JPH04347490A - Drain processing device for steam plant - Google Patents

Drain processing device for steam plant

Info

Publication number
JPH04347490A
JPH04347490A JP12013791A JP12013791A JPH04347490A JP H04347490 A JPH04347490 A JP H04347490A JP 12013791 A JP12013791 A JP 12013791A JP 12013791 A JP12013791 A JP 12013791A JP H04347490 A JPH04347490 A JP H04347490A
Authority
JP
Japan
Prior art keywords
steam
drain
condenser
moisture
water
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.)
Withdrawn
Application number
JP12013791A
Other languages
Japanese (ja)
Inventor
Eiichi Yamamoto
栄一 山本
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP12013791A priority Critical patent/JPH04347490A/en
Publication of JPH04347490A publication Critical patent/JPH04347490A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE:To prevent corrosion and the like in a steam generating device for a steam plant, which is generated by introducing impurities, such as iron series and the like which are removed from wet steam from a turbine and contained in drain. CONSTITUTION:Moisture in the wet steam of a high pressure turbine 2, driven by steam generated in a steam generating device 1, is removed by a moisture separator 3 as drain 12 while the exhaust steam of a low pressure turbine driven by the steam, whose moisture is removed already, is condensed in a condenser 6 and said drain and condensed water are circulated into the steam generating device 1 for a steam plant. The steam plant comprises a feed water heater 10, recovering the heat of drain removed from steam into water circulated to said steam generating device 1 and supplying the drain into the condenser 6, and a desalting device 8, provided at the down-stream side of the condenser 6 and removing impurities in water.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、原子力発電プラント等
の蒸気プラントのドレン処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drain treatment device for a steam plant such as a nuclear power plant.

【0002】0002

【従来の技術】従来の原子力発電プラントのドレン処理
装置を、図2によって説明する。
2. Description of the Related Art A conventional drain treatment device for a nuclear power plant will be explained with reference to FIG.

【0003】1は蒸気発生装置、2は蒸気発生装置で発
生した蒸気で駆動される高圧タービン、3は高圧タービ
ン2から出る湿り蒸気中の湿分をドレン12として回収
する湿分分離器、4は湿分分離器3で湿分を除去された
蒸気を加熱する加熱器、5は加熱器4で加熱された蒸気
で駆動される低圧タービンであり、低圧タービン5の排
気は復水器6で復水となる。前記の復水は、ポンプ7を
経て脱塩装置8及び給水ヒータ9,10,11を順次通
過した上、蒸気発生装置1の給水として循還されるよう
になっている。
1 is a steam generator; 2 is a high-pressure turbine driven by the steam generated by the steam generator; 3 is a moisture separator that collects moisture in the wet steam discharged from the high-pressure turbine 2 as a drain 12; 4; 5 is a heater that heats the steam from which moisture has been removed by the moisture separator 3; 5 is a low-pressure turbine driven by the steam heated by the heater 4; It becomes condensate. The condensed water passes through the pump 7, the desalination device 8, and the feed water heaters 9, 10, and 11 in sequence, and is then circulated as feed water to the steam generator 1.

【0004】一方、湿分分離器3で蒸気から分離された
ドレン12は、タンク13と制御弁14を経て前記給水
ヒータ11へ供給されて回収され、前記復水を加熱した
上復水と共に蒸気発生装置1へ循還するようになってい
る。
On the other hand, the condensate 12 separated from steam by the moisture separator 3 is supplied to the feed water heater 11 through a tank 13 and a control valve 14, and is recovered. It is designed to circulate to the generator 1.

【0005】この従来のドレン処理装置では、蒸気発生
器1からの蒸気は高圧タービン2で仕事をした後、湿り
蒸気となって湿分分離器3へ流入し、ここで蒸気中の湿
分は除去されてドレン12となり、タンク13、制御弁
14を経て給水ヒータ11で回収される。
In this conventional drain treatment device, steam from a steam generator 1 performs work in a high-pressure turbine 2, and then becomes wet steam and flows into a moisture separator 3, where the moisture in the steam is removed. It is removed and becomes a drain 12, which passes through a tank 13 and a control valve 14 and is recovered by the water heater 11.

【0006】また、湿分分離器3で湿分を除去された蒸
気は、加熱器4で加熱され低圧タービン5で仕事をした
後に復水器5で復水となり、ポンプ7を経て、脱塩装置
8で浄化された後に、給水ヒータ9,10,11で昇温
された上、前記の給水ヒータ11で回収されたドレン1
2と共に蒸気発生器1へ供給される。
[0006] Also, the steam from which moisture has been removed in the moisture separator 3 is heated in a heater 4, does work in a low-pressure turbine 5, becomes condensed water in a condenser 5, passes through a pump 7, and is desalinated. After being purified by the device 8, the drain 1 is heated by the feed water heaters 9, 10, and 11, and then recovered by the water feed heater 11.
2 is supplied to the steam generator 1.

【0007】[0007]

【発明が解決しようとする課題】前記の従来の原子力発
電プラントのドレン処理装置では、湿分分離器からのド
レン中には鉄分等の不純物が含まれている。このドレン
が給水ヒータを経て蒸気発生器へ供給されるために、ド
レン中の不純物が蒸気発生器に持ち込まれて、蒸気発生
器の腐食等の要旨となる問題点があった。
SUMMARY OF THE INVENTION In the conventional drain treatment apparatus for a nuclear power plant described above, the drain from the moisture separator contains impurities such as iron. Since this drain is supplied to the steam generator via the feedwater heater, impurities in the drain are brought into the steam generator, causing problems such as corrosion of the steam generator.

【0008】本発明は、以上の問題点を解決することが
できる蒸気プラントのドレン処理装置を提供しようとす
るものである。
The present invention aims to provide a drain treatment device for a steam plant that can solve the above problems.

【0009】[0009]

【課題を解決するための手段】本発明の蒸気プラントの
ドレン処理装置は、蒸気発生器で発生した蒸気で駆動さ
れる高圧タービンを出た湿り蒸気中の湿分を湿分分離器
でドレンとして除去し、湿分が除去された蒸気で駆動さ
れる低圧タービンの排気を復水器で復水させ、前記ドレ
ンと前記復水を前記蒸気発生装置へ循還させる蒸気プラ
ントにおいて、前記蒸気発生装置へ循還される水に前記
蒸気から除去されたドレンの熱を回収した上同ドレンを
前記復水器へ供給する給水ヒータ、及び前記復水器の後
流側に設けられた脱塩装置を備えている。
[Means for Solving the Problems] A drain treatment device for a steam plant according to the present invention uses a moisture separator to convert moisture in wet steam exiting a high-pressure turbine driven by steam generated in a steam generator into drain water. In a steam plant, the exhaust gas of a low-pressure turbine driven by steam from which moisture has been removed is condensed in a condenser, and the drain and the condensate are recycled to the steam generator, wherein the steam generator a water heater that recovers the heat of condensate removed from the steam and supplies the condensate to the condenser; and a desalination device provided on the downstream side of the condenser. We are prepared.

【0010】0010

【作用】本発明では、湿分分離器において高圧タービン
の湿り蒸気から除去され鉄分等の不純物を含むドレンは
、給水ヒータにおいて蒸気発生装置へ循還される水と熱
交換してその熱が回収された上、低圧タービンの排気の
復水器へ供給される。このドレンと復水器で発生する低
圧タービンの排気からの復水は、脱塩装置へ供給されて
不純物が除去され浄化された上蒸気発生装置へ給水とし
て循還する。
[Operation] In the present invention, condensate containing impurities such as iron, which is removed from the humid steam of the high-pressure turbine in the moisture separator, exchanges heat with water that is circulated to the steam generator in the feed water heater, and the heat is recovered. The exhaust gas of the low pressure turbine is then fed to the condenser. Condensate from the low-pressure turbine exhaust generated in this drain and condenser is supplied to a desalination device, where impurities are removed and purified, and then circulated as feed water to the upper steam generator.

【0011】このようにして、本発明では、蒸気発生装
置へ循還される給水中の鉄分等の不純物が除去されて、
蒸気発生装置の腐食等が防止される。
In this way, in the present invention, impurities such as iron in the water supplied to the steam generator are removed.
Corrosion of the steam generator is prevented.

【0012】0012

【実施例】本発明の一実施例を、図1によって説明する
。本実施例は、図2に示すと同じく原子力発電プラント
のドレン処理装置に係るものであって、同一の部分は、
図1において図2におけると同一の符号を付してその説
明を省略し、以下相違する部分について説明する。
[Embodiment] An embodiment of the present invention will be explained with reference to FIG. This example relates to a drain treatment device for a nuclear power plant similar to that shown in FIG. 2, and the same parts are as follows:
In FIG. 1, the same reference numerals as in FIG. 2 are given, and the explanation thereof will be omitted, and the different parts will be explained below.

【0013】本実施例では、タンク13に接続された制
御弁14の下流側に湿分分離器3で除去されたドレン1
2を受け入れるタンク15が設けられている。同タンク
15の底部は、同タンク15の水位制御用の制御弁18
を経て給水ヒータ9に接続され、同タンク15内のドレ
ン17が給水ヒータ9に供給されるようになっており、
また、同給水ヒータ9を出るドレンは復水器6へ供給さ
れて回収されるようになっている。また、前記タンク1
5の上部は給水ヒータ10に接続されており、同タンク
15からの蒸気16は給水ヒータ10で回収され、給水
ヒータ9から供給ヒータ10へ供給される水と混合する
ようになっている。
In this embodiment, the drain 1 removed by the moisture separator 3 is placed downstream of the control valve 14 connected to the tank 13.
A tank 15 is provided for receiving 2. The bottom of the tank 15 has a control valve 18 for controlling the water level of the tank 15.
It is connected to the water heater 9 through the tank 15, and the drain 17 in the tank 15 is supplied to the water heater 9.
Further, the drain coming out of the water supply heater 9 is supplied to the condenser 6 and recovered. In addition, the tank 1
The upper part of the tank 5 is connected to a feed water heater 10, and steam 16 from the tank 15 is collected by the feed water heater 10 and mixed with water supplied from the feed water heater 9 to the feed heater 10.

【0014】以上のように構成された本実施例では、湿
分分離器3からのドレン12は、制御弁14を経て給水
ヒータ10に接続された低圧のタンク15内にフラッシ
ュすることによって、同タンク15内で蒸気16とドレ
ン17に分離し、蒸気16は給水ヒータ10へ送られて
同給水ヒータ10へ供給される水に熱回収されると共に
、同給水ヒータ10に供給される水と共に蒸気発生器1
へ循還する。
In this embodiment configured as described above, the drain 12 from the moisture separator 3 is flushed into the low pressure tank 15 connected to the feed water heater 10 via the control valve 14. The steam 16 is separated into a steam 16 and a drain 17 in the tank 15, and the steam 16 is sent to the feed water heater 10, where its heat is recovered by the water supplied to the feed water heater 10, and it is converted into steam together with the water supplied to the feed water heater 10. Generator 1
Circulate to.

【0015】一方、タンク15内のドレン17は、制御
弁18を経て給水ヒータ9へ流入して同給水ヒータ9に
より熱回収された後に、復水器6へ回収される。この回
収されたドレン17は、復水器6において低圧タービン
5の排気より発生した復水と共にポンプ7を経て脱塩装
置8へ供給される。従って、湿分分離器3で発生するド
レン12中の不純物、即ちドレン17中の不純物は、脱
塩装置8で除去、浄化されて、清浄な水として蒸気発生
器1へ供給される。
On the other hand, the drain 17 in the tank 15 flows into the feed water heater 9 via the control valve 18, and after its heat is recovered by the feed water heater 9, it is recovered into the condenser 6. The recovered drain 17 is supplied to the desalination device 8 through the pump 7 together with condensate generated from the exhaust gas of the low pressure turbine 5 in the condenser 6 . Therefore, the impurities in the drain 12 generated in the moisture separator 3, that is, the impurities in the drain 17, are removed and purified by the desalination device 8 and supplied to the steam generator 1 as clean water.

【0016】以上の通り、本実施例では、蒸気発生器1
へ循還供給される給水中には、鉄分等の不純物が含まれ
ることがなく、不純物による蒸気発生器1の腐食等の発
生を防止することができる。
As mentioned above, in this embodiment, the steam generator 1
The water supplied for circulation does not contain impurities such as iron, and corrosion of the steam generator 1 due to impurities can be prevented.

【0017】なお、タンク15内の水位は制御弁18に
より所定の水位に制御される。また、湿分分離器3内の
ドレン12の水位は制御弁14によって所定の値に保持
され、湿分分離器3内の蒸気がタンク15へ流出するこ
とが防止される。また更に、前記のように給水ヒータ1
0と給水ヒータ9により回収された熱は、復水器6から
蒸気発生器1へ供給される水の加熱に有効に活用される
Note that the water level in the tank 15 is controlled to a predetermined water level by a control valve 18. Further, the water level of the drain 12 in the moisture separator 3 is maintained at a predetermined value by the control valve 14, and steam in the moisture separator 3 is prevented from flowing out to the tank 15. Furthermore, as described above, the water supply heater 1
The heat recovered by the water heater 9 and the water supply heater 9 is effectively used to heat water supplied from the condenser 6 to the steam generator 1.

【0018】[0018]

【発明の効果】以上の説明したように、本発明によれば
、湿分分離器からのドレン中に含まれている鉄分等の不
純物を脱塩装置で除去して浄化することができ、蒸気発
生器への不純物持ち込みを防止して蒸気発生器の健全性
向上に貢献することができる。
As explained above, according to the present invention, impurities such as iron contained in the drain from the moisture separator can be removed and purified by the desalination device. This can contribute to improving the health of the steam generator by preventing impurities from being brought into the generator.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明の一実施例の系統図である。FIG. 1 is a system diagram of an embodiment of the present invention.

【図2】従来の原子力発電プラントのドレン処理装置の
系統図である。
FIG. 2 is a system diagram of a conventional drain treatment device for a nuclear power plant.

【符号の説明】[Explanation of symbols]

1              蒸気発生装置2   
           高圧タービン3       
       湿分分離器4            
  加熱器5              低圧タービ
ン6              復水器7     
         ポンプ8            
  脱塩装置9,10,11  給水ヒータ 12            ドレン 14            制御弁 15            タンク 16            蒸気 17            ドレン 18            制御弁
1 Steam generator 2
High pressure turbine 3
Moisture separator 4
Heater 5 Low pressure turbine 6 Condenser 7
pump 8
Desalination equipment 9, 10, 11 Water supply heater 12 Drain 14 Control valve 15 Tank 16 Steam 17 Drain 18 Control valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  蒸気発生器で発生した蒸気で駆動され
る高圧タービンを出た湿り蒸気中の湿分を湿分分離器で
ドレンとして除去し、湿分が除去された蒸気で駆動され
る低圧タービンの排気を復水器で復水させ、前記ドレン
と前記復水を前記蒸気発生装置へ循還させる蒸気プラン
トにおいて、前記蒸気発生装置へ循還される水に前記蒸
気から除去されたドレンの熱を回収した上同ドレンを前
記復水器へ供給する給水ヒータ、及び前記復水器の後流
側に設けられた脱塩装置を備えたことを特徴とする蒸気
プラントのドレン処理装置。
Claim 1: Moisture in wet steam exiting a high-pressure turbine driven by steam generated in a steam generator is removed as drain in a moisture separator, and a low-pressure turbine is driven by the steam from which moisture has been removed. In a steam plant in which the exhaust gas of a turbine is condensed in a condenser and the condensate and the condensate are circulated to the steam generator, the condensate removed from the steam is added to the water that is recycled to the steam generator. A drain treatment device for a steam plant, comprising: a feed water heater that supplies the drain from which heat has been recovered to the condenser; and a desalination device provided on the downstream side of the condenser.
JP12013791A 1991-05-24 1991-05-24 Drain processing device for steam plant Withdrawn JPH04347490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12013791A JPH04347490A (en) 1991-05-24 1991-05-24 Drain processing device for steam plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12013791A JPH04347490A (en) 1991-05-24 1991-05-24 Drain processing device for steam plant

Publications (1)

Publication Number Publication Date
JPH04347490A true JPH04347490A (en) 1992-12-02

Family

ID=14778884

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12013791A Withdrawn JPH04347490A (en) 1991-05-24 1991-05-24 Drain processing device for steam plant

Country Status (1)

Country Link
JP (1) JPH04347490A (en)

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Effective date: 19980806