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JPH07119907A - Method and apparatus for controlling main steam pressure of coal-fired boiler - Google Patents

Method and apparatus for controlling main steam pressure of coal-fired boiler

Info

Publication number
JPH07119907A
JPH07119907A JP26493893A JP26493893A JPH07119907A JP H07119907 A JPH07119907 A JP H07119907A JP 26493893 A JP26493893 A JP 26493893A JP 26493893 A JP26493893 A JP 26493893A JP H07119907 A JPH07119907 A JP H07119907A
Authority
JP
Japan
Prior art keywords
coal
signal
steam pressure
main steam
function generator
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
JP26493893A
Other languages
Japanese (ja)
Inventor
Ichiro Tashiro
一郎 田代
Toshio Ueno
利夫 上野
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
Ishikawajima Harima Heavy Industries Co Ltd
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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP26493893A priority Critical patent/JPH07119907A/en
Publication of JPH07119907A publication Critical patent/JPH07119907A/en
Pending legal-status Critical Current

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  • Regulation And Control Of Combustion (AREA)
  • Control Of Combustion (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Abstract

PURPOSE:To enhance response of a main steam pressure of a coal fired boiler by increasing number of revolutions of a rotary classifier according to a pressure deviation when a measured value of a main steam pressure is higher than a set value, and decreasing the number of revolutions of the classifier is according to the pressure deviation when it is lower than the set value. CONSTITUTION:A signal from a second functional generator 21 is added to a signal from a high/low signal limiter 25 by a second adder 22, and output to a motor 26 of a rotary classifier 4. The number of revolutions of a rotary classifier 4 is increased in response to a pressure deviation when a measured value of a main steam pressure is higher than a set value. The number of revolutions of the classifier 4 is decreased according to the deviation when it is lower than the set value. Thus, a supply amount of pulverized coal 2' from a coal mill 3 to a coal fired boiler 5 can be immediately increased or decreased under the control of the number of revolutions of the classifier 4 preferentially to the control of a coal supply amount to the mill 3 by a coal feeder 1.

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、石炭焚きボイラの主蒸
気圧力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 main steam pressure control method and apparatus for a coal fired boiler.

【0002】[0002]

【従来の技術】図2は従来の石炭焚きボイラの主蒸気圧
力制御装置の一例を示すもので、図示するように、給炭
機1から供給された石炭2が石炭ミル3にて微粉砕さ
れ、その微粉炭2’が前記石炭ミル3の上部に装備した
回転式分級機4を介して石炭焚きボイラ5へと空気搬出
されて燃焼されるようになっており、該石炭焚きボイラ
5からの蒸気6がガバナ7を備えた主蒸気管8を介して
タービン9へと導かれるようになっている。
2. Description of the Related Art FIG. 2 shows an example of a conventional main steam pressure control device for a coal-fired boiler. As shown in the figure, coal 2 supplied from a coal feeder 1 is pulverized by a coal mill 3. , The pulverized coal 2'is air-carried out to the coal-fired boiler 5 through the rotary classifier 4 mounted on the upper part of the coal mill 3 and burned. The steam 6 is led to a turbine 9 via a main steam pipe 8 having a governor 7.

【0003】更に、前記主蒸気管8の所要位置における
蒸気流量が蒸気流量計10により計測され、該蒸気流量
計10からの信号が関数発生器11に入力されて燃焼プ
ログラムにより蒸気流量に応じた基本給炭量が換算され
るようになっていると共に、前記主蒸気管8の所要位置
における蒸気圧力が蒸気圧力計12により計測され、該
蒸気圧力計12からの信号が第一の引算器13に入力さ
れて主蒸気圧力設定値Aとの偏差が求められ、その信号
が第一の比例積分器14を介して加算器15に出力さ
れ、該加算器15において前記関数発生器11からの信
号に加算され、更に前記加算器15からの信号が第二の
引算器16に入力されて前記給炭機1に備えた給炭流量
計17からの現在の給炭量を示す信号との偏差が求めら
れ、前記第二の引算器16からの信号が第二の比例積分
器18を介して前記給炭機1の電動機19(回転数可変
のもの)に出力され、石炭焚きボイラ5からタービン9
に導かれる蒸気圧力が一定の設定値となるよう給炭量の
制御がなされるようになっている。
Further, the steam flow rate at a required position of the main steam pipe 8 is measured by a steam flow meter 10, and a signal from the steam flow meter 10 is input to a function generator 11 to respond to the steam flow rate by a combustion program. The basic coal feed rate is converted, the steam pressure at a required position of the main steam pipe 8 is measured by a steam pressure gauge 12, and the signal from the steam pressure gauge 12 is used as a first subtractor 13 The deviation from the main steam pressure set value A is obtained, and the signal is output to the adder 15 via the first proportional integrator 14, and the adder 15 outputs the signal from the function generator 11 to the adder 15. And the signal from the adder 15 is input to the second subtractor 16 to deviate from the signal indicating the current amount of coal feeding from the coal feeding flow meter 17 provided in the coal feeding machine 1. Is required, the second subtraction Signal from 16 is output to the second proportional integrator 18 through the stoker first electric motor 19 (of the variable rotational speed), coal-fired turbine from the boiler 5 9
The amount of coal supplied is controlled so that the steam pressure introduced into the tank becomes a constant set value.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、斯かる
従来手段では、石炭ミル3に給炭してから微粉炭2’と
して排出されるまでの時間遅れが大きい為、過渡的な主
蒸気圧力変化に対して応答性が低く、主蒸気圧力を制御
する指令に大きく遅れて実際の主蒸気圧力が追従してく
るといった不具合があり、良好な制御を行うことが困難
であった。
However, in such a conventional means, there is a large time delay from the time when coal is fed to the coal mill 3 to the time when the coal is discharged as the pulverized coal 2 ', which causes a transient change in the main steam pressure. On the other hand, there is a problem that the response is low, and the actual main steam pressure follows the command for controlling the main steam pressure greatly, making it difficult to perform good control.

【0005】本発明は上述の実情に鑑みてなしたもの
で、従来より応答性の高い石炭焚きボイラの主蒸気圧力
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 an object of the present invention is to provide a main steam pressure control method and apparatus for a coal-fired boiler, which has higher response than before.

【0006】[0006]

【課題を解決するための手段】本発明の請求項1に記載
の発明は、回転式分級機4を備えた石炭ミル3からの出
炭量により主蒸気圧力を制御する石炭焚きボイラ5の主
蒸気圧力制御方法であって、主蒸気圧力の計測値が設定
値より高い時に圧力偏差に応じて前記回転式分級機4の
回転数を上げ、主蒸気圧力の計測値が設定値より低い時
に圧力偏差に応じて前記回転式分級機4の回転数を下げ
るよう制御することを特徴とするものであり、本発明の
請求項2に記載の発明は、主蒸気管8の蒸気流量を計測
する蒸気流量計10と、該蒸気流量計10からの信号を
基本給炭量に換算する第一の関数発生器11と、主蒸気
管8の蒸気圧力を計測する蒸気圧力計12と、該蒸気圧
力計12からの信号を導いて主蒸気圧力設定値との偏差
を求める第一の引算器13と、該第一の引算器13で求
まる偏差をなくす信号を出力する第一の比例積分器14
と、該第一の比例積分器14からの信号を前記第一の関
数発生器11からの信号に加算する第一の加算器15
と、石炭ミル3に給炭を行う給炭機1に備えた給炭流量
計17と、該給炭流量計17からの信号を導いて前記第
一の加算器15からの信号との偏差を求める第二の引算
器16と、該第二の引算器16で求まる偏差をなくす信
号を前記給炭機1の電動機19に出力する第二の比例積
分器18とを備えた石炭焚きボイラ5の主蒸気圧力制御
装置であって、前記蒸気流量計10からの信号を石炭ミ
ル3に備えた回転式分級機4の基本回転数に換算する第
二の関数発生器21と、前記第一の引算器13からの信
号を前記回転式分級機4の回転数の増減量に換算する第
三の関数発生器23と、該第三の関数発生器23からの
信号の変化率を制限する変化率制限器24と、該変化率
制限器24からの信号の上限と下限を制限する高低信号
制限器25と、前記第二の関数発生器21からの信号に
前記高低信号制限器25からの信号を加算して前記回転
式分級機4の電動機26に出力する第二の加算器22と
を備えたことを特徴とするものである。
According to the invention described in claim 1 of the present invention, the main of a coal-fired boiler 5 for controlling the main steam pressure by the coal output from a coal mill 3 equipped with a rotary classifier 4 A steam pressure control method, wherein when the measured value of the main steam pressure is higher than a set value, the rotational speed of the rotary classifier 4 is increased according to the pressure deviation, and when the measured value of the main steam pressure is lower than the set value. The rotary classifier 4 is controlled so as to reduce the rotation speed according to the deviation. The invention according to claim 2 of the present invention is a steam measuring steam flow rate of the main steam pipe 8. A flow meter 10, a first function generator 11 for converting a signal from the steam flow meter 10 into a basic coal feed rate, a steam pressure gauge 12 for measuring the steam pressure of the main steam pipe 8, and a steam pressure gauge 12 The first parameter to derive the deviation from the main steam pressure set value by deriving the signal from A vessel 13, the first proportional integrator 14 which outputs a signal to eliminate deviations obtained by said first subtracter 13
And a first adder 15 for adding the signal from the first proportional integrator 14 to the signal from the first function generator 11.
And a coal feeding flow meter 17 provided in the coal feeding machine 1 for feeding coal to the coal mill 3 and a deviation from the signal from the first adder 15 by guiding a signal from the coal feeding flow meter 17 A coal-fired boiler equipped with a second subtractor 16 to be obtained and a second proportional integrator 18 for outputting a signal for eliminating the deviation obtained by the second subtractor 16 to the electric motor 19 of the coal feeder 1. The main function of the steam pressure control device 5 is a second function generator 21 for converting a signal from the steam flow meter 10 into a basic rotation speed of a rotary classifier 4 provided in the coal mill 3, and the first function generator 21. The third function generator 23 for converting the signal from the subtractor 13 into the amount of increase / decrease in the rotation speed of the rotary classifier 4 and the rate of change of the signal from the third function generator 23 are limited. A rate-of-change limiter 24, a high-low signal limiter 25 for limiting the upper and lower limits of the signal from the rate-of-change limiter 24, and A second adder 22 for adding the signal from the high / low signal limiter 25 to the signal from the second function generator 21 and outputting the signal to the electric motor 26 of the rotary classifier 4. To do.

【0007】[0007]

【作用】従って本発明の請求項1に記載の発明では、主
蒸気圧力の計測値が設定値より高い時に圧力偏差に応じ
て前記回転式分級機4の回転数を上げると、石炭ミル3
から石炭焚きボイラ5への微粉の供給量が抑制されて主
蒸気圧力が下げられ、一方、主蒸気圧力の計測値が設定
値より低い時に圧力偏差に応じて前記回転式分級機4の
回転数を下げるよう制御すると、石炭ミル3から石炭焚
きボイラ5への微粉の供給量が増加されて主蒸気圧力が
上げられる。
Therefore, according to the first aspect of the present invention, when the rotation speed of the rotary classifier 4 is increased according to the pressure deviation when the measured value of the main steam pressure is higher than the set value, the coal mill 3
The supply amount of fine powder from the coal to the coal-fired boiler 5 is suppressed to lower the main steam pressure, while the rotation speed of the rotary classifier 4 is changed according to the pressure deviation when the measured value of the main steam pressure is lower than the set value. If it is controlled so as to lower, the amount of fine powder supplied from the coal mill 3 to the coal-fired boiler 5 is increased and the main steam pressure is increased.

【0008】また、本発明の請求項2に記載の発明で
は、主蒸気圧力の計測値が設定値より高い場合に、蒸気
流量計10から出力された信号に基づいて第二の関数発
生器21で回転式分級機4の基本回転数を換算すると共
に、第一の引算器13からの信号に基づいて第三の関数
発生器23で回転式分級機4の回転数の増量分を変化率
制限器24、高低信号制限器25により例えば急激に上
昇して徐々に低下するような変化率で且つ石炭焚きボイ
ラ5での燃焼に支障を及ぼす上限を超えない信号として
第二の加算器22に入力し、該第二の加算器22にて前
記基本回転数に加算して前記回転式分級機4の電動機2
6に出力すると、前記回転式分級機4の回転数が主蒸気
圧力の計測値と設定値との圧力偏差に応じて上げられる
ので、石炭ミル3から石炭焚きボイラ5への微粉の供給
量が抑制され、主蒸気圧力が下げられる。
According to the second aspect of the present invention, the second function generator 21 is based on the signal output from the steam flow meter 10 when the measured value of the main steam pressure is higher than the set value. The basic rotation speed of the rotary classifier 4 is converted with, and the increment of the rotation speed of the rotary classifier 4 is changed by the third function generator 23 based on the signal from the first subtractor 13. By the limiter 24 and the high / low signal limiter 25, for example, to the second adder 22 as a signal that has a rate of change such that it rapidly rises and gradually decreases, and does not exceed the upper limit that interferes with combustion in the coal-fired boiler 5. It is input and is added to the basic rotation speed by the second adder 22 to drive the electric motor 2 of the rotary classifier 4.
When output to 6, the rotation speed of the rotary classifier 4 is increased according to the pressure deviation between the measured value and the set value of the main steam pressure, so that the supply amount of fine powder from the coal mill 3 to the coal-fired boiler 5 is increased. It is suppressed and the main steam pressure is reduced.

【0009】また、主蒸気圧力の計測値が設定値より低
い場合に、蒸気流量計10から出力された信号に基づい
て第二の関数発生器21で回転式分級機4の基本回転数
を換算すると共に、第一の引算器13からの信号に基づ
いて第三の関数発生器23で回転式分級機4の回転数の
減量分を変化率制限器24、高低信号制限器25により
例えば急激に低下して徐々に上昇するような変化率で且
つ石炭焚きボイラ5での燃焼に支障を及ぼす下限を超え
ない信号として第二の加算器22に入力し、該第二の加
算器22にて前記基本回転数に加算して前記回転式分級
機4の電動機26に出力すると、前記回転式分級機4の
回転数が主蒸気圧力の計測値と設定値との圧力偏差に応
じて下げられるので、石炭ミル3から石炭焚きボイラ5
への微粉の供給量が増加され、主蒸気圧力が上げられ
る。
When the measured value of the main steam pressure is lower than the set value, the basic rotation speed of the rotary classifier 4 is converted by the second function generator 21 based on the signal output from the steam flow meter 10. At the same time, based on the signal from the first subtracter 13, the third function generator 23 uses the change rate limiter 24 and the high / low signal limiter 25 to decrease the amount of rotation of the rotary classifier 4 rapidly, for example. Is input to the second adder 22 as a signal that has a rate of change that gradually decreases and gradually rises and that does not exceed the lower limit that interferes with combustion in the coal-fired boiler 5, and the second adder 22 When the rotation speed of the rotary classifier 4 is added to the basic rotation speed and output to the electric motor 26 of the rotary classifier 4, the rotation speed of the rotary classifier 4 is lowered according to the pressure deviation between the measured value of the main steam pressure and the set value. , Coal mill 3 to coal-fired boiler 5
The amount of fine powder supplied to the main steam is increased and the main steam pressure is increased.

【0010】[0010]

【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.

【0011】図1は本発明の一実施例を示すもので、図
2と同一の符号を付した部分は同一物を表わしている。
FIG. 1 shows an embodiment of the present invention, in which the same reference numerals as those in FIG. 2 represent the same parts.

【0012】前述した図2の主蒸気圧力制御装置と略同
様に構成した主蒸気圧力制御装置20において、蒸気流
量計10から出力された信号が、第二の関数発生器21
にも導かれて基本回転数プログラムにより蒸気流量に応
じた回転式分級機4の基本回転数に換算され、前記第二
の関数発生器21からの信号が第二の加算器22に入力
されるようになっている。
In the main steam pressure control device 20 having substantially the same structure as the main steam pressure control device of FIG. 2 described above, the signal output from the steam flow meter 10 is the second function generator 21.
Is also converted into the basic rotation speed of the rotary classifier 4 according to the steam flow rate by the basic rotation speed program, and the signal from the second function generator 21 is input to the second adder 22. It is like this.

【0013】更に、第一の引算器13から出力された信
号が、第三の関数発生器23にも導かれて圧力偏差に応
じた回転式分級機4の回転数の増減量に換算され、前記
第三の関数発生器23からの信号が変化率制限器24に
入力されて変化率を制限され、更に高低信号制限器25
に導かれて信号の上限と下限を制限されて第二の加算器
22に導かれるようになっており、該第二の加算器22
において前記第二の関数発生器21からの信号が前記高
低信号制限器25からの信号を加算されて前記回転式分
級機4の電動機26(回転数可変のもの)に出力され、
主蒸気圧力の計測値が設定値より高い時に圧力偏差に応
じて前記回転式分級機4の回転数を上げ、主蒸気圧力の
計測値が設定値より低い時に圧力偏差に応じて前記回転
式分級機4の回転数を下げる制御がなされるようにして
ある。
Further, the signal output from the first subtractor 13 is also led to the third function generator 23 and converted into an increase / decrease amount of the rotation speed of the rotary classifier 4 according to the pressure deviation. , The signal from the third function generator 23 is input to the rate-of-change limiter 24 to limit the rate of change, and the high-low signal limiter 25
And the upper and lower limits of the signal are limited to be guided to the second adder 22.
In, the signal from the second function generator 21 is added to the signal from the high / low signal limiter 25 and is output to the electric motor 26 (variable number of revolutions) of the rotary classifier 4,
When the measured value of the main steam pressure is higher than the set value, the rotation speed of the rotary classifier 4 is increased according to the pressure deviation, and when the measured value of the main steam pressure is lower than the set value, the rotary classification is performed according to the pressure deviation. The control for lowering the rotation speed of the machine 4 is performed.

【0014】而して、主蒸気圧力の計測値が設定値より
高い場合に、蒸気流量計10から出力された信号に基づ
いて第二の関数発生器21で回転式分級機4の基本回転
数を換算すると共に、第一の引算器13からの信号に基
づいて第三の関数発生器23で回転式分級機4の回転数
の増量分を換算し、該回転数の増量分を変化率制限器2
4、高低信号制限器25により急激に上昇して徐々に低
下するような変化率で且つ石炭焚きボイラ5での燃焼に
支障を及ぼす上限を超えない信号として第二の加算器2
2に入力し、該第二の加算器22にて前記基本回転数に
加算して前記回転式分級機4の電動機26に出力する
と、前記回転式分級機4の回転数が主蒸気圧力の計測値
と設定値との圧力偏差に応じて上げられるので、石炭ミ
ル3から石炭焚きボイラ5への微粉炭2’の供給量が抑
制され、主蒸気圧力が下げられる。
Therefore, when the measured value of the main steam pressure is higher than the set value, the basic rotation speed of the rotary classifier 4 is increased by the second function generator 21 based on the signal output from the steam flow meter 10. And the amount of increase in the number of revolutions of the rotary classifier 4 is converted by the third function generator 23 based on the signal from the first subtractor 13, and the amount of increase in the number of revolutions is changed. Limiter 2
4. The second adder 2 as a signal that has a rate of change that rapidly increases and gradually decreases by the high / low signal limiter 25 and that does not exceed the upper limit that interferes with combustion in the coal-fired boiler 5.
2 is input to the second adder 22 and is added to the basic rotation speed by the second adder 22, and is output to the electric motor 26 of the rotary classifier 4. The rotation speed of the rotary classifier 4 is the measurement of the main steam pressure. Since it is increased according to the pressure deviation between the value and the set value, the supply amount of the pulverized coal 2 ′ from the coal mill 3 to the coal-fired boiler 5 is suppressed, and the main steam pressure is reduced.

【0015】また、主蒸気圧力の計測値が設定値より低
い場合に、蒸気流量計10から出力された信号に基づい
て第二の関数発生器21で回転式分級機4の基本回転数
を換算すると共に、第一の引算器13からの信号に基づ
いて第三の関数発生器23で回転式分級機4の回転数の
減量分を換算し、該回転数の減量分を変化率制限器2
4、高低信号制限器25により急激に低下して徐々に上
昇するような変化率で且つ石炭焚きボイラ5での燃焼に
支障を及ぼす下限を超えない信号として第二の加算器2
2に入力し、該第二の加算器22にて前記基本回転数に
加算して前記回転式分級機4の電動機26に出力する
と、前記回転式分級機4の回転数が主蒸気圧力の計測値
と設定値との圧力偏差に応じて下げられるので、石炭ミ
ル3から石炭焚きボイラ5への微粉炭2’の供給量が増
加され、主蒸気圧力が上げられる。
When the measured value of the main steam pressure is lower than the set value, the second function generator 21 converts the basic rotation speed of the rotary classifier 4 based on the signal output from the steam flow meter 10. At the same time, based on the signal from the first subtractor 13, the third function generator 23 converts the reduction amount of the rotation speed of the rotary classifier 4, and the reduction amount of the rotation speed is changed by the rate-of-change limiter. Two
4. The second adder 2 as a signal having a rate of change that sharply decreases and gradually increases by the high / low signal limiter 25 and does not exceed a lower limit that hinders combustion in the coal-fired boiler 5.
2 is input to the second adder 22 and is added to the basic rotation speed by the second adder 22, and is output to the electric motor 26 of the rotary classifier 4. The rotation speed of the rotary classifier 4 is the measurement of the main steam pressure. Since it is lowered according to the pressure deviation between the value and the set value, the supply amount of the pulverized coal 2 ′ from the coal mill 3 to the coal-fired boiler 5 is increased, and the main steam pressure is increased.

【0016】従って上記実施例によれば、給炭機1によ
る石炭ミル3への給炭量の制御に先行して回転式分級機
4の回転数制御により石炭ミル3から石炭焚きボイラ5
への微粉炭2’の供給量を直ちに増減することができる
ので、主蒸気圧力変化に対する応答性を従来より大幅に
向上することができる。
Therefore, according to the above-described embodiment, prior to the control of the amount of coal fed to the coal mill 3 by the coal feeder 1, the rotation speed of the rotary classifier 4 is controlled to control the coal mill 3 to the coal-fired boiler 5.
Since the amount of pulverized coal 2'supplied to the steam generator can be immediately increased or decreased, the responsiveness to changes in the main steam pressure can be significantly improved as compared with the conventional case.

【0017】尚、本発明の石炭焚きボイラの主蒸気圧力
制御方法及び装置は、上述の実施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。
The method and apparatus for controlling the main steam pressure of the coal-fired boiler according to the present invention are not limited to the above-mentioned embodiments, and various modifications can be made without departing from the gist of the present invention. Of course.

【0018】[0018]

【発明の効果】上記した本発明の石炭焚きボイラの主蒸
気圧力制御方法及び装置によれば、給炭機1による石炭
ミル3への給炭量の制御に先行して回転式分級機4の回
転数制御により石炭ミル3から石炭焚きボイラ5への微
粉炭2’の供給量を直ちに増減することができるので、
主蒸気圧力変化に対する応答性を従来より大幅に向上す
ることができるという優れた効果を奏し得る。
According to the main steam pressure control method and apparatus for a coal-fired boiler of the present invention described above, the rotary classifier 4 is operated prior to the control of the amount of coal fed to the coal mill 3 by the coal feeder 1. Since the supply amount of the pulverized coal 2 ′ from the coal mill 3 to the coal-fired boiler 5 can be immediately increased / decreased by the rotation speed control,
The excellent effect that the responsiveness to the change in the main steam pressure can be significantly improved as compared with the conventional case can be obtained.

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

【図1】本発明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 the present invention.

【図2】従来例を示すブロック図である。FIG. 2 is a block diagram showing a conventional example.

【符号の説明】[Explanation of symbols]

1 給炭機 3 石炭ミル 4 回転式分級機 5 石炭焚きボイラ 8 主蒸気管 10 蒸気流量計 11 第一の関数発生器 12 蒸気圧力計 13 第一の引算器 14 第一の比例積分器 15 第一の加算器 16 第二の引算器 17 給炭流量計 18 第二の比例積分器 19 電動機 20 主蒸気圧力制御装置 21 第二の関数発生器 22 第二の加算器 23 第三の関数発生器 24 変化率制限器 25 高低信号制限器 26 電動機 DESCRIPTION OF SYMBOLS 1 Coal feeder 3 Coal mill 4 Rotary classifier 5 Coal fired boiler 8 Main steam pipe 10 Steam flow meter 11 First function generator 12 Steam pressure gauge 13 First subtractor 14 First proportional integrator 15 First adder 16 Second subtractor 17 Coal flow meter 18 Second proportional integrator 19 Electric motor 20 Main steam pressure controller 21 Second function generator 22 Second adder 23 Third function Generator 24 Change rate limiter 25 High and low signal limiter 26 Electric motor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 回転式分級機(4)を備えた石炭ミル
(3)からの出炭量により主蒸気圧力を制御する石炭焚
きボイラ(5)の主蒸気圧力制御方法であって、主蒸気
圧力の計測値が設定値より高い時に圧力偏差に応じて前
記回転式分級機(4)の回転数を上げ、主蒸気圧力の計
測値が設定値より低い時に圧力偏差に応じて前記回転式
分級機(4)の回転数を下げるよう制御することを特徴
とする石炭焚きボイラの主蒸気圧力制御方法。
1. A main steam pressure control method for a coal-fired boiler (5), wherein the main steam pressure is controlled by the coal output from a coal mill (3) equipped with a rotary classifier (4). When the measured pressure value is higher than the set value, the rotation speed of the rotary classifier (4) is increased according to the pressure deviation, and when the measured main steam pressure value is lower than the set value, the rotary classification is performed according to the pressure deviation. A main steam pressure control method for a coal-fired boiler, characterized by controlling the number of revolutions of the machine (4).
【請求項2】 主蒸気管(8)の蒸気流量を計測する蒸
気流量計(10)と、該蒸気流量計(10)からの信号
を基本給炭量に換算する第一の関数発生器(11)と、
主蒸気管(8)の蒸気圧力を計測する蒸気圧力計(1
2)と、該蒸気圧力計(12)からの信号を導いて主蒸
気圧力設定値との偏差を求める第一の引算器(13)
と、該第一の引算器(13)で求まる偏差をなくす信号
を出力する第一の比例積分器(14)と、該第一の比例
積分器(14)からの信号を前記第一の関数発生器(1
1)からの信号に加算する第一の加算器(15)と、石
炭ミル(3)に給炭を行う給炭機(1)に備えた給炭流
量計(17)と、該給炭流量計(17)からの信号を導
いて前記第一の加算器(15)からの信号との偏差を求
める第二の引算器(16)と、該第二の引算器(16)
で求まる偏差をなくす信号を前記給炭機(1)の電動機
(19)に出力する第二の比例積分器(18)とを備え
た石炭焚きボイラ(5)の主蒸気圧力制御装置であっ
て、前記蒸気流量計(10)からの信号を石炭ミル
(3)に備えた回転式分級機(4)の基本回転数に換算
する第二の関数発生器(21)と、前記第一の引算器
(13)からの信号を前記回転式分級機(4)の回転数
の増減量に換算する第三の関数発生器(23)と、該第
三の関数発生器(23)からの信号の変化率を制限する
変化率制限器(24)と、該変化率制限器(24)から
の信号の上限と下限を制限する高低信号制限器(25)
と、前記第二の関数発生器(21)からの信号に前記高
低信号制限器(25)からの信号を加算して前記回転式
分級機(4)の電動機(26)に出力する第二の加算器
(22)とを備えたことを特徴とする石炭焚きボイラの
主蒸気圧力制御装置。
2. A steam flow meter (10) for measuring a steam flow rate of a main steam pipe (8), and a first function generator (11) for converting a signal from the steam flow meter (10) into a basic coal feed rate. )When,
Steam pressure gauge (1 to measure the steam pressure of the main steam pipe (8)
2) and a first subtractor (13) for guiding the signal from the steam pressure gauge (12) to obtain the deviation from the main steam pressure set value.
And a first proportional integrator (14) for outputting a signal for eliminating the deviation obtained by the first subtractor (13), and a signal from the first proportional integrator (14) for the first proportional integrator (14). Function generator (1
1) A first adder (15) for adding to the signal from the coal mill (3), a coal feeding flow meter (17) provided in the coal feeding machine (1) for feeding coal to the coal mill (3), and the coal feeding flow rate. A second subtractor (16) for deriving a signal from the total (17) to obtain a deviation from the signal from the first adder (15), and the second subtractor (16)
A main steam pressure controller for a coal-fired boiler (5), comprising a second proportional-integrator (18) for outputting a signal for eliminating the deviation obtained in (1) to the electric motor (19) of the coal feeder (1), A second function generator (21) for converting a signal from the steam flow meter (10) into a basic rotation speed of a rotary classifier (4) provided in a coal mill (3); A third function generator (23) for converting the signal from the calculator (13) into an increase / decrease amount of the rotation speed of the rotary classifier (4), and a signal from the third function generator (23) Rate limiter (24) for limiting the rate of change of the signal, and a high / low signal limiter (25) for limiting the upper and lower limits of the signal from the rate of change limiter (24).
And a signal from the high / low signal limiter (25) is added to the signal from the second function generator (21) and output to the electric motor (26) of the rotary classifier (4). A main steam pressure control device for a coal-fired boiler, comprising an adder (22).
JP26493893A 1993-10-22 1993-10-22 Method and apparatus for controlling main steam pressure of coal-fired boiler Pending JPH07119907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26493893A JPH07119907A (en) 1993-10-22 1993-10-22 Method and apparatus for controlling main steam pressure of coal-fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26493893A JPH07119907A (en) 1993-10-22 1993-10-22 Method and apparatus for controlling main steam pressure of coal-fired boiler

Publications (1)

Publication Number Publication Date
JPH07119907A true JPH07119907A (en) 1995-05-12

Family

ID=17410278

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26493893A Pending JPH07119907A (en) 1993-10-22 1993-10-22 Method and apparatus for controlling main steam pressure of coal-fired boiler

Country Status (1)

Country Link
JP (1) JPH07119907A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999058246A1 (en) * 1998-05-13 1999-11-18 Abb Alstom Power Inc. Control method and system for a coal mill in boilers
KR101379558B1 (en) * 2012-12-18 2014-03-31 (주)하이텍산업개발 Discharge pressure removing apparatus for steam pipe line

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999058246A1 (en) * 1998-05-13 1999-11-18 Abb Alstom Power Inc. Control method and system for a coal mill in boilers
KR101379558B1 (en) * 2012-12-18 2014-03-31 (주)하이텍산업개발 Discharge pressure removing apparatus for steam pipe line

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