JP4722665B2 - Steam desuperheater - Google Patents

Steam desuperheater Download PDF

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JP4722665B2
JP4722665B2 JP2005300190A JP2005300190A JP4722665B2 JP 4722665 B2 JP4722665 B2 JP 4722665B2 JP 2005300190 A JP2005300190 A JP 2005300190A JP 2005300190 A JP2005300190 A JP 2005300190A JP 4722665 B2 JP4722665 B2 JP 4722665B2
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steam
cooling fluid
temperature
heat exchange
ejector
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JP2007107839A (en
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鎮麿 大石
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Tlv Co Ltd
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Description

本発明は、高温状態の蒸気を、所定の温度例えば飽和蒸気温度まで減温することのできる蒸気減温装置に関する。   The present invention relates to a steam temperature reducing apparatus capable of reducing the temperature of steam in a high temperature state to a predetermined temperature, for example, a saturated steam temperature.

蒸気減温装置は、過熱状態の高温蒸気に、冷却水等の冷却流体を供給して所定の温度まで蒸気を減温させるものである。   The steam temperature reducing device supplies a cooling fluid such as cooling water to overheated high temperature steam to reduce the temperature of the steam to a predetermined temperature.

この蒸気減温装置においては、加熱容器の二次側のドレン(復水)すなわち液体を冷却流体として、高温蒸気と接触させて蒸気の温度を減温するために、高温蒸気の全体が均一に減温されずに、減温蒸気に温度ムラを生じてしまう問題点があった。すなわち、高温蒸気にノズル等を介して冷却水を供給しても、蒸気と水滴が全体に且つ均一に混合されずに温度ムラを生じるのである。
特公平7−88933号公報
In this steam temperature reducing device, the secondary side drain (condensate) of the heating container, that is, the liquid, is used as a cooling fluid to contact the high temperature steam to reduce the temperature of the steam. There has been a problem that temperature unevenness occurs in the reduced temperature steam without being reduced in temperature. That is, even if the cooling water is supplied to the high-temperature steam through a nozzle or the like, the steam and water droplets are not mixed uniformly and entirely, resulting in temperature unevenness.
Japanese Patent Publication No. 7-88933

解決しようとする課題は、高温蒸気と冷却流体が全体に且つ均一に混合されて、減温蒸気に温度ムラを生じることのない蒸気減温装置を提供することである。   The problem to be solved is to provide a steam temperature reducing device in which the high temperature steam and the cooling fluid are uniformly and uniformly mixed so as not to cause temperature unevenness in the temperature reduced steam.

本発明は、高温蒸気中へ冷却流体を供給して、当該高温蒸気を所定温度状態まで減温するものにおいて、高温蒸気供給管に蒸気エゼクタを取り付けて、当該蒸気エゼクタを二重管構造として、当該二重管構造の内側を蒸気の流下するエゼクタ通路とし、二重管構造の外側を冷却流体が熱交換されて低温蒸気となる熱交換部として、当該外側の熱交換部の上端部に管路を取り付けて蒸気エゼクタの吸引口と接続すると共に、当該外側の熱交換部の下部に連通管を介して冷却流体タンクと接続し、当該連通管の冷却流体タンクの手前側に蒸気トラップを取り付け、当該冷却流体タンクの下部側面に循環路を取り付けて循環ポンプを接続し、当該循環路の上端を冷却流体供給管として、当該冷却流体供給管に外側の熱交換部へ供給する冷却流体の量をコントロールするための制御バルブを取り付けて、当該熱交換部で発生した低温蒸気を蒸気エゼクタの吸引口から高温蒸気中へ供給すると共に、熱交換部へ供給される冷却流体を所定温度まで加熱する冷却流体加熱部を設けて、当該冷却流体加熱部を上記循環路と連通したものである。 In the present invention, a cooling fluid is supplied into high-temperature steam to reduce the temperature of the high-temperature steam to a predetermined temperature state.A steam ejector is attached to the high-temperature steam supply pipe, and the steam ejector has a double-pipe structure. the inside of the double pipe structure and the ejector passage flowing down of steam, as a heat exchange unit comprising a low-temperature steam outside the cooling fluid is the heat exchange of the double tube structure, the tube to the upper end of the heat exchange portion of the outer Attach a passage to connect to the suction port of the steam ejector, connect to the cooling fluid tank through the communication pipe at the bottom of the outer heat exchange section, and attach a steam trap to the front side of the cooling fluid tank of the communication pipe The amount of the cooling fluid to be supplied to the outer heat exchanging portion to the cooling fluid supply pipe, with the circulation path attached to the lower side surface of the cooling fluid tank and connected to the circulation pump, with the upper end of the circulation path as the cooling fluid supply pipe Attaching a control valve for controlling to heat the low-temperature steam generated in the heat exchange unit is supplied from the suction port of the steam ejector into the hot vapor and the cooling fluid supplied to the heat exchanger to a predetermined temperature cooled A fluid heating unit is provided, and the cooling fluid heating unit communicates with the circulation path .

本発明の蒸気減温装置は、二重管構造の外側の熱交換部で高温蒸気と冷却流体が熱交換されて、冷却流体が蒸発して低温蒸気となり、蒸気エゼクタで高温蒸気と混合されることにより、高温蒸気と低温蒸気という蒸気同士のすみやかな混合となって、高温蒸気を温度ムラなく減温することができる。また、熱交換部へ供給される冷却流体を所定温度まで加熱する冷却流体加熱部を設けたことにより、熱交換部へ供給される冷却流体の温度が上昇して、熱交換部へ供給されると冷却流体が直ちに気化して低温蒸気となることによって、低温蒸気の発生効率を高めることができる。   In the steam temperature reducing device of the present invention, the high-temperature steam and the cooling fluid are heat-exchanged in the heat exchange section outside the double-pipe structure, the cooling fluid is evaporated to become low-temperature steam, and mixed with the high-temperature steam in the steam ejector. By this, it becomes quick mixing of the steam of high temperature steam and low temperature steam, and high temperature steam can be reduced in temperature without unevenness. Further, by providing a cooling fluid heating unit that heats the cooling fluid supplied to the heat exchange unit to a predetermined temperature, the temperature of the cooling fluid supplied to the heat exchange unit rises and is supplied to the heat exchange unit. As the cooling fluid is immediately vaporized into low-temperature steam, the generation efficiency of low-temperature steam can be increased.

本発明は、二重管構造の外側の熱交換部で高温蒸気と冷却流体が熱交換されて、冷却流体を蒸発させて低温蒸気を発生するものであり、この熱交換部での高温蒸気と冷却流体との熱交換は、間接的に高温蒸気と冷却流体が熱交換するものが好ましい。   The present invention heat-exchanges the high-temperature steam and the cooling fluid in the heat exchange section outside the double-pipe structure, and evaporates the cooling fluid to generate low-temperature steam. The heat exchange with the cooling fluid is preferably such that the high-temperature steam and the cooling fluid indirectly exchange heat.

図1は、本発明の1実施例の構成図であって、過熱状態の高温蒸気が左側から右側へ流下する高温蒸気供給管1と、冷却流体加熱部8、および、二重管構造の蒸気エゼクタ2とで蒸気減温装置を構成する。   FIG. 1 is a configuration diagram of an embodiment of the present invention, in which a high-temperature steam supply pipe 1 in which superheated high-temperature steam flows down from the left side to the right side, a cooling fluid heating unit 8, and a double-pipe structure steam. The ejector 2 constitutes a steam temperature reducing device.

二重管構造の蒸気エゼクタ2は、内側の通路4に冷却流体加熱部8を介在して高温蒸気供給管1と接続したエゼクタ通路とすると共に、外側の密閉状の空間5を熱交換部とする。外側の熱交換部5の上部に後述する冷却流体供給管6を接続する。図示はしないが、冷却流体供給管6の熱交換部5内の端部には、冷却流体を熱交換部5内へ噴霧するスプレーノズルを取り付ける。内側のエゼクタ通路4の出口側には、所定温度まで減温された蒸気を減温蒸気使用箇所へと流下させる減温蒸気管7を接続する。   The steam ejector 2 having a double pipe structure is an ejector passage connected to the high-temperature steam supply pipe 1 via the cooling fluid heating portion 8 in the inner passage 4 and the outer sealed space 5 as a heat exchange portion. To do. A cooling fluid supply pipe 6 to be described later is connected to the upper part of the outer heat exchange section 5. Although not shown, a spray nozzle for spraying the cooling fluid into the heat exchange unit 5 is attached to the end of the cooling fluid supply pipe 6 in the heat exchange unit 5. Connected to the outlet side of the inner ejector passage 4 is a temperature-reducing steam pipe 7 that causes the steam, which has been reduced in temperature to a predetermined temperature, to flow down to the location where the temperature-reducing steam is used.

外側の熱交換部5の上端部に管路3を取り付けて蒸気エゼクタ2の吸引口14と接続する。管路3には逆止弁17を取り付ける。逆止弁17は、外側の熱交換部5から吸引口14への流体の流下だけを許容し、反対方向の流体の通過を阻止するものである。   The pipe line 3 is attached to the upper end portion of the outer heat exchanging portion 5 and connected to the suction port 14 of the steam ejector 2. A check valve 17 is attached to the pipeline 3. The check valve 17 allows only the flow of fluid from the outer heat exchange section 5 to the suction port 14 and prevents passage of fluid in the opposite direction.

熱交換部5の下部には、熱交換部5内と連通した連通管11を接続して下方に配置した冷却流体タンク12と接続する。連通管11のタンク12の手前側には蒸気トラップ13を取り付ける。蒸気トラップ13は、連通管11内を流下してくる冷却流体と冷却流体の蒸発した低温蒸気との混合流体の内で、液体としての冷却流体だけをタンク12側へ通過排出し、気体としての低温蒸気は通過させることがないものである。 A communication pipe 11 communicating with the inside of the heat exchange unit 5 is connected to a lower part of the heat exchange unit 5 and connected to a cooling fluid tank 12 disposed below. A steam trap 13 is attached to the front side of the tank 12 of the communication pipe 11. The steam trap 13 passes and discharges only the cooling fluid as a liquid to the tank 12 side in the mixed fluid of the cooling fluid flowing down in the communication pipe 11 and the low-temperature steam evaporated from the cooling fluid, Low temperature steam is not allowed to pass through.

冷却流体タンク12には、上部に冷却流体例えば冷却水を補給する冷却流体補給管18を接続して、タンク12内部に所定量の冷却流体20を溜め置く。冷却流体補給管18には、管路を開閉することのできる開閉バルブ19を取り付ける。   A cooling fluid supply pipe 18 for supplying a cooling fluid such as cooling water is connected to the cooling fluid tank 12 at an upper portion, and a predetermined amount of the cooling fluid 20 is stored inside the tank 12. The cooling fluid supply pipe 18 is provided with an open / close valve 19 that can open and close the pipe line.

冷却流体タンク12の下部側面には循環路22を取り付けて循環ポンプ21を接続する。循環路22に冷却流体加熱部8を連通し、更にその上端を冷却流体供給管6とする。冷却流体加熱部8は、密閉円筒状タンクであり、その内部に冷却流体供給管6の一部がコイル状9に配置され、左側の高温蒸気供給管1から蒸気エゼクタ2へ供給される高温蒸気の一部の熱がコイル状冷却流体供給管9で冷却流体へ与えられることによって、冷却流体の温度を所定値まで昇温することができるものである。   A circulation path 22 is attached to the lower side surface of the cooling fluid tank 12 and a circulation pump 21 is connected thereto. The cooling fluid heating unit 8 is communicated with the circulation path 22, and the upper end thereof is referred to as a cooling fluid supply pipe 6. The cooling fluid heating unit 8 is a sealed cylindrical tank, in which a part of the cooling fluid supply pipe 6 is arranged in a coil shape 9, and the high temperature steam supplied from the high temperature steam supply pipe 1 on the left side to the steam ejector 2. Is provided to the cooling fluid through the coiled cooling fluid supply pipe 9, whereby the temperature of the cooling fluid can be raised to a predetermined value.

冷却流体タンク12の右下部側面に余剰流体排出管23を接続する。余剰流体排出管23には開閉バルブ24を取り付け、一方、冷却流体供給管6には、外側の熱交換部5へ供給する冷却流体の量をコントロールするための制御バルブ25を取り付ける。 An excess fluid discharge pipe 23 is connected to the lower right side surface of the cooling fluid tank 12. An opening / closing valve 24 is attached to the surplus fluid discharge pipe 23, while a control valve 25 is attached to the cooling fluid supply pipe 6 for controlling the amount of cooling fluid supplied to the outer heat exchange unit 5.

高温蒸気供給管1を左側から右側へ向かって流下する高温蒸気が、蒸気エゼクタ2の内側のエゼクタ通路4内を流下することによって吸引力が発生して、吸引口14から管路3と外側の熱交換部5の流体を吸引する。この吸引力によって熱交換部5内は、大気圧よりも低圧の真空圧力状態となる。従って、冷却流体供給管6から熱交換部5内へ供給される所定温度まで昇温した冷却流体20は、内側のエゼクタ通路4を流下する高温蒸気の一部の熱を奪ってただちに蒸発して低温蒸気となる。このように、高温蒸気と冷却流体が蒸気エゼクタ2で熱交換することによって、高温蒸気は一定の温度だけ温度低下する。   The high-temperature steam that flows down from the left side to the right side of the high-temperature steam supply pipe 1 flows through the ejector passage 4 inside the steam ejector 2, thereby generating a suction force. The fluid in the heat exchange unit 5 is sucked. Due to this suction force, the inside of the heat exchanging unit 5 is in a vacuum pressure state lower than the atmospheric pressure. Therefore, the cooling fluid 20 heated to the predetermined temperature supplied from the cooling fluid supply pipe 6 into the heat exchanging section 5 takes away the heat of a part of the high-temperature steam flowing down the inner ejector passage 4 and immediately evaporates. It becomes low temperature steam. As described above, the high temperature steam and the cooling fluid exchange heat with the steam ejector 2, so that the temperature of the high temperature steam is lowered by a certain temperature.

熱交換部5で発生した低温蒸気は、逆止弁17を通って蒸気エゼクタ2の吸引口14へ吸引され、高温蒸気供給管1から流下してきた高温蒸気と混合されて所定温度まで減温されて減温蒸気管7を流下する。このように、高温蒸気と低温蒸気を、蒸気エゼクタ2で混合することによって、高温蒸気の全体に低温蒸気が行き渡り、減温蒸気の温度ムラを防止することができる。 The low temperature steam generated in the heat exchanging section 5 is sucked into the suction port 14 of the steam ejector 2 through the check valve 17, mixed with the high temperature steam flowing down from the high temperature steam supply pipe 1, and reduced in temperature to a predetermined temperature. The temperature-reducing steam pipe 7 flows down. In this way, by mixing the high temperature steam and the low temperature steam with the steam ejector 2, the low temperature steam is spread over the entire high temperature steam, and temperature unevenness of the reduced temperature steam can be prevented.

外側の熱交換部5へ供給する冷却流体の量は、制御バルブ25のバルブ開度を適宜調節することによって、任意に制御することができる。また、熱交換部5へ供給する冷却流体の温度は、冷却流体加熱部8によって、同じく任意に制御することができる。 The amount of the cooling fluid supplied to the outer heat exchange unit 5 can be arbitrarily controlled by appropriately adjusting the valve opening of the control valve 25. Further, the temperature of the cooling fluid supplied to the heat exchange unit 5 can be arbitrarily controlled by the cooling fluid heating unit 8 as well.

本発明の蒸気減温装置の実施例を示す構成図。The block diagram which shows the Example of the steam temperature decreasing apparatus of this invention.

符号の説明Explanation of symbols

1 高温蒸気供給管
2 蒸気エゼクタ
4 内側のエゼクタ通路
5 外側の熱交換部
6 冷却流体供給管
7 減温蒸気管
8 冷却流体加熱部
12 冷却流体タンク
13 蒸気トラップ
14 吸引口
17 逆止弁
18 冷却流体補給管
21 循環ポンプ
22 循環路
25 制御バルブ
DESCRIPTION OF SYMBOLS 1 High temperature steam supply pipe 2 Steam ejector 4 Inner ejector passage 5 Outer heat exchange part 6 Cooling fluid supply pipe 7 Temperature-reducing steam pipe 8 Cooling fluid heating part 12 Cooling fluid tank 13 Steam trap 14 Suction port 17 Check valve 18 Cooling Fluid supply pipe 21 Circulation pump 22 Circulation path 25 Control valve

Claims (1)

高温蒸気中へ冷却流体を供給して、当該高温蒸気を所定温度状態まで減温するものにおいて、高温蒸気供給管に蒸気エゼクタを取り付けて、当該蒸気エゼクタを二重管構造として、当該二重管構造の内側を蒸気の流下するエゼクタ通路とし、二重管構造の外側を冷却流体が熱交換されて低温蒸気となる熱交換部として、当該外側の熱交換部の上端部に管路を取り付けて蒸気エゼクタの吸引口と接続すると共に、当該外側の熱交換部の下部に連通管を介して冷却流体タンクと接続し、当該連通管の冷却流体タンクの手前側に蒸気トラップを取り付け、当該冷却流体タンクの下部側面に循環路を取り付けて循環ポンプを接続し、当該循環路の上端を冷却流体供給管として、当該冷却流体供給管に外側の熱交換部へ供給する冷却流体の量をコントロールするための制御バルブを取り付けて、当該熱交換部で発生した低温蒸気を蒸気エゼクタの吸引口から高温蒸気中へ供給すると共に、熱交換部へ供給される冷却流体を所定温度まで加熱する冷却流体加熱部を設けて、当該冷却流体加熱部を上記循環路と連通したことを特徴とする蒸気減温装置。 A cooling fluid is supplied into the high temperature steam to reduce the temperature of the high temperature steam to a predetermined temperature state. A steam ejector is attached to the high temperature steam supply pipe, the steam ejector has a double pipe structure, and the double pipe The inside of the structure is an ejector passage where the steam flows down, and the outside of the double pipe structure is a heat exchange part in which the cooling fluid is heat-exchanged into low-temperature steam, and a pipe line is attached to the upper end of the outside heat exchange part Connected to the suction port of the steam ejector, connected to a cooling fluid tank via a communication pipe at the lower part of the outer heat exchange section, and attached a steam trap on the front side of the cooling fluid tank of the communication pipe. A circulation path is attached to the lower side of the tank and a circulation pump is connected. The upper end of the circulation path is used as a cooling fluid supply pipe, and the amount of cooling fluid supplied to the heat exchange section on the outside is controlled by the cooling fluid supply pipe. Attach the control valve to Le, heating the low-temperature steam generated in the heat exchange unit is supplied from the suction port of the steam ejector into the hot vapor and the cooling fluid supplied to the heat exchanger to a predetermined temperature cooled A steam temperature reducing device comprising a fluid heating unit, wherein the cooling fluid heating unit communicates with the circulation path .
JP2005300190A 2005-10-14 2005-10-14 Steam desuperheater Active JP4722665B2 (en)

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CN109140421A (en) * 2018-09-10 2019-01-04 广东粤电靖海发电有限公司 A kind of Thermal generation unit steam reheat system
WO2022048094A1 (en) * 2020-09-02 2022-03-10 李华玉 Method for reducing and utilizing heat transfer temperature difference in heat absorption process

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JPH0788933B2 (en) * 1987-03-30 1995-09-27 株式会社テイエルブイ Vacuum steam generator
JPH01105000A (en) * 1987-10-15 1989-04-21 Hitachi Ltd Vacuum ejector device
JP2900004B2 (en) * 1992-05-26 1999-06-02 丸善石油化学株式会社 Superheated steam cooler
JPH09196305A (en) * 1996-01-12 1997-07-29 Tlv Co Ltd Condensation recovery device
JPH10246401A (en) * 1997-03-04 1998-09-14 Shinei Kk Clean steam generating device

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Publication number Priority date Publication date Assignee Title
JP2003207102A (en) * 2002-01-11 2003-07-25 Toshiba Eng Co Ltd Attemperator
JP2005127638A (en) * 2003-10-24 2005-05-19 Toshiba Plant Systems & Services Corp Steam attemperator
JP2005278577A (en) * 2004-03-30 2005-10-13 Miura Co Ltd Thawing apparatus

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