JPS61134509A - High pressure system clean-up system of plant - Google Patents

High pressure system clean-up system of plant

Info

Publication number
JPS61134509A
JPS61134509A JP25563684A JP25563684A JPS61134509A JP S61134509 A JPS61134509 A JP S61134509A JP 25563684 A JP25563684 A JP 25563684A JP 25563684 A JP25563684 A JP 25563684A JP S61134509 A JPS61134509 A JP S61134509A
Authority
JP
Japan
Prior art keywords
cleanup
pressure
water
feed water
high pressure
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
JP25563684A
Other languages
Japanese (ja)
Inventor
慎也 鈴木
中村 泰昭
浦 勝己
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 JP25563684A priority Critical patent/JPS61134509A/en
Publication of JPS61134509A publication Critical patent/JPS61134509A/en
Pending legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、ブレボイラクリーンアップに係り、特に、フ
リー/アップ時期短縮とするプレボイラクリーンアップ
系統に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a breboiler cleanup, and particularly to a preboiler cleanup system that shortens the free/up time.

〔発明の背景〕[Background of the invention]

従来、火力発電所の蒸気タービンプラントにおいて、復
水器で復水した水は、脱塩装置、各種予熱器、低圧給水
加熱器(以下、低圧ヒータ)、脱気器及び高圧ヒータを
経てボイラに達する。このような系統に流れる給水には
、配管及びヒータに付着している鉄、銅、その他の元素
から成る不純物が含まれている。これら不純物がボイラ
に持ち込まれると蒸発管の管壁に付着してスケールとな
シ伝熱を阻害して管材が過熱され蒸発管破裂となる場合
もある。このため、タービン及びボイラ内に腐蝕生成物
の堆積を生じないように、ボイラ給水の水質基準を定め
ているが、発電プラントの運転停止中に、給水中の汚染
物の濃度が起動時の水質基準による制御値を越える恐れ
があるので、ボイラ及びプレボイラに於けるクリーンア
ップを行なってい不。プレボイラ系に於いては、各系統
毎にクリーンアップを行ない、jIk終的にボイラの通
水基準値を満足させる。
Conventionally, in a steam turbine plant of a thermal power plant, water condensed in a condenser is sent to a boiler via a desalination device, various preheaters, a low-pressure feed water heater (hereinafter referred to as a low-pressure heater), a deaerator, and a high-pressure heater. reach The water supply that flows through these systems contains impurities consisting of iron, copper, and other elements that adhere to pipes and heaters. When these impurities are brought into the boiler, they adhere to the walls of the evaporator tubes and form scales that inhibit heat transfer, causing the tube material to overheat and sometimes causing the evaporator tubes to burst. For this reason, water quality standards for boiler feed water have been established to prevent the accumulation of corrosion products inside the turbine and boiler. The boiler and pre-boiler were not cleaned up as there was a risk of exceeding the standard control values. In the preboiler system, cleanup is performed for each system, and jIk ultimately satisfies the water flow standard value of the boiler.

次に、従来の一般的なプレボイラ系のクリーンアップに
ついて、第3図面の簡単な説明する。
Next, the cleanup of a conventional general preboiler system will be briefly explained with reference to the third drawing.

従来、プレボイラ系のクリーンアップは、復水再循環ラ
インクリーンアップ→低圧うインクリーンアップ→高圧
うイ/クリーンアップの順でクリーンアップは進行する
Conventionally, cleanup of a preboiler system proceeds in the following order: condensate recirculation line cleanup -> low pressure ink cleanup -> high pressure ink/cleanup.

即ち、復水再循墳ライ/クリーンアップに於いては、復
水器1→復水ポンプ2→脱塩装置3→復水再循環ライン
10→復水器1の閉回路を形成し、本回路に於いて、ブ
ロー、循環を行ない、低圧ヒータの通水基準値を満足さ
せた後、次のステップの低圧クリーンアップに進む。
In other words, in condensate recirculation/cleanup, a closed circuit of condenser 1 → condensate pump 2 → desalination device 3 → condensate recirculation line 10 → condenser 1 is formed, and the main After blowing and circulating the circuit to satisfy the low pressure heater water flow standards, proceed to the next step, low pressure cleanup.

低圧ラインクリーンアップに於いては、復水器l→復水
ポング2→脱塩装置3→低圧ヒータ4→脱気器5→脱気
器貯水槽6→低圧クリーンアップライン13→復水器l
の閉回路を形成し、系統内の不純物をブロー、循3II
Iによシボ質を向上させ、高圧ヒータ通水基準を満足さ
せた後、次の高圧ラインクリーンアップを実施する。
In low pressure line cleanup, condenser 1 → condensate pump 2 → demineralizer 3 → low pressure heater 4 → deaerator 5 → deaerator water tank 6 → low pressure cleanup line 13 → condenser 1
Forms a closed circuit, blows out impurities in the system, and circulates 3II
After improving the grain texture and satisfying the high-pressure heater water flow standards, the next high-pressure line cleanup is performed.

高圧クリーンアップは、復水器1→復水ポンプ2→脱塩
装置3→低圧ヒータ4→脱気器5→脱気器貯水槽6→給
水ブースタポンプ7→給水ポンプバイパスライン14→
高圧ヒータ9→高圧クリーンアツプライン16→復水器
1の閉回路によシブローと循環によシボ質を向上させ、
ボイラ通水基準値を満足させる。
High pressure cleanup is performed by condenser 1 → condensate pump 2 → demineralizer 3 → low pressure heater 4 → deaerator 5 → deaerator water tank 6 → water booster pump 7 → water pump bypass line 14 →
High pressure heater 9 → high pressure clean up line 16 → condenser 1 closed circuit to improve grain quality through sieving and circulation.
Satisfy boiler water flow standard values.

以上の如ぐ、各クリーンアップに於いて、鉄及びその他
不純物の多い初期の汚水は系外にブローさせ、ある程度
まで純度が高まったところで循環に切り替え、各循環回
路内の脱塩装置によって除去し、水質目標値に達するよ
うにクリーンアップを行ない、順次クリーンアップ範囲
を拡大させる。
As described above, in each cleanup, the initial wastewater containing a lot of iron and other impurities is blown out of the system, and when the purity has increased to a certain degree, it is switched to circulation, and removed by the desalination equipment in each circulation circuit. Cleanup will be carried out to reach water quality target values, and the scope of cleanup will be gradually expanded.

このため、高圧ラインクリーンアップに於いては、Uf
c8Eラインクリーンアップにて除去された低圧ライン
に、高圧ライ/中の水質の悪化された汚      1
水を再び流入させ、特に鉄分の多い高圧ヒータ廻シの汚
水を脱塩装置を通し、ブロー・循環によりクリーンアッ
プを行なうので、純水は多量に使用され、時間も長く費
やす必要が有る。
For this reason, in high pressure line cleanup, Uf
c8E In the low pressure line removed during line cleanup, there was dirt that deteriorated the water quality in the high pressure line/inside 1
The water is allowed to flow in again, and the waste water from the high-pressure heater, which has a particularly high iron content, is passed through a desalination device and cleaned up by blowing and circulation, so a large amount of pure water is used and it takes a long time.

第4図に従来のクリーンアップ工程及び鉄分濃度との関
係を示す。
FIG. 4 shows the relationship between the conventional cleanup process and the iron concentration.

〔発明の目的〕[Purpose of the invention]

本発明は、上記従来技術を改善すべく、低圧クリーンア
ップ系統と高圧クリーンアップ系統を同時に実施し、特
に従来多くの時間を費やしていた高圧ヒータ廻シのクリ
ーンアップを単独で実施することによプ、純水量の節約
、クリーンアップ時間の短縮、補機動力の低減を目的と
するものである。
In order to improve the above-mentioned prior art, the present invention implements a low pressure cleanup system and a high pressure cleanup system simultaneously, and in particular, performs the cleanup of the high pressure heater circuit alone, which conventionally took a lot of time. The purpose is to save pure water, shorten clean-up time, and reduce auxiliary machine power.

〔発明の概要〕[Summary of the invention]

本発明は、プレボイラクリーンアップに於いて高圧ヒー
タ廻シに多く時間がかかシ鉄分除去が難しいという実績
に基づき、高圧ヒータ廻シ単独りリー/アップ系統を設
け、電磁フィルタによ〕鉄分を効果的に除去し、さらに
低圧クリーンアップ系統と同時に実施可能とすることで
、クリーンアップ所要時間の短縮を可能とするものであ
る。
The present invention is based on the experience that high-pressure heater rotation takes a lot of time during pre-boiler cleanup and is difficult to remove iron.The present invention provides a separate leak/up system for the high-pressure heater and uses an electromagnetic filter to remove iron. This method effectively removes the wastewater and can be performed simultaneously with the low-pressure cleanup system, thereby making it possible to shorten the time required for cleanup.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を第1図により説明する。 An embodiment of the present invention will be described below with reference to FIG.

尚、第3図と同一部分については同一符号で示す。Note that the same parts as in FIG. 3 are indicated by the same reference numerals.

第3図と異なる点は、高圧クリーンアップ系統16から
分岐し給水ブースタポンプ入口管20に接続する系統及
び電磁フィルタ21、切替弁23゜24.25を設置し
ている点であシ、その他は、第3図と同一である。
The difference from FIG. 3 is that a system branched from the high-pressure cleanup system 16 and connected to the water supply booster pump inlet pipe 20, an electromagnetic filter 21, and a switching valve 23°24.25 are installed. , is the same as in FIG.

本発明によるクリーンアップ運用方法を以下に示す。The cleanup operation method according to the present invention is shown below.

本発明による運用方法の特徴は、低圧クリーンアップと
高圧クリ−7アツプを同時に実施可能とするところにあ
シ、高圧クリーンアップ系統への水11D及び補給が必
要となるが、補給水系統から給水ブースタポンプへの単
独水損シでもよいし、切替弁23を開し復水系統からの
水abでもよい。
The feature of the operation method according to the present invention is that low-pressure cleanup and high-pressure cleanup can be carried out simultaneously.Although it is necessary to supply water 11D and replenishment to the high-pressure cleanup system, water is supplied from the make-up water system. The booster pump may be supplied with water alone, or the switching valve 23 may be opened to supply water from the condensate system.

低圧クリーンアップ運用法は、復水器l→復水ポンプ2
→脱塩装fit3→低圧ヒータ4を介し、脱気器貯水タ
ンク6から止弁19を通)復水器1に到る閉回路によシ
、ブロー及び循環を行なう。この場合、低圧クリーンア
ップによる除鉄効果は、脱塩装置3により可能となる。
Low pressure cleanup operation method is condenser 1 → condensate pump 2
→ Desalination equipment fit 3 → Low pressure heater 4, deaerator water storage tank 6 to condenser 1 (through stop valve 19), blowing, blowing and circulation are performed. In this case, the iron removal effect by low-pressure cleanup is made possible by the desalination device 3.

一方、高圧クリーンアップ運用法は、低圧クリーンアッ
プと同時に実施するため、前述高圧クリーンアップ系親
水I!l!シ完了後、切替弁23.28を全閉とし、給
水ブースタポンプ7を起動させ、給水ブースタポンプ7
→給水ポンプバイパス系統14→高圧ヒータ9を経て、
本発明とする高圧クリーンアップ系統21→電磁フイル
タ22→切替弁25を介し、給水ブースタポンプ7に到
る閉回路によシブロー及び循環を行なう。この場合、電
磁フィルタ22によシ除鉄効果が可能となる。
On the other hand, the high-pressure cleanup operation method is carried out simultaneously with low-pressure cleanup, so the high-pressure cleanup system hydrophilic I! l! After completing the switching, the switching valves 23 and 28 are fully closed, the water booster pump 7 is started, and the water booster pump 7 is activated.
→ Water supply pump bypass system 14 → Via high pressure heater 9,
The high-pressure clean-up system 21 of the present invention → the electromagnetic filter 22 → the switching valve 25, and the closed circuit that reaches the water supply booster pump 7 performs sieving and circulation. In this case, the electromagnetic filter 22 can remove iron.

以上の運用法によシ低圧クリーンアップと高圧クリーン
アップを同時に実施し、水質確認後、プレボイラ全体の
クリーンアップを切替弁23.28を全開、24.25
を全閉に切替え、復水器1→復水ポ/ブ2→脱塩装置3
→低圧ヒータ4→脱気器5→給水ブースタポンプ7→給
水ポンプバイパス系統14→高圧ヒータ9→高圧クリー
ンアツプ系統16→復水器1の閉回路にて実施するが、
さらに除鉄効果を上げるため、脱気器5に補助蒸気12
を導入し、加温によシ鉄分の除去を図る。
According to the above operation method, low-pressure cleanup and high-pressure cleanup were carried out simultaneously, and after checking the water quality, the entire preboiler was cleaned up by fully opening the switching valve 23.28 and 24.25.
Switch to fully closed, condenser 1 → condensate port/tub 2 → desalination equipment 3
→ Low pressure heater 4 → Deaerator 5 → Water booster pump 7 → Water pump bypass system 14 → High pressure heater 9 → High pressure cleanup system 16 → Condenser 1.
In order to further increase the iron removal effect, auxiliary steam 12 is added to the deaerator 5.
The aim is to remove iron by heating.

本発明によるプレボイラクリーンアップの予想効果を第
2図に示す。
The expected effects of preboiler cleanup according to the present invention are shown in FIG.

第2図よりプレボイラ系統の効果としては、従来のクリ
ーンアップ方法に対し、復水プロー、復水再循環及び、
低圧クリーンアップと同時に高圧ヒータ廻シのクリーン
アップを実施でき、全体のプレボイラクリーンアップ所
要時間を大巾に短縮することが可能である。
From Figure 2, the effects of the preboiler system are as follows: Condensate plow, condensate recirculation, and
The high-pressure heater rotation can be cleaned up at the same time as the low-pressure cleanup, making it possible to significantly shorten the overall preboiler cleanup time.

〔発明の効果〕〔Effect of the invention〕

以上の説明によシ、今まで実績的に多くの時間を費やし
ていた高圧クリーンアップ連用を低圧クーンアツプと同
時に実施すること及び、電磁フィルタによる除鉄効果の
増大によシ、プレイポイう系統クリーンアップ時間は大
巾に短縮可能である。
According to the above explanation, it is possible to carry out continuous high-pressure clean-up, which has traditionally taken a lot of time, at the same time as low-pressure clean-up, and to increase the effect of iron removal using electromagnetic filters. The time can be drastically reduced.

尚、上記クリーンアップ所要時間の短縮化に伴ない使用
純水の節約及び、ポンプ等補機動力低減の効果もある。
In addition, with the shortening of the time required for cleanup, there is also the effect of saving pure water used and reducing the power of auxiliary equipment such as pumps.

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

K1図は本発明の一実施例を示す系統図、嬉2図は本発
明によるクリーンアップ工程及び鉄分濃度を示す説明図
、第3図は従来のプレボイラクリーンアップ系統を示す
系統図、第4図は従来のクリーンアップ工程及び鉄分濃
度を示す説明図である。 1・・・復水器、2・・・復水ポンプ、3・・・脱塩装
置、4・・・低圧ヒータ、5・・・脱気器、7・・・給
水ブースタポンプ、9・・・高圧ヒータ、11・・・復
水系統、22・・・電磁フィルタ、23〜25・・・切
替弁。
Figure K1 is a system diagram showing an embodiment of the present invention, Figure 2 is an explanatory diagram showing the cleanup process and iron concentration according to the present invention, Figure 3 is a system diagram showing a conventional preboiler cleanup system, and Figure 4 is a system diagram showing an example of the present invention. The figure is an explanatory diagram showing a conventional cleanup process and iron concentration. 1... Condenser, 2... Condensate pump, 3... Desalination device, 4... Low pressure heater, 5... Deaerator, 7... Water supply booster pump, 9... - High pressure heater, 11... Condensate system, 22... Electromagnetic filter, 23-25... Switching valve.

Claims (1)

【特許請求の範囲】[Claims] 1、給水中の溶存気体を除去する脱気器と給水ポンプ単
独又は、給水ブースタポンプを直列に前置した蒸気発生
器給水供給装置と、高圧給水加熱器及びそれらの機器群
を連絡する管及び弁類で構成される蒸気動力プラントの
給水系統に於いて、最終高圧給水加熱器出口給水管から
分岐し、蒸気発生器給水供給装置入口管に接続する循環
回路を設け、且つ該循環回路中の循環法は、専用設置又
は他設備と兼用した不溶解固形物除去装置を貫流する如
く構成したことを特徴とするプラントの高圧系クリーン
アップ系統。
1. A deaerator for removing dissolved gas in the feed water, a feed water pump alone, or a steam generator feed water supply system with a feed water booster pump installed in series, a high pressure feed water heater, and pipes connecting the equipment group. In the water supply system of a steam power plant consisting of valves, a circulation circuit is provided that branches from the final high-pressure feedwater heater outlet water supply pipe and connects to the steam generator feedwater supply system inlet pipe, and The circulation method is a high-pressure cleanup system for a plant that is configured to flow through an undissolved solids removal device that is installed exclusively or is used in conjunction with other equipment.
JP25563684A 1984-12-05 1984-12-05 High pressure system clean-up system of plant Pending JPS61134509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25563684A JPS61134509A (en) 1984-12-05 1984-12-05 High pressure system clean-up system of plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25563684A JPS61134509A (en) 1984-12-05 1984-12-05 High pressure system clean-up system of plant

Publications (1)

Publication Number Publication Date
JPS61134509A true JPS61134509A (en) 1986-06-21

Family

ID=17281494

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25563684A Pending JPS61134509A (en) 1984-12-05 1984-12-05 High pressure system clean-up system of plant

Country Status (1)

Country Link
JP (1) JPS61134509A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003014884A (en) * 2001-07-02 2003-01-15 Mitsubishi Heavy Ind Ltd Supply water purification apparatus and nuclear power facility
JP2003222305A (en) * 2002-02-01 2003-08-08 Mitsubishi Heavy Ind Ltd Clean-up operating device of power generation plant and operating method
JP2015190711A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Device and method for cleaning up water supply system
JP2015190710A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Device and method for cleaning up water supply system
JP2015190709A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Cleanup device and cleanup method for water supply system
JP5878223B1 (en) * 2014-10-21 2016-03-08 中国電力株式会社 Low pressure cleanup method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003014884A (en) * 2001-07-02 2003-01-15 Mitsubishi Heavy Ind Ltd Supply water purification apparatus and nuclear power facility
JP2003222305A (en) * 2002-02-01 2003-08-08 Mitsubishi Heavy Ind Ltd Clean-up operating device of power generation plant and operating method
JP2015190711A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Device and method for cleaning up water supply system
JP2015190710A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Device and method for cleaning up water supply system
JP2015190709A (en) * 2014-03-28 2015-11-02 三菱日立パワーシステムズ株式会社 Cleanup device and cleanup method for water supply system
JP5878223B1 (en) * 2014-10-21 2016-03-08 中国電力株式会社 Low pressure cleanup method

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