JPH08243429A - Method for controlling coal output amount of mill and device therefor - Google Patents

Method for controlling coal output amount of mill and device therefor

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Publication number
JPH08243429A
JPH08243429A JP5142395A JP5142395A JPH08243429A JP H08243429 A JPH08243429 A JP H08243429A JP 5142395 A JP5142395 A JP 5142395A JP 5142395 A JP5142395 A JP 5142395A JP H08243429 A JPH08243429 A JP H08243429A
Authority
JP
Japan
Prior art keywords
coal
output
signal
command
mill
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
JP5142395A
Other languages
Japanese (ja)
Inventor
Hiroshi Kunisada
寛 国貞
Tomomitsu Kashiwagi
智光 柏木
Hisashi Sakai
久 酒井
Shigeru Kusama
滋 草間
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP5142395A priority Critical patent/JPH08243429A/en
Publication of JPH08243429A publication Critical patent/JPH08243429A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To bring coal output amount close to target value even when a kind of coal is changed by performing new dynamic characteristic evaluation prior to change of an output command and obtaining a correction signal of output amount in accordance therewith and controlling coal feed amount and the number of revolutions of a classifier by the correction signal. CONSTITUTION: The dynamic characteristic evaluation part 70 of a simulating device 64 performs subtraction through respective data of the previously stored standard conditions in accordance with coal moisture 66, hardness 67 of coal, primary air flow rate 68, the number of revolutions 69 of a classifier which have been measured prior to change of an output command 22 and the conversion factor of dead time, and time-lag is calculated. When the output command 22 is changed, new dynamic characteristics T1 ', T2 ' are calculated from the dynamic characteristic storing change width (B2 -B1 ) of output command value B1 , B2 . Furthermore, dynamic characteristics T1 , T2 close to practice are evaluated by multiplying the previously calculated conversion factor. An additional signal correction arithmetic part 85 calculates a preceding additional signal 36 from the dynamic characteristics T1 , T2 . An additional signal correction part 86 outputs an additional correction signal 87 according to the preceding additional signal 36.

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、ミル出炭量制御方法及
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 mill coal output control method and apparatus.

【0002】[0002]

【従来の技術】図4は石炭焚ボイラ等に備えられるミル
1の一例を示したもので、図4では1台のミル1が例示
されているが、通常は1つのボイラに対して複数台のミ
ル1が接続されている。
2. Description of the Related Art FIG. 4 shows an example of a mill 1 provided in a coal-fired boiler or the like. In FIG. 4, one mill 1 is illustrated, but normally, there are a plurality of mills for one boiler. Mill 1 of is connected.

【0003】ミル1は、図示するように、石炭バンカ2
の石炭3を、給炭機モータ4により給炭量を調整できる
ようにした給炭機5により給炭管6を介してミルケーシ
ング7内に投入するようになっており、前記給炭管6か
ら投入された石炭3を、電動機に接続された減速機8を
介して回転駆動される粉砕テーブル9の上面と、圧下装
置10により前記粉砕テーブル9上面に圧接されつつ粉
砕テーブル9の回転に追従して転動する粉砕ローラ11
との間で粉砕するようにしている。
The mill 1 includes a coal bunker 2 as shown in the drawing.
The coal 3 is charged into the mill casing 7 through the coal feeding pipe 6 by the coal feeding device 5 whose amount can be adjusted by the coal feeding motor 4. Follow the rotation of the crushing table 9 while pressing the coal 3 charged from the crushing table 9 with the upper surface of the crushing table 9 which is rotationally driven through the speed reducer 8 connected to the electric motor and the upper surface of the crushing table 9 by the reduction device 10. Grinding roller 11 rolling and rolling
I'm trying to crush between.

【0004】該粉砕によって生じた粉体12は、前記粉
砕テーブル9を囲むように環状に設けられた吹出しポー
ト13からの搬送のための一次空気14によりミルケー
シング7内を吹上げられ、ミルケーシング7内部を上下
に区画する漏斗状のスリットコーン15の周方向複数箇
所に外縁部16を隆起させることによって形成されたス
リット開口部17を通して上方に搬送され、更に上方に
導かれた粉体12は、ミルケーシング7内上部に備えら
れて分級機モータ18により回転が駆動されている回転
式分級機19に導かれて分級され、所定粒度以下の細か
い微粉のみがミルケーシング7頂部に接続された微粉送
出管20を介して石炭焚ボイラ21等のバーナに供給さ
れるようになっている。
The powder 12 produced by the pulverization is blown up in the mill casing 7 by the primary air 14 for transportation from the blow-out port 13 provided in an annular shape so as to surround the pulverizing table 9, and the mill casing 7 is blown. 7 The powder 12 that has been conveyed upward through the slit openings 17 formed by raising the outer edge portion 16 at a plurality of circumferential positions of the funnel-shaped slit cone 15 that divides the interior into upper and lower parts, and is guided further upward is , The fine powder of which the fine particles of a predetermined particle size or less are connected to the rotary classifier 19 which is provided in the upper part of the inside of the mill casing 7 and whose rotation is driven by the classifier motor 18 and which is classified. It is adapted to be supplied to a burner such as a coal-fired boiler 21 via a delivery pipe 20.

【0005】前記回転式分級機19により弾かれた粗粉
は、前記スリットコーン15のスリット開口部17間の
傾斜面を滑落してスリットコーン15下端から粉砕テー
ブル9の中央部に戻されるようになっている。また、前
記石炭焚ボイラ21の制御を行っている出力指令22が
出炭量制御装置23に入力されて、前記給炭機モータ4
の回転数を制御すると共に、分級機モータ18の回転数
を制御するようになっている。石炭焚ボイラ21は、前
記ミル1にて粉砕されて空気搬送により微粉送出管20
を介して供給されてくる微粉炭を燃焼して蒸気を作るよ
うにしている。
The coarse powder repelled by the rotary classifier 19 slides down the inclined surface between the slit openings 17 of the slit cone 15 and is returned from the lower end of the slit cone 15 to the central portion of the crushing table 9. Has become. Further, the output command 22 for controlling the coal-fired boiler 21 is input to the coal output control device 23, and the coal feeder motor 4 is supplied.
The rotation speed of the classifier motor 18 is controlled while the rotation speed of the classifier motor is controlled. The coal-fired boiler 21 is crushed by the mill 1 and conveyed by air to convey the fine powder delivery pipe 20.
The pulverized coal supplied through the is burned to produce steam.

【0006】図5は、前記ミル1の出炭量制御装置23
の一例を示したもので、出炭量制御装置23は、出炭量
指令回路24と、給炭量制御回路25と、分級機回転数
制御回路26とを備えている。
FIG. 5 shows a coal output control device 23 of the mill 1.
As an example, the coal output control device 23 includes a coal output command circuit 24, a coal supply control circuit 25, and a classifier rotation speed control circuit 26.

【0007】出炭量指令回路24は、出力指令22が変
化率制限器27に入力されていると共に、出力指令22
の変化と同時に変化率設定指令28が前記変化率制限器
27に入力されて、負荷上昇時と負荷下降時に所定の変
化率を与えた出力指令信号29が得られるようになって
おり、該出力指令信号29が引算器30に入力され、該
引算器30にて蒸気タービン21aの発電機21bの出
力を検出している出力検出器31aからの出力検出信号
31と引算してその差の信号32を関数発生器33に導
き、差の信号32を出炭量に変換して、図6に示すよう
な出炭量指令信号34を作成している。
In the coal output command circuit 24, the output command 22 is input to the change rate limiter 27, and the output command 22 is output.
The change rate setting command 28 is input to the change rate limiter 27 at the same time as the change of the output, and an output command signal 29 giving a predetermined change rate is obtained when the load increases and when the load decreases. The command signal 29 is input to the subtractor 30, and the subtractor 30 subtracts the output detection signal 31 from the output detector 31a detecting the output of the generator 21b of the steam turbine 21a and subtracting the difference. Is output to the function generator 33, the difference signal 32 is converted into a coal output, and a coal output command signal 34 as shown in FIG. 6 is created.

【0008】一方、前記変化率設定指令28を関数発生
器35に入力することにより、図7中破線で示すような
先行付加信号36を作成し、該先行付加信号36を加算
器37により、前記出炭量指令信号34に加算するよう
にしている。
On the other hand, by inputting the change rate setting command 28 to the function generator 35, a preceding additional signal 36 as shown by the broken line in FIG. 7 is created, and the preceding additional signal 36 is added by the adder 37. It is configured to be added to the coal output command signal 34.

【0009】また、前記出力検出信号31を関数発生器
38に入力して出力検出信号31の大きさに応じた主蒸
気圧力換算値39を求め、該主蒸気圧力換算値39を引
算器40に入力すると共に、石炭焚ボイラ21から蒸気
タービン21aに供給される主蒸気の圧力を検出してい
る主蒸気圧力検出器41aからの検出信号41を前記引
算器40に入力して引算し、差の信号42を関数発生器
43により出炭量の補正信号44に変換し、加算器45
にて前記出炭量指令信号34に加算している。
Further, the output detection signal 31 is input to a function generator 38 to obtain a main steam pressure conversion value 39 corresponding to the magnitude of the output detection signal 31, and the main steam pressure conversion value 39 is subtracted from the subtractor 40. And the detection signal 41 from the main steam pressure detector 41a that detects the pressure of the main steam supplied from the coal-fired boiler 21 to the steam turbine 21a is input to the subtractor 40 and subtracted. , The difference signal 42 is converted into a coal output correction signal 44 by the function generator 43, and the adder 45
Is added to the coal output command signal 34.

【0010】また、出力検出信号31を関数発生器46
に入力して出力検出信号31の大きさに応じた主蒸気温
度換算値47を求め、該主蒸気温度換算値47を前記主
蒸気の温度を検出している主蒸気温度検出器48aの検
出信号48と共に引算器49に入力することにより引算
し、差の信号50を関数発生器51により出炭量の補正
信号52に変換し、加算器53にて前記出炭量指令信号
34に加算している。
Further, the output detection signal 31 is supplied to the function generator 46.
To the main steam temperature conversion value 47 corresponding to the magnitude of the output detection signal 31, and the main steam temperature conversion value 47 is detected by the main steam temperature detector 48a detecting the temperature of the main steam. The difference signal 50 is converted into a correction signal 52 for the coal output by the function generator 51, and added to the output command signal 34 by the adder 53. are doing.

【0011】給炭量制御回路25は、前記出炭量指令回
路24の加算器53からの出炭量指令信号34と、給炭
機5(図4)による給炭量(例えば給炭機モータ4の駆
動速度)を検出している速度検出器54aの給炭量検出
信号54とを引算器55に入力して、引算して求められ
た差からなる給炭制御信号56により、給炭機5の給炭
機モータ4の回転を制御するようになっている。
The coal supply amount control circuit 25 includes a coal output amount command signal 34 from the adder 53 of the coal output amount command circuit 24 and an amount of coal supplied by the coal supply machine 5 (FIG. 4) (for example, a coal supply machine motor). 4) is input to the subtractor 55 and the coal feed control signal 56 including the difference obtained by subtraction is supplied to the subtracter 55. The rotation of the coal feeder motor 4 of the coal machine 5 is controlled.

【0012】また、分級機回転数制御回路26は、前記
給炭量制御回路25の給炭制御信号56を関数発生器5
7に入力して、給炭制御信号56に対応した回転式分級
機19(図4)の回転数を求め、この回転数信号58
を、回転式分級機19の回転数(例えば分級機モータ1
8の駆動速度)を検出している回転数検出器59aの分
級機回転数検出信号59に加算器60を介して加算した
回転数制御信号61により、分級機モータ18の回転数
を制御するようになっている。
Further, the classifier rotation speed control circuit 26 outputs the coal supply control signal 56 of the coal supply amount control circuit 25 to the function generator 5
7 to obtain the rotation speed of the rotary classifier 19 (FIG. 4) corresponding to the coal feeding control signal 56, and the rotation speed signal 58
The rotational speed of the rotary classifier 19 (for example, the classifier motor 1
The driving speed of the classifier motor 18 is controlled by a rotation speed control signal 61 that is added to the classifier rotation speed detection signal 59 of the rotation speed detector 59a, which is detected via the adder 60. It has become.

【0013】図4に示すように、石炭焚ボイラ21で
は、特に起動・停止時等において、出力指令22によっ
て負荷が増加したり減少したりする制御が行われるが、
ミル1に供給された石炭3は、粉砕テーブル9と粉砕ロ
ーラ11によって粉砕された後、一次空気14によって
上昇させられ、回転式分級機19により粗粉が分離され
て微粉のみが微粉送出管20を介して石炭焚ボイラ21
に供給されるようになっているため、前記出力指令22
が変化して出炭量制御装置23からの給炭制御信号56
が変化しても、給炭機5により微粉炭ミル1への給炭量
が変化してから石炭焚ボイラ21に供給される微粉の出
炭量が実際に変化するまでに大きな時間遅れが生じてし
まう。
As shown in FIG. 4, in the coal-fired boiler 21, the load is increased or decreased by the output command 22 especially at the time of starting and stopping.
The coal 3 supplied to the mill 1 is crushed by the crushing table 9 and the crushing roller 11 and then raised by the primary air 14, the coarse powder is separated by the rotary classifier 19, and only the fine powder is sent to the fine powder delivery pipe 20. Through the coal-fired boiler 21
Is supplied to the output command 22.
Changes and the coal feed control signal 56 from the coal output control device 23
Even if the value changes, a large time delay occurs after the amount of coal supplied to the pulverized coal mill 1 is changed by the coal feeder 5 and before the amount of fine coal output to the coal-fired boiler 21 actually changes. Will end up.

【0014】このため、図6に示すように変化する出炭
量指令信号34に基づいて、単に前記給炭機モータ4及
び分級機モータ18を制御した場合には、図8に示すよ
うに出炭量指令信号34(目標値)と実際の出炭量との
間に非常に大きな偏差S1を生じてしまう問題がある。
この点、ガスや油を燃料とするボイラ等では、出力指令
の変化に応じて直ちに燃料流量を制御することができる
ので、前記したような時間遅れは殆ど問題にならない。
Therefore, when the coal feeder motor 4 and the classifier motor 18 are simply controlled based on the coal output command signal 34 which changes as shown in FIG. 6, the output as shown in FIG. There is a problem that a very large deviation S 1 occurs between the coal amount command signal 34 (target value) and the actual amount of coal produced.
In this respect, in a boiler or the like that uses gas or oil as fuel, the fuel flow rate can be immediately controlled according to changes in the output command, so the above-mentioned time delay does not pose a problem.

【0015】上記した出炭量の応答遅れを防止するため
に、図5及び図7に示すように、関数発生器33からの
出炭量指令信号34に対し、関数発生器35からの先行
付加信号36を加算器37によって加算する(図7に点
線で示す)ようにしており、このように先行付加信号3
6を上乗せした出炭量指令信号34に基づいて前記給炭
機モータ4及び分級機モータ18を制御した場合には、
図7に斜線で示すように出炭量指令信号34(目標値)
との偏差S2を小さくすることができる。
In order to prevent the response delay of the coal output as described above, as shown in FIGS. 5 and 7, the coal output command signal 34 from the function generator 33 is added in advance to the coal output command signal 34 from the function generator 35. The signal 36 is added by the adder 37 (indicated by a dotted line in FIG. 7), and thus the preceding additional signal 3
When the coal feeder motor 4 and the classifier motor 18 are controlled based on the coal output command signal 34 with 6 added,
As shown by the diagonal lines in FIG. 7, the coal output command signal 34 (target value)
The deviation S 2 between and can be reduced.

【0016】[0016]

【発明が解決しようとする課題】しかし、前記図5に示
した従来の出炭量制御装置23においても、石炭3の水
分、石炭3の硬度(HGI)、一次空気14の流量、回
転式分級機19の回転数等が変化した場合には、前記応
答遅れの度合いが変化してしまう問題がある。特に、産
地や種類の異なる石炭3を原料として用いている石炭焚
ボイラ21の場合には、炭種が変ることにより石炭3の
水分や硬度がその都度変化することによってミル1の出
炭特性に大きく影響することになり、そのために図7に
斜線で示す目標値である出炭量指令信号34と実際の出
炭量との偏差S2が大きくなって、石炭焚ボイラ21の
主蒸気温度や主蒸気圧力を大きく変動させてしまう要因
となり、制御性を悪化させてしまう問題を生じていた。
However, also in the conventional coal output control device 23 shown in FIG. 5, the water content of the coal 3, the hardness (HGI) of the coal 3, the flow rate of the primary air 14, the rotary classification. When the rotation speed of the machine 19 changes, there is a problem that the degree of the response delay changes. In particular, in the case of the coal-fired boiler 21 that uses different origins and different types of coal 3 as a raw material, the water content and hardness of the coal 3 change each time due to a change in the coal type, and the coal output characteristics of the mill 1 are improved. This has a large effect, and therefore the deviation S 2 between the target coal output command signal 34, which is the target value shown by hatching in FIG. 7, and the actual output amount becomes large, and the main steam temperature of the coal-fired boiler 21 and This causes a large change in the main steam pressure, which causes a problem of deteriorating controllability.

【0017】本発明は、斯かる実情に鑑みてなしたもの
で、炭種が変化した場合にも、出炭量を目標値である出
炭指令信号に近付けて安定した出炭量制御を行うことが
できるミル出炭量制御方法及び装置を提供することを目
的としている。
The present invention has been made in view of the above circumstances, and enables stable coal output control by bringing the coal output close to the target output command signal even when the coal type changes. An object of the present invention is to provide a mill output control method and apparatus capable of controlling the amount of coal output.

【0018】[0018]

【課題を解決するための手段】本発明は、出力指令に基
づいて得た出炭量指令信号に、前記出力指令が変化した
際に先行付加信号を付加してミルの給炭量と分級機の回
転数を制御するようにしているミル出炭量制御方法であ
って、石炭の水分、石炭の硬度、一次空気流量、分級機
回転数の各々が変化した際における出力指令の変化時で
のミル出炭量の動特性を予め計測して記憶しておき、出
力指令の変化に先立って新たに得た石炭の水分、石炭の
硬度、一次空気流量、分級機回転数について前記記憶し
ておいたミル出炭量の動特性に基づいて新たな動特性評
価を行い、該動特性評価に基づいて、出力指令の変化時
に出炭量指令信号に付加する先行付加信号の立上がり角
度と、初期付加高さとを変更した付加補正信号を得、該
付加補正信号に基づいて給炭量及び分級機回転数を制御
することを特徴とするミル出炭量制御方法、に係るもの
である。
According to the present invention, a coal feed amount and a classifier of a mill are added to a coal output amount command signal obtained on the basis of an output command by adding a preceding additional signal when the output command changes. A method for controlling the amount of coal output from a mill that controls the number of revolutions of coal, the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the number of revolutions of the classifier The dynamic characteristics of the coal output of the mill are measured and stored in advance, and the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the number of revolutions of the classifier that are newly obtained prior to the change in the output command are stored in advance. The new dynamic characteristic is evaluated based on the dynamic characteristic of the coal output of the mill, and based on the dynamic characteristic evaluation, the rising angle of the preceding addition signal to be added to the output instruction signal when the output command changes and the initial addition. A height-changed additional correction signal is obtained and based on the additional correction signal. Mill coal output control method and controlling the coal feed amount and classifier rotational speed have those according to.

【0019】また、本発明は、出力指令の変化時に変化
率設定指令による変化率で変化させるようにした出炭量
指令信号を出力し、かつ前記出力指令の変化時に、前記
出炭量指令信号に先行付加信号を付加するようにしてい
る出炭量指令回路と、該出炭量指令回路の出炭量指令信
号を入力してミルへの給炭量を制御する給炭量制御回路
と、該給炭量制御回路の給炭制御信号に基づいて分級機
の回転数を制御する分級機回転数制御回路とを備えたミ
ル出炭量制御装置であって、石炭の水分、石炭の硬度、
一次空気流量、分級機回転数の各々が変化した際におけ
る出力指令の変化時でのミル出炭量の動特性を予め計測
して記憶しておき、出力指令の変化に先立って新たに得
た石炭の水分、石炭の硬度、一次空気流量、分級機回転
数について前記記憶しておいたミル出炭量の動特性に基
づいて新たな動特性評価を行い、該動特性評価に基づい
て、出力指令の変化時に出炭量指令信号に付加する先行
付加信号の立上がり角度と初期付加高さとを補正する付
加補正信号を、前記給炭量制御回路と分級機回転数制御
回路に出力するシュミレート装置を備えたことを特徴と
するミル出炭量制御装置、にかかるものである。
Further, according to the present invention, when the output command changes, a coal output amount command signal which is changed at a change rate according to a change rate setting command is output, and when the output command changes, the coal output amount command signal is output. A coal output amount command circuit for adding a preceding addition signal to, and a coal supply amount control circuit for inputting the coal output amount command signal of the coal output amount command circuit to control the amount of coal supplied to the mill, A mill coal output control device comprising a classifier rotation speed control circuit that controls the rotation speed of a classifier based on a coal supply control signal of the coal supply rate control circuit, wherein the water content of coal, the hardness of coal,
The dynamic characteristics of the mill coal output when the output command changes when the primary air flow rate and the classifier rotation speed change respectively were measured and stored in advance, and were newly obtained prior to the change of the output command. Moisture of coal, hardness of coal, primary air flow rate, a new dynamic characteristic evaluation based on the dynamic characteristics of the mill output of coal stored for the classifier rotation speed, and based on the dynamic characteristic evaluation, output A simulation device that outputs an additional correction signal for correcting the rising angle and the initial additional height of the preceding additional signal added to the coal output command signal when the command changes to the coal supply control circuit and the classifier rotation speed control circuit The present invention relates to a mill coal output control device characterized by being provided.

【0020】[0020]

【作用】本発明では、石炭の水分、石炭の硬度、一次空
気流量、分級機回転数の各々が変化した際における出力
指令の変化時でのミル出炭量の動特性を予め計測して記
憶しておき、出力指令の変化に先立って新たに得た石炭
の水分、石炭の硬度、一次空気流量、分級機回転数につ
いて、前記記憶しておいたミル出炭量の動特性に基づい
て新たな動特性評価を行い、該動特性評価に基づいて、
出力指令の変化時に出炭量指令信号に付加する先行付加
信号の立上がり角度と、初期付加高さとを変更する出炭
量補正信号を得て、該出炭量補正信号に基づいて給炭量
及び分級機回転数を制御するようにしているので、炭種
が変化して石炭の水分や硬度が変化しても、出炭量を目
標値である出炭指令信号に近付けて安定した出炭量制御
を行うことができる。
In the present invention, the dynamic characteristics of the mill coal output at the time when the output command changes when the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the number of revolutions of the classifier change are measured and stored in advance. It should be noted that, regarding the newly obtained water content of coal, hardness of coal, primary air flow rate, and classifier rotation speed prior to the change of the output command, based on the stored dynamic characteristics of the mill coal output, Performing a dynamic characteristic evaluation, based on the dynamic characteristic evaluation,
Obtaining a coal output amount correction signal for changing the rising angle of the preceding addition signal added to the coal output amount command signal when the output command changes and the initial addition height, and based on the output amount correction signal, the coal supply amount and Since the classifier speed is controlled, even if the coal type changes and the water content and hardness of the coal change, the coal output can be brought closer to the target output command signal, which is a stable output. Control can be performed.

【0021】[0021]

【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0022】図1は、前記図5の出炭量制御装置23に
適用した本発明の一実施例を示したもので、図中同一の
符号を付したものは同一物を表わしている。
FIG. 1 shows an embodiment of the present invention applied to the coal output control device 23 of FIG. 5, and the same reference numerals in the drawing represent the same parts.

【0023】図1に示すように、図5と同様の出炭量指
令回路24を備えて、出力指令22の変化時に変化率設
定指令28による変化率で変化させるようにして出炭量
指令信号34を出力し、且つ前記出力指令22の変化時
に、前記出炭量指令信号34に先行付加信号36を付加
するようにしている。
As shown in FIG. 1, a coal output command circuit 24 similar to that shown in FIG. 5 is provided so that when the output command 22 changes, the output command 22 is changed at a change rate according to a change rate setting command 28. When the output command 22 changes, the preceding addition signal 36 is added to the coal output amount command signal 34.

【0024】更に、前記出炭量指令回路24の出炭量指
令信号34を入力して給炭機モータ4に給炭制御信号5
6を出力してミル1(図1)への給炭量を制御する給炭
制御回路62を備え、更に該給炭制御回路62の給炭制
御信号56に基づいて分級機モータ18に回転数制御信
号61を出力して回転式分級機19(図1)の回転数を
制御する分級機回転数制御回路63を備えている。
Further, the coal output command signal 34 of the coal output command circuit 24 is input to the coal supply motor 4 to supply the coal supply control signal 5
6 is provided with a coal feeding control circuit 62 for controlling the amount of coal fed to the mill 1 (FIG. 1), and further, based on the coal feeding control signal 56 of the coal feeding control circuit 62, the number of revolutions of the classifier motor 18 is increased. A classifier rotation speed control circuit 63 that outputs a control signal 61 to control the rotation speed of the rotary classifier 19 (FIG. 1) is provided.

【0025】更に、前記構成に加えて動特性評価用シュ
ミレート装置64を備える。
Further, in addition to the above configuration, a dynamic characteristic evaluation simulator 64 is provided.

【0026】シュミレート装置64には、図1、2に示
すように、前記出炭量指令回路24に入力されている出
力指令22と変化率設定指令28が入力されて、負荷上
昇時と負荷下降時に所定の変化率が与えられた出力指令
信号29を得てそれを表示し、更に前記出炭量指令回路
24にて出力指令信号29を出炭量に変換し、更に先行
付加信号36を加算すると共に、主蒸気圧力及び主蒸気
圧力等による補正が加えられた後の加算器53出口の出
炭量指令信号34を入力して表示するようにした出炭量
指令信号入力部65を備えている。
As shown in FIGS. 1 and 2, the simulation device 64 receives the output command 22 and the change rate setting command 28 input to the coal output amount command circuit 24, and when the load increases and the load decreases. At some time, an output command signal 29 given a predetermined rate of change is obtained and displayed, and further, the output command signal 29 is converted into a coal output by the coal output command circuit 24, and a preceding addition signal 36 is further added. In addition, a coal output command signal input unit 65 for inputting and displaying the coal output command signal 34 at the outlet of the adder 53 after correction by the main steam pressure and the main steam pressure is provided. There is.

【0027】また、シュミレート装置64には、ミル1
(図1)の出炭特性に影響を及ぼす石炭の水分66、石
炭の硬度67、一次空気流量68、分級機回転数69の
各々のデータが入力され、該各々のデータを変化させた
際のミル出炭量の動特性を演算することができる動特性
評価部70を備えている。この時、前記石炭の水分66
及び石炭の硬度67は炭種が変る度に変化し、しかも出
炭特性に大きな影響を及ぼす要件であるのでこれを評価
して入力するようにしており、また一次空気流量68及
び分級機回転数69の変化も出炭量の動特性への影響が
大きくしかも小さな時間遅れで直ちに影響が出るのでこ
れも評価して入力するようにしている。
The simulating device 64 includes a mill 1
The respective data of the moisture content 66 of coal, the hardness 67 of coal, the primary air flow rate 68, and the number of revolutions of the classifier 69 which influence the coal output characteristics of (FIG. 1) are input, and when the respective data are changed. A dynamic characteristic evaluation unit 70 capable of calculating the dynamic characteristics of the coal output of the mill is provided. At this time, the water content of the coal 66
The hardness 67 of the coal and the hardness of the coal change every time the type of coal changes, and since it is a requirement that has a great influence on the coal output characteristics, they are evaluated and entered, and the primary air flow rate 68 and the number of revolutions of the classifier The change in 69 also has a large effect on the dynamic characteristics of the coal output, and it also has an immediate effect with a small time delay, so this is also evaluated and input.

【0028】動特性評価部70は、例えば出力指令22
が出力指令値B1’(40%)から出力指令値B2’(1
00%)に増加した場合において、出力指令22の増加
点から実際に出炭量の増加が開始される点までのむだ時
間T1’と、実際の出炭量の増加が開始される点と、変
化前の出力指令値B1’(40%)と変化後の出力指令
値B2’(100%)との差の67%の点までに実際の
出炭量が変化するまでに要した時間遅れT2’とを、石
炭の水分66’、石炭の硬度67’、一次空気流量6
8’、分級機回転数69’の平均的な1つの基準の条件
について予め求め、その基準の条件を図3に示す条件記
憶部71に記憶させると共に、前記石炭の水分66’、
石炭の硬度67’、一次空気流量68’、分級機回転数
69’を各々単独で変化させた(基準の条件に対して差
をもたせた)際におけるむだ時間T1’と時間遅れT2
とに対する影響を複数点で評価して、その結果を関数発
生器72〜75に入力しておくようにしている。
The dynamic characteristic evaluation section 70, for example, outputs the output command 22.
From the output command value B 1 '(40%) to the output command value B 2 ' (1
00%), the dead time T 1 ′ from the increase point of the output command 22 to the point at which the actual increase of the coal output is started, and the point at which the actual increase of the coal output is started. , It was necessary for the actual coal output to change up to the point of 67% of the difference between the output command value B 1 '(40%) before the change and the output command value B 2 ' (100%) after the change. Time delay T 2 'with coal moisture 66', coal hardness 67 ', primary air flow 6
8 ', the average one standard condition of the classifier rotation speed 69' is obtained in advance, and the standard condition is stored in the condition storage unit 71 shown in FIG.
The dead time T 1 'and the time delay T 2 ' when the hardness 67 'of the coal, the primary air flow rate 68', and the classifier rotation speed 69 'are individually changed (different from the standard condition).
The effect on and is evaluated at a plurality of points, and the result is input to the function generators 72 to 75.

【0029】また、前記基準の条件において、出力指令
値B1’,B2’の変化幅B2’−B1’が種々変化するよ
うに出力指令22を変えた場合のむだ時間T1’’と時
間遅れT2’’を計測し、変化幅B2’−B1’とむだ時
間T1’’及び時間遅れT2’’との関係を動特性記憶部
76に記憶するようにしており、新たな出力指令22に
よる出力指令値B1,B2を入力すると、変化幅B2−B1
と前記記憶されたむだ時間T1’’及び時間遅れT2’’
との関係からむだ時間T1’及び時間遅れT2’が求めら
れるようになっている。
Further, under the above-mentioned standard conditions, the dead time T 1 'when the output command 22 is changed so that the change width B 2 ' -B 1 'of the output command values B 1 ' and B 2 'changes variously. 'and time delay T 2' measured ', and the relationship between the variation width B 2' -B 1 'and the dead time T 1' 'and the time delay T 2' 'to be stored in the dynamic characteristic storage section 76 Therefore, when the output command values B 1 and B 2 by the new output command 22 are input, the change width B 2 −B 1
And the stored dead time T 1 ″ and time delay T 2
Therefore, the dead time T 1 'and the time delay T 2 ' are required.

【0030】また、前記動特性評価部70には、新たに
評価された石炭の水分66、石炭の硬度67、一次空気
流量68、分級機回転数69の夫々が独自に設けられた
引算器77〜80に入力されるようになっており、更に
前記条件記憶部71に記憶された基準の条件の対応する
石炭の水分66’、石炭の硬度67’、一次空気流量6
8’、分級機回転数69’のデータが引算器77〜80
に入力されて引算され、その差の信号が夫々対応した前
記関数発生器72〜75に入力されてむだ時間T 1’と
時間遅れT2’の換算係数に変換され、該換算係数の夫
々が掛算器81〜84を介して前記動特性記憶部76か
らのむだ時間T1’と時間遅れT2’とに掛算されて、新
たなむだ時間T1と時間遅れT2とが求められるようにな
っている。
Further, the dynamic characteristic evaluation section 70 is newly provided with
Moisture 66 of coal evaluated, hardness of coal 67, primary air
A flow rate of 68 and a classifier rotation speed of 69 were individually provided.
It is input to the subtracters 77-80, and
Corresponding to the reference condition stored in the condition storage unit 71.
Moisture 66 'of coal, hardness 67' of coal, primary air flow rate 6
8 ', classifier rotation speed 69' data is subtractor 77-80
Before being input to and subtracted, and the signals of the difference corresponded respectively
Time delay T input to the function generators 72 to 75 1'When
Time delay T2Is converted into a conversion coefficient of
Each of the above-mentioned dynamic characteristic storage units 76 through the multipliers 81 to 84
Ranotam Time T1’And time delay T2Is multiplied by
Standing time T1And time delay T2So that
ing.

【0031】更に、前記シュミレート装置64には付加
信号修正演算部85と付加信号修正部86とを備える。
Further, the simulation device 64 is provided with an additional signal correction calculation section 85 and an additional signal correction section 86.

【0032】付加信号修正演算部85は、付加信号修正
部86に斜線で示す先行付加信号36の立上がり角度α
と初期付加高さLとを設定するもので、前記動特性評価
部70によって演算された動特性T1,T2を入力してT
1/T1’,T2/T2’と立上がり角度α及び初期付加高
さLの大きさを予め評価して得ておいたデータから演算
して求め、その結果を表示するようになっている。
The additional signal correction calculation unit 85 indicates to the additional signal correction unit 86 the rising angle α of the preceding additional signal 36 indicated by the diagonal lines.
And the initial additional height L are set, and the dynamic characteristics T 1 and T 2 calculated by the dynamic characteristic evaluation unit 70 are input to T
1 / T 1 ′, T 2 / T 2 ′, the rising angle α and the size of the initial additional height L are calculated from the data obtained in advance, and the results are displayed. There is.

【0033】前記付加信号修正演算部85によって新た
に得られた立上がり角度α1と初期付加高さL1が、前記
付加信号修正部86に入力され、先行付加信号36に対
して図中二点鎖線で示すように先行付加信号36aの形
状が変更されその結果が表示されると共に、先行付加信
号36aによる付加補正信号87が出力されるようにな
っている。この時、先行付加信号36,36aにより付
加される信号の大きさ(面積)は同一になるように制御
される。
The rising angle α 1 and the initial additional height L 1 newly obtained by the additional signal correction operation unit 85 are input to the additional signal correction unit 86, and two points are shown in the figure with respect to the preceding additional signal 36. As shown by the chain line, the shape of the preceding addition signal 36a is changed and the result is displayed, and the addition correction signal 87 based on the preceding addition signal 36a is output. At this time, the magnitudes (areas) of the signals added by the preceding additional signals 36, 36a are controlled to be the same.

【0034】前記付加信号修正部86からの付加補正信
号87を、図1に示す出炭量指令回路24から給炭制御
回路62に入力されている出炭量指令信号34に加算器
88を介して加算すると共に、前記付加補正信号87を
関数変換器89によって分級機の回転数の信号に変換し
て分級機回転数制御回路63の関数発生器57からの回
転数信号58に加算器90を介して加算するようにして
いる。
The additional correction signal 87 from the additional signal correction section 86 is added to the coal output amount command signal 34 input to the coal supply control circuit 62 from the coal output amount command circuit 24 shown in FIG. The additional correction signal 87 is converted by the function converter 89 into a rotation speed signal of the classifier, and the adder 90 is added to the rotation speed signal 58 from the function generator 57 of the classifier rotation speed control circuit 63. I am trying to add through.

【0035】また、上記実施例では出力指令22の増加
時についてのみ詳述したが、出力指令22の減少時につ
いても同様の操作を行うことができる。
Further, in the above embodiment, the detailed description was given only when the output command 22 was increased, but the same operation can be performed when the output command 22 is decreased.

【0036】次に上記実施例の作用を説明する。Next, the operation of the above embodiment will be described.

【0037】出力指令22の変化に先立って計測した石
炭の水分66、石炭の硬度67、一次空気流量68、分
級機回転数69の各々のデータをシュミレート装置64
に入力すると、図3に示すように、前記石炭の水分6
6、石炭の硬度67、一次空気流量68、分級機回転数
69の夫々が独自に設けられた引算器77〜80に入力
され、条件記憶部71に記憶された対応した基準の条件
である石炭の水分66’、石炭の硬度67’、一次空気
流量68’、分級機回転数69’のデータと引算され、
その差の信号が夫々対応した関数発生器72〜75に入
力されてむだ時間T 1’と時間遅れT2’の換算係数に変
換され、該換算係数の夫々が掛算器81〜84に入力さ
れる。
Stone measured before the change of the output command 22
Moisture 66 of coal, hardness 67 of coal, primary air flow rate 68, min
Each data of the class machine speed 69 is simulated by the simulator 64
When input to, as shown in FIG.
6, coal hardness 67, primary air flow rate 68, classifier speed
Each of the 69 inputs to its own subtractor 77-80
The corresponding reference condition stored in the condition storage unit 71
Moisture 66 'of coal, hardness of coal 67', primary air
Subtracted with the data of flow rate 68 ', classifier rotation speed 69',
The difference signals are input to the corresponding function generators 72 to 75.
Forced dead time T 1’And time delay T2’Conversion factor
Are converted and the respective conversion factors are input to the multipliers 81 to 84.
Be done.

【0038】一方、前記出力指令22が変化すると、出
力指令22の出力指令値B1,B2が図3の動特性記憶部
76に入力され、出力指令値の変化幅B2−B1と動特性
記憶部76に記憶されたむだ時間T1’’及び時間遅れ
2’’との関係から新たなむだ時間T1’及び時間遅れ
2’が直ちに求められる。
On the other hand, when the output command 22 changes, the output command values B 1 and B 2 of the output command 22 are input to the dynamic characteristic storage unit 76 of FIG. 3, and the output command value change width B 2 -B 1 dead time stored in the dynamic characteristic storage section 76 T 1 '' and the time delay T 2 '' and a new dead time from the relationship of T 1 'and the time delay T 2' is obtained immediately.

【0039】このようにして求められた新たな動特性T
1’,T2’に、前記関数発生器72〜75からの計測デ
ータに基づいた換算係数が掛算器81〜84によって掛
算されることにより修正されて実際に近い動特性T1
2の評価が行われる。
The new dynamic characteristic T thus obtained
1 ′ and T 2 ′ are corrected by being multiplied by the conversion factors based on the measurement data from the function generators 72 to 75 by the multipliers 81 to 84, and the dynamic characteristics T 1 ,
An evaluation of T 2 is made.

【0040】動特性評価部70によって新たに求められ
た動特性T1,T2は、図2の付加信号修正演算部85に
入力され、付加信号修正部86に示す先行付加信号36
の立上がり角度α1と初期付加高さL1とを、前記動特性
1,T2のT1/T1’及びT 2/T2’との比から新たに
求める。このようにして新たに求められた立上がり角度
α1と初期付加高さL1により、前記付加信号修正部86
における先行付加信号36の形状を例えば二点鎖線で示
す36aのように変更する付加補正信号87が出力され
る。
Newly obtained by the dynamic characteristic evaluation unit 70.
Dynamic characteristics T1, T2Is added to the additional signal correction calculator 85 of FIG.
The preceding additional signal 36 inputted and shown to the additional signal correction unit 86
Rising angle α1And initial additional height L1And the dynamic characteristics
T1, T2Of T1/ T1’And T 2/ T2From the ratio with
Ask. The rising angle newly obtained in this way
α1And initial additional height L1Accordingly, the additional signal correction unit 86
The shape of the preceding additional signal 36 in FIG.
And an additional correction signal 87 for changing like
It

【0041】前記付加信号修正部86からの付加補正信
号87を、図1に示す出炭量指令回路24から給炭制御
回路62に入力している出炭量指令信号34に加算器8
8を介して加算することにより給炭制御信号56を修正
すると共に、前記付加補正信号87を、関数変換器89
によって分級機の回転数の信号に変換した後、分級機回
転数制御回路63の関数発生器57からの回転数信号5
8に加算器90を介して加算することにより、回転数制
御信号61を修正する。
The additional correction signal 87 from the additional signal correction section 86 is added to the coal output amount command signal 34 input to the coal supply control circuit 62 from the coal output amount command circuit 24 shown in FIG.
8 to correct the coal feed control signal 56 and add the additional correction signal 87 to the function converter 89.
After being converted into a signal of the number of rotations of the classifier by the number of rotations signal 5 from the function generator 57 of the number-of-class rotations control circuit 63.
The number of revolutions control signal 61 is corrected by adding the value to 8 through the adder 90.

【0042】上記によれば、特に炭種が変化することに
より石炭の水分66及び石炭の硬度67が変化した場合
において、出力指令22が変更された場合に、先行付加
信号36を修正する付加補正信号87によって出炭量指
令信号34を自動的に補正することができ、これにより
図7に斜線で示した目標値である出炭量指令信号34と
実際の出炭量との偏差S2を極力小さくすることができ
る。
According to the above, the addition correction for correcting the preceding addition signal 36 when the output command 22 is changed, particularly when the water content 66 of the coal and the hardness 67 of the coal change due to the change of the coal type. The signal 87 can automatically correct the coal output command signal 34, and as a result, the deviation S 2 between the coal output command signal 34 and the actual coal output, which is the target value shown by hatching in FIG. 7, can be calculated. It can be made as small as possible.

【0043】尚、上記実施例においては分級機の回転数
を制御する場合について説明したが、分級機ベーンの開
度を制御するようにしたり、或いは粉砕ローラの圧下力
を制御するようにしても良い。
In the above embodiment, the case where the number of revolutions of the classifier is controlled has been described, but the opening of the classifier vane may be controlled or the rolling force of the crushing roller may be controlled. good.

【0044】[0044]

【発明の効果】本発明によれば、石炭の水分、石炭の硬
度、一次空気流量、分級機回転数の各々が変化した際に
おける出力指令の変化時でのミル出炭量の動特性を予め
計測して記憶しておき、出力指令の変化に先立って新た
に得た石炭の水分、石炭の硬度、一次空気流量、分級機
回転数について、前記記憶しておいたミル出炭量の動特
性に基づいて新たな動特性評価を行い、該動特性評価に
基づいて、出力指令の変化時に出炭量指令信号に付加す
る先行付加信号の立上がり角度と、初期付加高さとを変
更する出炭量補正信号を得て、該出炭量補正信号に基づ
いて給炭量及び分級機回転数を制御するようにしている
ので、炭種が変化して石炭の水分や硬度が変化しても、
出炭量を目標値である出炭指令信号に近付けて安定した
出炭量制御を行うことができる優れた効果を奏し得る。
EFFECTS OF THE INVENTION According to the present invention, the dynamic characteristics of the mill coal output when the output command changes when the water content of the coal, the hardness of the coal, the primary air flow rate, and the number of revolutions of the classifier change are determined in advance. Measured and memorized, the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the classifier rotation speed newly obtained prior to the change of the output command, the dynamic characteristics of the memorized mill output Based on the dynamic characteristic evaluation, based on the dynamic characteristic evaluation, the rising angle of the preceding additional signal added to the coal output amount command signal when the output command changes, and the coal output amount for changing the initial addition height. Since the correction signal is obtained and the coal supply amount and the classifier rotation speed are controlled based on the coal output correction signal, even if the coal type changes and the water content or hardness of the coal changes,
It is possible to achieve an excellent effect that the coal output can be brought close to the target coal output command signal and the stable coal output control can be performed.

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

【図1】本発明の出炭量制御装置の一実施例を示すブロ
ック図である。
FIG. 1 is a block diagram showing an embodiment of a coal output control device of the present invention.

【図2】図1のシュミレート装置の一例を示すフローチ
ャートである。
FIG. 2 is a flowchart showing an example of the simulator of FIG.

【図3】図2の動特性評価部の一例を示すブロック図で
ある。
FIG. 3 is a block diagram showing an example of a dynamic characteristic evaluation unit in FIG.

【図4】ミルの一例を示す切断正面図である。FIG. 4 is a cut front view showing an example of a mill.

【図5】従来の出炭量制御装置のブロック図である。FIG. 5 is a block diagram of a conventional coal output control device.

【図6】出炭量指令信号の一例を示す線図である。FIG. 6 is a diagram showing an example of a coal output command signal.

【図7】出炭量指令信号に先行付加信号を付加した状態
と、その場合における出炭量指令信号と実際の出炭量と
の偏差を示す線図である。
FIG. 7 is a diagram showing a state in which a preceding addition signal is added to the coal production amount command signal and a deviation between the coal production amount command signal and the actual coal production amount in that case.

【図8】出炭量指令信号に先行付加信号を付加しない場
合の出炭量指令信号と実際の出炭量との偏差を示す線図
である。
FIG. 8 is a diagram showing a deviation between a coal output amount command signal and an actual coal output amount when a preceding addition signal is not added to the coal output amount command signal.

【符号の説明】[Explanation of symbols]

1 ミル(微粉炭ミル) 5 給炭機 19 分級機(回転式分級機) 22 出力指令 23 出炭量制御装置 24 出炭量指令回路 25 給炭量制御回路 26 分級機回転数制御回路 28 変化率設定指令 34 出炭量指令信号 36 先行付加信号(基準) 36a 先行付加信号 56 給炭制御信号 61 回転数制御信号 62 給炭制御回路 63 分級機回転数制御回路 64 シュミレート装置 66 石炭の水分 66’ 石炭の水分(基準) 67 石炭の硬度 67’ 石炭の硬度(基準) 68 一次空気流量 68’ 一次空気流量(基準) 69 分級機回転数 69’ 分級機回転数(基準) 87 付加補正信号 α 立上がり角度(基準) α1 立上がり角度 L 初期付加高さ(基準) L1 初期付加高さ T1 むだ時間(動特性) T2 時間遅れ(動特性) T1’ むだ時間(動特性)(基準) T2’ 時間遅れ(動特性)(基準) T1’’ むだ時間(動特性)(基準) T2’’ 時間遅れ(動特性)(基準)1 mill (pulverized coal mill) 5 coal feeder 19 classifier (rotary classifier) 22 output command 23 coal output control device 24 coal output command circuit 25 coal supply control circuit 26 classifier speed control circuit 28 change Rate setting command 34 Coal output command signal 36 Preceding additional signal (reference) 36a Preceding additional signal 56 Coal feeding control signal 61 Rotation speed control signal 62 Coal feeding control circuit 63 Classifier rotation speed control circuit 64 Simulation device 66 Coal moisture 66 'Coal moisture (standard) 67 Coal hardness 67' Coal hardness (standard) 68 Primary air flow rate 68 'Primary air flow rate (standard) 69 Classifier rotation speed 69' Classifier rotation speed (standard) 87 Additional correction signal α rising angle (reference) alpha 1 rising angle L initial additional height (reference) L 1 initial additional height T 1 dead time (dynamic characteristics) T 2 hours behind (dynamic characteristics) T 1 'dead time (dynamic characteristics) Reference) T 2 'time delay (dynamics) (reference) T 1' 'dead time (dynamic characteristics) (reference) T 2' 'time delay (dynamics) (reference)

───────────────────────────────────────────────────── フロントページの続き (72)発明者 草間 滋 東京都江東区豊洲三丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Shigeru Kusama 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawajima Harima Heavy Industries Co., Ltd. Toyosu General Office

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 出力指令に基づいて得た出炭量指令信号
に、前記出力指令が変化した際に先行付加信号を付加し
てミルの給炭量と分級機の回転数を制御するようにして
いるミル出炭量制御方法であって、石炭の水分、石炭の
硬度、一次空気流量、分級機回転数の各々が変化した際
における出力指令の変化時でのミル出炭量の動特性を予
め計測して記憶しておき、 出力指令の変化に先立って新たに得た石炭の水分、石炭
の硬度、一次空気流量、分級機回転数について前記記憶
しておいたミル出炭量の動特性に基づいて新たな動特性
評価を行い、 該動特性評価に基づいて、出力指令の変化時に出炭量指
令信号に付加する先行付加信号の立上がり角度と、初期
付加高さとを変更する付加補正信号を得、 該付加補正信号に基づいて給炭量及び分級機回転数を制
御することを特徴とするミル出炭量制御方法。
1. A coal feed amount command signal obtained on the basis of an output command is added with a preceding additional signal when the output command changes to control the coal feed amount of the mill and the rotation speed of the classifier. The method of controlling the amount of coal output from a mill, in which the dynamic characteristics of the amount of coal output from the mill when the output command changes when the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the rotation speed of the classifier change Dynamic characteristics of the mill coal output, which were measured and stored in advance, and were previously stored prior to the change of the output command, regarding the moisture content of the coal, the hardness of the coal, the primary air flow rate, and the rotation speed of the classifier. Based on the dynamic characteristic evaluation, and based on the dynamic characteristic evaluation, an additional correction signal for changing the rising angle of the preceding additional signal to be added to the coal output command signal when the output command changes and the initial additional height. Based on the additional correction signal, A mill coal output control method characterized by controlling the number of turns.
【請求項2】 出力指令の変化時に変化率設定指令によ
る変化率で変化させるようにした出炭量指令信号を出力
し、かつ前記出力指令の変化時に、前記出炭量指令信号
に先行付加信号を付加するようにしている出炭量指令回
路と、 該出炭量指令回路の出炭量指令信号を入力してミルへの
給炭量を制御する給炭量制御回路と、 該給炭量制御回路の給炭制御信号に基づいて分級機の回
転数を制御する分級機回転数制御回路とを備えたミル出
炭量制御装置であって、 石炭の水分、石炭の硬度、一次空気流量、分級機回転数
の各々が変化した際における出力指令の変化時でのミル
出炭量の動特性を予め計測して記憶しておき、出力指令
の変化に先立って新たに得た石炭の水分、石炭の硬度、
一次空気流量、分級機回転数について前記記憶しておい
たミル出炭量の動特性に基づいて新たな動特性評価を行
い、該動特性評価に基づいて、出力指令の変化時に出炭
量指令信号に付加する先行付加信号の立上がり角度と初
期付加高さとを補正する付加補正信号を、前記給炭量制
御回路と分級機回転数制御回路に出力するシュミレート
装置を備えたことを特徴とするミル出炭量制御装置。
2. A coal output amount command signal that is changed at a change rate according to a change rate setting command when the output command changes, and when the output command changes, a preceding addition signal to the coal output amount command signal. Of the coal output amount command circuit, a coal supply amount control circuit for inputting a coal output amount command signal of the coal output amount command circuit to control the amount of coal supplied to the mill, and the coal supply amount A mill coal output control device comprising a classifier rotation speed control circuit for controlling the rotation speed of a classifier based on a coal feed control signal of a control circuit, wherein the water content of coal, hardness of coal, primary air flow rate, The dynamic characteristics of the mill coal output at the time of the change of the output command when each of the classifier rotation speed is changed and stored in advance, the moisture of the coal newly obtained prior to the change of the output command, Hardness of coal,
A new dynamic characteristic evaluation is performed on the basis of the stored dynamic characteristics of the mill coal output amount regarding the primary air flow rate and the classifier rotation speed, and based on the dynamic characteristic evaluation, the coal output amount command is issued when the output command changes. A mill equipped with a simulation device for outputting an additional correction signal for correcting the rising angle and the initial additional height of the preceding additional signal added to the signal to the coal supply amount control circuit and the classifier rotation speed control circuit. Coal output control device.
JP5142395A 1995-03-10 1995-03-10 Method for controlling coal output amount of mill and device therefor Pending JPH08243429A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5142395A JPH08243429A (en) 1995-03-10 1995-03-10 Method for controlling coal output amount of mill and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5142395A JPH08243429A (en) 1995-03-10 1995-03-10 Method for controlling coal output amount of mill and device therefor

Publications (1)

Publication Number Publication Date
JPH08243429A true JPH08243429A (en) 1996-09-24

Family

ID=12886524

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5142395A Pending JPH08243429A (en) 1995-03-10 1995-03-10 Method for controlling coal output amount of mill and device therefor

Country Status (1)

Country Link
JP (1) JPH08243429A (en)

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