JP2002054890A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JP2002054890A JP2002054890A JP2000242195A JP2000242195A JP2002054890A JP 2002054890 A JP2002054890 A JP 2002054890A JP 2000242195 A JP2000242195 A JP 2000242195A JP 2000242195 A JP2000242195 A JP 2000242195A JP 2002054890 A JP2002054890 A JP 2002054890A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- pipe
- steam
- cooling fluid
- heat exchanger
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
- F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
- F28D15/0233—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes the conduits having a particular shape, e.g. non-circular cross-section, annular
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【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、水等の冷却流体で熱交換して凝縮させ
ることによって、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 The present invention relates to a method of 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 with a moyamoya gas or uses hot water whose temperature has been increased by exchanging heat with a cooling fluid to separately 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、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 JP-A-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、熱交換効率に限界があり蒸気を確実に凝縮させるこ
とができずに、残った蒸気が熱交換器周辺に排出されて
モヤモヤと立ち込め、環境上問題となることがあった。
熱交換器に供給される蒸気の量は常に一定ではなく、変
動するケースが多くあり、多量の蒸気が熱交換器に流入
した場合に、全ての蒸気を凝縮させることができなくな
るからである。In the above-mentioned conventional heat exchanger, the heat exchange efficiency is limited, so that the steam cannot be surely condensed. There were times when we got stuck and became an environmental problem.
This is because the amount of steam supplied to the heat exchanger is not always constant and fluctuates in many cases. When a large amount of steam flows into the heat exchanger, all the steam cannot be condensed.
【0004】従って本発明の課題は、多量の蒸気が流入
しても効率良く熱交換して、外部に蒸気が排出されるこ
とのない熱交換器を得ることである。Accordingly, an object of the present invention is to provide a heat exchanger that efficiently exchanges heat even when a large amount of steam flows in and does not discharge steam 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、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、熱交換容器の内部に冷却流体の通過す
る冷却流体管を取り付けて、当該冷却流体管の周囲に、
蒸気の保有する熱を吸熱し、冷却流体に放熱するヒート
パイプ部材を具備したものである。Means taken to solve the above problem is to supply steam and a cooling fluid to a heat exchange container and condense the steam by exchanging heat with the cooling fluid. Attach a cooling fluid pipe through which the cooling fluid passes inside the heat exchange container, and around the cooling fluid pipe,
It is provided with a heat pipe member that absorbs heat held by steam and radiates heat to a cooling fluid.
【0006】[0006]
【発明の実施の形態】熱交換容器内の蒸気は、冷却流体
管の外表面に接触して熱交換されて凝縮する。冷却流体
管の周囲に、蒸気の保有する熱を吸熱し、冷却流体に放
熱するヒートパイプ部材を具備したことにより、冷却流
体管だけで熱交換しきれない量の蒸気が流入してきた場
合でも、このヒートパイプ部材によって効率良く蒸気を
熱交換して凝縮させることができ、外部に蒸気を排出す
ることがない。BEST MODE FOR CARRYING OUT THE INVENTION Steam in a heat exchange vessel contacts the outer surface of a cooling fluid pipe and exchanges heat to condense. By providing a heat pipe member around the cooling fluid pipe that absorbs heat held by the steam and radiates heat to the cooling fluid, even when an amount of steam that cannot be exchanged by the cooling fluid pipe alone flows in, The heat pipe member can efficiently exchange heat and condense the steam, and does not discharge the steam to the outside.
【0007】[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、熱交換容器1内に
配置した冷却流体管5と、冷却流体管5の周囲に取り付
けたヒートパイプ部材6と、蒸気の凝縮したドレンを排
出するオーバーフロー管3、及び、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とで熱交換器
を構成する。In FIG. 1, a heat exchange vessel 1, a steam supply pipe 2 for supplying steam to be condensed, a cooling fluid pipe 5 arranged in the heat exchange vessel 1, and a cooling fluid pipe 5 are attached. A heat exchanger is constituted by the heat pipe member 6, the overflow pipe 3 for discharging the condensed drain of steam, and the open-to-atmosphere pipe 4 provided at the center of the heat exchange vessel 1 as an open-to-atmosphere section.
【0008】熱交換容器1内で大気開放管4の外周に、
銅製長尺パイプをコイル状に形成した冷却流体管5を配
置して、冷却流体管5の下部入口側を冷却流体供給管8
と接続すると共に、上部出口側は温水排出管9と接続す
る。熱交換容器1に供給された蒸気が冷却流体管5の外
表面と接触して凝縮するものである。In the heat exchange vessel 1, on the outer periphery of the open-to-atmosphere pipe 4,
A cooling fluid pipe 5 in which a long copper pipe is formed in a coil shape is arranged, and a lower inlet side of the cooling fluid pipe 5 is connected to a cooling fluid supply pipe 8.
And the upper outlet side is connected to the hot water discharge pipe 9. The steam supplied to the heat exchange vessel 1 comes into contact with the outer surface of the cooling fluid pipe 5 and condenses.
【0009】オーバーフロー管3は鉛直直線状で、上端
11を大気開放管4内に開口し下端12を熱交換容器1
外部の大気中に開口する。蒸気の凝縮したドレンが熱交
換容器1底部からオーバーフロー管3を通って外部に排
出されるものである。The overflow pipe 3 is a vertical straight line, and the upper end 11 is opened in the open pipe 4 and the lower end 12 is connected to the heat exchange vessel 1.
Open to the outside atmosphere. The drain in which the vapor is condensed is discharged from the bottom of the heat exchange vessel 1 to the outside through the overflow pipe 3.
【0010】冷却流体管5の下方部の周囲に、ヒートパ
イプ部材6を取り付ける。ヒートパイプ部材6は、いわ
ゆるループ型細管ヒートパイプが適する。ループ型細管
ヒートパイプ6は、ループ状に形成した細管内に熱輸送
用の作動流体を収容して、このループ型細管の一部を吸
熱部とすると共に、吸熱部以外を放熱部として用いるこ
とによって、薄型平板形状で優れた熱伝達能力を有する
ものである。A heat pipe member 6 is attached around the lower part of the cooling fluid pipe 5. As the heat pipe member 6, a so-called loop-type thin tube heat pipe is suitable. The loop-type thin tube heat pipe 6 contains a working fluid for heat transport in a loop-shaped thin tube, and uses a part of the loop-type thin tube as a heat absorbing portion and uses a portion other than the heat absorbing portion as a heat radiating portion. Therefore, it has a thin flat plate shape and excellent heat transfer capability.
【0011】ループ型細管ヒートパイプ6は、冷却流体
管5と同様にコイル状の平板で、中央部分7を冷却流体
管5の外表面の一部に接して配置し、両端部分13,1
4を熱交換容器1内に配置する。中央部分7が冷却流体
管5を介して冷却流体に放熱する放熱部であり、中央部
分7以外の両端部分13,14が蒸気から熱を吸熱する
吸熱部である。ループ型細管ヒートパイプ6の内部は図
示はしないが、多数の細管をループ状に且つ並列に形成
して全体を一本の連続した細管として、その内部を真空
状態にして作動液体を封入したものである。The loop-type thin tube heat pipe 6 is a coil-shaped flat plate similar to the cooling fluid pipe 5, the central portion 7 is arranged in contact with a part of the outer surface of the cooling fluid pipe 5, and both end portions 13, 1.
4 is placed in the heat exchange vessel 1. The central portion 7 is a heat radiating portion that radiates heat to the cooling fluid via the cooling fluid pipe 5, and both end portions 13 and 14 other than the central portion 7 are heat absorbing portions that absorb heat from steam. The inside of the loop type thin tube heat pipe 6 is not shown, but a number of thin tubes are formed in a loop and in parallel to form a single continuous thin tube, and the working liquid is sealed in a vacuum state inside. It is.
【0012】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内に供給する。蒸気供給管2から熱交換
容器1内へ供給される蒸気が、冷却流体管5で冷却され
て凝縮しドレンとなって熱交換容器1の底部に滴下す
る。The steam supply pipe 2 is connected to an outlet side of a steam-using device (not shown), a re-evaporation tank, or the like, and supplies steam to the heat exchange vessel 1 for condensation. The steam supplied from the steam supply pipe 2 into the heat exchange vessel 1 is cooled by the cooling fluid pipe 5 and condensed to be drained and dropped on the bottom of the heat exchange vessel 1.
【0013】ループ型細管ヒートパイプ6の吸熱部であ
る両端部分13,14で、冷却流体管5で冷却しきれな
い蒸気の熱が吸熱されて凝縮しドレンとなるものであ
る。吸熱部13,14で吸熱された熱は、ループ型細管
ヒートパイプ6内を熱移動して放熱部である中央部分7
から冷却流体管5内の冷却流体に放熱される。The heat of the steam that cannot be cooled by the cooling fluid pipe 5 is absorbed by the heat absorbing portions 13 and 14 of the loop-type thin tube heat pipe 6 at both end portions 13 and 14, and is condensed to form a drain. The heat absorbed by the heat absorbing portions 13 and 14 moves through the loop-type thin tube heat pipe 6 and moves to the central portion 7 serving as a heat radiating portion.
From the cooling fluid in the cooling fluid pipe 5.
【0014】ループ型細管ヒートパイプ6で凝縮したド
レンも下方に滴下して熱交換容器1の低部に溜まる。溜
ま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、オーバーフロー管3の上端11から外
部へ排除される。The drain condensed in the loop-type thin tube heat pipe 6 also drops downward and accumulates in the lower part of the heat exchange vessel 1. The accumulated drain rises in the open-to-atmosphere pipe 4 due to the pressure of the supplied steam, and is discharged from the upper end 11 of the overflow pipe 3 to the outside.
【0015】[0015]
【発明の効果】本発明によれば、冷却流体管の周囲に蒸
気の保有する熱を吸熱し、冷却流体に放熱するヒートパ
イプ部材を具備したことにより、冷却流体管だけで熱交
換しきれない量の蒸気が流入してきた場合でも、このヒ
ートパイプ部材によって効率良く蒸気を熱交換して凝縮
させることができ、外部に蒸気を排出することがない熱
交換器を得ることができる。According to the present invention, a heat pipe member is provided around the cooling fluid pipe to absorb the heat of the steam and radiate the heat to the cooling fluid. Even when a large amount of steam flows in, the heat pipe member can efficiently exchange heat and condense the steam, and a heat exchanger that does not discharge steam to the outside can be obtained.
【図1】本発明の熱交換器の実施例を示す構成図。FIG. 1 is a configuration diagram showing an embodiment of a heat exchanger of the present invention.
1 熱交換容器 2 蒸気供給管 3 オーバーフロー管 4 大気開放管 5 冷却流体管 6 ヒートパイプ部材 7 放熱部 8 冷却流体供給管 9 温水回収管 13,14 吸熱部 DESCRIPTION OF SYMBOLS 1 Heat exchange container 2 Steam supply pipe 3 Overflow pipe 4 Open air pipe 5 Cooling fluid pipe 6 Heat pipe member 7 Heat radiating part 8 Cooling fluid supply pipe 9 Hot water recovery pipe 13, 14 Heat absorbing part
Claims (1)
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、熱交換容器の内部に冷却流体の通過する
冷却流体管を取り付けて、当該冷却流体管の周囲に、蒸
気の保有する熱を吸熱し、冷却流体に放熱するヒートパ
イプ部材を具備し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 vessel and condensing the steam by exchanging heat with the cooling fluid, wherein a cooling fluid pipe through which the cooling fluid passes is provided inside the heat exchange vessel. A heat pipe member around the cooling fluid pipe, the heat pipe member absorbing heat held by the steam and releasing the heat to the cooling fluid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000242195A JP2002054890A (en) | 2000-08-10 | 2000-08-10 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000242195A JP2002054890A (en) | 2000-08-10 | 2000-08-10 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2002054890A true JP2002054890A (en) | 2002-02-20 |
Family
ID=18733250
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000242195A Pending JP2002054890A (en) | 2000-08-10 | 2000-08-10 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2002054890A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006308186A (en) * | 2005-04-28 | 2006-11-09 | Tlv Co Ltd | Vaporization cooling device |
JP2007139222A (en) * | 2005-11-15 | 2007-06-07 | Tlv Co Ltd | Waste steam recovering device |
JP2007139221A (en) * | 2005-11-15 | 2007-06-07 | Tlv Co Ltd | Waste steam recovering device |
JP2011127791A (en) * | 2009-12-15 | 2011-06-30 | Tlv Co Ltd | Waste steam recovering device |
-
2000
- 2000-08-10 JP JP2000242195A patent/JP2002054890A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006308186A (en) * | 2005-04-28 | 2006-11-09 | Tlv Co Ltd | Vaporization cooling device |
JP2007139222A (en) * | 2005-11-15 | 2007-06-07 | Tlv Co Ltd | Waste steam recovering device |
JP2007139221A (en) * | 2005-11-15 | 2007-06-07 | Tlv Co Ltd | Waste steam recovering device |
JP4628933B2 (en) * | 2005-11-15 | 2011-02-09 | 株式会社テイエルブイ | Waste steam recovery device |
JP4628934B2 (en) * | 2005-11-15 | 2011-02-09 | 株式会社テイエルブイ | Waste steam recovery device |
JP2011127791A (en) * | 2009-12-15 | 2011-06-30 | Tlv Co Ltd | Waste steam recovering device |
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