JPH0310380B2 - - Google Patents
Info
- Publication number
- JPH0310380B2 JPH0310380B2 JP9846783A JP9846783A JPH0310380B2 JP H0310380 B2 JPH0310380 B2 JP H0310380B2 JP 9846783 A JP9846783 A JP 9846783A JP 9846783 A JP9846783 A JP 9846783A JP H0310380 B2 JPH0310380 B2 JP H0310380B2
- Authority
- JP
- Japan
- Prior art keywords
- mill
- coal
- fuel
- pulverized
- coal feeder
- 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.)
- Expired
Links
- 239000003245 coal Substances 0.000 claims description 53
- 239000000446 fuel Substances 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 10
- 238000002485 combustion reaction Methods 0.000 claims description 3
- 238000001514 detection method Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Landscapes
- Feeding And Controlling Fuel (AREA)
- Disintegrating Or Milling (AREA)
Description
【発明の詳細な説明】
本発明は、石炭焚ボイラ等における微粉炭燃料
の供給制御方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the supply of pulverized coal fuel in a coal-fired boiler or the like.
石炭焚ボイラ等に微粉炭燃料を供給する微粉炭
供給装置は、例えば第1図に示す如く、バンカー
1からの石炭2を、給炭機モータ3により駆動す
るようにしたコンベヤ式の給炭機4を介して微粉
炭装置(以下ミルと言う)5に供給し、該ミル5
に備えたミルローラ6により微粉化させた後、下
側の風箱7から上昇する空気流8に乗せて燃料管
9を通り図示しないボイラ等のバーナに供給する
ようにしている。 A pulverized coal supply device for supplying pulverized coal fuel to a coal-fired boiler or the like is, for example, a conveyor-type coal feeder in which coal 2 from a bunker 1 is driven by a coal feeder motor 3, as shown in FIG. 4 to a pulverized coal device (hereinafter referred to as the mill) 5, and the mill 5
After being pulverized by a mill roller 6 provided at the bottom, the fuel is carried on an air flow 8 rising from a lower wind box 7, passes through a fuel pipe 9, and is supplied to a burner such as a boiler (not shown).
このような微粉炭供給装置におけるボイラ等に
対する微粉炭燃料の供給量の調整は、給炭機モー
タ3の回転数を制御信号Aによつて制御すること
により行うようにしており、従来は第2図に示す
ように、給炭機モータ3に設けた回転数検出計a
からの検出信号bを、ボイラ等からのマスタ指令
eと引算器dにより比較し、その差が最小になる
ように調節計eを介して給炭機モータ3の回転を
制御するようにしている。 In such a pulverized coal supply device, the amount of pulverized coal fuel supplied to the boiler etc. is adjusted by controlling the rotation speed of the coal feeder motor 3 using the control signal A. As shown in the figure, a rotation speed detection meter a provided on the coal feeder motor 3
The detection signal b from the boiler etc. is compared with the master command e from the boiler etc. using the subtractor d, and the rotation of the coal feeder motor 3 is controlled via the controller e so that the difference is minimized. There is.
しかし、上記従来方式においては、ミル5の出
力が給炭機モータ3の回転数により制御されてい
るのみであり、そのときの燃料流量は何等考慮さ
れておらず、燃料流量を考慮したフイードバツク
制御は不可能であつた。即ち、第1図に示すよう
に、燃料流量を変えようとして給炭機モータ3の
回転数の変化を行つても、ミル5内に石炭が投入
され、ミルローラ6によつて微粉化された後空気
流8に乗せられてボイラ等に送られるまでには長
い無駄時間、時間遅れがあり、そのために前記従
来の制御方式においては、例えば燃料増のマスタ
指令により給炭機モータ3の回転数を増加させて
も、燃料流量が所望量に増大するまでには時間が
掛かるので更に増加指令が続行し、その後燃料流
量が所定量に達し、その量を維持するようなマス
タ指令が来ても、すでにミル5内には多量の石炭
が投入されているために燃料流量は増大し続け
る。このため、今度は燃料減のマスタ指令が働ら
くようになるが、燃料流量が減少するまでには時
間が掛かるので、更に減少指令が続行する。この
ように、従来の制御方式においては、給炭機モー
タ3の回転数を必要回転数に制御しても、ミル5
出力(燃料流量)が必ずしも過度的に必要量得ら
れず、プロセス量の大きな変動を引き起す問題を
生じていた。 However, in the conventional method described above, the output of the mill 5 is only controlled by the rotation speed of the coal feeder motor 3, and the fuel flow rate at that time is not taken into account at all, and feedback control that takes the fuel flow rate into account is performed. was impossible. That is, as shown in FIG. 1, even if the number of revolutions of the coal feeder motor 3 is changed in an attempt to change the fuel flow rate, the coal is fed into the mill 5 and after being pulverized by the mill rollers 6. There is a long dead time and time delay before the air is carried by the air flow 8 and sent to a boiler etc. Therefore, in the conventional control method, for example, the rotation speed of the coal feeder motor 3 is controlled by a master command to increase fuel. Even if it is increased, it takes time for the fuel flow rate to increase to the desired amount, so the increase command continues, and even if the fuel flow rate reaches a predetermined amount and a master command to maintain that amount comes, Since a large amount of coal has already been put into the mill 5, the fuel flow rate continues to increase. Therefore, the master command to reduce the fuel comes into effect, but since it takes time for the fuel flow rate to decrease, the decrease command continues. In this way, in the conventional control system, even if the rotation speed of the coal feeder motor 3 is controlled to the required rotation speed, the mill 5
The required amount of output (fuel flow rate) cannot necessarily be obtained excessively, resulting in a problem of large fluctuations in the process amount.
本発明は、こうした点に鑑み、給炭機によつて
ミルに投入される石炭の量を計測し、その計測値
のときの石炭がミルから微粉炭として送り出され
るときのミル出力を推定し、そのミル出力推定信
号をフイードバツク信号としてマスタ指令と比較
制御することにより、プロセスの変動をなくして
制御性の向上を図ることを目的とする。 In view of these points, the present invention measures the amount of coal fed into a mill by a coal feeder, estimates the mill output when the coal is sent out as pulverized coal from the mill at the measured value, The purpose is to eliminate process fluctuations and improve controllability by comparing and controlling the mill output estimation signal with a master command as a feedback signal.
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.
第3図は前記第1図の微粉炭供給装置に適用し
た本発明の一例を示すもので、マスタ指令10
を、フイードバツク引算器11及びフイードバツ
ク調節計12を介した後、更に引算器13及び調
節計14を経て制御信号Aとして給炭機モータ3
に入力するようにしている。また給炭機モータ3
に設けた回転数検出計15の検出信号16を、前
記引算器13に導入する一方、給炭機モータ3の
1回転当りの石炭投入重量17を入力された掛算
器18に導入して石炭の投入量を計測し、その計
測信号19を、ミル出力推定演算器20に導入し
てそのミル出力推定信号21を前記フイードバツ
ク引算器11に導入する。前記ミル出力推定演算
器20は、
e-LS/1+TS
L:無駄時間
T:1時遅れ時定数
S:ラプラス演算子
を考慮することにより、現在の給炭機モータ3の
回転数によりミル5に供給された石炭が、粉砕さ
れた後、微粉炭としてミル5からボイラ等に送給
されるときの量を推定するようにしている。 FIG. 3 shows an example of the present invention applied to the pulverized coal supply device shown in FIG.
is passed through a feedback subtracter 11 and a feedback controller 12, and then further through a subtracter 13 and a controller 14 to be sent to the coal feeder motor 3 as a control signal A.
I am trying to input it into . Also, the coal feeder motor 3
The detection signal 16 of the rotation speed detector 15 provided at The input amount is measured, the measured signal 19 is introduced into the mill output estimation calculator 20, and the mill output estimation signal 21 is introduced into the feedback subtracter 11. The mill output estimation calculator 20 calculates the output of the mill 5 according to the current rotational speed of the coal feeder motor 3 by considering e -LS /1+TS L: dead time T: 1 time delay time constant S: Laplace operator. After the supplied coal is pulverized, the amount to be sent as pulverized coal from the mill 5 to a boiler etc. is estimated.
従つて、上記において、例えば燃料増のマスタ
指令10が来るとフイードバツク引算器11、フ
イードバツク調節計12、引算器13、及び調節
計14を介して給炭機モータ3の回転数が増大さ
れる。このとき回転数検出計15の検出信号16
が引算器13に導入され、給炭機モータ3の回転
数がフイードバツク調節計12からの指令22に
一致するように調整される。一方、前記回転数の
検出信号16が掛算器18に導かれて給炭器4か
らミル5に投入されている石炭の量が計測され、
この計測信号19がミル出力推定演算器20に入
力される。ミル出力推定演算器20は、今ミル5
に投入されている石炭が微粉化され微粉炭として
ボイラ等に送給されるときの燃料流量を推定し、
そのミル出力推定信号21がフイードバツク引算
器11にフイードバツクされてマスタ指令10と
比較される。マスタ指令10の方が大きければ、
給炭機モータ3の回転数は増加し続けるが、ミル
出力推定信号21がマスタ指令10と一致すると
直ちに給炭機モータ3の回転数がその状態に維持
される。従つてミル5に対する石炭の供給過多等
を生じることなく、所定時間には指令された流量
の燃料がミル5から送り出されるようになり、プ
ロセスに変動を生じるようなことがなくなる。 Therefore, in the above, for example, when the master command 10 to increase fuel is received, the rotation speed of the coal feeder motor 3 is increased via the feedback subtractor 11, feedback controller 12, subtracter 13, and controller 14. Ru. At this time, the detection signal 16 of the rotation speed detector 15
is introduced into the subtractor 13, and the rotational speed of the coal feeder motor 3 is adjusted to match the command 22 from the feedback controller 12. On the other hand, the rotation speed detection signal 16 is guided to a multiplier 18 to measure the amount of coal being fed into the mill 5 from the coal feeder 4,
This measurement signal 19 is input to a mill output estimation calculator 20. The mill output estimation calculator 20 is now mill 5.
Estimate the fuel flow rate when the coal input to the boiler is pulverized and sent to the boiler etc. as pulverized coal.
The mill output estimation signal 21 is fed back to the feedback subtractor 11 and compared with the master command 10. If master command 10 is larger,
The rotation speed of the coal feeder motor 3 continues to increase, but as soon as the mill output estimation signal 21 matches the master command 10, the rotation speed of the coal feeder motor 3 is maintained at that state. Therefore, the commanded flow rate of fuel is delivered from the mill 5 at a predetermined time without causing an oversupply of coal to the mill 5, and there is no possibility of fluctuations in the process.
尚、本発明は上記実施例にのみ限定されるもの
ではなく、ボイラ以外の種々の燃焼炉に対する微
粉炭燃料の供給制御に適用し得ること、その他本
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、等は勿論である。 It should be noted that the present invention is not limited to the above-mentioned embodiments, but can be applied to supply control of pulverized coal fuel to various combustion furnaces other than boilers, and various other changes can be made without departing from the gist of the present invention. Of course, it is possible to add .
上述した本発明の微粉炭燃料の供給制御方法に
よれば、給炭機によりミルに供給されている石炭
の量から、ミルより微粉炭として送り出される出
力を推定し、それをフイードバツクしてマスタ指
令と比較するようにしているので、ミル出力がマ
スタ指令と一致するように給炭機の石炭投入量を
調整してプロセスの変動をなくし制御性の向上を
図ることができる。 According to the pulverized coal fuel supply control method of the present invention described above, the output to be sent out as pulverized coal from the mill is estimated from the amount of coal being supplied to the mill by the coal feeder, and the output is fed back to the master command. Since the mill output is compared with the master command, it is possible to adjust the coal input amount of the coal feeder so that the mill output matches the master command, thereby eliminating process fluctuations and improving controllability.
第1図は微粉炭供給装置の一例を示す説明図、
第2図は従来における微粉炭燃料の供給制御方式
の説明図、第3図は本発明の方法を実施する装置
の一例を示す説明図である。
3は給炭機モータ、4は給炭機、5はミル、1
0はマスタ指令、11はフイードバツク引算器、
12はフイードバツク調節計、15は回転数検出
計、18は掛算器、19は計測信号、20はミル
出力推定演算器、21はミル出力推定信号を示
す。
FIG. 1 is an explanatory diagram showing an example of a pulverized coal supply device;
FIG. 2 is an explanatory diagram of a conventional pulverized coal fuel supply control system, and FIG. 3 is an explanatory diagram showing an example of an apparatus for implementing the method of the present invention. 3 is a coal feeder motor, 4 is a coal feeder, 5 is a mill, 1
0 is the master command, 11 is the feedback subtractor,
12 is a feedback controller, 15 is a rotation speed detector, 18 is a multiplier, 19 is a measurement signal, 20 is a mill output estimation calculator, and 21 is a mill output estimation signal.
Claims (1)
微粉化した燃料を燃焼炉に供給制御する方法にお
いて、給炭機によりミルに投入する石炭量を計測
し、該計測値におけるミル出力を推定し、該ミル
出力推定信号をフイードバツク信号として前記燃
焼炉からのマスタ指令と比較制御することを特徴
とする微粉炭燃料の供給制御方法。1 In a method of feeding coal into a mill using a coal feeder and controlling the supply of fuel pulverized by the mill to a combustion furnace, the amount of coal fed into the mill using the coal feeder is measured, and the mill output based on the measured value is calculated. A method for controlling the supply of pulverized coal fuel, characterized in that the estimated mill output signal is used as a feedback signal to compare and control the mill output with a master command from the combustion furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9846783A JPS59225754A (en) | 1983-06-02 | 1983-06-02 | Pulverized coal fuel supply control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9846783A JPS59225754A (en) | 1983-06-02 | 1983-06-02 | Pulverized coal fuel supply control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59225754A JPS59225754A (en) | 1984-12-18 |
| JPH0310380B2 true JPH0310380B2 (en) | 1991-02-13 |
Family
ID=14220477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9846783A Granted JPS59225754A (en) | 1983-06-02 | 1983-06-02 | Pulverized coal fuel supply control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59225754A (en) |
-
1983
- 1983-06-02 JP JP9846783A patent/JPS59225754A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59225754A (en) | 1984-12-18 |
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