JPS588992A - Sidestream condensation system - Google Patents

Sidestream condensation system

Info

Publication number
JPS588992A
JPS588992A JP10554681A JP10554681A JPS588992A JP S588992 A JPS588992 A JP S588992A JP 10554681 A JP10554681 A JP 10554681A JP 10554681 A JP10554681 A JP 10554681A JP S588992 A JPS588992 A JP S588992A
Authority
JP
Japan
Prior art keywords
condensate
desalting
condensing
condenser
condensating
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
Application number
JP10554681A
Other languages
Japanese (ja)
Inventor
Hitoshi Ishimaru
等 石丸
Hirotsugu Nagai
永井 洋次
Toyohiko Masuda
豊彦 増田
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.)
Hitachi Engineering Co Ltd
Hitachi Ltd
Original Assignee
Hitachi Engineering Co Ltd
Hitachi 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 Hitachi Engineering Co Ltd, Hitachi Ltd filed Critical Hitachi Engineering Co Ltd
Priority to JP10554681A priority Critical patent/JPS588992A/en
Publication of JPS588992A publication Critical patent/JPS588992A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22DPREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
    • F22D11/00Feed-water supply not provided for in other main groups
    • F22D11/006Arrangements of feedwater cleaning with a boiler

Landscapes

  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PURPOSE:To rationalize arrangement and pipings of means in the sidestream condensation system by a method wherein condensating and desalting bypass lines provided at a plurality of condensating and desalting devices are normally opened partially, closed when a seawater leakag occurs in the condenser so as to flow condensate to the condensing and desalting devices. CONSTITUTION:In the normal operation, a predetermined amount of condensate from a condensating and filtering device 6 is sent to some of the plurality of condensing and desalting devices 17 to undergo a water quality treatment therein, whereas th rest flows through a bypass valve 18. The condensate, both from the device 17 and through a valve 18, joints at the outlet of the condensing and desalting device 17. If a salt detector 19 detects a seawater leakage in a coolant pipe group in the condenser 1, the detector 19 provides an output representing the amount of leakage to a discriminator 20, which closes rapidly the bypass valve 18 of the condensing and desalting device 17 as soon as the leakage reaches a permissible limit value. Under this control, the whole amount of the condensate fow through all of the condensing and desalting devices 17, thereby preventing any entrance of chlorine ions into the nuclear reactor.

Description

【発明の詳細な説明】 本発明は、サイドストリーム復水系統に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a sidestream condensate system.

従来のサイトス) IJ−ム復水系統の構成を第1図に
よって説明する。
The configuration of a conventional IJ-mu condensate system will be explained with reference to FIG.

蒸気タービン排気蒸気及び、給水加熱器ドレンは復水器
1内で凝縮され復水として第1ホツトウエル2に入る。
Steam turbine exhaust steam and feed water heater drain are condensed in the condenser 1 and enter the first hot well 2 as condensate.

第1ホツトウエル2の復水は復水浄化循環ポンプ3によ
り昇圧され、復水E過装置6及び、復水脱塩装置7を有
する復水浄化装置へ送られ、水質処理(不純分処理)さ
れた後、タービン及び弁のグランド部の封入蒸気を凝縮
するグランド蒸気復水器8及び、復水器1内の非凝縮気
体を抽出するために使用される蒸気式エゼクタの排出蒸
気を凝縮させる空気抽出器9へ送られる。
The condensate in the first hot well 2 is pressurized by a condensate purification circulation pump 3 and sent to a condensate purification device having a condensate E-filtration device 6 and a condensate desalination device 7, where it is treated for water quality (impurity treatment). After that, a gland steam condenser 8 condenses the sealed steam in the gland section of the turbine and valves, and air condenses the exhaust steam of the steam ejector used to extract non-condensable gas in the condenser 1. It is sent to the extractor 9.

グランド蒸気復水器8及び空気抽出器9での熱交換によ
り温度上昇した復水け、水位制御弁12を介して、復水
ポンプのサクションヘッダ13より復水器第2ホントウ
エル14に戻る。
The condensate whose temperature has increased due to heat exchange in the grand steam condenser 8 and the air extractor 9 returns to the condenser second real well 14 from the suction header 13 of the condensate pump via the water level control valve 12 .

サイドストリームタンク11の水位制御弁12を介して
、復水ポンプサクションヘッダ13に入る復水のうち、
発電プラント運転負荷に応じて必要流量を復水ポンプ1
5により主系統16へ送水する。その残りの余剰水は第
2ホントウェル14の上部よりオーバーフローし、第1
ホントウエル2へ戻る。
Of the condensate that enters the condensate pump suction header 13 via the water level control valve 12 of the side stream tank 11,
Condensate pump 1 adjusts the required flow rate according to the power plant operating load.
5, the water is sent to the main system 16. The remaining surplus water overflows from the upper part of the second real well 14 and
Return to Honto Well 2.

中間貯槽11は、サイドストリーム復水系統に静水頭に
よって圧力印加を行い、水柱分離再結合を防止する事を
目的として設置され、水位制御弁12により水位を一定
に保たれている。
The intermediate storage tank 11 is installed for the purpose of applying pressure to the side stream condensate system using a static head to prevent water column separation and recombination, and the water level is kept constant by a water level control valve 12.

この様なサイドストリーム復水系統における、配置計画
及び配管計画において一番重要視されるのは、復水濾過
装置6及び、復水脱塩装置17である。これは、各装置
が、約10系列に分かれており、各系列毎に、出入口弁
、流量検出装置、流量制御弁、復水濾過塔、あるいは、
復水脱塩塔及び各分枝配管があり、高さ方向及び水平方
向において最大のうえに、複雑にこみ合った配管ルート
を構成する為である。この様に、復水浄化装置の系列数
す彦わち塔数が多い事は、合理的な、配置計画及び配管
計画の疎外要因となる。
In such a side stream condensate system, the most important elements in the layout plan and piping plan are the condensate filtration device 6 and the condensate desalination device 17. This means that each device is divided into about 10 series, and each series has an inlet/outlet valve, a flow rate detection device, a flow rate control valve, a condensate filtration tower, or
This is because there is a condensate desalination tower and each branch pipe, which is the largest in the height and horizontal directions, and also constitutes a complicated pipe route. In this way, the large number of series of condensate purification equipment, that is, the number of towers, becomes a factor that precludes rational layout planning and piping planning.

本発明の目的は、各機器の配置計画、配管計画の合理化
を図ったサイドストリーム復水系統を提供するところに
ある。
An object of the present invention is to provide a side stream condensate system in which the arrangement plan of each device and the piping plan are rationalized.

本発明の特徴は、複数の復水脱塩装置に設けた復水脱塩
装置パイパスラインを、適状運転中はその一部を開とし
て運転し、復水器での海水リークが有った時は、検塩装
置によって検出し、該バイパスラインを閉じて全数の復
水脱塩装置に復水を流通させて復水を浄化するようにし
たサイドストリーム復水系統にある。
A feature of the present invention is that the condensate desalination equipment bypass lines installed in a plurality of condensate desalination equipment are operated with some of them open during proper operation, and seawater leakage from the condensers occurs. In the side stream condensate system, the condensate is detected by a salt detection device, the bypass line is closed, and the condensate is passed through all the condensate desalination devices to purify the condensate.

本発明の一実施例であるサイドストリーム復水系統を@
2図に示す。
A side stream condensate system that is an embodiment of the present invention @
Shown in Figure 2.

図において、蒸気タービン排気蒸気及び、給水加熱器ド
レンは、復水器1内で凝縮され復水として第1ホントウ
エル2に入る。第1ホントウエル2の復水は、復水浄化
循環ポンプ3により昇圧され復水濾過装置6により、水
質処理される。復水濾過装置6を出た復水のうちある所
要流量は一部の復水脱塩装置17に通水し水質処理され
、残りの流量はバイパス弁18を通り、復水脱塩装置1
7の出口で合流する。合流した復水は、グランド蒸気復
水器8、突気抽出器9で熱交換した後、水位制御弁12
を介して復水ポンプサクションヘッダ13に入り、発電
プラント運転負荷に応じて必要量が復水ポンプ15によ
って主系統16に送られ、余剰分の復水は復水器第2ホ
ントウエル14に入り、オーバフローして、復水器第1
ホントウエル2に戻る。
In the figure, steam turbine exhaust steam and feed water heater drain are condensed in a condenser 1 and enter a first real well 2 as condensate. The condensate in the first real well 2 is pressurized by the condensate purification circulation pump 3 and subjected to water quality treatment by the condensate filtration device 6. A certain required flow rate of the condensate that has exited the condensate filtration device 6 is passed through a part of the condensate desalination device 17 for water quality treatment, and the remaining flow passes through the bypass valve 18 and is then transferred to the condensate desalination device 1.
Merge at exit 7. The combined condensate undergoes heat exchange in the grand steam condenser 8 and the gust extractor 9, and then passes through the water level control valve 12.
The required amount is sent to the main system 16 by the condensate pump 15 according to the operating load of the power plant, and the excess condensate enters the condenser second real well 14. , overflows and the first condenser
Return to Honto Well 2.

復水の水質処理機能を有する、復水濾過装置6と復水脱
塩装置17のうち、復水濾過装置6は主に復水中のクラ
ッドを除去し、復水脱塩装置17は主に塩素イオンの除
去を機能として持っている。
Of the condensate filtration device 6 and condensate desalination device 17, which have condensate water quality treatment functions, the condensate filtration device 6 mainly removes crud in condensate, and the condensate desalination device 17 mainly removes chlorine. Its function is to remove ions.

通常運転中、原子炉入口の給水の水質を確保する為には
、第1図の系統構成において十分であり、また、第2図
の復水脱塩装置塔数の減らした場合で、復水脱塩装置1
7をバイパスする復水があってもクランドの除去は、復
水濾過装置6によって、大部分が遠域される。復水脱塩
装置17は、復水器1の冷却管巣における海水リーク時
に、塩素イオンが、原子炉に持ちこまれ、ステンレス鋼
でできている原子炉構成機器及び配管の応力腐食割れを
引き起す事を防止すあ為に、塩素イオン除去の目的で設
置されている。
During normal operation, the system configuration shown in Figure 1 is sufficient to ensure the quality of the water supply at the reactor inlet. Desalination equipment 1
Even if there is condensate that bypasses the condensate filter 7, most of the crud is removed by the condensate filtration device 6. In the condensate desalination device 17, when seawater leaks from the cooling pipes of the condenser 1, chlorine ions are carried into the reactor and cause stress corrosion cracking of reactor components and piping made of stainless steel. It is installed for the purpose of removing chlorine ions to prevent this.

ここで、検塩装置19において、復水器1における冷却
管巣の海水リークを検出し、海水リーク量を判定器20
に出力する。判定器20は、海水リーク量が許容限界値
に達したら、復水脱塩装置17のバイパス弁18を急閉
する。この制御によって、復水は全て、全数の復水脱塩
装置17を通る事になり、塩素イオンが、原子炉に持ち
込まれる事はない。
Here, the salt detection device 19 detects seawater leakage from the cooling pipe nest in the condenser 1, and determines the amount of seawater leakage using the determination device 20.
Output to. The determiner 20 suddenly closes the bypass valve 18 of the condensate desalination device 17 when the amount of seawater leakage reaches an allowable limit value. With this control, all condensate passes through all the condensate desalination devices 17, and chlorine ions are not brought into the reactor.

この場合において、サイドストリーム復水系統の復水流
量は減少し、復水器第2ホントウエル14のレベル低下
として表われるが、この時、原子炉の負荷を低下させる
事によって、安定した運転が継続される。
In this case, the condensate flow rate of the sidestream condensate system decreases, which appears as a drop in the level of the condenser second real well 14, but at this time, stable operation can be achieved by reducing the reactor load. Continued.

ここで、復水脱塩塔塔数の減少だけで、約7億円の設備
器低減が可能となる。
Here, just by reducing the number of condensate demineralization columns, it is possible to reduce equipment by approximately 700 million yen.

本発明によれば、次の効果が有る。According to the present invention, there are the following effects.

復水脱塩装置塔数を減少させることが可能となり、建屋
の配置スペース、保守点検スペース、が改善されると共
に、従来非常に複雑とされていた、復水脱塩装置廻りの
配管計画が合理的となる。
It is now possible to reduce the number of condensate desalination equipment towers, improving building space and maintenance/inspection space, and streamlining the piping planning around the condensate desalination equipment, which was previously considered to be extremely complicated. become a target.

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

第1図は従来のサイドストリーム復水系統図、第2図は
本発明の一実施例であるサイドストリーム復水系統図で
ある。
FIG. 1 is a conventional side stream condensate system diagram, and FIG. 2 is a side stream condensate system diagram according to an embodiment of the present invention.

Claims (1)

【特許請求の範囲】[Claims] 1、蒸気タービンの排気蒸気の凝縮水を溜め、かつ、そ
の復水を復水浄化系統へ送る復水器の第1ホントウエル
と、復水浄化系統からの復水を溜める復水器の第2ホン
トウエルと、該復水浄化系統から第2ホントウエルに復
水を導く系統から分岐して発電プラントの要求する復水
量を供給する主系統を備えたサイドストリーム復水系統
において、前記復水浄化系統に備えられた複数の復水脱
塩装置にバイパス弁を設置し、第1ホントウエル近傍に
復水の検塩装置を設置し、更に該検塩装置の検出信号に
応じて該バイパス弁の開閉を操作する制御装置を設置し
たことを特徴とするサイドストリーム復水系統。
1. The first well of the condenser that stores condensed water from the exhaust steam of the steam turbine and sends the condensate to the condensate purification system, and the first well of the condenser that stores condensate from the condensate purification system. In a side stream condensate system comprising two main wells and a main system branching from a system that leads condensate from the condensate purification system to the second real well and supplying the amount of condensate required by the power generation plant, the condensate A bypass valve is installed in a plurality of condensate desalination devices provided in the purification system, a condensate salt test device is installed near the first real well, and the bypass valve is installed in accordance with the detection signal of the salt test device. A side stream condensate system characterized by installing a control device that operates the opening and closing of the side stream condensate system.
JP10554681A 1981-07-08 1981-07-08 Sidestream condensation system Pending JPS588992A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10554681A JPS588992A (en) 1981-07-08 1981-07-08 Sidestream condensation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10554681A JPS588992A (en) 1981-07-08 1981-07-08 Sidestream condensation system

Publications (1)

Publication Number Publication Date
JPS588992A true JPS588992A (en) 1983-01-19

Family

ID=14410573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10554681A Pending JPS588992A (en) 1981-07-08 1981-07-08 Sidestream condensation system

Country Status (1)

Country Link
JP (1) JPS588992A (en)

Similar Documents

Publication Publication Date Title
CN107665744B (en) Nuclear power station secondary loop flusher and its purging method
US20160125965A1 (en) Power Plant
CN110160113A (en) A kind of nuclear power plant's heating system and its heating method
JPS588992A (en) Sidestream condensation system
GB1053515A (en)
JPS6179905A (en) Drain recovery system
US4434620A (en) Condensation system for power plant
CN110486709A (en) A kind of nuclear power station steam generator drainage
RU2697652C1 (en) Method and system of bringing a nuclear power plant into a safe state after extreme impact
Legkostupova et al. Upgrading the SPP-500-1 moisture separators-steam reheaters used in the Leningrad NPP turbine units
US2341738A (en) Steam plant
JPS54141903A (en) Condensing equipment
Marguet The Secondary Circuit and the Cold Source
JP4573315B2 (en) Condensate purification system and operation method thereof
CA3066162C (en) Method and system for bringing a nuclear power plant into a safe state after extreme effect
JPS59138995A (en) Condensed water system
JPS5869397A (en) Steam generating plant
JPS6134073B2 (en)
JPH0148519B2 (en)
JPS6027914B2 (en) Condensate purification equipment for steam-powered plants
WO2023180588A2 (en) Deaerator systems and methods of servicing of deaerator
JPH09211185A (en) Nuclear power plant
SU1744277A1 (en) Condenser technical water-supply system
JP2004076651A (en) Steam turbine plant
JP2909301B2 (en) How to pump up the feedwater heater drain