JP2010216695A - Heat exchanger - Google Patents

Heat exchanger Download PDF

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JP2010216695A
JP2010216695A JP2009062284A JP2009062284A JP2010216695A JP 2010216695 A JP2010216695 A JP 2010216695A JP 2009062284 A JP2009062284 A JP 2009062284A JP 2009062284 A JP2009062284 A JP 2009062284A JP 2010216695 A JP2010216695 A JP 2010216695A
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steam
heat exchange
cooling fluid
vacuum pump
pump means
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JP2009062284A
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JP5384150B2 (en
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Tetsuya Mita
哲也 見田
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TLV Co Ltd
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TLV Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To obtain a heat exchanger capable of securely carrying out heat exchange between steam and cooling fluid. <P>SOLUTION: A steam supply pipe 2 and a cooling fluid supply pipe 3 are respectively connected to a heat exchanging container 1. A vacuum pump means 4 is arranged below the heat exchanging container 1 and connected to a condensate discharge pipe 7, and it is connected to an upper part of the heat exchanging container 1 via a communication pipe 8. The vacuum pump means 4 is formed using a circulation pump 11, an ejector 5, a cooling water tank 12, and a circulation passage 13. Inside of the heat exchanging container 1 is also sucked by suction force generated by a vacuum pump means 4 and made to be a decompression state not more than the atmospheric pressure, which can make a lot of steam flow from a steam generation source into the heat exchanging container 1. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、各種蒸気使用装置で使用され残った蒸気や、蒸気が凝縮した高温復水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、冷却流体と蒸気を熱交換して温度上昇した温水を別途使用することにより蒸気の保有熱を有効利用することのできる熱交換器に関する。  In the present invention, the remaining steam used in various steam-using devices and the re-evaporated steam generated from the high-temperature condensate in which the steam is condensed are exchanged by heat exchange with a cooling fluid such as water to condense with moyamoya. The present invention relates to a heat exchanger that can effectively use the retained heat of steam by eliminating steam or separately using hot water whose temperature has been increased by heat exchange between a cooling fluid and steam.

従来の熱交換器は、大気開放部にフィルター部を設けると共に、このフィルター部の出口側に第二の冷却流体供給部を配置したもので、熱交換すべき蒸気中に空気等の不凝縮気体が混入していても、フィルター部で蒸気や復水を捕捉し冷却することによって、外部へモヤモヤと立ち昇る蒸気を排出することがないものである。 A conventional heat exchanger is provided with a filter part in the atmosphere opening part and a second cooling fluid supply part arranged on the outlet side of the filter part, and non-condensable gas such as air in steam to be heat exchanged. Even if water is mixed in, the steam that rises to the outside will not be discharged by trapping and cooling the steam and condensate in the filter section.

上記従来の熱交換器では、蒸気の発生源と熱交換容器の間の圧力差が小さい場合に、あるいは、圧力差がほとんど無い場合に、熱交換容器へ蒸気がほとんど流入することができずに、熱交換容器で蒸気と冷却流体の熱交換を確実に行うことができない問題があった。 In the above conventional heat exchanger, when the pressure difference between the steam source and the heat exchange vessel is small, or when there is almost no pressure difference, almost no steam can flow into the heat exchange vessel. There is a problem in that heat exchange between the steam and the cooling fluid cannot be performed reliably in the heat exchange container.

特開平11−37668号公報JP-A-11-37668

解決しようとする問題点は、蒸気発生源の蒸気を熱交換容器へより多く流入させることによって、蒸気と冷却流体の熱交換を確実に行うことである。   The problem to be solved is to ensure heat exchange between the steam and the cooling fluid by allowing more steam from the steam generation source to flow into the heat exchange vessel.

本発明は、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、熱交換容器の内部を、循環ポンプとエゼクタと冷却水タンクからなる真空ポンプ手段と接続したものである。  In the present invention, steam and cooling fluid are supplied to a heat exchange container provided with an atmosphere opening part, and the steam is condensed by exchanging heat with the cooling fluid. The inside of the heat exchange container includes a circulation pump and an ejector. It is connected to a vacuum pump means comprising a cooling water tank.

本発明は、熱交換容器の内部を、循環ポンプとエゼクタと冷却水タンクからなる真空ポンプ手段と接続したことにより、この真空ポンプ手段で発生する吸引力でもって、熱交換容器の内部を吸引して大気圧以下の減圧状態とすることができ、蒸気発生源と熱交換容器の間の圧力差を充分に確保して、蒸気と冷却流体の熱交換を確実に行うことができるという利点がある。   According to the present invention, the inside of the heat exchange container is connected to the vacuum pump means including the circulation pump, the ejector, and the cooling water tank, so that the inside of the heat exchange container is sucked by the suction force generated by the vacuum pump means. The pressure can be reduced to below atmospheric pressure, and there is an advantage that the pressure difference between the steam generation source and the heat exchange vessel can be sufficiently secured, and the heat exchange between the steam and the cooling fluid can be performed reliably. .

本発明に係る熱交換器の実施例を示す構成図である。It is a block diagram which shows the Example of the heat exchanger which concerns on this invention.

本発明は、熱交換容器の内部を、真空ポンプ手段と接続したものであるが、真空ポンプ手段を駆動するための駆動流体としては水を使用することができる。 In the present invention, the inside of the heat exchange vessel is connected to the vacuum pump means, but water can be used as a driving fluid for driving the vacuum pump means.

図1において、円筒状の熱交換容器1と、蒸気源から熱交換容器1へ蒸気を供給する蒸気供給管2と、熱交換容器1へ冷却流体を供給する冷却流体供給管3と、熱交換容器1と接続した真空ポンプ手段4とで熱交換器を構成する。   In FIG. 1, a cylindrical heat exchange container 1, a steam supply pipe 2 for supplying steam from a steam source to the heat exchange container 1, a cooling fluid supply pipe 3 for supplying a cooling fluid to the heat exchange container 1, and heat exchange The vacuum pump means 4 connected to the container 1 constitutes a heat exchanger.

蒸気供給管2の左端部は、図示しない蒸気使用装置と接続する。熱交換容器1の上部中央部には、大気開放部としての大気開放管6を取り付けると共に、熱交換容器1の下部中央部には、蒸気が凝縮した復水を真空ポンプ手段4へ流下させる復水排出管7を取り付ける。熱交換容器1の内部構造は図示しないが、従来の熱交換容器と同様のものである。 The left end of the steam supply pipe 2 is connected to a steam using device (not shown). An air release pipe 6 serving as an air release part is attached to the upper central part of the heat exchange vessel 1, and a condensate condensed with steam flows down to the vacuum pump means 4 at the lower central part of the heat exchange vessel 1. A water discharge pipe 7 is attached. Although the internal structure of the heat exchange vessel 1 is not shown, it is the same as a conventional heat exchange vessel.

熱交換容器1の上端に連通管8を介して真空ポンプ手段4のエゼクタ5と接続する。また、熱交換容器1の右側面下部に、冷却流体としての冷却水を供給する冷却流体供給管3を接続する。冷却流体供給管3は、熱交換容器1の内部をコイル状に配置して、上端を冷却流体排出管10と接続する。冷却流体供給管3を分岐して、補給水管路17を接続する。 The upper end of the heat exchange vessel 1 is connected to the ejector 5 of the vacuum pump means 4 through the communication pipe 8. A cooling fluid supply pipe 3 that supplies cooling water as a cooling fluid is connected to the lower part of the right side surface of the heat exchange container 1. The cooling fluid supply pipe 3 arranges the inside of the heat exchange container 1 in a coil shape, and connects the upper end with the cooling fluid discharge pipe 10. The cooling fluid supply pipe 3 is branched and a makeup water pipe 17 is connected.

熱交換容器1の下端部の復水排出管7を、真空ポンプ手段4のエゼクタ5の吸込室9と接続する。真空ポンプ手段4を、循環ポンプ11とエゼクタ5と冷却水タンク12、及び、これらを連通する循環路13とで形成する。 The condensate discharge pipe 7 at the lower end of the heat exchange container 1 is connected to the suction chamber 9 of the ejector 5 of the vacuum pump means 4. The vacuum pump means 4 is formed by a circulation pump 11, an ejector 5, a cooling water tank 12, and a circulation path 13 that communicates these.

真空ポンプ手段4は、冷却水タンク12内の水を、循環ポンプ11が吸引してエゼクタ5へ吐出することにより、エゼクタ5の吸込室9に吸引力を発生するものである。  The vacuum pump means 4 generates a suction force in the suction chamber 9 of the ejector 5 when the circulating pump 11 sucks the water in the cooling water tank 12 and discharges it to the ejector 5.

吸込室9で吸引力を発生して、熱交換容器1の内部流体の一部も吸引されることによって、熱交換容器1の内部は大気圧以下の減圧状態となり、蒸気供給管2からの蒸気の多くが熱交換容器1内へ流入して、冷却流体と熱交換され、確実に復水となる。 A suction force is generated in the suction chamber 9, and a part of the internal fluid of the heat exchange container 1 is also sucked, so that the inside of the heat exchange container 1 is in a reduced pressure state below atmospheric pressure, and the steam from the steam supply pipe 2 Most of the water flows into the heat exchange vessel 1 and exchanges heat with the cooling fluid, so that condensate is reliably obtained.

蒸気を熱源として利用するさまざまな蒸気使用機器の蒸気回収装置として適用できる。   It can be applied as a steam recovery device for various steam-using equipment that uses steam as a heat source.

1 熱交換容器
2 蒸気供給管
3 冷却流体供給管
4 真空ポンプ手段
5 エゼクタ
6 大気開放感
7 復水排出管
9 吸込室
11 循環ポンプ
12 冷却水タンク
13 循環路
DESCRIPTION OF SYMBOLS 1 Heat exchange container 2 Steam supply pipe 3 Cooling fluid supply pipe 4 Vacuum pump means 5 Ejector 6 A feeling of openness to the atmosphere 7 Condensate discharge pipe 9 Suction chamber 11 Circulation pump 12 Cooling water tank 13 Circulation path

Claims (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、熱交換容器の内部を、循環ポンプとエゼクタと冷却水タンクからなる真空ポンプ手段と接続したことを特徴とする熱交換器。   Steam and cooling fluid are supplied to a heat exchange vessel provided with an atmosphere opening, and the vapor is condensed by exchanging heat with the cooling fluid. The inside of the heat exchange vessel is separated from the circulation pump, ejector, and cooling water tank. A heat exchanger characterized by being connected to a vacuum pump means.
JP2009062284A 2009-03-16 2009-03-16 Heat exchanger Active JP5384150B2 (en)

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JP5384150B2 JP5384150B2 (en) 2014-01-08

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102852785A (en) * 2011-06-29 2013-01-02 沈阳铝镁设计研究院有限公司 Water circulation system for sealing and cooling device
CN102997704A (en) * 2012-08-22 2013-03-27 张美玲 Industrial water vapor condenser
WO2014046147A1 (en) * 2012-09-20 2014-03-27 三菱重工業株式会社 Steam providing system and co2 recovery facilities provided with same
CN105135904A (en) * 2015-04-27 2015-12-09 温州泰丰竹业有限公司 Steam indirect heating hot water circulation system
KR20180051738A (en) * 2016-11-08 2018-05-17 제주대학교 산학협력단 A vacuum drying system and method using the same

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52154758U (en) * 1976-05-20 1977-11-24
JPS54156254A (en) * 1978-05-31 1979-12-10 Kato Yasuaki Cooling device of circulating water
JPS5787102U (en) * 1980-11-19 1982-05-29
JP2001066031A (en) * 1999-08-30 2001-03-16 Samson Co Ltd Vacuum cooler having vapor ejector by-pass route
JP2008045787A (en) * 2006-08-11 2008-02-28 Tlv Co Ltd Evaporative cooling device
JP2008286430A (en) * 2007-05-15 2008-11-27 Tlv Co Ltd Heat exchanger

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52154758U (en) * 1976-05-20 1977-11-24
JPS54156254A (en) * 1978-05-31 1979-12-10 Kato Yasuaki Cooling device of circulating water
JPS5787102U (en) * 1980-11-19 1982-05-29
JP2001066031A (en) * 1999-08-30 2001-03-16 Samson Co Ltd Vacuum cooler having vapor ejector by-pass route
JP2008045787A (en) * 2006-08-11 2008-02-28 Tlv Co Ltd Evaporative cooling device
JP2008286430A (en) * 2007-05-15 2008-11-27 Tlv Co Ltd Heat exchanger

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102852785A (en) * 2011-06-29 2013-01-02 沈阳铝镁设计研究院有限公司 Water circulation system for sealing and cooling device
CN102997704A (en) * 2012-08-22 2013-03-27 张美玲 Industrial water vapor condenser
WO2014046147A1 (en) * 2012-09-20 2014-03-27 三菱重工業株式会社 Steam providing system and co2 recovery facilities provided with same
JP5897142B2 (en) * 2012-09-20 2016-03-30 三菱重工業株式会社 Steam supply system and CO2 recovery equipment equipped with the same
US10195561B2 (en) 2012-09-20 2019-02-05 Mitsubishi Heavy Industries Engineering, Ltd. Steam supply system and CO2 recovery unit including the same
CN105135904A (en) * 2015-04-27 2015-12-09 温州泰丰竹业有限公司 Steam indirect heating hot water circulation system
KR20180051738A (en) * 2016-11-08 2018-05-17 제주대학교 산학협력단 A vacuum drying system and method using the same
KR101874300B1 (en) * 2016-11-08 2018-07-09 제주대학교 산학협력단 A vacuum drying system and method using the same

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