JPH1026343A - Method and apparatus for calculating coal output upon purging remaining coal in mill of coal fired boiler - Google Patents

Method and apparatus for calculating coal output upon purging remaining coal in mill of coal fired boiler

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Publication number
JPH1026343A
JPH1026343A JP17931196A JP17931196A JPH1026343A JP H1026343 A JPH1026343 A JP H1026343A JP 17931196 A JP17931196 A JP 17931196A JP 17931196 A JP17931196 A JP 17931196A JP H1026343 A JPH1026343 A JP H1026343A
Authority
JP
Japan
Prior art keywords
coal
output
signal
mill
time
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
JP17931196A
Other languages
Japanese (ja)
Other versions
JP3769822B2 (en
Inventor
Shigekazu Furukawa
繁一 古川
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IHI Corp
Original Assignee
IHI Corp
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Filing date
Publication date
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Priority to JP17931196A priority Critical patent/JP3769822B2/en
Publication of JPH1026343A publication Critical patent/JPH1026343A/en
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Publication of JP3769822B2 publication Critical patent/JP3769822B2/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

PROBLEM TO BE SOLVED: To prevent decrease of exhaust gas and rise of a vapor temperature by accurately obtaining coal output to estimated to be discharged from a mill at the time of purging remaining coal and eliminating supply of the coal more than a required amount exceeding a fuel flow command into a furnace of a boiler. SOLUTION: The method comprises the steps of holding a coal output 11 at the time of stopping a stoker 3 at the time of mill tripping to make a remaining coal signal 12, multiplying the signal 12 by a coal output simulation gain 34 given as a function of a time based on test data previously obtained to obtain a coal output simulation signal 21, and outputting a coal output 23 estimated to be outputted from the mill at the time of purging the remaining coal.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、石炭焚ボイラのミ
ル残炭パージ時における出炭量算出方法及び装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for calculating a coal output during a coal residue boiler purge in a coal-fired boiler.

【0002】[0002]

【従来の技術】一般に、石炭焚ボイラの場合、図3に示
される如く、コールバンカ1に貯留された石炭を、モー
タ等の駆動装置2によって駆動される給炭機3により、
石炭粉砕用のミル4へ投入し、該ミル4において粉砕さ
れた微粉炭を微粉炭管5を介してバーナ6へ空気搬送
し、ボイラ7の火炉8内において燃焼させるようになっ
ている。
2. Description of the Related Art Generally, in the case of a coal-fired boiler, as shown in FIG. 3, coal stored in a coal bunker 1 is supplied to a coal feeder 3 driven by a drive device 2 such as a motor.
The pulverized coal pulverized in the mill 4 for coal pulverization is pneumatically conveyed to the burner 6 through the pulverized coal pipe 5 and burned in the furnace 8 of the boiler 7.

【0003】尚、図中、9はモータ等の駆動装置10に
よって開閉される石炭ゲートである。
In FIG. 1, reference numeral 9 denotes a coal gate which is opened and closed by a driving device 10 such as a motor.

【0004】前記ミル4からボイラ7の火炉8内へ供給
される石炭(微粉炭)の出炭量は、直接計測することが
できないため、給炭機3上に現在ある石炭の重量を図示
していないロードセル等で測定すると共に、給炭機3の
駆動装置2の回転数を測定し、これらの積を給炭機3か
らミル4へ供給される給炭量とし、該給炭量を前記ミル
4からボイラ7の火炉8内へ供給されるであろう石炭の
出炭量としている。
Since the amount of coal (pulverized coal) supplied from the mill 4 into the furnace 8 of the boiler 7 cannot be directly measured, the weight of the coal present on the coal feeder 3 is shown. In addition to the measurement using a load cell or the like, the number of revolutions of the driving device 2 of the coal feeder 3 is measured, and the product of these is defined as the coal feed supplied from the coal feeder 3 to the mill 4. This is the amount of coal that will be supplied from the mill 4 to the furnace 8 of the boiler 7.

【0005】又、前記ミル4は、一基のボイラ7に対し
て、通常、複数台(例えば六台)設けられており、ボイ
ラ7の定常運転時においては、各ミル4の出炭量の合計
と、ボイラ負荷指令(MWD)に基づく燃料流量指令と
を比較し、該比較結果に応じて各給炭機3への給炭量指
令を求め、該給炭量指令に基づいて各給炭機3の制御を
行うようになっている。
In general, a plurality of (for example, six) mills 4 are provided for one boiler 7, and when the boiler 7 is in a normal operation, the amount of coal output of each mill 4 is reduced. The sum is compared with a fuel flow rate command based on a boiler load command (MWD), and based on the comparison result, a coal feed command to each coal feeder 3 is obtained. The device 3 is controlled.

【0006】一方、例えば、一台のミル4に何らかの異
常が発生した場合、該ミル4と、それに対応する給炭機
3とを緊急停止させるが、何らかの異常が発生したミル
4をそのまま放置しておくと、ミル4内に残った石炭が
発火する可能性があるため、ミル4の緊急停止後、ミル
4内に残った石炭を火炉8内へパージする、いわゆる残
炭パージを行う必要がある。
On the other hand, for example, when any abnormality occurs in one of the mills 4, the mill 4 and the corresponding coal feeder 3 are urgently stopped, but the mill 4 in which any abnormality has occurred is left as it is. In this case, since coal remaining in the mill 4 may ignite, it is necessary to perform so-called residual coal purging in which the coal remaining in the mill 4 is purged into the furnace 8 after the emergency stop of the mill 4. is there.

【0007】しかしながら、前述の如く、一台のミル4
を緊急停止した後、残りの複数台(例えば五台)のミル
4からボイラ7の火炉8内へ供給される石炭の出炭量が
バランスしている状態で、緊急停止したミル4の残炭パ
ージを行った場合、前記燃料流量指令を上回る必要以上
の石炭がボイラ7の火炉8内へ供給されてしまうことと
なり、燃料過多となって排ガスO2が低下したり、蒸気
温度が上昇する虞れがあった。
However, as described above, one mill 4
After the emergency stop of the mill 4, the remaining coal of the mill 4 that is emergency stopped is in a state in which the amount of coal supplied from the remaining plural (for example, five) mills 4 into the furnace 8 of the boiler 7 is balanced. If the purging is performed, unnecessarily large amount of coal exceeding the fuel flow rate command will be supplied into the furnace 8 of the boiler 7, resulting in excessive fuel and a decrease in the exhaust gas O 2 and an increase in steam temperature. There was.

【0008】このため、従来においては、図4及び図5
に示される如く、定常運転時には給炭機3からミル4へ
投入される給炭量11をそのまま信号12として出力す
る(図中、b側に切り換えられる)一方、ミルトリップ
時には給炭機3停止時点での給炭量11をホールドして
残炭量を表わす信号12として出力する(図中、a側に
切り換えられる)切換器13と、ミルトリップ後の残炭
パージミル起動指令14が出力された時点から所要時間
(t[分])の間だけ“1”の信号15を出力するタイ
マ16と、定常運転時には信号発生器17から出力され
る“0”の信号18を信号19として出力する(図中、
b側に切り換えられる)一方、ミルトリップ後の残炭パ
ージミル起動時には前記切換器13から出力される信号
12を、前記タイマ16で設定された時間の間だけ信号
19として出力する(図中、a側に切り換えられる)切
換器20と、該切換器20から出力される信号19が変
化した場合に、その信号19の変化に対し、予め設定し
た時間遅れが生じるよう追従させて、残炭パージ時にミ
ル4から出炭されると予測される出炭量模擬信号21を
出力する一次遅れ器22と、該一次遅れ器22から出力
される出炭量模擬信号21を前記給炭機3からミル4へ
投入される給炭量11に加え、出炭量23を出力する加
算器24とから出炭量算出装置を構成していた。
For this reason, in the prior art, FIGS.
As shown in FIG. 2, during the steady operation, the amount of coal 11 supplied to the mill 4 from the coal feeder 3 is output as it is as a signal 12 (switched to the b side in the figure). A switcher 13 that holds the coal supply amount 11 at the time and outputs it as a signal 12 representing the remaining coal amount (switched to a side in the figure) and a residual coal purge mill start command 14 after the mill trip are output. A timer 16 that outputs a signal 15 of “1” only for a required time (t [minutes] from the time) and a signal 18 of “0” output from a signal generator 17 during a steady operation are output as a signal 19 ( In the figure,
On the other hand, when the residual coal purge mill is started after the mill trip, the signal 12 output from the switch 13 is output as the signal 19 only for the time set by the timer 16 (a in the figure). Switch 20), and when the signal 19 output from the switch 20 changes, the change in the signal 19 is followed so as to cause a preset time delay, and the remaining coal is purged when the residual coal is purged. A primary delay unit 22 that outputs a coal removal amount simulation signal 21 predicted to be removed from the mill 4, and a coal removal amount simulation signal 21 output from the primary delay unit 22 is transmitted from the coal feeder 3 to the mill 4. In addition to the coal feed amount 11 fed into the furnace, an adder 24 that outputs a coal output 23 constitutes a coal output calculation device.

【0009】前述の如き従来の出炭量算出装置の場合、
定常運転時には、給炭機3からミル4へ投入される給炭
量11が加算器24へ出力されると共に、該給炭量11
が切換器13を経由し、そのまま信号12として切換器
20へ出力されるが、該切換器20においては定常運転
時には信号発生器17から出力される“0”の信号18
が信号19として一次遅れ器22へ出力され、該一次遅
れ器22から前記加算器24へ出力される出炭量模擬信
号21は“0”となるため、加算器24からは給炭量1
1がそのまま出炭量23として出力される。
In the case of the conventional coal output calculation device as described above,
At the time of steady operation, the amount of coal 11 charged into the mill 4 from the coal feeder 3 is output to the adder 24 and the amount of coal 11
Is output as it is as a signal 12 to the switch 20 via the switch 13, and in the switch 20, a "0" signal 18 output from the signal generator 17 during the steady operation is output.
Is output as a signal 19 to the primary delay unit 22, and the coal output simulation signal 21 output from the primary delay unit 22 to the adder 24 is “0”.
1 is output as it is as the coal output 23.

【0010】一方、ミル4に何らかの異常が発生し、該
ミル4と、それに対応する給炭機3とを緊急停止させた
場合、図5に示される如く、給炭量11はミルトリップ
時にx[ton/h]から“0”となるが、切換器13
は給炭機3停止時点での給炭量11をホールドして残炭
量を表わす信号12として切換器20へ出力する。
On the other hand, if an abnormality occurs in the mill 4 and the mill 4 and the corresponding coal feeder 3 are urgently stopped, as shown in FIG. [Ton / h] is changed to “0”.
Holds the coal supply amount 11 at the time of stopping the coal feeder 3 and outputs the signal to the switch 20 as a signal 12 representing the remaining coal amount.

【0011】ミルトリップ後、残炭パージミル起動指令
14が出力されると、タイマ16から所要時間(t
[分])の間だけ“1”の信号15が出力され、前記切
換器13から出力される信号12が、前記タイマ16で
設定された時間の間だけ切換器20から信号19として
一次遅れ器22へ出力され、該一次遅れ器22において
は、切換器20から出力される信号19の変化に対し、
予め設定した時間遅れが生じるよう追従させて、残炭パ
ージ時にミル4から出炭されると予測される出炭量模擬
信号21が加算器24へ出力され、該加算器24におい
て、前記一次遅れ器22から出力される出炭量模擬信号
21が前記給炭機3からミル4へ投入される給炭量11
(ミルトリップ後は“0”となっている)に加えられ、
出炭量23として出力される。
After the mill trip, when the residual coal purge mill start command 14 is output, the required time (t
[Minutes]), the signal 15 of “1” is output, and the signal 12 output from the switch 13 is changed from the switch 20 to the signal 19 only as a signal 19 during the time set by the timer 16. 22. In the first-order lag unit 22, a change in the signal 19 output from the switch 20 is
Following a preset time delay, a coal removal amount simulation signal 21 predicted to be removed from the mill 4 at the time of residual coal purge is output to an adder 24, and the primary delay is generated by the adder 24. The coal output simulation signal 21 output from the boiler 22 is supplied to the mill 4 from the coal feeder 3 to the coal feed 11
("0" after the mill trip)
It is output as the coal output 23.

【0012】これにより、一台のミル4を緊急停止した
後、残りの複数台(例えば五台)のミル4からボイラ7
の火炉8内へ供給される石炭の出炭量23がバランスし
ている状態で、緊急停止したミル4の残炭パージを行っ
た場合には、残炭パージによってボイラ7の火炉8内へ
供給される石炭の出炭量23の分だけ、残りの複数台の
ミル4からボイラ7の火炉8内へ供給される石炭の出炭
量23が減少される。
Thus, after one of the mills 4 is stopped in an emergency, the remaining plurality of (for example, five) mills 4 are removed from the boiler 7.
When the residual coal purging of the mill 4 that has been emergency stopped is performed in a state where the coal output 23 of the coal supplied into the furnace 8 is balanced, the residual coal is supplied into the furnace 8 of the boiler 7 by the residual coal purging. The amount of coal output 23 of the coal supplied from the remaining plurality of mills 4 into the furnace 8 of the boiler 7 is reduced by the amount of coal output 23 of the coal.

【0013】[0013]

【発明が解決しようとする課題】前述の如く、残炭パー
ジを開始してミル4から石炭が出炭される場合、その出
炭量23は、残炭パージ開始からある時間経過するまで
は増加して行き、その後、略一定となる状態が所定時間
継続し、続いて減少して行くパターンとなるが、前述の
如く、単に一次遅れ器22を設けて出炭量模擬信号21
を作成するのでは、残炭パージ開始からある時間経過す
るまでの出炭量23増加の傾きと、出炭量23減少の傾
きとを一義的に決まる同一のカーブでしか設定すること
ができないため、実際の出炭量との誤差が大きくなり、
精度的に見て充分であるとは言えず、依然として燃料過
多となって排ガスO2が低下したり、蒸気温度が上昇す
る虞れがあり、改善の余地が残されていた。
As described above, when coal is discharged from the mill 4 by starting the residual coal purge, the coal output 23 increases until a certain time has elapsed since the start of the residual coal purge. After that, the state of becoming substantially constant continues for a predetermined time and then decreases, but as described above, the primary delay device 22 is simply provided and the coal output simulation signal 21 is provided.
Is created, the slope of the increase in the coal output 23 and the slope of the decrease in the coal output 23 from the start of the residual coal purge until a certain time has elapsed can be set only by the same curve that is uniquely determined. , The difference from the actual coal output increases,
Viewed in precision manner not be said to be sufficient, or reduces the exhaust gas O 2 is still fuel-excess, there is a possibility that the steam temperature is increased, room for improvement has been left.

【0014】本発明は、斯かる実情に鑑み、残炭パージ
時にミル4から出炭されると予測される出炭量23を精
度よく求めることができ、燃料流量指令を上回る必要以
上の石炭がボイラ7の火炉8内へ供給されてしまうこと
をなくし、排ガスO2の低下並びに蒸気温度の上昇を防
止し得る石炭焚ボイラのミル残炭パージ時における出炭
量算出方法及び装置を提供しようとするものである。
According to the present invention, in view of such circumstances, it is possible to accurately obtain the coal removal amount 23 predicted to be removed from the mill 4 at the time of purging residual coal, and to obtain coal that exceeds the fuel flow rate command more than necessary. A method and an apparatus for calculating the amount of coal output at the time of purging remaining coal in a mill of a coal-fired boiler that can prevent the exhaust gas O 2 from being reduced and prevent the steam temperature from increasing without being supplied into the furnace 8 of the boiler 7. Is what you do.

【0015】[0015]

【課題を解決するための手段】本発明は、ミルトリップ
時に給炭機3停止時点での給炭量11をホールドして残
炭量とし、該残炭量に対して、時間の関数として与えら
れる出炭量模擬ゲイン34を掛け、残炭パージ時にミル
4から出炭されると予測される出炭量23を求めること
を特徴とする石炭焚ボイラのミル残炭パージ時における
出炭量算出方法にかかるものである。
According to the present invention, the amount of coal 11 at the time when the coal feeder 3 is stopped at the time of the mill trip is held as the remaining coal, and the remaining coal is given as a function of time. A coal output boiler simulated gain 34 to obtain a coal output 23 predicted to be removed from the mill 4 when the residual coal is purged. It depends on the method.

【0016】又、本発明は、定常運転時には給炭機3か
らミル4へ投入される給炭量11をそのまま信号12と
して出力する一方、ミルトリップ時には給炭機3停止時
点での給炭量11をホールドして残炭量を表わす信号1
2として出力する切換器13と、定常運転時には信号発
生器25から出力される“0”の信号26を信号30と
して出力する一方、ミルトリップ後の残炭パージミル起
動時には信号発生器27から出力される“1”の信号2
8を信号30として出力する切換器29と、該切換器2
9から出力される信号30が“0”から“1”へ変化し
た場合に、その変化率を設定値以下の範囲内に制限する
処理を行って変化率補正信号32を出力する変化率制限
器31と、該変化率制限器31から出力される変化率補
正信号32に基づき出炭量模擬ゲイン34を求めて出力
する関数発生器33と、該関数発生器33から出力され
る出炭量模擬ゲイン34を前記切換器13から出力され
る給炭量11の信号12に掛け、残炭パージ時にミル4
から出炭されると予測される出炭量模擬信号21を出力
する乗算器35と、該乗算器35から出力される出炭量
模擬信号21を前記給炭機3からミル4へ投入される給
炭量11に加え、出炭量23を出力する加算器24とを
備えたことを特徴とする石炭焚ボイラのミル残炭パージ
時における出炭量算出装置にかかるものである。
Also, according to the present invention, during steady operation, the amount of coal 11 fed from the coal feeder 3 to the mill 4 is output as a signal 12 as it is, while at the time of a mill trip, the amount of coal supplied when the coal feeder 3 is stopped. Signal 1 indicating the remaining coal amount by holding 11
The switch 13 outputs the signal as 2 and the signal 26 of “0” output from the signal generator 25 during the steady operation is output as the signal 30, while the signal generator 27 outputs the signal when the residual coal purge mill is started after the mill trip. "1" signal 2
8 as a signal 30;
9. When the signal 30 output from 9 changes from “0” to “1”, the rate-of-change limiter outputs a rate-of-change correction signal 32 by performing processing for limiting the rate of change to within a set value or less. 31, a function generator 33 for obtaining and outputting a coal output simulation gain 34 based on a change rate correction signal 32 output from the change rate limiter 31, and a coal output simulation output from the function generator 33 The gain 34 is multiplied by the signal 12 of the coal supply 11 output from the switch 13, and the mill 4
A multiplier 35 that outputs a coal output simulation signal 21 that is predicted to be output from the coal mill, and a coal output simulation signal 21 that is output from the multiplier 35 is input from the coal feeder 3 to the mill 4. The present invention relates to an apparatus for calculating a coal output at the time of a mill residual coal purge of a coal-fired boiler, comprising an adder 24 that outputs a coal output 23 in addition to the coal feed 11.

【0017】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0018】本発明の石炭焚ボイラのミル残炭パージ時
における出炭量算出方法においては、ミルトリップ時に
給炭機3停止時点での給炭量11をホールドして残炭量
とし、該残炭量に対して、予め行ったテストデータに基
づき時間の関数として与えられる出炭量模擬ゲイン34
が掛けられ、残炭パージ時にミル4から出炭されると予
測される出炭量23が求められる。
In the method for calculating the amount of coal output during the purging of residual coal in a mill of a coal-fired boiler according to the present invention, the amount of supplied coal 11 at the time when the coal feeder 3 is stopped at the time of a mill trip is held as the residual coal amount. The coal output simulation gain 34 given as a function of time based on test data performed in advance for the coal output.
Is applied, and a coal removal amount 23 that is predicted to be removed from the mill 4 during the residual coal purge is obtained.

【0019】又、本発明の石炭焚ボイラのミル残炭パー
ジ時における出炭量算出装置においては、定常運転時に
は、給炭機3からミル4へ投入される給炭量11が加算
器24へ出力されると共に、該給炭量11が切換器13
を経由し、そのまま信号12として乗算器35へ出力さ
れるが、該乗算器35には、定常運転時には信号発生器
25から出力される“0”の信号26が切換器29と変
化率制限器31と関数発生器33とを介して出炭量模擬
ゲイン34として出力され、乗算器35から前記加算器
24へ出力される出炭量模擬信号21は“0”となるた
め、加算器24からは給炭量11がそのまま出炭量23
として出力される一方、ミル4に何らかの異常が発生
し、該ミル4と、それに対応する給炭機3とを緊急停止
させた場合、給炭量11はミルトリップ時に“0”とな
るが、切換器13は給炭機3停止時点での給炭量11を
ホールドして残炭量を表わす信号12として乗算器35
へ出力し、ミルトリップ後、残炭パージのためにミル4
が起動されると、信号発生器27から出力される“1”
の信号28が切換器29から信号30として変化率制限
器31へ出力され、該変化率制限器31において、
“0”から“1”へ変化した切換器29からの信号30
の変化率を設定値以下の範囲内に制限する処理が行わ
れ、変化率補正信号32が関数発生器33へ出力され、
該関数発生器33において前記変化率制限器31から出
力される変化率補正信号32に基づき出炭量模擬ゲイン
34が求められて乗算器35へ出力され、該乗算器35
において、前記関数発生器33から出力される出炭量模
擬ゲイン34が前記切換器13から出力される給炭量1
1の信号12に掛けられ、残炭パージ時にミル4から出
炭されると予測される出炭量模擬信号21が前記加算器
24へ出力され、該加算器24において、前記乗算器3
5から出力される出炭量模擬信号21が前記給炭機3か
らミル4へ投入される給炭量11(ミルトリップ後は
“0”となっている)に加えられ、出炭量23として出
力される。
In the apparatus for calculating the amount of coal output during the purging of residual coal in a mill of a coal-fired boiler according to the present invention, the amount of coal 11 fed into the mill 4 from the coal feeder 3 is supplied to the adder 24 during steady operation. Is output and the coal supply amount 11 is
, And is output as it is to the multiplier 35 as the signal 12. The signal 35 of “0” output from the signal generator 25 during the steady operation is output to the switch 29 and the change rate limiter The coal output simulation signal 21 which is output as the coal output simulation gain 34 via the function generator 31 and the function generator 33 and output from the multiplier 35 to the adder 24 is "0". Means that the amount of coal supply 11 is the same
On the other hand, if any abnormality occurs in the mill 4 and the mill 4 and the corresponding coal feeder 3 are urgently stopped, the coal supply amount 11 becomes “0” at the time of the mill trip, The switch 13 holds the coal supply amount 11 at the time of stopping the coal feeder 3 and outputs a signal 12 representing the remaining coal amount to the multiplier 35.
After mill trip, mill 4 to purge residual coal
Is activated, “1” output from the signal generator 27 is output.
Is output from the switch 29 to the change rate limiter 31 as a signal 30. In the change rate limiter 31,
The signal 30 from the switch 29 that has changed from “0” to “1”
Is performed to limit the rate of change of the range within a set value or less, a rate-of-change correction signal 32 is output to a function generator 33,
In the function generator 33, a coal output simulation gain 34 is obtained based on the change rate correction signal 32 output from the change rate limiter 31, and is output to a multiplier 35.
In the above, the coal output simulation gain 34 output from the function generator 33 corresponds to the coal output 1 output from the switch 13.
1 is output to the adder 24, and a coal output simulation signal 21 predicted to be output from the mill 4 when the residual coal is purged is output to the adder 24.
5 is added to the coal feed 11 (to be “0” after the mill trip) fed into the mill 4 from the coal feeder 3 and output as the coal output 23. Is output.

【0020】これにより、一台のミル4を緊急停止した
後、残りの複数台のミル4からボイラ7の火炉8内へ供
給される石炭の出炭量23がバランスしている状態で、
緊急停止したミル4の残炭パージを行った場合には、残
炭パージによってボイラ7の火炉8内へ供給される石炭
の出炭量23の分だけ、残りの複数台のミル4からボイ
ラ7の火炉8内へ供給される石炭の出炭量23が減少さ
れる。
Thus, after the emergency stop of one mill 4, the coal output 23 of the coal supplied from the remaining plurality of mills 4 into the furnace 8 of the boiler 7 is balanced.
When the residual coal is purged from the mill 4 that has been stopped urgently, the remaining plurality of mills 4 feed the boiler 7 from the remaining plurality of mills 4 by the coal output amount 23 supplied to the furnace 8 of the boiler 7 by the residual coal purge. The amount of coal output 23 of the coal supplied into the furnace 8 is reduced.

【0021】ここで、従来のように、単に一次遅れ器2
2を設けて出炭量模擬信号21を作成するのでは、残炭
パージ開始からある時間経過するまでの出炭量23増加
の傾きと、出炭量23減少の傾きとを一義的に決まる同
一のカーブでしか設定することができないが、本発明の
場合には、変化率制限器31と関数発生器33との組合
せにより、残炭パージ開始からある時間経過するまでの
出炭量23増加の傾きと、出炭量23が略一定となる状
態と、出炭量23減少の傾きとをそれぞれ、実機でのテ
ストデータに対応させた時間の関数として設定すること
ができるため、前記加算器24から出力される出炭量2
3と実際の出炭量との誤差が最小限に抑えられ、燃料過
多となって排ガスO2が低下したり、蒸気温度が上昇す
ることがなくなる。
Here, as in the prior art, simply the first-order lag device 2
2 to create the coal output simulation signal 21, the gradient of the increase in the coal output 23 from the start of the residual coal purge until a certain time elapses and the gradient of the decrease in the coal output 23 are uniquely determined. However, in the case of the present invention, the combination of the change rate limiter 31 and the function generator 33 increases the coal output 23 until a certain time has elapsed since the start of the residual coal purge. The slope, the state in which the coal output 23 is substantially constant, and the slope of the decrease in the coal output 23 can be set as a function of time corresponding to test data in an actual machine. Output 2 from coal
The error between 3 and the actual coal output is minimized, so that there is no excess fuel and the exhaust gas O 2 does not drop and the steam temperature does not rise.

【0022】[0022]

【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0023】図1及び図2は本発明を実施する形態の一
例であって、図中、図3〜図5と同一の符号を付した部
分は同一物を表わしており、29は定常運転時には信号
発生器25から出力される“0”の信号26を信号30
として出力する一方、ミルトリップ後の残炭パージミル
起動時には信号発生器27から出力される“1”の信号
28を信号30として出力する切換器、31は前記切換
器29から出力される信号30が“0”から“1”へ変
化した場合に、その変化率を設定値以下の範囲内に制限
する処理を行って変化率補正信号32を出力する変化率
制限器、33は前記変化率制限器31から出力される変
化率補正信号32に基づき出炭量模擬ゲイン34を求め
て出力する関数発生器、35は前記関数発生器33から
出力される出炭量模擬ゲイン34を切換器13から出力
される給炭量11の信号12に掛け、残炭パージ時にミ
ル4から出炭されると予測される出炭量模擬信号21を
出力する乗算器であり、該乗算器35から出力される出
炭量模擬信号21を、加算器24において給炭機3から
ミル4へ投入される給炭量11に加え、出炭量23を出
力するよう構成してある。
FIGS. 1 and 2 show an example of an embodiment of the present invention. In the figures, the parts denoted by the same reference numerals as those in FIGS. 3 to 5 represent the same parts. The signal 26 of “0” output from the signal generator 25 is
On the other hand, at the start of the residual coal purge mill after the mill trip, a switch that outputs the signal 1 of “1” output from the signal generator 27 as the signal 30, and the signal 31 output from the switch 29 is the signal 31. When the rate of change from "0" to "1", a rate-of-change limiter that performs a process of limiting the rate of change to within a set value or less and outputs a rate-of-change correction signal 32; A function generator 35 for obtaining and outputting a coal output simulation gain 34 based on the change rate correction signal 32 output from 31, and outputs a coal output simulation gain 34 output from the function generator 33 from the switch 13. A multiplier 12 which multiplies the signal 12 of the supplied coal quantity 11 to output a coal output simulation signal 21 which is predicted to be output from the mill 4 when the residual coal is purged. Coal power simulation signal 21 In addition to the coal feed amount 11 to be introduced from the coal feeder 3 to the mill 4 in the adder 24, it is configured to output a coal output 23.

【0024】尚、前記変化率制限器31の変化率と、関
数発生器33の関数は、それぞれ予め行ったテストデー
タに基づいて設定するようになっている。
The change rate of the change rate limiter 31 and the function of the function generator 33 are set based on test data previously performed.

【0025】次に、上記図示例の作動を説明する。Next, the operation of the above illustrated example will be described.

【0026】定常運転時には、給炭機3からミル4へ投
入される給炭量11が加算器24へ出力されると共に、
該給炭量11が切換器13を経由し、そのまま信号12
として乗算器35へ出力されるが、該乗算器35には、
定常運転時には信号発生器25から出力される“0”の
信号26が切換器29と変化率制限器31と関数発生器
33とを介して出炭量模擬ゲイン34として出力され、
乗算器35から前記加算器24へ出力される出炭量模擬
信号21は“0”となるため、加算器24からは給炭量
11がそのまま出炭量23として出力される。
During normal operation, the amount 11 of coal supplied to the mill 4 from the coal feeder 3 is output to the adder 24,
The coal supply amount 11 passes through the switch 13 and the signal 12
Is output to the multiplier 35.
At the time of steady operation, the signal 26 of “0” output from the signal generator 25 is output as the coal output simulation gain 34 via the switch 29, the change rate limiter 31, and the function generator 33,
Since the coal output simulation signal 21 output from the multiplier 35 to the adder 24 is “0”, the coal feed 11 is output from the adder 24 as it is as the coal output 23.

【0027】一方、ミル4に何らかの異常が発生し、該
ミル4と、それに対応する給炭機3とを緊急停止させた
場合、図2に示す如く、給炭量11はミルトリップ時に
x[ton/h]から“0”となるが、切換器13は給
炭機3停止時点での給炭量11をホールドして残炭量を
表わす信号12として乗算器35へ出力する。
On the other hand, if some abnormality occurs in the mill 4 and the mill 4 and the corresponding coal feeder 3 are stopped immediately, as shown in FIG. 2, the coal supply amount 11 becomes x [ ton / h] to “0”, but the switch 13 holds the coal supply 11 at the time of stopping the coal feeder 3 and outputs it to the multiplier 35 as a signal 12 representing the remaining coal.

【0028】ミルトリップ後、残炭パージのためにミル
4が起動されると、信号発生器27から出力される
“1”の信号28が切換器29から信号30として変化
率制限器31へ出力され、該変化率制限器31におい
て、“0”から“1”へ変化した切換器29からの信号
30の変化率を設定値以下の範囲内に制限する処理が行
われ、変化率補正信号32が関数発生器33へ出力さ
れ、該関数発生器33において前記変化率制限器31か
ら出力される変化率補正信号32に基づき出炭量模擬ゲ
イン34が求められて乗算器35へ出力され、該乗算器
35において、前記関数発生器33から出力される出炭
量模擬ゲイン34が前記切換器13から出力される給炭
量11の信号12に掛けられ、残炭パージ時にミル4か
ら出炭されると予測される出炭量模擬信号21が前記加
算器24へ出力され、該加算器24において、前記乗算
器35から出力される出炭量模擬信号21が前記給炭機
3からミル4へ投入される給炭量11(ミルトリップ後
は“0”となっている)に加えられ、出炭量23として
出力される。
After the mill trip, when the mill 4 is started for purging the residual coal, a "1" signal 28 output from the signal generator 27 is output from the switch 29 to the change rate limiter 31 as a signal 30. Then, the change rate limiter 31 performs a process of limiting the change rate of the signal 30 from the switch 29 that has changed from “0” to “1” within a range equal to or less than a set value, and the change rate correction signal 32 Is output to a function generator 33, a coal output simulation gain 34 is obtained based on the change rate correction signal 32 output from the change rate limiter 31 in the function generator 33, and is output to a multiplier 35. In the multiplier 35, the coal output simulation gain 34 output from the function generator 33 is multiplied by the signal 12 of the coal feed 11 output from the switch 13, and coal is output from the mill 4 when the residual coal is purged. Expected The coal quantity simulation signal 21 is output to the adder 24, where the coal output quantity simulation signal 21 output from the multiplier 35 is supplied from the coal feeder 3 to the mill 4 in the adder 24. 11 (the value is “0” after the mill trip) and is output as the coal output 23.

【0029】これにより、一台のミル4を緊急停止した
後、残りの複数台(例えば五台)のミル4からボイラ7
の火炉8内へ供給される石炭の出炭量23がバランスし
ている状態で、緊急停止したミル4の残炭パージを行っ
た場合には、残炭パージによってボイラ7の火炉8内へ
供給される石炭の出炭量23の分だけ、残りの複数台の
ミル4からボイラ7の火炉8内へ供給される石炭の出炭
量23が減少される。
Thus, after the emergency stop of one of the mills 4, the boiler 7 is removed from the remaining multiple (for example, five) mills 4.
When the residual coal purging of the mill 4 that has been emergency stopped is performed in a state where the coal output 23 of the coal supplied into the furnace 8 is balanced, the residual coal is supplied into the furnace 8 of the boiler 7 by the residual coal purging. The amount of coal output 23 of the coal supplied from the remaining plurality of mills 4 into the furnace 8 of the boiler 7 is reduced by the amount of coal output 23 of the coal.

【0030】ここで、従来のように、単に一次遅れ器2
2を設けて出炭量模擬信号21を作成するのでは、残炭
パージ開始からある時間経過するまでの出炭量23増加
の傾きと、出炭量23減少の傾きとを一義的に決まる同
一のカーブでしか設定することができないが、本図示例
の場合には、変化率制限器31と関数発生器33との組
合せにより、残炭パージ開始からある時間経過するまで
の出炭量23増加の傾きと、出炭量23が略一定となる
状態と、出炭量23減少の傾きとをそれぞれ、実機での
テストデータに対応させた時間の関数として設定するこ
とができるため、前記加算器24から出力される出炭量
23と実際の出炭量との誤差が最小限に抑えられ、燃料
過多となって排ガスO2が低下したり、蒸気温度が上昇
することがなくなる。
Here, as in the conventional case, the first-order lag device 2 is simply used.
2 to create the coal output simulation signal 21, the gradient of the increase in the coal output 23 from the start of the residual coal purge until a certain time elapses and the gradient of the decrease in the coal output 23 are uniquely determined. However, in the case of the illustrated example, the combination of the change rate limiter 31 and the function generator 33 increases the coal output 23 until a certain time elapses from the start of the residual coal purge. , The state in which the coal output 23 is substantially constant, and the slope of the decrease in the coal output 23, respectively, can be set as functions of time corresponding to the test data in the actual machine. The error between the coal output 23 output from 24 and the actual coal output is kept to a minimum, and there is no excess fuel, so that the exhaust gas O 2 does not decrease and the steam temperature does not increase.

【0031】こうして、残炭パージ時にミル4から出炭
されると予測される出炭量23を精度よく求めることが
でき、燃料流量指令を上回る必要以上の石炭がボイラ7
の火炉8内へ供給されてしまうことをなくし、排ガスO
2の低下並びに蒸気温度の上昇を防止し得る。
In this way, it is possible to accurately obtain the coal removal amount 23 that is predicted to be removed from the mill 4 during the residual coal purging.
To the furnace 8 without exhaust gas O
2 as well as an increase in steam temperature.

【0032】尚、本発明の石炭焚ボイラのミル残炭パー
ジ時における出炭量算出方法及び装置は、上述の図示例
にのみ限定されるものではなく、本発明の要旨を逸脱し
ない範囲内において種々変更を加え得ることは勿論であ
る。
It should be noted that the method and apparatus for calculating the coal output at the time of purging the remaining coal in the mill of the coal-fired boiler of the present invention are not limited to the above-described illustrated examples, but may be made within the scope of the present invention. Of course, various changes can be made.

【0033】[0033]

【発明の効果】以上、説明したように本発明の石炭焚ボ
イラのミル残炭パージ時における出炭量算出方法及び装
置によれば、残炭パージ時にミル4から出炭されると予
測される出炭量23を精度よく求めることができ、燃料
流量指令を上回る必要以上の石炭がボイラ7の火炉8内
へ供給されてしまうことをなくし、排ガスO2の低下並
びに蒸気温度の上昇を防止し得るという優れた効果を奏
し得る。
As described above, according to the method and apparatus for calculating the amount of coal removed during the purging of residual coal in a coal-fired boiler according to the present invention, it is predicted that coal will be released from the mill 4 when purging residual coal. the coal output 23 can be accurately obtained, excessive coal above the fuel flow rate command eliminated that would be supplied to the furnace 8 of the boiler 7, to prevent deterioration and increase of the steam temperature of the exhaust gas O 2 An excellent effect of obtaining can be achieved.

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

【図1】本発明を実施する形態の一例のブロック図であ
る。
FIG. 1 is a block diagram illustrating an example of an embodiment of the present invention.

【図2】本発明を実施する形態の一例のタイムチャート
図である。
FIG. 2 is a time chart of an example of an embodiment of the present invention.

【図3】一般的な石炭焚ボイラの石炭の供給系統を表わ
す概略図である。
FIG. 3 is a schematic diagram illustrating a coal supply system of a general coal-fired boiler.

【図4】従来の石炭焚ボイラのミル残炭パージ時におけ
る出炭量算出装置の一例を表わすブロック図である。
FIG. 4 is a block diagram showing an example of a conventional coal output amount calculation device at the time of purging remaining coal in a mill of a coal-fired boiler.

【図5】図4に示す従来例のタイムチャート図である。FIG. 5 is a time chart of the conventional example shown in FIG.

【符号の説明】[Explanation of symbols]

3 給炭機 4 ミル 11 給炭量 12 信号 13 切換器 21 出炭量模擬信号 23 出炭量 24 加算器 25 信号発生器 26 信号 27 信号発生器 28 信号 29 切換器 30 信号 31 変化率制限器 32 変化率補正信号 33 関数発生器 34 出炭量模擬ゲイン 35 乗算器 Reference Signs List 3 coal feeder 4 mill 11 coal feed 12 signal 13 switch 21 coal output simulation signal 23 coal output 24 adder 25 signal generator 26 signal 27 signal generator 28 signal 29 switch 30 signal 31 change rate limiter 32 Rate-of-change correction signal 33 Function generator 34 Simulated gain of coal output 35 Multiplier

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ミルトリップ時に給炭機(3)停止時点
での給炭量(11)をホールドして残炭量とし、該残炭
量に対して、時間の関数として与えられる出炭量模擬ゲ
イン(34)を掛け、残炭パージ時にミル(4)から出
炭されると予測される出炭量(23)を求めることを特
徴とする石炭焚ボイラのミル残炭パージ時における出炭
量算出方法。
1. A coal output (11) held at the time of a stop of a coal feeder (3) at the time of a mill trip is held as a remaining coal amount, and a coal output amount given as a function of time with respect to the remaining coal amount. Multiplying a simulated gain (34) to obtain a coal removal amount (23) predicted to be removed from the mill (4) at the time of purging residual coal; Amount calculation method.
【請求項2】 定常運転時には給炭機(3)からミル
(4)へ投入される給炭量(11)をそのまま信号(1
2)として出力する一方、ミルトリップ時には給炭機
(3)停止時点での給炭量(11)をホールドして残炭
量を表わす信号(12)として出力する切換器(13)
と、 定常運転時には信号発生器(25)から出力される
“0”の信号(26)を信号(30)として出力する一
方、ミルトリップ後の残炭パージミル起動時には信号発
生器(27)から出力される“1”の信号(28)を信
号(30)として出力する切換器(29)と、 該切換器(29)から出力される信号(30)が“0”
から“1”へ変化した場合に、その変化率を設定値以下
の範囲内に制限する処理を行って変化率補正信号(3
2)を出力する変化率制限器(31)と、 該変化率制限器(31)から出力される変化率補正信号
(32)に基づき出炭量模擬ゲイン(34)を求めて出
力する関数発生器(33)と、 該関数発生器(33)から出力される出炭量模擬ゲイン
(34)を前記切換器(13)から出力される給炭量
(11)の信号(12)に掛け、残炭パージ時にミル
(4)から出炭されると予測される出炭量模擬信号(2
1)を出力する乗算器(35)と、 該乗算器(35)から出力される出炭量模擬信号(2
1)を前記給炭機(3)からミル(4)へ投入される給
炭量(11)に加え、出炭量(23)を出力する加算器
(24)とを備えたことを特徴とする石炭焚ボイラのミ
ル残炭パージ時における出炭量算出装置。
2. In a steady operation, the amount (11) of coal supplied from the coal feeder (3) to the mill (4) is directly changed to a signal (1).
A switch (13) which outputs the signal as (2), and at the time of a mill trip, holds the coal supply (11) at the time of stopping the coal feeder (3) and outputs it as a signal (12) representing the remaining coal.
During normal operation, a signal (26) of "0" output from the signal generator (25) is output as a signal (30), while when the residual coal purge mill is started after the mill trip, the signal is output from the signal generator (27). A switch (29) that outputs the signal (28) of “1” as a signal (30), and a signal (30) output from the switch (29) is “0”.
Is changed from "1" to "1", the rate of change is limited to a range equal to or less than a set value, and the rate-of-change correction signal (3
A rate-of-change limiter (31) for outputting 2) and a function for obtaining and outputting a coal output simulation gain (34) based on a rate-of-change correction signal (32) output from the rate-of-change limiter (31) Multiplying the coal output simulation signal (34) output from the function generator (33) by the coal output (11) signal (12) output from the switch (13); Coal removal amount simulation signal (2) which is predicted to be removed from the mill (4) during the residual coal purge.
A multiplier (35) that outputs 1), and a coal output simulation signal (2) that is output from the multiplier (35).
1) is provided with an adder (24) for outputting a coal output (23) in addition to the coal feed (11) fed from the coal feeder (3) to the mill (4). Output calculation device at the time of mill residual coal purge of a coal-fired boiler.
JP17931196A 1996-07-09 1996-07-09 Method and apparatus for calculating coal output when purging mill residue of coal fired boiler Expired - Fee Related JP3769822B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17931196A JP3769822B2 (en) 1996-07-09 1996-07-09 Method and apparatus for calculating coal output when purging mill residue of coal fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17931196A JP3769822B2 (en) 1996-07-09 1996-07-09 Method and apparatus for calculating coal output when purging mill residue of coal fired boiler

Publications (2)

Publication Number Publication Date
JPH1026343A true JPH1026343A (en) 1998-01-27
JP3769822B2 JP3769822B2 (en) 2006-04-26

Family

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103234219A (en) * 2013-04-24 2013-08-07 广东电网公司电力科学研究院 Circumference air quantity adjustment method and system for pulverized coal boiler after fire coal kind changing
CN104238494A (en) * 2014-07-29 2014-12-24 国家电网公司 Thermal power generating unit coal feed amount control method based on frequency modulation and peak regulation of power grid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103234219A (en) * 2013-04-24 2013-08-07 广东电网公司电力科学研究院 Circumference air quantity adjustment method and system for pulverized coal boiler after fire coal kind changing
CN104238494A (en) * 2014-07-29 2014-12-24 国家电网公司 Thermal power generating unit coal feed amount control method based on frequency modulation and peak regulation of power grid

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