector to be condensed. The sucked steam is mixed with the cooling fluid in the ejector and supplied to an indirect heat exchange unit connected to the outlet side, and the indirect heat exchange unit further condenses the steam in the upper chamber.

【0007】このように、熱交換容器の上室に至った凝
縮すべく蒸気だけが、エゼクタに吸引されて冷却流体と
混合されると共に間接熱交換部で熱交換されて凝縮す
る。従って、冷却管で熱交換されるだけの従来の熱交換
器と比較して、エゼクタで吸引される割合だけ蒸気の凝
縮が進み、より少ない冷却流体でもって蒸気を確実に凝
縮させることができる。
As described above, only the vapor that has reached the upper chamber of the heat exchange vessel is sucked by the ejector and mixed with the cooling fluid, and is condensed by heat exchange in the indirect heat exchange section. Therefore, as compared with the conventional heat exchanger in which only heat is exchanged in the cooling pipe, the condensation of the steam is advanced by the rate sucked by the ejector, and the steam can be surely condensed with a smaller cooling fluid.

【0008】[0008]

【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管2と、冷却流体供給管3
と、冷却流体供給管3に接続し熱交換容器1内に配置し
たエゼクタ4、及び、エゼクタ4の出口側に連設した間
接熱交換部5とで熱交換器を構成する。
1, a heat exchange vessel 1, a steam supply pipe 2 for supplying steam to be condensed, and a cooling fluid supply pipe 3 are shown.
And an ejector 4 connected to the cooling fluid supply pipe 3 and arranged in the heat exchange vessel 1 and an indirect heat exchange section 5 connected to the outlet side of the ejector 4 to form a heat exchanger.

【0009】熱交換容器1は、上下の2室20,21に
隔壁22で分割すると共に、隔壁22に連通管23を取
り付けて上室20と下室21を連通する。また、隔壁2
2に貫通孔24を設けて、上室20内で蒸気が凝縮して
生じた液体のドレンを下室21へ滴下させる。
The heat exchange vessel 1 is divided into upper and lower two chambers 20 and 21 by a partition wall 22 and a communication pipe 23 is attached to the partition wall 22 to communicate the upper chamber 20 and the lower chamber 21. Also, partition 2
2 is provided with a through hole 24, and a liquid drain generated by condensation of the vapor in the upper chamber 20 is dropped into the lower chamber 21.

【0010】上室20に接続した冷却流体供給管3は図
示しない冷却水等の冷却流体源と接続すると共に、バル
ブ6を介してエゼクタ4のノズル部7と接続する。ノズ
ル部7の内部には絞り部を内蔵すると共に吸引部として
の吸引口8を設ける。吸引口8の上端部を開口して上室
20内と連通する。ノズル部7の右方にディフュ―ザ部
9を設け、更にその下方にコイル状に間接熱交換部5を
配置する。
[0010] The cooling fluid supply pipe 3 connected to the upper chamber 20 is connected to a cooling fluid source such as cooling water (not shown) and is connected to the nozzle portion 7 of the ejector 4 via the valve 6. The nozzle unit 7 has a built-in throttle unit and a suction port 8 as a suction unit. The upper end of the suction port 8 is opened to communicate with the upper chamber 20. A diffuser section 9 is provided on the right side of the nozzle section 7, and a coil-like indirect heat exchange section 5 is further disposed below the diffuser section 9.

【0011】間接熱交換部5は、銅管等の熱伝導率の高
い材料を用いて上室20内の全体に行き渡るように配置
すると共に、その下端部をバルブ10を介して冷却流体
排出管11と接続する。冷却流体排出管11は、エゼク
タ4と間接熱交換部5で上室20内の蒸気と熱交換して
温度の上昇した冷却流体を、別途の利用箇所へ導くもの
である。
The indirect heat exchanging section 5 is disposed so as to extend over the entire inside of the upper chamber 20 using a material having high thermal conductivity such as a copper pipe, and the lower end thereof is connected to the cooling fluid discharge pipe via a valve 10. 11 is connected. The cooling fluid discharge pipe 11 exchanges heat with the steam in the upper chamber 20 in the ejector 4 and the indirect heat exchange section 5 to guide the cooling fluid whose temperature has increased to a separate use location.

【0012】熱交換容器1の上室20の上部には、バル
ブ12を介して大気開放管13を取り付ける。バルブ1
2を開弁することにより上室20内を大気と連通し、閉
弁することにより遮断することができるものである。ま
た、バルブ15を介してガス抜き弁16を取り付ける。
ガス抜き弁16は、上室20内に溜った空気等の不凝縮
ガスを自動的に外部へ排除するもので、図示はしていな
いがバイメタルやサ―モワックス等の感熱素子を用い、
雰囲気温度が所定温度以下、例えば80度C以下、にな
ると開弁してガスを排除し、所定温度以上になると閉弁
して蒸気の外部への漏洩を防止するものである。
An open-to-atmosphere pipe 13 is attached to the upper part of the upper chamber 20 of the heat exchange vessel 1 via a valve 12. Valve 1
The upper chamber 20 communicates with the atmosphere by opening the valve 2, and can be shut off by closing the valve. Further, a degassing valve 16 is attached via a valve 15.
The degassing valve 16 automatically removes non-condensable gas such as air accumulated in the upper chamber 20 to the outside, and uses a heat sensitive element such as bimetal or thermo wax (not shown).
When the ambient temperature becomes lower than a predetermined temperature, for example, 80 ° C. or lower, the valve is opened to remove gas, and when the temperature becomes higher than the predetermined temperature, the valve is closed to prevent leakage of steam to the outside.

【0013】下室21と接続した蒸気供給管2は図示し
ない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の下室21内へ供給す
る。従って、下室21内には蒸気供給管2から供給され
た凝縮すべく蒸気が滞留しており、その蒸気は連通管2
3を通って上室20内へ至る。下室21の下端には凝縮
した蒸気を所定箇所へ供給するための管17を接続す
る。
A steam supply pipe 2 connected to the lower chamber 21 is connected to an outlet side of a steam-using device (not shown), a re-evaporation tank or the like to supply steam to the lower chamber 21 of the heat exchange vessel 1 for condensation. Therefore, the steam supplied from the steam supply pipe 2 to be condensed stays in the lower chamber 21, and the steam is supplied to the communication pipe 2.
3 and into the upper chamber 20. A pipe 17 for supplying condensed steam to a predetermined location is connected to the lower end of the lower chamber 21.

【0014】冷却水供給管3から供給される冷却流体
は、エゼクタ4のノズル部7で絞られて流速を増し吸引
力を発生して吸引口8から上室20内の蒸気の一部を吸
引して混合し間接熱交換部5へ供給される。従って、凝
縮すべく蒸気はエゼクタ4に吸引され冷却流体と混合さ
れて凝縮すると共に、間接熱交換部5でもって更に凝縮
される。凝縮した蒸気は液体状のドレンとなって隔壁2
2の貫通孔24から下室21へ滴下し、管17を通って
所定箇所へ供給される。
The cooling fluid supplied from the cooling water supply pipe 3 is throttled by the nozzle portion 7 of the ejector 4 to increase the flow velocity, generate a suction force, and suck a part of the steam in the upper chamber 20 from the suction port 8. And mixed and supplied to the indirect heat exchange unit 5. Therefore, the vapor is sucked into the ejector 4 to be condensed, mixed with the cooling fluid and condensed, and further condensed by the indirect heat exchange section 5. The condensed vapor turns into a liquid drain to form a partition 2
The liquid is dropped into the lower chamber 21 from the second through hole 24 and supplied to a predetermined location through the pipe 17.

【0015】隔壁22の貫通孔24から下室21へ滴下
したドレンは、下室21内の蒸気の一部を凝縮すること
ができる。
The drain dropped from the through hole 24 of the partition 22 into the lower chamber 21 can condense a part of the vapor in the lower chamber 21.

【0016】熱交換容器1の下室21から上室20へ至
った凝縮すべく蒸気だけがエゼクタ4に吸引されて冷却
流体と混合されると共に、間接熱交換部5で熱交換され
て更に凝縮される。
Only the vapor that has reached the upper chamber 20 from the lower chamber 21 of the heat exchange vessel 1 is sucked by the ejector 4 and mixed with the cooling fluid, and is further heat-exchanged by the indirect heat exchange unit 5 to be further condensed. Is done.

【0017】本実施例においては、熱交換容器1の上室
20内に1台のエゼクタ4を配置した例を示したが、熱
交換容器1の大きさや蒸気の供給量に応じてエゼクタの
数は2台以上の複数台でも適宜配置することができるも
のである。
In this embodiment, an example in which one ejector 4 is disposed in the upper chamber 20 of the heat exchange vessel 1 has been described. However, the number of ejectors 4 depends on the size of the heat exchange vessel 1 and the amount of steam supply. Can be appropriately arranged even if two or more units are used.

【0018】[0018]

【発明の効果】本発明によれば、熱交換容器を少なくと
も上下2室に分割して、凝縮すべく蒸気だけを上室に至
らしめ、上室内のエゼクタの吸引部で蒸気を吸引して冷
却流体と混合すると共に、エゼクタの出口側に連設した
間接熱交換部で更に蒸気を凝縮することができ、より少
ない冷却流体でもって蒸気を確実に凝縮させることがで
きる。
According to the present invention, the heat exchange vessel is divided into at least two upper and lower chambers, and only steam is condensed to the upper chamber, and the steam is sucked and cooled by the suction portion of the ejector in the upper chamber. As well as mixing with the fluid, the steam can be further condensed in the indirect heat exchange section connected to the outlet side of the ejector, and the steam can be surely condensed with less cooling fluid.

【0019】また、エゼクタの吸引部に蒸気が吸引され
ることにより、熱交換容器の上室内での蒸気の対流が促
進され、間接熱交換部との熱交換効率が向上して更に確
実に蒸気を凝縮させることができる。
Further, since the steam is sucked into the suction portion of the ejector, the convection of the steam in the upper chamber of the heat exchange container is promoted, the efficiency of heat exchange with the indirect heat exchange portion is improved, and the steam is more reliably. Can be condensed.

【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構成図であ
る。
FIG. 1 is a configuration diagram showing an embodiment of a heat exchanger of the present invention.

【符号の説明】[Explanation of symbols]

1 熱交換容器 2 蒸気供給管 3 冷却流体供給管 4 エゼクタ 8 吸引口 11 冷却流体排出管 16 ガス抜き弁 20 上室 21 下室 22 隔壁 23 連通管 DESCRIPTION OF SYMBOLS 1 Heat exchange container 2 Steam supply pipe 3 Cooling fluid supply pipe 4 Ejector 8 Suction port 11 Cooling fluid discharge pipe 16 Gas release valve 20 Upper chamber 21 Lower chamber 22 Partition wall 23 Communication pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 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当該蒸気を
凝縮させるものにおいて、熱交換容器を少なくとも上下
2室に分割して、分割したそれぞれの室を連通する連通
管を取り付け、少なくとも上下2室に分割した下室に凝
縮すべく蒸気を供給する蒸気供給管を接続し、上室に冷
却流体供給管とエゼクタを接続して当該エゼクタの吸引
部を上室内に開口すると共に、熱交換容器の上室内でエ
ゼクタの出口側に間接熱交換部を連設したことを特徴と
する熱交換器。
1. A method in which steam and a cooling fluid are supplied to a heat exchange vessel and the steam is condensed by exchanging heat with the cooling fluid, wherein the heat exchange vessel is divided into at least two upper and lower chambers. A communication pipe for communicating the respective chambers is attached, a steam supply pipe for supplying steam to be condensed is connected to at least a lower chamber divided into upper and lower chambers, and a cooling fluid supply pipe and an ejector are connected to the upper chamber. A heat exchanger, characterized in that a suction part of an ejector is opened in an upper chamber and an indirect heat exchange part is connected to an outlet side of the ejector in the upper chamber of the heat exchange container.
JP8196897A 1997-03-14 1997-03-14 Heat exchanger Pending JPH10253270A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8196897A JPH10253270A (en) 1997-03-14 1997-03-14 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8196897A JPH10253270A (en) 1997-03-14 1997-03-14 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH10253270A true JPH10253270A (en) 1998-09-25

Family

ID=13761308

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8196897A Pending JPH10253270A (en) 1997-03-14 1997-03-14 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH10253270A (en)

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