JP2006136848A - Heat exchange apparatus - Google Patents

Heat exchange apparatus Download PDF

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Publication number
JP2006136848A
JP2006136848A JP2004330421A JP2004330421A JP2006136848A JP 2006136848 A JP2006136848 A JP 2006136848A JP 2004330421 A JP2004330421 A JP 2004330421A JP 2004330421 A JP2004330421 A JP 2004330421A JP 2006136848 A JP2006136848 A JP 2006136848A
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steam
pipe
heat exchanger
heat exchange
gas
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Japanese (ja)
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Masakatsu Okamoto
雅克 岡本
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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 provide a heat exchange apparatus capable of forcibly circulating a part of steam through a heat exchanger without using a steam ejector. <P>SOLUTION: A steam supplying pipe 2 and a fluid discharging pipe 3 are connected to the heat exchanger 1. A control valve 7 is installed on the steam supplying pipe 2. The fluid discharging pipe 3 is connected to a gas-liquid separator 6. A circulating steam pipe 10 is connected to a steam blower 5. A suction unit 4 is connected to the lower part of the gas-liquid separator 6 while interposing a steam trap 15 between them. A part of the steam supplied to a jacket part 9 of the heat exchanger from the steam supplying pipe 2 is condensed and becomes a condensation. The mixed fluid of the condensation with a part of steam falls into the gas-liquid separator 6 through the fluid discharging pipe 3. Only the steam separated from the condensation in the gas-liquid separator 6 is circulated forcibly into the jacket part 9 through the circulating steam pipe 10 by the steam blower 5. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、蒸気を熱源として、熱交換器内で被加熱物を加熱する熱交換装置に関する。   The present invention relates to a heat exchange apparatus that heats an object to be heated in a heat exchanger using steam as a heat source.

熱交換装置は、熱交換器に蒸気供給管と流体排出管を接続して、この流体排出管にエゼクタ装置を接続することにより、熱交換器で熱交換によって蒸気の凝縮した復水と一部の残存蒸気とを、エゼクタ装置で吸引するものである。   The heat exchange device connects the steam supply pipe and the fluid discharge pipe to the heat exchanger, and connects the ejector device to the fluid discharge pipe, so that a part of the condensate in which the steam is condensed by heat exchange in the heat exchanger. The remaining steam is sucked by the ejector device.

この熱交換装置においては、熱交換器での蒸気消費量が変動した場合に、熱交換器内の蒸気の圧力や温度が大きく変動してしまう問題があった。通常、エゼクタ装置の駆動蒸気量と吸引流体量の間には所定の関係があり、ある一定の吸引流体量を確保するためには所定量の駆動蒸気が必要となり、この必要駆動蒸気量よりも熱交換器の蒸気消費量が下回ってしまった場合には熱交換器内の蒸気の圧力や温度が大きく変動してしまうのである。
特開平2−213601号公報
In this heat exchange device, when the steam consumption in the heat exchanger fluctuates, there is a problem that the pressure and temperature of the steam in the heat exchanger fluctuate greatly. In general, there is a predetermined relationship between the drive steam amount and the suction fluid amount of the ejector device, and a predetermined amount of drive steam is required to secure a certain amount of suction fluid. If the steam consumption of the heat exchanger falls below, the steam pressure and temperature in the heat exchanger will fluctuate greatly.
JP-A-2-213601

解決しようとする課題は、蒸気圧力や温度の変動をもたらすエゼクタ装置を用いることなく、一部の蒸気を熱交換器へ循環させることのできる熱交換装置を提供することである。   The problem to be solved is to provide a heat exchange device that can circulate a part of steam to a heat exchanger without using an ejector device that causes fluctuations in steam pressure and temperature.

本発明は、熱交換器に蒸気供給管と流体排出管を接続して、当該蒸気供給管から供給した蒸気でもって熱交換を行い、熱交換によって蒸気が凝縮した復水を流体排出管から吸引装置で吸引するものにおいて、流体排出管から一部の蒸気を熱交換器へ循環する電動蒸気循環手段を取り付けて、蒸気供給管から熱交換器へ供給する蒸気を熱交換面の全体に供給する蒸気噴出部を配置すると共に、当該蒸気噴出部を噴出蒸気が熱交換面に向けて噴出される方向に取り付けたことを特徴とする。   The present invention connects a steam supply pipe and a fluid discharge pipe to a heat exchanger, performs heat exchange with the steam supplied from the steam supply pipe, and sucks condensate condensed by the heat exchange from the fluid discharge pipe. In what is sucked by the device, electric steam circulation means for circulating a part of the steam from the fluid discharge pipe to the heat exchanger is attached, and the steam supplied from the steam supply pipe to the heat exchanger is supplied to the entire heat exchange surface. The steam ejecting portion is disposed, and the steam ejecting portion is attached in a direction in which the ejected steam is ejected toward the heat exchange surface.

本発明の熱交換装置は、流体排出管に電動蒸気循環手段を取り付けたことにより、この電動蒸気循環手段によって一部の蒸気を熱交換器内へ循環させることができる。   In the heat exchange device of the present invention, by attaching the electric steam circulation means to the fluid discharge pipe, a part of the steam can be circulated into the heat exchanger by the electric steam circulation means.

本発明は、電動蒸気循環手段を取り付けるものであり、この電動蒸気循環手段としては、蒸気ブロワーや蒸気コンプレッサー等、従来から使用されているものを用いることができる。   In the present invention, an electric steam circulation means is attached. As this electric steam circulation means, those conventionally used such as a steam blower and a steam compressor can be used.

図1は、本発明の1実施例の構成図であって、熱交換器1と蒸気供給管2と流体排出管3と吸引装置4と電動蒸気循環手段5、及び、蒸気噴出部11とで熱交換装置を構成する。   FIG. 1 is a configuration diagram of one embodiment of the present invention, which includes a heat exchanger 1, a steam supply pipe 2, a fluid discharge pipe 3, a suction device 4, an electric steam circulation means 5, and a steam ejection section 11. A heat exchange device is configured.

熱交換器1は反応釜8とジャケット部9とで構成して、ジャケット部9へ加熱用の蒸気を供給する蒸気供給管2には、蒸気の供給量を制御するための制御弁7を取り付ける。蒸気供給管2のジャケット部9側端部に蒸気噴出部11を設ける。本実施例の蒸気噴出部11は断面正方形のリング状で、反応釜8上部の全周に配置すると共に、下端部25から反応釜8の外周で且つ斜め下方(矢印26で示す方向)へ蒸気が噴出されるように噴出孔を全周にわたって均等に配置する。   The heat exchanger 1 includes a reaction kettle 8 and a jacket portion 9, and a control valve 7 for controlling the supply amount of steam is attached to the steam supply pipe 2 that supplies steam for heating to the jacket portion 9. . A steam ejection part 11 is provided at the end of the steam supply pipe 2 on the jacket part 9 side. The steam ejection part 11 of the present embodiment has a ring shape with a square cross section, and is disposed on the entire circumference of the upper part of the reaction vessel 8, and is steamed downward (in the direction indicated by the arrow 26) from the lower end part 25 to the outer circumference of the reaction vessel 8. The spray holes are evenly arranged over the entire circumference so as to be ejected.

ジャケット部9の下部に流体排出管3を接続して気液分離器6を取り付ける。気液分離器6は、流体排出管3の通路面積を急拡大したタンク形状のもので、流体排出管3を流下する復水と蒸気、及び、復水の一部が再蒸発した再蒸発蒸気との混合流体から気液を分離することができるものである。気液分離器6の上部に、気液分離された蒸気を電動蒸気循環手段としての蒸気ブロワー5へ導く循環蒸気管10を接続する。   The fluid discharge pipe 3 is connected to the lower part of the jacket part 9 and the gas-liquid separator 6 is attached. The gas-liquid separator 6 has a tank shape in which the passage area of the fluid discharge pipe 3 is rapidly expanded, and condensate and steam flowing down the fluid discharge pipe 3 and re-evaporated steam in which a part of the condensate is re-evaporated. The gas-liquid can be separated from the mixed fluid. Connected to the upper part of the gas-liquid separator 6 is a circulating steam pipe 10 that guides the vapor separated into the steam blower 5 as electric steam circulating means.

蒸気ブロワー5の吸引部に循環蒸気管10と気液分離器6とを介して流体排出管3を接続する。循環蒸気管10には制御弁13を取り付ける。蒸気ブロワー5の回転によって、循環蒸気管10と後述する連通管22からの蒸気を蒸気供給管2へ循環供給することができる。   The fluid discharge pipe 3 is connected to the suction part of the steam blower 5 through the circulation steam pipe 10 and the gas-liquid separator 6. A control valve 13 is attached to the circulation steam pipe 10. By the rotation of the steam blower 5, steam from the circulation steam pipe 10 and a communication pipe 22 described later can be circulated and supplied to the steam supply pipe 2.

気液分離器6の下部には、開閉弁14と並列に、蒸気は排出することがなく復水だけを排出する機能を有する蒸気トラップ15を接続する。蒸気トラップ15の出口は吸引装置4と接続する。   A steam trap 15 having a function of discharging only condensate without discharging steam is connected to the lower part of the gas-liquid separator 6 in parallel with the on-off valve 14. The outlet of the steam trap 15 is connected to the suction device 4.

吸引装置4は、エゼクタ16とタンク17と循環ポンプ18とを循環路19で連結して構成する。タンク17の上部には冷却水を補給する冷却水補給管20を接続し、循環蒸気管10と連通する連通管22を接続する。連通管22には調節弁23を取り付ける。また、循環路19の一部を分岐して余剰水排出管21を接続する。   The suction device 4 is configured by connecting an ejector 16, a tank 17, and a circulation pump 18 with a circulation path 19. A cooling water supply pipe 20 for supplying cooling water is connected to the upper portion of the tank 17, and a communication pipe 22 communicating with the circulation steam pipe 10 is connected. A control valve 23 is attached to the communication pipe 22. Further, a part of the circulation path 19 is branched and the surplus water discharge pipe 21 is connected.

反応釜8を加熱する場合、蒸気供給管2と蒸気噴出部11から所定圧力の蒸気をジャケット部9内へ供給する。ジャケット部9で反応釜8に熱を奪われた蒸気は凝縮して復水となり、流体排出管3から気液分離器6へ流下して気液が分離され、復水の分離された蒸気だけが循環蒸気管10から蒸気ブロワー5へ吸引され、再度ジャケット部9へ供給されることによって、加熱用の蒸気は強制的に循環される。   When the reaction kettle 8 is heated, steam of a predetermined pressure is supplied from the steam supply pipe 2 and the steam ejection part 11 into the jacket part 9. The steam that has been deprived of heat in the reaction vessel 8 by the jacket portion 9 condenses into condensate, and flows down from the fluid discharge pipe 3 to the gas-liquid separator 6 to separate the gas and liquid. Is sucked into the steam blower 5 from the circulation steam pipe 10 and supplied to the jacket portion 9 again, whereby the heating steam is forcibly circulated.

蒸気噴出部11から反応釜8の全周へ且つ斜め下方へ蒸気が噴出されることによって、反応釜8の外表面に付着し下方へ流下する復水を吹き飛ばして除去すると共に、残存復水の流下速度も速めることができて、蒸気と反応釜8外表面との間の熱伝達を促進して熱交換効率を高めることができる。   Steam is ejected from the steam ejection portion 11 to the entire circumference of the reaction vessel 8 and obliquely downward, so that the condensate adhering to the outer surface of the reaction vessel 8 and flowing downward is blown off and removed, and the remaining condensate is removed. The flow speed can be increased, heat transfer between the steam and the outer surface of the reaction vessel 8 can be promoted, and the heat exchange efficiency can be increased.

吸引装置4は、タンク17内の水を循環ポンプ18によってエゼクタ16へ循環させることによって、エゼクタ16で吸引力を発生するものである。気液分離器6で分離された液体としての復水は、蒸気トラップ15を通過して吸引装置4のエゼクタ16に吸引されタンク17に至る。タンク17で高温復水から再び蒸発した再蒸発蒸気は、調節弁23、13と連通管22を通って蒸気ブロワー5へ吸引される。   The suction device 4 generates suction force by the ejector 16 by circulating water in the tank 17 to the ejector 16 by the circulation pump 18. Condensate as a liquid separated by the gas-liquid separator 6 passes through the steam trap 15 and is sucked into the ejector 16 of the suction device 4 and reaches the tank 17. The re-evaporated steam evaporated again from the high-temperature condensate in the tank 17 is sucked into the steam blower 5 through the control valves 23 and 13 and the communication pipe 22.

本発明の熱交換装置の実施例を示す構成図。The block diagram which shows the Example of the heat exchange apparatus of this invention.

符号の説明Explanation of symbols

1 熱交換器
2 蒸気供給管
3 流体排出管
4 吸引装置
5 蒸気ブロワー
6 気液分離器
8 反応釜
9 ジャケット部
10 循環蒸気管
11 蒸気噴出部

DESCRIPTION OF SYMBOLS 1 Heat exchanger 2 Steam supply pipe 3 Fluid discharge pipe 4 Suction apparatus 5 Steam blower 6 Gas-liquid separator 8 Reactor 9 Jacket part 10 Circulating steam pipe 11 Steam ejection part

Claims (1)

熱交換器に蒸気供給管と流体排出管を接続して、当該蒸気供給管から供給した蒸気でもって熱交換を行い、熱交換によって蒸気が凝縮した復水を流体排出管から吸引装置で吸引するものにおいて、流体排出管から一部の蒸気を熱交換器へ循環する電動蒸気循環手段を取り付けて、蒸気供給管から熱交換器へ供給する蒸気を熱交換面の全体に供給する蒸気噴出部を配置すると共に、当該蒸気噴出部を噴出蒸気が熱交換面に向けて噴出される方向に取り付けたことを特徴とする熱交換装置。
A steam supply pipe and a fluid discharge pipe are connected to the heat exchanger, heat is exchanged with the steam supplied from the steam supply pipe, and condensate condensed by the heat exchange is sucked from the fluid discharge pipe with a suction device. In the apparatus, an electric steam circulation means for circulating a part of the steam from the fluid discharge pipe to the heat exchanger is attached, and a steam jet part for supplying the steam supplied from the steam supply pipe to the heat exchanger over the entire heat exchange surface is provided. A heat exchanging apparatus characterized in that the steam ejecting portion is disposed in a direction in which the ejected steam is ejected toward the heat exchange surface.
JP2004330421A 2004-11-15 2004-11-15 Heat exchange apparatus Pending JP2006136848A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009250582A (en) * 2008-04-10 2009-10-29 Kobe Steel Ltd Boiler blowdown energy recovery system
JP2011062596A (en) * 2009-09-15 2011-03-31 Tlv Co Ltd Steam heater
CN102886234A (en) * 2012-09-14 2013-01-23 横店集团浙江英洛华硅材料有限公司 Improved structure of purification kettle
CN106824008A (en) * 2017-03-13 2017-06-13 苏州安利化工有限公司 Unpacked instrument and the quick feeding method of reactor for the heat that reactor quickly feeds intake

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63217191A (en) * 1987-03-05 1988-09-09 Chiyoda Chem Eng & Constr Co Ltd Heat exchanging method of tank and tank with jacket type heat exchanger
JPH0361275U (en) * 1989-10-13 1991-06-17
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JP2004160908A (en) * 2002-11-15 2004-06-10 Tlv Co Ltd Steam heating apparatus

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63217191A (en) * 1987-03-05 1988-09-09 Chiyoda Chem Eng & Constr Co Ltd Heat exchanging method of tank and tank with jacket type heat exchanger
JPH0361275U (en) * 1989-10-13 1991-06-17
JPH04369302A (en) * 1991-06-14 1992-12-22 Tlv Co Ltd Vacuum steam generating device
JP2004160908A (en) * 2002-11-15 2004-06-10 Tlv Co Ltd Steam heating apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009250582A (en) * 2008-04-10 2009-10-29 Kobe Steel Ltd Boiler blowdown energy recovery system
JP2011062596A (en) * 2009-09-15 2011-03-31 Tlv Co Ltd Steam heater
CN102886234A (en) * 2012-09-14 2013-01-23 横店集团浙江英洛华硅材料有限公司 Improved structure of purification kettle
CN106824008A (en) * 2017-03-13 2017-06-13 苏州安利化工有限公司 Unpacked instrument and the quick feeding method of reactor for the heat that reactor quickly feeds intake

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