JPH0949606A - Variable pressure once-through boiler - Google Patents

Variable pressure once-through boiler

Info

Publication number
JPH0949606A
JPH0949606A JP20359595A JP20359595A JPH0949606A JP H0949606 A JPH0949606 A JP H0949606A JP 20359595 A JP20359595 A JP 20359595A JP 20359595 A JP20359595 A JP 20359595A JP H0949606 A JPH0949606 A JP H0949606A
Authority
JP
Japan
Prior art keywords
water
boiler
outlet port
economizer
flow rate
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
JP20359595A
Other languages
Japanese (ja)
Inventor
Shigekazu Hori
茂和 堀
Kazuo Murakami
和生 村上
Hideo Mori
英生 森
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP20359595A priority Critical patent/JPH0949606A/en
Publication of JPH0949606A publication Critical patent/JPH0949606A/en
Pending legal-status Critical Current

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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

PROBLEM TO BE SOLVED: To permit conducting the reduction of deterioration in water quality at the inlet port of an economizer as well as the reduction in consumption of life of the pipe base of a feed water pipe upon the inflow of stagnated water, kept in the condition of dead water for a long period of time whereby the water quality is deteriorated and the temperature thereof is reduced, by a method wherein a purge water tube, connecting the outlet port of a boiler recirculating flow rate regulating value and a feed water tube at the outlet port of the economizer, is installed. SOLUTION: The outlet port of a boiler recirculating flow rate regulating valve 12 is connected to the outlet port of an economizer 2 through a purge water tube 19 whereby dead water in the outlet port of the boiler recirculating flow rate regulating valve 12 is purged to the outlet port of the economizer 2 utilizing a pressure difference between the outlet port and the inlet port of the economizer 2. This operation can not be covered by the warming tube 16 of a boiler circulation pump. According to this method, boiler feed water, treated by chemical treatment, is taken into the outlet port tube of the boiler recirculating flow rate regulating valve 12 at all times whereby dead water is prevented, local deterioration of water quality as well as the cooling of a pipeline is prevented, the deterioration of quality of boiler feed water upon starting the recirculatlng operation and the thermal shock of a tube base are prevented. Especially, when composite water treatment is applied on the feed water treatment of the boiler, it is effective as the countermeasure of corrosion of parts whereat dead water is stagnated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は変圧貫流ボイラに係り、
特に変圧貫流ボイラの起動時、低負荷時におけるボイラ
再循環配管での水再循環装置におけるボイラ給水の水質
悪化を低減するのに好適な変圧貫流ボイラに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a transformer once-through boiler,
In particular, the present invention relates to a transformer once-through boiler suitable for reducing deterioration of water quality of boiler feed water in a water recirculation device in a boiler recirculation pipe when the transformer once-through boiler is activated and has a low load.

【0002】[0002]

【従来の技術】従来のボイラ装置は、図3に示されるよ
うに、ボイラ循環ポンプ11、ボイラ循環ポンプ出入口
のボイラ再循環配管13、汽水分離器貯水タンクドレン
レベル調節弁15及び汽水分離器貯水タンクドレン管1
4は、通常運転中はボイラ水が再循環しないため死水部
となる。
2. Description of the Related Art As shown in FIG. 3, a conventional boiler apparatus includes a boiler circulation pump 11, a boiler recirculation pipe 13 at the inlet and outlet of the boiler circulation pump, a brackish water separator water storage tank drain level control valve 15 and a brackish water separator water storage. Tank drain pipe 1
No. 4 is a dead water part because boiler water is not recirculated during normal operation.

【0003】これらの系統の死水及び負荷降下時のボイ
ラ再循環運転までのボイラ再循環配管13での停滞部の
温度降下防止策として、節炭器出口のボイラ給水の一部
を、ボイラ循環ポンプウォーミング配管16、汽水分離
器貯水タンクドレンレベル調節弁ウォーミング配管17
で取り出し、ボイラ循環ポンプ11の出口及び汽水分離
器ドレンタンクレベル調節弁15に注水して、死水の排
除及びボイラ循環ポンプ11、汽水分離器貯水タンクド
レンレベル調節弁15のウォーミングを実施していた。
As a measure to prevent a temperature drop in the stagnant portion of the boiler recirculation pipe 13 until the boiler recirculation operation at the time of dead water and load drop of these systems, a part of the boiler feed water at the outlet of the economizer is used as a boiler circulation pump. Warming piping 16, brackish water separator water storage tank drain level control valve warming piping 17
The water is taken out at the outlet of the boiler circulation pump 11 and injected into the brackish water separator drain tank level control valve 15 to remove dead water and warm the boiler circulation pump 11 and the brackish water separator storage tank drain level control valve 15. It was

【0004】しかし、ボイラ再循環流量調節弁12の出
口のボイラ再循環配管13における死水、ウォーミング
の対策は考慮されていなかった。
However, measures against dead water and warming in the boiler recirculation pipe 13 at the outlet of the boiler recirculation flow rate control valve 12 have not been considered.

【0005】なお、図3において、1は給水管、2は節
炭器、3は火炉、4は蒸発器、5は過熱器、6は過熱低
減器、7は過熱低減器スプレー管、9は汽水分離器、1
0は汽水分離器貯水タンク、18はボイラ循環ポンプウ
ォーミング逃がし管、20は主蒸気管である。
In FIG. 3, 1 is a water supply pipe, 2 is a economizer, 3 is a furnace, 4 is an evaporator, 5 is a superheater, 6 is an overheat reducer, 7 is an overheat reducer spray pipe, and 9 is Brackish water separator, 1
0 is a brackish water separator water storage tank, 18 is a boiler circulation pump warming relief pipe, and 20 is a main steam pipe.

【0006】[0006]

【発明が解決しようとする課題】上記従来技術は、通常
運転中の死水の排除及びウォーミングの配慮がされてお
らず、負荷降下の際のボイラ再循環運転時のボイラ循環
流量調節弁出口滞留水の給水への流れ込みによる節炭器
入口の給水水質の悪化、滞留冷水流入による給水管管台
部のサーマルショックによる寿命消費の増大の問題が考
えられる。
In the above-mentioned prior art, the dead water during normal operation is not removed and warming is not taken into consideration, and the boiler circulation flow rate control valve outlet retention during boiler recirculation operation during load drop It is considered that there is a problem that the quality of the water supply at the inlet of the economizer is deteriorated due to the flow of water into the water supply, and the lifespan consumption is increased due to the thermal shock of the water supply pipe abutment due to the inflow of accumulated cold water.

【0007】本発明の目的は、長期間死水となり水質が
悪化及び温度が低下した滞留水が、給水管へ流入した場
合の節炭器入口水質の悪化及び給水管管台の寿命消費を
低減することができる変圧貫流ボイラを提供することに
ある。
An object of the present invention is to reduce the deterioration of the water quality at the inlet of the economizer and the consumption of the life of the water supply nozzle when the accumulated water, which has been dead water for a long period of time and whose water quality has deteriorated and whose temperature has decreased, flows into the water supply pipe. The purpose is to provide a transformer once-through boiler.

【0008】[0008]

【課題を解決するための手段】上記目的は、ボイラ再循
環流量調節弁出口部と節炭器出口給水管とを結ぶパージ
水管を設置することにより達成される。
The above object can be achieved by installing a purge water pipe connecting the outlet of the boiler recirculation flow rate control valve and the economizer outlet water supply pipe.

【0009】[0009]

【作用】パージ水管には、節炭器入口と出口の差圧が作
用する。それによって、ボイラ再循環流量調節弁出口の
水は節炭器出口連絡管側に流れ、その分、新水が給水管
からボイラ再循環流量調節弁側へ流れ込み、常に給水が
入れ替わるので、死水による滞留水水質の悪化、放熱に
より冷却されることがない。
[Operation] A differential pressure between the inlet and outlet of the economizer acts on the purge water pipe. As a result, the water at the boiler recirculation flow rate control valve outlet flows to the economizer outlet communication pipe side, and the new water flows from the water supply pipe to the boiler recirculation flow rate control valve side by that amount, and the water supply is always replaced, so dead water is generated. The quality of accumulated water is not deteriorated, and it is not cooled by heat radiation.

【0010】[0010]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。
Embodiments of the present invention will be described below with reference to the drawings.

【0011】図1は本発明の第1の実施例に係る変圧貫
流ボイラの給水系統図である。
FIG. 1 is a water supply system diagram of a variable pressure once-through boiler according to a first embodiment of the present invention.

【0012】ボイラの起動時には、給水管1から定格流
量の約5%の給水が節炭器2、火炉3、蒸発器4へ送ら
れ、かつ汽水分離器9、汽水分離貯水タンク10を経て
ボイラ再循環配管13への給水はボイラ循環ポンプ11
で上昇され、ボイラ再循環流量調節弁12で調節され、
定格流量の約23%のボイラ給水が流れ、ボイラの最低
給水量が確保される。
At the time of starting the boiler, about 5% of the rated flow rate of the feed water is sent from the feed water pipe 1 to the economizer 2, the furnace 3, and the evaporator 4, and further passes through the brackish water separator 9 and the brackish water separation water storage tank 10 to the boiler. Water is supplied to the recirculation pipe 13 by the boiler circulation pump 11
And is adjusted by the boiler recirculation flow rate control valve 12,
About 23% of the rated flow rate of boiler feed water flows, and the minimum feed amount of boiler is secured.

【0013】このとき、給水は汽水分離器9で汽水分離
され、ドレンとして給水の全量が汽水分離器貯水タンク
10に流入し、その内、汽水分離器貯水タンクドレンレ
ベル調節弁15は、約5%の給水を図示していない復水
器へ逃がしながら、汽水分離器貯水タンク10のレベル
を制御する。
At this time, the feed water is subjected to brackish water separation by the brackish water separator 9, and the entire amount of the feed water as a drain flows into the brackish water separator storage tank 10, of which the brackish water separator storage tank drain level control valve 15 has about 5 The level of the brackish water separator water storage tank 10 is controlled while letting% water supply to a condenser not shown.

【0014】この状態でボイラが点火されると、蒸発器
4出口で蒸気が発生してくるようになり、ボイラの昇
温、85kg/cm2 までの昇圧が行われ、発生した蒸
気は過熱器5、主蒸気管20を経て図示していないター
ビンに供給される。
When the boiler is ignited in this state, steam is generated at the outlet of the evaporator 4, the temperature of the boiler is raised and the pressure is increased to 85 kg / cm 2 , and the generated steam is superheated. 5, it is supplied to a turbine (not shown) via the main steam pipe 20.

【0015】さらに、負荷上昇に伴い燃料量が多くなる
と、蒸発器4での蒸気割合が増し、約28%負荷で蒸発
器4の出口で全て蒸気となり、ボイラは貫流モードへ移
行し、さらに給水量、燃料量が増加され、ボイラの圧
力、タービン出力が増加する。28%負荷以上では汽水
分離器9での発生ドレンが無くなることから、ボイラ再
循環流量調節弁12は全閉となり、ボイラ循環ポンプ1
1の運転は停止する。
Further, when the amount of fuel increases as the load increases, the steam ratio in the evaporator 4 increases, and at the load of about 28%, all steam becomes steam at the outlet of the evaporator 4, the boiler shifts to the once-through mode, and the feed water is further supplied. The amount of fuel and the amount of fuel are increased, and the boiler pressure and turbine output are increased. When the load is 28% or more, the drainage generated in the brackish water separator 9 disappears, so the boiler recirculation flow rate control valve 12 is fully closed, and the boiler circulation pump 1
The operation of 1 is stopped.

【0016】この状態では、ボイラ循環ポンプ11、ボ
イラ再循環配管13、及び汽水分離器貯水タンクドレン
レベル調節弁15は死水となる。ボイラの停止または負
荷降下では、前述の逆動作で貫流モードから循環モード
に移行するため、汽水分離器9では水(約300℃、8
5kg/cm2 飽和水)が発生する。そして、そのボイ
ラ水をボイラ循環ポンプ11、ボイラ再循環配管13、
及び汽水分離器ドレンタンクレベル調節弁15へ流すた
め、またボイラ水質の悪化、節炭器2の管台のサーマル
ショックを防止するため、予め貫流モード中の死水のパ
ージ及びウォーミングを行う必要がある。
In this state, the boiler circulation pump 11, the boiler recirculation pipe 13, and the brackish water separator water storage tank drain level control valve 15 become dead water. When the boiler is stopped or the load is reduced, the reverse operation described above shifts from the once-through mode to the circulation mode. Therefore, in the steam separator 9, water (about 300 ° C., 8
5 kg / cm 2 saturated water) is generated. Then, the boiler water is supplied to the boiler circulation pump 11, the boiler recirculation pipe 13,
In order to flow to the drain water tank level control valve 15 of the brackish water separator, and to prevent deterioration of boiler water quality and thermal shock of the nozzle of the economizer 2, it is necessary to purge and warm dead water in the once-through mode in advance. is there.

【0017】その方法は、節炭器2の出口のボイラ水を
ボイラ循環ポンプ11の出口、及び汽水分離器ドレンタ
ンクレベル調節弁15に注水し、汽水分離器貯水タンク
10へパージすることにより実施され、パージ水は系内
の汽水分離器貯水タンク10で回収するため、ボイラ循
環ポンプウォーミング逃がし配管18より過熱低減器6
の入口の過熱低減器スプレー管7へ逃がされる。
The method is carried out by injecting the boiler water at the outlet of the economizer 2 into the outlet of the boiler circulation pump 11 and the steam tank separator drain tank level control valve 15 and purging it into the steam separator water storage tank 10. Since the purged water is recovered in the brackish water separator water storage tank 10 in the system, the boiler circulation pump warming relief pipe 18 is used to remove the overheat reducer 6.
Is released to the superheat reducer spray pipe 7 at the inlet of the.

【0018】本発明は、ボイラ再循環流量調節弁12の
出口と節炭器2の出口とをパージ水管19で連絡するこ
とにより、節炭器2の出口と入口の差圧を利用して前述
のボイラ循環ポンプウォーミング管16ではカバーでき
ないボイラ再循環流量調節弁12の出口の死水を節炭器
2の出口へパージするものである。
The present invention utilizes the differential pressure between the outlet and inlet of the economizer 2 by connecting the outlet of the boiler recirculation flow rate control valve 12 and the outlet of the economizer 2 with the purge water pipe 19. The dead water at the outlet of the boiler recirculation flow rate control valve 12 that cannot be covered by the boiler circulation pump warming pipe 16 is purged to the outlet of the economizer 2.

【0019】それにより、常に薬品処理されたボイラ給
水をボイラ再循環流量調節弁12出口管へ取り込み死水
を防止し、局部的な水質悪化、配管の冷却を防ぎ、ボイ
ラ再循環運転開始時のボイラ給水水質の悪化、管台のサ
ーマルショックを防止する。図2は本発明の第2の実施
例に係る変圧貫流ボイラの給水系統図である。
As a result, the boiler feed water, which has been always treated with chemicals, is taken into the outlet pipe of the boiler recirculation flow rate control valve 12 to prevent dead water, to prevent local deterioration of water quality and cooling of the pipe, and to start the boiler recirculation operation. Prevents water quality deterioration and thermal shock of the nozzle. FIG. 2 is a water supply system diagram of a once-through type boiler according to a second embodiment of the present invention.

【0020】本実施例は、パージ水取り出し位置をボイ
ラ再循環流量調節弁12入口とし、ボイラ再循環流量調
節弁12を開運転するものである。
In this embodiment, the purge water take-out position is the inlet of the boiler recirculation flow rate control valve 12, and the boiler recirculation flow rate control valve 12 is opened.

【0021】この実施例の効果は、ボイラ再循環流量調
節弁12の前流配管にまでパージ範囲を広げ、かつ起動
用大型弁の当該弁自体ウォーミングも可能となることが
挙げられる。
The effect of this embodiment is that the purge range can be extended to the upstream pipe of the boiler recirculation flow rate control valve 12, and the large startup valve itself can be warmed.

【0022】[0022]

【発明の効果】以上説明したように、本発明によれば、
ボイラ再循環流量調節弁出口部と節炭器出口給水管とを
結ぶパージ水管を設置するようにしたので、ボイラの長
期高負荷帯運転後の停止及び負荷下げ時において、死水
部を減らすことによる循環モード始時の水質悪化及び管
台のサーマルショックの軽減が図れる効果がある。特
に、ボイラ給水処理に複合水処理を適用した場合には、
死水部の腐食(孔食)の対策として有効である。
As described above, according to the present invention,
Since a purge water pipe that connects the outlet of the boiler recirculation flow rate control valve and the water supply pipe of the economizer is installed, it is possible to reduce the dead water portion when stopping and reducing the load after long-term high load operation of the boiler. There is an effect that water quality deterioration at the beginning of the circulation mode and thermal shock of the nozzle can be reduced. Especially when applying complex water treatment to boiler feedwater treatment,
It is effective as a measure against corrosion (pitting corrosion) in the dead water area.

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

【図1】本発明の第1の実施例に係る変圧貫流ボイラの
給水系統図である。
FIG. 1 is a water supply system diagram of a variable pressure once-through boiler according to a first embodiment of the present invention.

【図2】本発明の第2の実施例に係る変圧貫流ボイラの
給水系統図である。
FIG. 2 is a water supply system diagram of a variable pressure once-through boiler according to a second embodiment of the present invention.

【図3】従来例の変圧貫流ボイラの給水系統図である。FIG. 3 is a water supply system diagram of a conventional once-through transformer.

【符号の説明】[Explanation of symbols]

1 給水管 2 節炭器 3 火炉 4 蒸発器 5 過熱器 6 過熱低減器 7 過熱低減器スプレー管 9 汽水分離器 10 汽水分離器貯水タンク 11 ボイラ循環ポンプ 12 ボイラ再循環流量調節弁 13 ボイラ再循環配管 19 パージ水管 1 Water supply pipe 2 Coal saver 3 Furnace 4 Evaporator 5 Superheater 6 Superheat reducer 7 Superheat reducer Spray pipe 9 Brackish water separator 10 Brackish water separator Water storage tank 11 Boiler circulation pump 12 Boiler recirculation flow control valve 13 Boiler recirculation Piping 19 Purge water pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ボイラ循環ポンプとボイラ再循環流量調
節弁とボイラ再循環配管から成るボイラ起動用再循環系
統を有する変圧貫流ボイラにおいて、 前記ボイラ再循環配管と節炭器の出口の間に、前記ボイ
ラ再循環配管から前記節炭器の出口へ通常運転時の死水
をパージするパージ配管を設けたことを特徴とする変圧
貫流ボイラ。
1. A transformer once-through boiler having a boiler start-up recirculation system consisting of a boiler circulation pump, a boiler recirculation flow rate control valve, and a boiler recirculation pipe, wherein the boiler recirculation pipe and the outlet of the economizer are connected to each other. A transformer once-through boiler, wherein a purge pipe for purging dead water during normal operation is provided from the boiler recirculation pipe to the outlet of the economizer.
JP20359595A 1995-08-09 1995-08-09 Variable pressure once-through boiler Pending JPH0949606A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20359595A JPH0949606A (en) 1995-08-09 1995-08-09 Variable pressure once-through boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20359595A JPH0949606A (en) 1995-08-09 1995-08-09 Variable pressure once-through boiler

Publications (1)

Publication Number Publication Date
JPH0949606A true JPH0949606A (en) 1997-02-18

Family

ID=16476675

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20359595A Pending JPH0949606A (en) 1995-08-09 1995-08-09 Variable pressure once-through boiler

Country Status (1)

Country Link
JP (1) JPH0949606A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104613457A (en) * 2015-01-29 2015-05-13 上海上电电力工程有限公司 Smoke temperature rising system for maintaining normal operation of SCR for direct-flow and natural circulation boilers
CN106224936A (en) * 2016-08-25 2016-12-14 中国大唐集团科学技术研究院有限公司华东分公司 A kind of low-level (stack-gas) economizer optimizes operation control system and control method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104613457A (en) * 2015-01-29 2015-05-13 上海上电电力工程有限公司 Smoke temperature rising system for maintaining normal operation of SCR for direct-flow and natural circulation boilers
CN106224936A (en) * 2016-08-25 2016-12-14 中国大唐集团科学技术研究院有限公司华东分公司 A kind of low-level (stack-gas) economizer optimizes operation control system and control method thereof
CN106224936B (en) * 2016-08-25 2018-11-27 中国大唐集团科学技术研究院有限公司华东分公司 A kind of control method of low-level (stack-gas) economizer optimization operation control system

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