JPH02192501A - Water feed control device during fcb of drum boiler - Google Patents

Water feed control device during fcb of drum boiler

Info

Publication number
JPH02192501A
JPH02192501A JP846589A JP846589A JPH02192501A JP H02192501 A JPH02192501 A JP H02192501A JP 846589 A JP846589 A JP 846589A JP 846589 A JP846589 A JP 846589A JP H02192501 A JPH02192501 A JP H02192501A
Authority
JP
Japan
Prior art keywords
drum level
load
opening
steam
drum
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.)
Granted
Application number
JP846589A
Other languages
Japanese (ja)
Other versions
JP2698141B2 (en
Inventor
Tadao Shiozaki
塩崎 忠雄
Takayo Kawase
川瀬 隆世
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 JP846589A priority Critical patent/JP2698141B2/en
Publication of JPH02192501A publication Critical patent/JPH02192501A/en
Application granted granted Critical
Publication of JP2698141B2 publication Critical patent/JP2698141B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Abstract

PURPOSE:To prevent the excessive increase of a drum level due to the excessive feed of water by a method wherein simultaneously with the starting of FCB, a regulating valve for the feed of steam to a turbine for driving a boiler water feed pump is rapidly controlled for opening operation, and after the starting of the rise of a drum level, the valve is throttled according to a load and then returned to normal control. CONSTITUTION:A steam feed regulating valve 13 is rapidly controlled for opening to a set specified opening simultaneously with FCB (forced load cutoff). Lowering phenomenon of a drum level is stopped, and converted into a rise. A differentiator 40 raptures the rise phenomenon to control a switching device 42. A change rate controller 45 outputs a target value signal, outputted according to a load from a function generator 43, and an opening signal, corresponding to a rate of change single outputted according to a load from a function generator 44, to a steam feed regulating control derive part 12, and the opening of the regulating valve is controlled according to restoration of a drum level. When the drum level is restored to a value within an allowable deviation based on a given set value, an H/L monitor 41 raptures the restoration to switch a switching device 7, and transfer to drum level single element control corresponding to a drum level signal is effected.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はドラムボイラのFCB (急速負荷遮断)時の
給水制御装置に係り、特にFCB時のボイラ給水ポンプ
駆動用タービンへの蒸気供給加減制御に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a feed water control device for a drum boiler during FCB (rapid load shedding), and particularly to control of steam supply to a turbine for driving a boiler feed water pump during FCB. Regarding.

【従来の技術〕[Conventional technology]

ドラムボイラへ給水するボイラ給水ポンプを翻動するタ
ービンへの蒸気供給量制御は、ドラムレベルが所定の値
となるように蒸気供給加減弁の開度を制御することによ
って行なっている。
The amount of steam supplied to the turbine, which operates the boiler feed water pump that supplies water to the drum boiler, is controlled by controlling the opening degree of the steam supply control valve so that the drum level becomes a predetermined value.

第4図は、従来のこの種の給水制御装置を示しており、
1は減算器、2はP+Il1節器(3要素)。
Figure 4 shows a conventional water supply control device of this type.
1 is a subtractor, 2 is a P+I1 node (3 elements).

3はP+I調節器(単要素)、4は加算器、5はP+I
調節器、6は切替器(3要素−単要素)、7は切替器、
8は切替器(ホールド用)、9は関数発生器、10は加
算器、11は切替器(ホールド用)。
3 is P+I regulator (single element), 4 is adder, 5 is P+I
regulator, 6 is a switch (3 elements - single element), 7 is a switch,
8 is a switch (for hold), 9 is a function generator, 10 is an adder, and 11 is a switch (for hold).

12は蒸気供給加減弁操作駆動部、13は蒸気供給加減
弁である。
Reference numeral 12 indicates a steam supply control valve operation drive unit, and 13 indicates a steam supply control valve.

以上のような給水制御装置において、FCB時には、P
CBと同時に蒸気供給加減弁13の開度を規定開度まで
急速に開操作制御してドラムレベルの低下(タービン加
減弁絞込みによる圧力上昇と急速な燃料絞込みによる気
泡の収縮による)を防止するが、その後通常の制御に戻
すときにボイラ発生蒸気流量よりも給水流量が多くなる
と、ドラムレベルが上昇し、オーバーシュートによって
ドラムレベルが過上昇することがある。
In the water supply control device as described above, during FCB, P
At the same time as the CB, the opening of the steam supply control valve 13 is rapidly controlled to a specified opening to prevent the drum level from dropping (due to pressure increase due to turbine control valve throttling and air bubble contraction due to rapid fuel throttling). If the flow rate of feed water becomes larger than the flow rate of steam generated by the boiler when returning to normal control after that, the drum level will rise, and the drum level may rise excessively due to overshoot.

タービン駆動のボイラ給水ポンプを用いた給水制御にお
いて、PCB時の給水制御の難点は、ボイラ給水ポンプ
駆動用タービンの駆動蒸気源であるタービン油気蒸気が
PCBと同時に喪失するので0缶ボイラの蒸気に切替る
操作が必要であり、この時の駆動蒸気源の確保とボイラ
給水ポンプ駆動用タービンへの蒸気供給加減弁制御であ
る。
In feed water control using a turbine-driven boiler feed water pump, the difficulty in controlling the feed water during PCB is that the turbine oil steam, which is the driving steam source for the turbine that drives the boiler feed water pump, is lost at the same time as the PCB, so the steam of the zero-can boiler is lost. At this time, it is necessary to secure the driving steam source and control the steam supply control valve to the boiler feed water pump driving turbine.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

特に、従来の給水制御装置では、PCB時のドラムレベ
ルの低下を防止した後の給水過多についての配慮がなさ
れておらず、ドラムレベルが過上昇する問題があった。
In particular, conventional water supply control devices do not take into account excessive water supply after preventing a drop in the drum level during PCB, and there is a problem in which the drum level rises excessively.

従って、本発明の目的は、PCB時のドラムレベルの低
下防止はもちろんのこと、その後の給水過多によるドラ
ムレベルの過上昇を防止することができる給水制御装置
を提供することにある。
Therefore, an object of the present invention is to provide a water supply control device that can not only prevent the drum level from decreasing during PCB but also prevent the drum level from rising excessively due to excessive water supply thereafter.

〔課題を解決するための手段〕[Means to solve the problem]

この目的を達成するために5本発明は、タービン駆動の
ボイラ給水ポンプを用いたドラムボイラのFe2時の給
水制御装置において、PCB開始と同時に前記ボイラ給
水ポンプ駆動用タービンへの蒸気供給加減弁を規定開度
まで急速に開操作制御し、ドラムレベルが上昇開始後は
負荷に応じて定められた変化率に従って前記蒸気供給加
減弁を絞込み操作制御し、その後通常の加減操作制御に
戻す加減弁操作制御回路を設けたことを特徴とする。
In order to achieve this object, the present invention provides a feed water control system for Fe2 of a drum boiler using a turbine-driven boiler feed water pump, in which the steam supply control valve to the turbine for driving the boiler feed water pump is controlled at the same time as the start of PCB. Opening control is performed rapidly to a specified opening degree, and after the drum level starts to rise, the steam supply control valve is controlled to be narrowed down according to a rate of change determined according to the load, and then the control valve is returned to normal control. It is characterized by being equipped with a control circuit.

〔作用〕[Effect]

PCBと同時に蒸気供給加減弁が規定開度まで急速に開
操作されるのでボイラ給水ポンプは十分な給水量を確保
してドラムレベルの低下を抑制する。そして、ドラムレ
ベルの低下が止まって上昇に転じると負荷に応じて定め
られた変化率に従って前記蒸気供給加減弁を絞込み操作
制御し、その後通常の加減操作制御に戻すので、給水過
多によるドラムレベルの過上昇が防止できる。
Since the steam supply control valve is rapidly opened to the specified opening at the same time as the PCB, the boiler feed water pump ensures a sufficient amount of water supply and suppresses a drop in the drum level. When the drum level stops decreasing and begins to rise, the steam supply control valve is throttled and controlled according to the rate of change determined according to the load, and then returns to normal control, so that the drum level due to excessive water supply is reduced. Excessive rise can be prevented.

〔実施例〕〔Example〕

以下、第1図〜第3図を参照して本発明の詳細な説明す
る。
Hereinafter, the present invention will be explained in detail with reference to FIGS. 1 to 3.

第2図は、蒸気タービン運転プラントの系統図であり、
21はボイラ、22はタービン蒸気加減弁、23は高中
圧タービン、24は低圧タービン、25は復水器、26
.27はタービン駆動形ボイラ給水ポンプ、28は電動
機駆動形ボイラ給水ポンプ、29は給水流量調節弁、3
0はタービン油気パイプ、31は2SH入口蒸気パイプ
である。
Figure 2 is a system diagram of a steam turbine operating plant;
21 is a boiler, 22 is a turbine steam control valve, 23 is a high and intermediate pressure turbine, 24 is a low pressure turbine, 25 is a condenser, 26
.. 27 is a turbine-driven boiler feed pump, 28 is an electric motor-driven boiler feed pump, 29 is a feed water flow rate control valve, 3
0 is a turbine oil pipe, and 31 is a 2SH inlet steam pipe.

13は前記ボイラ給水ポンプ26.27の邸動用タービ
ンへの蒸気供給加減弁であり、第4図を参照して前述し
た従来の蒸気供給加減弁と同じものである。
Reference numeral 13 denotes a steam supply control valve for the boiler feed water pump 26, 27 to the turbine for operation, which is the same as the conventional steam supply control valve described above with reference to FIG.

前記ボイラ給水ポンプ26.27の駆動用タービンへの
蒸気供給源としては1通常、45%負荷以上ではタービ
ン油気が使用され、45%負荷未満では低温再熱蒸気が
使用され、Fe2時には前記両蒸気とも喪失するので0
缶ボイラの蒸気が使用される(切替えられる)。
As a steam supply source to the driving turbine of the boiler feed water pump 26, 27, normally, turbine oil is used at a load of 45% or more, low-temperature reheated steam is used at a load of less than 45%, and in the case of Fe2, both of the above are used. It is also lost as steam, so it is 0.
Can boiler steam is used (switched over).

第1図は前記蒸気供給加減弁13を開閉操作制御する給
水制御装置のブロック図であり、第4図を参照して前述
した従来の給水制御装置と同一の構成部品には同一参照
符号を付してその説明を省略する。
FIG. 1 is a block diagram of a water supply control device that controls the opening/closing operation of the steam supply control valve 13, and the same components as those of the conventional water supply control device described above with reference to FIG. 4 are given the same reference numerals. The explanation will be omitted.

40はドラムレベルの変化量を微分する微分器、41は
ドラムレベルの設定値に対する高低をモニタするH/L
モニタ、42は切替器7と切替器11の間に設けられた
切替器、43は負荷に応じた目標値信号を発生する関数
発生器、44は負荷に応じた変化率信号を発生する関数
発生器、45は変化率制限器である。
40 is a differentiator that differentiates the amount of change in the drum level, and 41 is a H/L that monitors the level of the drum level relative to the set value.
A monitor, 42 a switch provided between the switch 7 and the switch 11, 43 a function generator that generates a target value signal according to the load, and 44 a function generator that generates a rate of change signal according to the load. 45 is a rate of change limiter.

次に第3図を参照しながら制御動作を説明する。Next, the control operation will be explained with reference to FIG.

蒸気供給加減弁13の開閉操作制御はPCBと同時に加
算器10で設定される規定の開度になるように切替器7
と切替器42によって切替えられ。
The opening/closing operation of the steam supply control valve 13 is controlled by the switching device 7 so that the opening degree is set to the specified opening degree by the adder 10 at the same time as the PCB.
and is switched by the switch 42.

蒸気供給加減弁13はこの規定の開度まで急速に開操作
される。このとき、加算器10は関数発生器9から負荷
に応じて出力される開度補正信号と現在の開度信号を加
算して規定の開度信号を発生する。・この規定の開度信
号は、負荷が大きいほど大きくなる。
The steam supply control valve 13 is rapidly opened to this prescribed opening degree. At this time, the adder 10 adds the opening correction signal output from the function generator 9 according to the load and the current opening signal to generate a specified opening signal.・This specified opening signal becomes larger as the load becomes larger.

PCBと同時にドラムレベルは下降するが、蒸気供給加
減弁13の開度が増して給水流量が増えることによりや
がて下降現象は止まり、上昇に転じる。微分器40はこ
の上昇現象を捉えて切替器42を制御し、変化率制限器
45から出力される開度信号を蒸気供給加減弁操作駆動
部12に与えて開閉操作制御(絞込み操作制御)を開始
する。
The drum level falls at the same time as the PCB, but as the opening degree of the steam supply control valve 13 increases and the water supply flow rate increases, the downward phenomenon eventually stops and begins to rise. The differentiator 40 captures this rising phenomenon and controls the switch 42, and provides the opening signal output from the rate of change limiter 45 to the steam supply control valve operation drive unit 12 to perform opening/closing operation control (narrowing operation control). Start.

このとき変化率制限器45は、関数発生器43から負荷
に応じて出力される目標値信号と関数発生器44から負
荷に応じて出力される変化率信号に応じた開度信号を出
力する。ドラムレベルの最下点からの回復速度は、高負
荷でのPCBでは遅く。
At this time, the rate of change limiter 45 outputs an opening signal according to the target value signal output from the function generator 43 according to the load and the rate of change signal output from the function generator 44 according to the load. Recovery speed from the lowest point of drum level is slow for PCB under high load.

低負荷でのPCBでは早い。このために、関数発生器4
4は負荷に応じた変化率信号を発生して加減弁開度をド
ラムレベルの回復に合わせて制御する。
It is fast for PCB with low load. For this purpose, function generator 4
4 generates a change rate signal according to the load to control the opening degree of the adjustment valve in accordance with the recovery of the drum level.

ドラムレベルが所定の設定値に対して許容偏差以内に回
復すると、H/Lモニタ41がこれを捉えて前記切替器
7を切替え、ドラムレベル信号に応じたドラムレベル単
要素制御に移る。
When the drum level recovers to within the allowable deviation with respect to the predetermined set value, the H/L monitor 41 detects this and switches the switch 7 to switch to drum level single element control according to the drum level signal.

〔発明の効果〕〔Effect of the invention〕

以上のように本発明は、PCB開始と同時に前記ボイラ
給水ポンプ駆動用タービンへの蒸気供給加減弁を規定開
度まで急速に開操作制御し、ドラムレベルが上昇開始後
は負荷に応じて定められた変化率に従って前記蒸気供給
加減弁を絞込み操作制御し、その後通常の加減操作制御
に戻すようにしているので、給水過多によるドラムレベ
ルの過上昇を防止することができる。
As described above, the present invention rapidly controls the opening of the steam supply control valve to the turbine for driving the boiler feed water pump to a specified opening at the same time as the start of PCB, and after the drum level starts to rise, the control valve is opened according to the load. Since the steam supply control valve is controlled in a narrow manner according to the rate of change, and then returned to normal control, it is possible to prevent the drum level from rising excessively due to excessive water supply.

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

第1図は本発明になるドラムボイラのPCB時の給水制
御装置のブロック図、第2図は蒸気タービン運転プラン
トの系統図、第3図は制御特性図、第4図は従来のドラ
ムボイラのPCB時の給水制御装置のブロック図である
。 12・・・・・・蒸気供給加減弁操作駆動部。 13・・・・・・蒸気供給加減弁、  40・・・・・
・微分器、41・・・・・・H/Lモニタ、  42・
・・・・・切替器、43.44・・・・・・関数発生器
、  45・・・・・・変化率制限器。 第tv!J 第2図 蒸気、′嚇沿77D深井 第3図 O t 時間 本発明により特I注 従来孜術に1か持I江 第4図 給水流量 神ラムしベル 薫謎シん量 蒸合Lイヰ給刀0ノ入弁
Fig. 1 is a block diagram of the feed water control device during PCB of the drum boiler according to the present invention, Fig. 2 is a system diagram of a steam turbine operation plant, Fig. 3 is a control characteristic diagram, and Fig. 4 is a diagram of a conventional drum boiler. It is a block diagram of a water supply control device at the time of PCB. 12... Steam supply control valve operation drive unit. 13... Steam supply control valve, 40...
・Differentiator, 41...H/L monitor, 42・
......Switcher, 43.44...Function generator, 45...Change rate limiter. Part tv! J Fig. 2 Steam, 77D Fukai Fig. 3 O t Time According to the present invention, the custom-made conventional method has 1 or I River Fig. 4 Water supply flow rate God Ram and bell smoke mysterious sink amount 0 no entry into the supply sword

Claims (1)

【特許請求の範囲】 1、タービン駆動のボイラ給水ポンプを用いたドラムボ
イラのFCB時の給水制御装置において、FCB開始と
同時に前記ボイラ給水ポンプ駆動用タービンへの蒸気供
給加減弁を規定開度まで急速に開操作制御し、ドラムレ
ベルが上昇開始後は負荷に応じて定められた変化率に従
つて前記蒸気供給加減弁を絞込み操作制御し、その後通
常の加減操作制御に戻す加減弁操作制御回路を設けたこ
とを特徴とするドラムボイラの FCB時の給水制御装置。
[Claims] 1. In a water supply control device during FCB of a drum boiler using a turbine-driven boiler feed pump, at the same time as FCB starts, the steam supply control valve to the turbine for driving the boiler feed water pump is adjusted to a specified opening degree. A regulating valve operation control circuit that rapidly controls the opening operation, and after the drum level starts to rise, controls the steam supply regulating valve to narrow down according to a rate of change determined according to the load, and then returns to normal regulating operation control. A water supply control device for FCB of a drum boiler, characterized in that it is provided with:
JP846589A 1989-01-19 1989-01-19 Water supply control device for FCB of drum boiler Expired - Fee Related JP2698141B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP846589A JP2698141B2 (en) 1989-01-19 1989-01-19 Water supply control device for FCB of drum boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP846589A JP2698141B2 (en) 1989-01-19 1989-01-19 Water supply control device for FCB of drum boiler

Publications (2)

Publication Number Publication Date
JPH02192501A true JPH02192501A (en) 1990-07-30
JP2698141B2 JP2698141B2 (en) 1998-01-19

Family

ID=11693883

Family Applications (1)

Application Number Title Priority Date Filing Date
JP846589A Expired - Fee Related JP2698141B2 (en) 1989-01-19 1989-01-19 Water supply control device for FCB of drum boiler

Country Status (1)

Country Link
JP (1) JP2698141B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104964268A (en) * 2015-07-23 2015-10-07 济南裕兴化工有限责任公司 Automatic water feeding method, using electric contact water level indicator signal, of boiler DSC system
CN112944322A (en) * 2021-03-03 2021-06-11 宝钢湛江钢铁有限公司 Control method of water supply system in FCB process of thermal power generator set
CN113565575A (en) * 2021-08-16 2021-10-29 京能十堰热电有限公司 Boiler wall temperature protection assessment and control method for steam pump fault combined electric pump
CN115264485A (en) * 2022-09-27 2022-11-01 国网山西省电力公司电力科学研究院 Water level automatic control system for water storage tank of supercritical boiler

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104964268A (en) * 2015-07-23 2015-10-07 济南裕兴化工有限责任公司 Automatic water feeding method, using electric contact water level indicator signal, of boiler DSC system
CN104964268B (en) * 2015-07-23 2017-03-15 济南裕兴化工有限责任公司 The method that Boiler DCS System realizes automatic loading water using electric contact point fluviograph signal
CN112944322A (en) * 2021-03-03 2021-06-11 宝钢湛江钢铁有限公司 Control method of water supply system in FCB process of thermal power generator set
CN113565575A (en) * 2021-08-16 2021-10-29 京能十堰热电有限公司 Boiler wall temperature protection assessment and control method for steam pump fault combined electric pump
CN115264485A (en) * 2022-09-27 2022-11-01 国网山西省电力公司电力科学研究院 Water level automatic control system for water storage tank of supercritical boiler
CN115264485B (en) * 2022-09-27 2023-01-13 国网山西省电力公司电力科学研究院 Water level automatic control system for water storage tank of supercritical boiler

Also Published As

Publication number Publication date
JP2698141B2 (en) 1998-01-19

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