JP3790005B2 - Heat exchanger - Google Patents

Heat exchanger Download PDF

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Publication number
JP3790005B2
JP3790005B2 JP08196697A JP8196697A JP3790005B2 JP 3790005 B2 JP3790005 B2 JP 3790005B2 JP 08196697 A JP08196697 A JP 08196697A JP 8196697 A JP8196697 A JP 8196697A JP 3790005 B2 JP3790005 B2 JP 3790005B2
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JP
Japan
Prior art keywords
steam
heat exchange
cooling fluid
ejector
heat
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.)
Expired - Fee Related
Application number
JP08196697A
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Japanese (ja)
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JPH10253269A (en
Inventor
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 JP08196697A priority Critical patent/JP3790005B2/en
Publication of JPH10253269A publication Critical patent/JPH10253269A/en
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Description

【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。
【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。
【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。
【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。
【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、冷却流体供給管にエゼクタを接続して当該エゼクタの吸引部を熱交換容器内の上方に開口すると共に、熱交換容器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。
【0006】
【発明の実施の形態】
エゼクタに冷却流体を供給することにより吸引部で吸引力を生じて、熱交換容器内に供給された蒸気の一部を吸引する。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熱交換容器内の蒸気を凝縮させる。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。
【0007】
【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。
【0008】
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熱交換容器1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、更にその右下方にコイル状に間接熱交換部5を配置する。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熱交換容器1内の全体に行き渡るように配置すると共に、その下部をバルブ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で熱交換容器1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。
【0009】
熱交換容器1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12を開弁することにより熱交換容器1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、熱交換容器1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。
【0010】
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内へ供給する。従って、熱交換容器1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いる。熱交換容器1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。
【0011】
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。熱交換容器1内の上方に滞留している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。また、熱交換容器1内の上方以下部に滞留している凝縮すべく蒸気は間接熱交換部5でもって凝縮される。凝縮した蒸気は液体状のドレンとなって下端の管17から所定箇所へ至る。
【0012】
熱交換容器1内の蒸気の一部がエゼクタ4に吸引され混合されることにより、蒸気の凝縮を加速することができると共に、熱交換容器1内の蒸気の対流を促進して更に効率良く蒸気を凝縮させることができる。
【0013】
本実施例においては、熱交換容器1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。
【0014】
【発明の効果】
本発明によれば、冷却流体供給管にエゼクタを接続し、エゼクタの吸引部を熱交換容器内に開口すると共に、エゼクタの出口側に間接熱交換部を連設したことにより、吸引部で一部の蒸気を吸引して蒸気の凝縮を速めることができ、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。
【0015】
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。
【図面の簡単な説明】
【図1】本発明の熱交換器の実施例を示す構成図である。
【符号の説明】
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
[0001]
BACKGROUND OF THE INVENTION
The present invention eliminates the steam that can be trapped in the moyamoya by condensing the remaining steam used in various steam-using devices or re-evaporated steam generated from high-temperature drain by heat exchange with a cooling fluid such as water. Alternatively, the present invention relates to one that effectively uses the retained heat of steam by separately using a heat exchanged cooling fluid.
[0002]
[Prior art]
A conventional heat exchanger of this type is disclosed in, for example, Japanese Patent Application Laid-Open No. 60-120186. This is because a cooling pipe is installed in a heat recovery chamber having a steam supply port, an atmosphere opening portion is communicated with the heat recovery chamber, and condensate is stored in the atmosphere opening portion and the lower portion of the heat recovery chamber, It is possible to prevent heat from flowing into the heat recovery chamber and efficiently exchange heat.
[0003]
[Problems to be solved by the invention]
The conventional heat exchanger has a problem that a large amount of cooling water is required to completely condense the steam. In other words, since the supplied steam only exchanges heat with the cooling pipe in the heat recovery chamber, when it is necessary to completely condense a large amount of steam, such as when it is desired to eliminate the state of confusion with the steam. A large amount of cooling water is required.
[0004]
Therefore, the technical problem of the present invention is to obtain a heat exchanger capable of reliably condensing steam without requiring a large amount of cooling fluid.
[0005]
[Means for Solving the Problems]
Means taken in order to solve the above-mentioned problem is to supply steam and a cooling fluid to a heat exchange vessel and to condense the steam by exchanging the heat with the cooling fluid, and in the cooling fluid supply pipe, an ejector And the suction part of the ejector is opened upward in the heat exchange container, and the indirect heat exchange part is connected to the outlet side of the ejector in the heat exchange container.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
By supplying a cooling fluid to the ejector, a suction force is generated at the suction portion, and a part of the steam supplied into the heat exchange container is sucked. Further, the sucked steam is mixed with the cooling fluid in the ejector and supplied to the indirect heat exchanging section connected to the outlet side, and the in-heat exchanging section further condenses the steam in the heat exchange container. Therefore, compared with a conventional heat exchanger that only performs heat exchange in the cooling pipe, condensation of the vapor proceeds at a rate that is sucked by the ejector, and the vapor can be reliably condensed with less cooling fluid.
[0007]
【Example】
In FIG. 1, a heat exchange container 1, a steam supply pipe 2 for supplying steam to be condensed, a cooling fluid supply pipe 3, an ejector 4 connected to the cooling fluid supply pipe 3 and disposed in the heat exchange container 1, and A heat exchanger is configured with the indirect heat exchange unit 5 provided continuously on the outlet side of the ejector 4.
[0008]
The cooling fluid supply pipe 3 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. Inside the nozzle part 7, a throttle part is built and a suction port 8 as a suction part is provided. The upper end of the suction port 8 is opened to communicate with the heat exchange container 1. A diffuser unit 9 is provided on the right side of the nozzle unit 7, and an indirect heat exchange unit 5 is arranged in a coil shape on the lower right side of the diffuser unit 9. The indirect heat exchanging section 5 is arranged so as to reach the entire inside of the heat exchanging vessel 1 using a material having high thermal conductivity such as a copper pipe, and the lower portion thereof is connected to the cooling fluid discharge pipe 11 via the valve 10. To do. The cooling fluid discharge pipe 11 guides the cooling fluid whose temperature has been increased by exchanging heat with the steam in the heat exchange container 1 by the ejector 4 and the indirect heat exchanging section 5 to a separate use location.
[0009]
An air release pipe 13 is attached to the upper part of the heat exchange vessel 1 through a valve 12. By opening the valve 12, the heat exchange vessel 1 communicates with the atmosphere, and can be shut off by closing the valve. A gas vent valve 16 is attached via the valve 15. The degassing valve 16 automatically removes non-condensable gas such as air accumulated in the heat exchange vessel 1 to the outside. Although not shown, the degassing valve 16 uses a thermal element such as bimetal or thermo wax to When the temperature is lower than a predetermined temperature, for example, 80 degrees C or lower, the valve is opened to exclude gas, and when the temperature is higher than the predetermined temperature, the valve is closed to prevent vapor from leaking to the outside.
[0010]
The steam supply pipe 2 is connected to an outlet side of a steam using apparatus (not shown), a re-evaporation tank or the like, and supplies steam into the heat exchange container 1 for condensation. Therefore, steam stays in the heat exchange vessel 1 for condensation supplied from the steam supply pipe 2. A pipe 17 for supplying condensed steam to a predetermined location is connected to the lower end of the heat exchange vessel 1.
[0011]
The cooling fluid supplied from the cooling water supply pipe 3 is squeezed by the nozzle portion 7 of the ejector 4 to increase the flow velocity, generate a suction force, and suck and mix a part of the steam from the suction port 8 to mix the indirect heat exchange portion. 5 is supplied. In order to condense, the steam staying above in the heat exchange vessel 1 is sucked into the ejector 4 and mixed with the cooling fluid to condense. Further, the steam staying in the upper part and the lower part in the heat exchange vessel 1 is condensed by the indirect heat exchange unit 5 to be condensed. The condensed vapor becomes a liquid drain and reaches a predetermined location from the lower end pipe 17.
[0012]
A part of the steam in the heat exchange vessel 1 is sucked and mixed by the ejector 4, so that the condensation of the steam can be accelerated, and the convection of the steam in the heat exchange vessel 1 is promoted to further improve the steam efficiency. Can be condensed.
[0013]
In the present embodiment, an example in which one ejector 4 is arranged in the heat exchange container 1 is shown, but the number of ejectors is two or more according to the size of the heat exchange container 1 and the supply amount of steam. However, it can be appropriately arranged.
[0014]
【The invention's effect】
According to the present invention, the ejector is connected to the cooling fluid supply pipe, the suction part of the ejector is opened in the heat exchange container, and the indirect heat exchange part is continuously provided on the outlet side of the ejector. The steam can be sucked to accelerate the condensation of the steam, and the steam can be reliably condensed with less cooling fluid.
[0015]
In addition, the steam is sucked into the suction part of the ejector, so that the convection of the steam in the heat exchange vessel is promoted, the heat exchange efficiency with the indirect heat exchange part is improved, and the steam can be more reliably condensed. it can.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a heat exchanger according to the present invention.
[Explanation 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 Degassing Valve

Claims (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、冷却流体供給管にエゼクタを接続して当該エゼクタの吸引部を熱交換容器内の上方に開口すると共に、熱交換容器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。Supplying steam and cooling fluid to a heat exchange container and condensing the steam by heat exchange of the steam with the cooling fluid. A heat exchanger characterized in that an indirect heat exchanging portion is continuously provided on the outlet side of the ejector in the heat exchange vessel while opening upward in the inside.
JP08196697A 1997-03-14 1997-03-14 Heat exchanger Expired - Fee Related JP3790005B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08196697A JP3790005B2 (en) 1997-03-14 1997-03-14 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08196697A JP3790005B2 (en) 1997-03-14 1997-03-14 Heat exchanger

Publications (2)

Publication Number Publication Date
JPH10253269A JPH10253269A (en) 1998-09-25
JP3790005B2 true JP3790005B2 (en) 2006-06-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP08196697A Expired - Fee Related JP3790005B2 (en) 1997-03-14 1997-03-14 Heat exchanger

Country Status (1)

Country Link
JP (1) JP3790005B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009275996A (en) * 2008-05-15 2009-11-26 Tlv Co Ltd Heating and cooling device
JP5855929B2 (en) * 2011-12-22 2016-02-09 株式会社テイエルブイ Heat exchanger

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