JPH1057769A - Method for controlling injection of denitrating ammonia into coal-fired boiler and device therefor - Google Patents

Method for controlling injection of denitrating ammonia into coal-fired boiler and device therefor

Info

Publication number
JPH1057769A
JPH1057769A JP8222399A JP22239996A JPH1057769A JP H1057769 A JPH1057769 A JP H1057769A JP 8222399 A JP8222399 A JP 8222399A JP 22239996 A JP22239996 A JP 22239996A JP H1057769 A JPH1057769 A JP H1057769A
Authority
JP
Japan
Prior art keywords
combustion amount
flow rate
signal
amount command
coal
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
JP8222399A
Other languages
Japanese (ja)
Other versions
JP3911729B2 (en
Inventor
Kazuyoshi Sakamoto
和由 阪本
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 JP22239996A priority Critical patent/JP3911729B2/en
Publication of JPH1057769A publication Critical patent/JPH1057769A/en
Application granted granted Critical
Publication of JP3911729B2 publication Critical patent/JP3911729B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PROBLEM TO BE SOLVED: To inject a required amt. of ammonia even at a load decreasing as well as at a load increasing and to prevent the outlet NOx of a denitrater from exceeding a stipulated value. SOLUTION: When the load of a coal-fired boiler is increased, the waste gas flow rate 8 is obtained practically in follow-up to the change in the combustion rate command signal 7, the required ammonia injection 10 is obtained based on the waste gas flow rate 8, the inlet NOx of a denitrater and the molar ratio and outputted. Meanwhile, when the load of the coal-fired boiler is decreased, the waste gas flow rate 8 is obtained in follow-up to the change in the combustion rate command signal 2 so that the preset time lag is secured, and the required ammonia injection 10 is obtained based on the flow rate 8, the inlet NOx of the denitrater and the molar ratio and outputted.

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、石炭焚ボイラの脱
硝アンモニア注入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 method and an apparatus for controlling an injection amount of denitrified ammonia in a coal-fired boiler.

【0002】[0002]

【従来の技術】一般に、石炭焚ボイラから排出される排
ガス中には、窒素酸化物(NOx)が含まれているた
め、このようなNOxは脱硝装置によって除去する必要
がある。
2. Description of the Related Art Generally, nitrogen oxides (NOx) are contained in exhaust gas discharged from a coal-fired boiler, and such NOx must be removed by a denitration device.

【0003】図3は従来の石炭焚ボイラの一例を表わす
ものであって、1は石炭焚ボイラ、2は石炭焚ボイラ1
からの排ガスが流通するダクト、3はダクト2途中に設
けられ且つ内部に触媒が充填された脱硝装置、4は誘引
通風機、5は脱硝装置3へ流入する排ガス中に含まれる
入口NOx(単位は[ppm])を検出する入口NOx
計、6は脱硝装置3を通過した排ガス中に含まれる出口
NOx(単位は[ppm])を検出する出口NOx計であ
り、ダクト2内へアンモニアを注入し、脱硝装置3内の
触媒によって石炭焚ボイラ1からの排ガス中に含まれる
NOxを還元することにより、出口NOx計6によって検
出される出口NOxを規定値以下に抑制するようになっ
ているが、この場合のアンモニアの注入量に関しては、
図4に示されるような制御装置において演算が行われ
る。
FIG. 3 shows an example of a conventional coal-fired boiler, where 1 is a coal-fired boiler and 2 is a coal-fired boiler.
3 is a denitration device provided in the middle of the duct 2 and filled with a catalyst, 4 is an induction ventilator, 5 is an inlet NOx contained in exhaust gas flowing into the denitration device 3 (unit). Is [ppm])
Reference numeral 6 denotes an outlet NOx meter for detecting outlet NOx (unit: [ppm]) contained in exhaust gas that has passed through the denitration device 3. By reducing NOx contained in the exhaust gas from the boiler 1, the outlet NOx detected by the outlet NOx meter 6 is suppressed to a specified value or less. ,
The calculation is performed in a control device as shown in FIG.

【0004】前記制御装置は、燃焼量指令信号(FF
D)7に基づき排ガス流量8(単位は[Nm3/h])
を求めて出力する関数発生器9と、該関数発生器9から
出力される排ガス流量8に比例定数κと入口NOx計5
によって検出された脱硝装置3の入口NOxとモル比と
を掛け、必要アンモニア注入量10(単位は[kg/
h])を求めて出力する演算器11とを備えてなる構成
を有しており、該演算器11で演算された必要アンモニ
ア注入量10に基づいて、前記ダクト2へ注入される実
際のアンモニア注入量の調整が行われるようになってい
る。尚、前記モル比は、出口NOxを規定値以下に抑制
する際に、除去すべきNOx1モルに対して必要となる
アンモニアのモル数で表わされる数値である。
[0004] The control device includes a combustion amount command signal (FF).
D) Exhaust gas flow rate 8 based on 7 (unit is [Nm 3 / h])
And a function generator 9 for calculating and outputting a proportional constant κ and an inlet NOx total 5 for an exhaust gas flow rate 8 output from the function generator 9.
Is multiplied by the molar ratio at the inlet NOx of the denitration apparatus 3 detected by the above method, and the required ammonia injection amount 10 (unit is [kg /
h]), and calculates and outputs the actual ammonia injected into the duct 2 based on the required ammonia injection amount 10 calculated by the arithmetic unit 11. The adjustment of the injection amount is performed. The molar ratio is a numerical value represented by the number of moles of ammonia necessary for 1 mole of NOx to be removed when the outlet NOx is suppressed to a specified value or less.

【0005】前記関数発生器9には、図5に示されるよ
うな関数が入力されており、該関数は、燃焼量指令信号
7の増減に対し略比例させて排ガス流量8を増減させる
ことを表わしており、又、前記演算器11は、三つの乗
算器11a,11b,11cとを有している。
[0005] A function as shown in FIG. 5 is input to the function generator 9. The function is to increase or decrease the exhaust gas flow rate 8 substantially in proportion to the increase or decrease of the combustion amount command signal 7. The arithmetic unit 11 has three multipliers 11a, 11b and 11c.

【0006】これにより、石炭焚ボイラ1の負荷上昇時
には、図6に示される如く、燃焼量指令信号と略比例す
る形でアンモニア注入量が時間の経過と共に増加される
一方、石炭焚ボイラ1の負荷降下時には、図6に示され
る如く、燃焼量指令信号と略比例する形でアンモニア注
入量が時間の経過と共に減少されるようになっている。
As a result, when the load of the coal-fired boiler 1 is increased, as shown in FIG. 6, the amount of ammonia injected is increased with the passage of time in a manner substantially proportional to the combustion amount command signal. At the time of load reduction, as shown in FIG. 6, the ammonia injection amount is reduced with time in a manner substantially proportional to the combustion amount command signal.

【0007】[0007]

【発明が解決しようとする課題】前述の如き石炭焚ボイ
ラ1の場合、燃料としての微粉炭の供給をミル(図示せ
ず)から行っているが、該ミルでの出炭特性の遅れによ
り、燃焼量指令信号に対して実際の燃焼量は、図6に示
されるように、負荷上昇時には、若干少なめとなる一
方、負荷降下時には、若干多めとなる傾向を示す。
In the case of the coal-fired boiler 1 as described above, pulverized coal as fuel is supplied from a mill (not shown). As shown in FIG. 6, the actual combustion amount with respect to the combustion amount command signal tends to be slightly smaller when the load increases, and slightly larger when the load decreases.

【0008】このため、前述の如く、アンモニア注入量
を燃焼量指令信号をベースとして決定した場合、負荷上
昇時には、実際の燃焼量に相当するアンモニア注入量よ
り若干多めのアンモニアが前記ダクト2へ注入されるこ
ととなり、問題はないが、負荷降下時には、実際の燃焼
量に相当するアンモニア注入量より若干少なめのアンモ
ニアしか前記ダクト2へ注入されなくなり、脱硝装置3
の出口NOxが規定値を越えてしまう可能性があった。
Therefore, as described above, when the amount of injected ammonia is determined based on the combustion amount command signal, when the load increases, a little more amount of ammonia than the amount of injected ammonia corresponding to the actual amount of combustion is injected into the duct 2. There is no problem, but when the load drops, only a little less ammonia than the amount of ammonia injected corresponding to the actual combustion amount is injected into the duct 2 and the denitration device 3
Exit NOx may exceed the specified value.

【0009】本発明は、斯かる実情に鑑み、負荷上昇時
だけでなく負荷降下時においても、必要量のアンモニア
を注入することができ、脱硝装置の出口NOxが規定値
を越えてしまうことを防止し得る石炭焚ボイラの脱硝ア
ンモニア注入量制御方法及び装置を提供しようとするも
のである。
The present invention has been made in view of the above-mentioned circumstances, and it is possible to inject a required amount of ammonia not only at the time of load increase but also at the time of load decrease, and that the NOx at the outlet of the denitration apparatus exceeds a specified value. An object of the present invention is to provide a method and an apparatus for controlling the amount of denitrified ammonia injection into a coal-fired boiler that can be prevented.

【0010】[0010]

【課題を解決するための手段】本発明は、石炭焚ボイラ
の負荷上昇時には、燃焼量指令信号の変化に略追従させ
て排ガス流量を求め、該排ガス流量と脱硝装置の入口N
Oxとモル比とに基づき必要アンモニア注入量を求めて
出力する一方、石炭焚ボイラの負荷降下時には、燃焼量
指令信号の変化に対し予め設定した時間遅れが生じるよ
う追従させて排ガス流量を求め、該排ガス流量と脱硝装
置の入口NOxとモル比とに基づき必要アンモニア注入
量を求めて出力することを特徴とする石炭焚ボイラの脱
硝アンモニア注入量制御方法にかかるものである。
According to the present invention, when the load of a coal-fired boiler rises, the flow rate of the exhaust gas is obtained by substantially following the change in the combustion amount command signal.
While obtaining and outputting the required ammonia injection amount based on Ox and the molar ratio, when the load of the coal-fired boiler falls, the exhaust gas flow rate is obtained by following a change in the combustion amount command signal so that a predetermined time delay occurs, The present invention relates to a method for controlling a denitration ammonia injection amount of a coal-fired boiler, wherein a required ammonia injection amount is obtained and output based on the exhaust gas flow rate, the NOx at the inlet of the denitration device, and the molar ratio.

【0011】又、本発明は、燃焼量指令信号が変化した
場合に、該燃焼量指令信号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、燃焼量指令一次遅れ信
号を出力する一次遅れ器と、該一次遅れ器から出力され
る燃焼量指令一次遅れ信号と燃焼量指令信号のうち値の
高い方を選択し、燃焼量指令選択信号として出力する高
信号選択器と、該高信号選択器から出力される燃焼量指
令選択信号に基づき排ガス流量を求めて出力する関数発
生器と、該関数発生器から出力される排ガス流量に比例
定数と入口NOx計によって検出された脱硝装置の入口
NOxとモル比とを掛け、必要アンモニア注入量を求め
て出力する演算器とを備えたことを特徴とする石炭焚ボ
イラの脱硝アンモニア注入量制御装置にかかるものであ
る。
Further, the present invention provides a primary output signal for outputting a combustion amount command primary delay signal by following a change in the combustion amount command signal so that a predetermined time delay occurs when the combustion amount command signal changes. A delay unit, a combustion signal command output from the primary delay unit, a high signal selector for selecting a higher value of the primary delay signal and the combustion signal command signal and outputting the selected signal as a combustion command selection signal; A function generator that calculates and outputs an exhaust gas flow rate based on a combustion amount command selection signal output from the selector, and a proportional constant to the exhaust gas flow rate output from the function generator and an inlet of the denitration device detected by an inlet NOx meter The present invention relates to a denitration ammonia injection amount control device for a coal-fired boiler, comprising: an arithmetic unit for multiplying NOx by a molar ratio to obtain and output a required ammonia injection amount.

【0012】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.

【0013】本発明の石炭焚ボイラの脱硝アンモニア注
入量制御方法においては、石炭焚ボイラの負荷上昇時に
は、燃焼量指令信号の変化に略追従させて排ガス流量が
求められ、該排ガス流量と脱硝装置の入口NOxとモル
比とに基づき必要アンモニア注入量が求められて出力さ
れ、該必要アンモニア注入量に基づいて、実際のアンモ
ニア注入量の調整が行われる一方、石炭焚ボイラの負荷
降下時には、燃焼量指令信号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排ガス流量が求めら
れ、該排ガス流量と脱硝装置の入口NOxとモル比とに
基づき必要アンモニア注入量が求められて出力され、該
必要アンモニア注入量に基づいて、実際のアンモニア注
入量の調整が行われる。
In the method for controlling the amount of denitrified ammonia injected into a coal-fired boiler according to the present invention, when the load on the coal-fired boiler rises, the flow rate of the exhaust gas is obtained substantially following the change in the combustion command signal. The required ammonia injection amount is calculated and output based on the inlet NOx and the molar ratio of the fuel, and the actual ammonia injection amount is adjusted based on the required ammonia injection amount. The exhaust gas flow rate is obtained by following the change in the amount command signal such that a preset time delay occurs, and the required ammonia injection amount is obtained and output based on the exhaust gas flow rate, the NOx and the molar ratio at the inlet of the denitration device, and output. Adjustment of the actual ammonia injection amount is performed based on the required ammonia injection amount.

【0014】この結果、石炭焚ボイラの負荷上昇時に
は、燃焼量指令信号と略比例する形でアンモニア注入量
が時間の経過と共に増加される一方、石炭焚ボイラの負
荷降下時には、実際の燃焼量に相当するアンモニア注入
量と少なくとも略同量のアンモニアを前記ダクトへ注入
することが可能となり、脱硝装置の出口NOxが規定値
を越えてしまうことがなくなる。
As a result, when the load of the coal-fired boiler rises, the amount of injected ammonia is increased with the passage of time in a manner substantially proportional to the combustion amount command signal. At least approximately the same amount of ammonia as the corresponding amount of ammonia can be injected into the duct, so that the outlet NOx of the denitration device does not exceed a specified value.

【0015】又、本発明の石炭焚ボイラの脱硝アンモニ
ア注入量制御装置においては、石炭焚ボイラの負荷上昇
時には、燃焼量指令信号も増加し、該燃焼量指令信号が
一次遅れ器へ入力され、該一次遅れ器において燃焼量指
令信号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、燃焼量指令一次遅れ信号が高信号選択器へ
出力され、該高信号選択器において前記一次遅れ器から
出力される燃焼量指令一次遅れ信号と燃焼量指令信号の
うち値の高い方、即ち燃焼量指令信号が選択され、該燃
焼量指令信号がそのまま燃焼量指令選択信号として関数
発生器へ出力され、該関数発生器において前記高信号選
択器から出力される燃焼量指令選択信号に基づき関数発
生器において排ガス流量が求められて演算器へ出力さ
れ、該演算器において前記関数発生器から出力される排
ガス流量に比例定数と入口NOx計によって検出された
脱硝装置の入口NOxとモル比とが掛けられ、必要アン
モニア注入量が求められて出力され、該演算器で演算さ
れた必要アンモニア注入量に基づいて、ダクトへ注入さ
れる実際のアンモニア注入量の調整が行われる一方、石
炭焚ボイラの負荷降下時には、燃焼量指令信号も減少
し、該燃焼量指令信号が一次遅れ器へ入力され、該一次
遅れ器において燃焼量指令信号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、燃焼量指令一次遅
れ信号が高信号選択器へ出力され、該高信号選択器にお
いて前記一次遅れ器から出力される燃焼量指令一次遅れ
信号と燃焼量指令信号のうち値の高い方、即ち燃焼量指
令一次遅れ信号が選択され、該燃焼量指令一次遅れ信号
が燃焼量指令選択信号として関数発生器へ出力され、該
関数発生器において前記高信号選択器から出力される燃
焼量指令選択信号に基づき関数発生器において排ガス流
量が求められて演算器へ出力され、該演算器において前
記関数発生器から出力される排ガス流量に比例定数と入
口NOx計によって検出された脱硝装置の入口NOxとモ
ル比とが掛けられ、必要アンモニア注入量が求められて
出力され、該演算器で演算された必要アンモニア注入量
に基づいて、ダクトへ注入される実際のアンモニア注入
量の調整が行われる。
In the apparatus for controlling the amount of denitrated ammonia injected into a coal-fired boiler according to the present invention, when the load on the coal-fired boiler rises, the combustion amount command signal also increases, and the combustion amount command signal is input to the first-order lag device. The primary delay unit follows the change in the combustion amount command signal such that a preset time delay occurs, and outputs a combustion amount command primary delay signal to a high signal selector. The higher one of the combustion amount command primary delay signal and the combustion amount command signal output from, that is, the combustion amount command signal is selected, and the combustion amount command signal is output to the function generator as a combustion amount command selection signal as it is. The function generator determines the exhaust gas flow rate based on the combustion amount command selection signal output from the high signal selector in the function generator and outputs the calculated exhaust gas flow rate to an arithmetic unit. The flow rate of the exhaust gas output from the function generator is multiplied by the proportionality constant, the NOx at the inlet of the denitration apparatus detected by the inlet NOx meter, and the molar ratio, and the required ammonia injection amount is obtained and output, and is calculated by the calculator. Based on the required amount of injected ammonia, the actual amount of injected ammonia to be injected into the duct is adjusted. On the other hand, when the load of the coal-fired boiler drops, the combustion amount command signal also decreases, and the combustion amount command signal becomes primary. Input to the delay unit, the primary delay unit follows the change in the combustion amount command signal such that a preset time delay occurs, and the combustion amount command primary delay signal is output to the high signal selector, and the high signal selection is performed. The higher of the combustion amount command primary delay signal and the combustion amount command signal output from the primary delayer, that is, the combustion amount command primary delay signal, is selected. The next delay signal is output to the function generator as a combustion amount command selection signal, and the function generator determines the exhaust gas flow rate on the basis of the combustion amount command selection signal output from the high signal selector. Is output to the calculator, the proportionality constant is multiplied by the exhaust gas flow rate output from the function generator by the NOx inlet NOx and the molar ratio detected by the inlet NOx meter, and the required ammonia injection amount is determined. The actual amount of ammonia injected into the duct is adjusted based on the required amount of ammonia that is output and calculated by the arithmetic unit.

【0016】この結果、石炭焚ボイラの負荷上昇時に
は、燃焼量指令信号と略比例する形でアンモニア注入量
が時間の経過と共に増加される一方、石炭焚ボイラの負
荷降下時には、燃焼量指令一次遅れ信号と略比例する形
でアンモニア注入量が時間の経過と共に減少されるよう
になり、負荷降下時においても、実際の燃焼量に相当す
るアンモニア注入量と少なくとも略同量のアンモニアを
前記ダクトへ注入することが可能となり、脱硝装置の出
口NOxが規定値を越えてしまうことがなくなる。
As a result, when the load of the coal-fired boiler rises, the ammonia injection amount is increased with the passage of time in a manner substantially proportional to the combustion amount command signal. The amount of injected ammonia is reduced with the passage of time in a manner substantially proportional to the signal, and even when the load is reduced, at least approximately the same amount of ammonia as the amount of injected ammonia corresponding to the actual combustion amount is injected into the duct. It is possible to prevent the NOx at the outlet of the denitration apparatus from exceeding a specified value.

【0017】[0017]

【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.

【0018】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6と同一の符号を付した部
分は同一物を表わしており、基本的な構成は図3〜図6
に示す従来のものと同様であるが、本図示例の特徴とす
るところは、図1及び図2に示す如く、燃焼量指令信号
7が変化した場合に、該燃焼量指令信号7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、燃焼量
指令一次遅れ信号7’を出力する一次遅れ器12と、該
一次遅れ器12から出力される燃焼量指令一次遅れ信号
7’と燃焼量指令信号7のうち値の高い方を選択し、燃
焼量指令選択信号7”として出力する高信号選択器13
とを追加装備し、該高信号選択器13から出力される燃
焼量指令選択信号7”に基づき関数発生器9において排
ガス流量8を求めて演算器11へ出力し、該演算器11
において前記関数発生器9から出力される排ガス流量8
に比例定数κと入口NOx計5によって検出された脱硝
装置3の入口NOxとモル比とを掛け、必要アンモニア
注入量10を求めて出力し、該演算器11で演算された
必要アンモニア注入量10に基づいて、ダクト2へ注入
される実際のアンモニア注入量の調整を行うよう構成し
た点にある。
FIGS. 1 and 2 show an example of an embodiment of the present invention. In the drawings, the portions denoted by the same reference numerals as those in FIGS. 3 to 6 represent the same components. 3 to 6
However, the present embodiment is characterized in that when the combustion amount command signal 7 changes as shown in FIGS. On the other hand, a primary delay unit 12 that outputs a combustion amount command primary delay signal 7 ′ while following a preset time delay, and a combustion amount command primary delay signal 7 ′ output from the primary delay unit 12 and a combustion amount High signal selector 13 which selects the higher value of command signal 7 and outputs it as combustion amount command selection signal 7 "
The function generator 9 obtains the exhaust gas flow rate 8 based on the combustion amount command selection signal 7 "output from the high signal selector 13 and outputs it to the arithmetic unit 11.
At the exhaust gas flow rate 8 output from the function generator 9
Is multiplied by the molar ratio and the NOx at the inlet of the denitration device 3 detected by the inlet NOx meter 5 to obtain and output the required ammonia injection amount 10. The required ammonia injection amount 10 calculated by the calculator 11 Based on the above, the actual amount of ammonia injected into the duct 2 is adjusted.

【0019】次に、上記図示例の作動を説明する。Next, the operation of the illustrated example will be described.

【0020】石炭焚ボイラ1の負荷上昇時には、燃焼量
指令信号7も増加し、該燃焼量指令信号7が一次遅れ器
12へ入力され、該一次遅れ器12において燃焼量指令
信号7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、燃焼量指令一次遅れ信号7’が高信号選択
器13へ出力され、該高信号選択器13において前記一
次遅れ器12から出力される燃焼量指令一次遅れ信号
7’と燃焼量指令信号7のうち値の高い方、即ち燃焼量
指令信号7が選択され、該燃焼量指令信号7がそのまま
燃焼量指令選択信号7”として関数発生器9へ出力さ
れ、該関数発生器9において前記高信号選択器13から
出力される燃焼量指令選択信号7”に基づき関数発生器
9において排ガス流量8が求められて演算器11へ出力
され、該演算器11において前記関数発生器9から出力
される排ガス流量8に比例定数κと入口NOx計5によ
って検出された脱硝装置3の入口NOxとモル比とが掛
けられ、必要アンモニア注入量10が求められて出力さ
れ、該演算器11で演算された必要アンモニア注入量1
0に基づいて、ダクト2へ注入される実際のアンモニア
注入量の調整が行われる。
When the load of the coal-fired boiler 1 rises, the combustion amount command signal 7 also increases, and the combustion amount command signal 7 is input to the primary delay unit 12, and the primary delay unit 12 changes the combustion amount command signal 7. On the other hand, a combustion amount command primary delay signal 7 ′ is output to the high signal selector 13 so as to follow a preset time delay, and the combustion amount command output from the primary delay unit 12 in the high signal selector 13. The higher value of the primary delay signal 7 'and the combustion amount command signal 7, that is, the combustion amount command signal 7, is selected, and the combustion amount command signal 7 is output to the function generator 9 as it is as the combustion amount command selection signal 7 ". Then, the function generator 9 calculates the exhaust gas flow rate 8 based on the combustion amount command selection signal 7 "output from the high signal selector 13 and outputs it to the calculator 11. In Then, the exhaust gas flow rate 8 output from the function generator 9 is multiplied by the proportionality constant κ, the NOx at the inlet of the denitration device 3 detected by the inlet NOx meter 5 and the molar ratio, and the required ammonia injection amount 10 is obtained and output. And the required ammonia injection amount 1 calculated by the arithmetic unit 11
Based on 0, adjustment of the actual amount of ammonia injected into the duct 2 is performed.

【0021】一方、石炭焚ボイラ1の負荷降下時には、
燃焼量指令信号7も減少し、該燃焼量指令信号7が一次
遅れ器12へ入力され、該一次遅れ器12において燃焼
量指令信号7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、燃焼量指令一次遅れ信号7’が高信
号選択器13へ出力され、該高信号選択器13において
前記一次遅れ器12から出力される燃焼量指令一次遅れ
信号7’と燃焼量指令信号7のうち値の高い方、即ち燃
焼量指令一次遅れ信号7’が選択され、該燃焼量指令一
次遅れ信号7’が燃焼量指令選択信号7”として関数発
生器9へ出力され、該関数発生器9において前記高信号
選択器13から出力される燃焼量指令選択信号7”に基
づき関数発生器9において排ガス流量8が求められて演
算器11へ出力され、該演算器11において前記関数発
生器9から出力される排ガス流量8に比例定数κと入口
NOx計5によって検出された脱硝装置3の入口NOxと
モル比とが掛けられ、必要アンモニア注入量10が求め
られて出力され、該演算器11で演算された必要アンモ
ニア注入量10に基づいて、ダクト2へ注入される実際
のアンモニア注入量の調整が行われる。
On the other hand, when the load of the coal-fired boiler 1 drops,
The combustion amount command signal 7 also decreases, and the combustion amount command signal 7 is input to the primary delay unit 12, and the primary delay unit 12 follows the change in the combustion amount command signal 7 such that a preset time delay occurs. , The combustion amount command primary delay signal 7 ′ is output to the high signal selector 13, and the combustion amount command primary delay signal 7 ′ and the combustion amount command signal 7 output from the primary delay device 12 in the high signal selector 13. The higher value, ie, the combustion amount command primary delay signal 7 'is selected, and the combustion amount command primary delay signal 7' is output to the function generator 9 as the combustion amount command selection signal 7 ", and the function generator 9 is selected. The exhaust gas flow rate 8 is obtained by the function generator 9 based on the combustion amount command selection signal 7 ″ output from the high signal selector 13 and output to the arithmetic unit 11, where the function generator 9 outputs Output The gas flow rate 8 is multiplied by the proportional constant κ and the inlet NOx detected by the inlet NOx meter 5 and the molar ratio, and the required ammonia injection amount 10 is obtained and output, and calculated by the calculator 11. Based on the required ammonia injection amount 10, the actual ammonia injection amount injected into the duct 2 is adjusted.

【0022】この結果、石炭焚ボイラ1の負荷上昇時に
は、図2に示す如く、燃焼量指令信号7と略比例する形
でアンモニア注入量が時間の経過と共に増加される一
方、石炭焚ボイラ1の負荷降下時には、図2に示す如
く、燃焼量指令一次遅れ信号7’と略比例する形でアン
モニア注入量が時間の経過と共に減少されるようにな
り、負荷降下時においても、実際の燃焼量に相当するア
ンモニア注入量と略同量のアンモニアを前記ダクト2へ
注入することが可能となり、脱硝装置3の出口NOxが
規定値を越えてしまうことがなくなる。
As a result, when the load of the coal-fired boiler 1 increases, as shown in FIG. 2, the ammonia injection amount is increased with time in a manner substantially proportional to the combustion amount command signal 7, while the coal-fired boiler 1 At the time of load reduction, as shown in FIG. 2, the ammonia injection amount is reduced with time in a manner substantially proportional to the combustion amount command primary delay signal 7 '. A substantially same amount of ammonia as the corresponding amount of ammonia can be injected into the duct 2, so that the outlet NOx of the denitration device 3 does not exceed a specified value.

【0023】尚、一次遅れ器12において燃焼量指令信
号7の変化に対し予め設定する時間遅れを若干長めとす
れば、ダクト2へ注入されるアンモニアの量を実際の燃
焼量に相当するアンモニア注入量より若干多めにできる
ことは言うまでもない。
If the time delay preset in the primary delay unit 12 with respect to the change in the combustion amount command signal 7 is made slightly longer, the amount of ammonia injected into the duct 2 is reduced by the amount of ammonia injected corresponding to the actual combustion amount. Needless to say, it can be slightly larger than the amount.

【0024】こうして、負荷上昇時だけでなく負荷降下
時においても、必要量のアンモニアを注入することがで
き、脱硝装置3の出口NOxが規定値を越えてしまうこ
とを防止し得る。
In this way, not only when the load rises but also when the load drops, the required amount of ammonia can be injected, and the NOx at the outlet of the denitration device 3 can be prevented from exceeding a specified value.

【0025】尚、本発明の石炭焚ボイラの脱硝アンモニ
ア注入量制御方法及び装置は、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 controlling the amount of denitrated ammonia injected into a coal-fired boiler of the present invention are not limited to the illustrated examples described above, and various changes can be made without departing from the scope of the present invention. Of course.

【0026】[0026]

【発明の効果】以上、説明したように本発明の石炭焚ボ
イラの脱硝アンモニア注入量制御方法及び装置によれ
ば、負荷上昇時だけでなく負荷降下時においても、必要
量のアンモニアを注入することができ、脱硝装置の出口
NOxが規定値を越えてしまうこと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 controlling the amount of denitrated ammonia injected into a coal-fired boiler according to the present invention, it is possible to inject a required amount of ammonia not only at the time of increasing the load but also at the time of decreasing the load. Therefore, an excellent effect of preventing the outlet NOx of the denitration device from exceeding a specified value can be obtained.

【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における負荷上昇
時と負荷降下時の燃焼量指令信号とアンモニア注入量と
燃焼量との関係を表わす線図である。
FIG. 2 is a diagram showing a relationship between a combustion amount command signal, an ammonia injection amount, and a combustion amount when the load is increased and when the load is decreased in an example of an embodiment of the present invention.

【図3】従来例の全体概要構成図である。FIG. 3 is an overall schematic configuration diagram of a conventional example.

【図4】従来例のブロック図である。FIG. 4 is a block diagram of a conventional example.

【図5】図4に示される関数発生器に設定されている関
数を表わす線図である。
FIG. 5 is a diagram showing functions set in the function generator shown in FIG. 4;

【図6】従来例における負荷上昇時と負荷降下時の燃焼
量指令信号とアンモニア注入量と燃焼量との関係を表わ
す線図である。
FIG. 6 is a diagram showing a relationship between a combustion amount command signal, an ammonia injection amount, and a combustion amount when the load is increased and when the load is decreased in the conventional example.

【符号の説明】[Explanation of symbols]

1 石炭焚ボイラ 3 脱硝装置 5 入口NOx計 7 燃焼量指令信号 7’ 燃焼量指令一次遅れ信号 7” 燃焼量指令選択信号 8 排ガス流量 9 関数発生器 10 必要アンモニア注入量 11 演算器 12 一次遅れ器 13 高信号選択器 DESCRIPTION OF SYMBOLS 1 Coal-fired boiler 3 Denitration device 5 Inlet NOx meter 7 Combustion amount command signal 7 'Combustion amount command primary delay signal 7 "Combustion amount command selection signal 8 Exhaust gas flow 9 Function generator 10 Required ammonia injection amount 11 Computing unit 12 Primary delay unit 13 High signal selector

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 石炭焚ボイラの負荷上昇時には、燃焼量
指令信号の変化に略追従させて排ガス流量を求め、該排
ガス流量と脱硝装置の入口NOxとモル比とに基づき必
要アンモニア注入量を求めて出力する一方、石炭焚ボイ
ラの負荷降下時には、燃焼量指令信号の変化に対し予め
設定した時間遅れが生じるよう追従させて排ガス流量を
求め、該排ガス流量と脱硝装置の入口NOxとモル比と
に基づき必要アンモニア注入量を求めて出力することを
特徴とする石炭焚ボイラの脱硝アンモニア注入量制御方
法。
When the load of a coal-fired boiler rises, an exhaust gas flow rate is obtained by substantially following a change in a combustion amount command signal, and a required ammonia injection amount is obtained based on the exhaust gas flow rate, the NOx at the inlet of the denitration apparatus, and the molar ratio. On the other hand, when the load of the coal-fired boiler drops, the exhaust gas flow rate is obtained by following the change in the combustion amount command signal so that a preset time delay occurs, and the exhaust gas flow rate, the NOx and the molar ratio at the inlet of the denitration device are determined. A method for controlling a denitration ammonia injection amount of a coal-fired boiler, wherein a required ammonia injection amount is obtained and output based on the following.
【請求項2】 燃焼量指令信号が変化した場合に、該燃
焼量指令信号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、燃焼量指令一次遅れ信号を出力する
一次遅れ器と、 該一次遅れ器から出力される燃焼量指令一次遅れ信号と
燃焼量指令信号のうち値の高い方を選択し、燃焼量指令
選択信号として出力する高信号選択器と、 該高信号選択器から出力される燃焼量指令選択信号に基
づき排ガス流量を求めて出力する関数発生器と、 該関数発生器から出力される排ガス流量に比例定数と入
口NOx計によって検出された脱硝装置の入口NOxとモ
ル比とを掛け、必要アンモニア注入量を求めて出力する
演算器とを備えたことを特徴とする石炭焚ボイラの脱硝
アンモニア注入量制御装置。
2. A primary delay unit that outputs a combustion amount command primary delay signal by following a change in the combustion amount command signal such that a predetermined time delay occurs when the combustion amount command signal changes, A high signal selector that selects the higher value of the combustion amount command primary delay signal and the combustion amount command signal output from the primary delay unit and outputs the selected value as a combustion amount command selection signal; A function generator for obtaining and outputting an exhaust gas flow rate based on a combustion amount command selection signal to be output, a proportional constant to the exhaust gas flow rate output from the function generator, and an inlet NOx and a molar ratio of a NOx detector detected by an inlet NOx meter. And a calculator for calculating and outputting a required ammonia injection amount. The denitrification ammonia injection amount control device for a coal-fired boiler.
JP22239996A 1996-08-23 1996-08-23 Denitration ammonia injection amount control method and apparatus for coal fired boiler Expired - Fee Related JP3911729B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22239996A JP3911729B2 (en) 1996-08-23 1996-08-23 Denitration ammonia injection amount control method and apparatus for coal fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22239996A JP3911729B2 (en) 1996-08-23 1996-08-23 Denitration ammonia injection amount control method and apparatus for coal fired boiler

Publications (2)

Publication Number Publication Date
JPH1057769A true JPH1057769A (en) 1998-03-03
JP3911729B2 JP3911729B2 (en) 2007-05-09

Family

ID=16781773

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5952515A (en) * 1982-09-21 1984-03-27 Babcock Hitachi Kk Method for controlling flow rate of ammonia in waste gas denitration apparatus
JPS5965729U (en) * 1982-10-27 1984-05-02 三菱重工業株式会社 Denitration equipment
JPS60216829A (en) * 1984-04-13 1985-10-30 Mitsubishi Heavy Ind Ltd Denitration apparatus
JPS6119290B2 (en) * 1978-12-01 1986-05-16 Hitachi Ltd
JPS6187519U (en) * 1984-11-15 1986-06-07
JPS62227426A (en) * 1986-03-31 1987-10-06 Babcock Hitachi Kk Ammonia pouring control device
JPH02251223A (en) * 1989-03-24 1990-10-09 Ishikawajima Harima Heavy Ind Co Ltd Controller of nox in exhaust gas
JPH02124556U (en) * 1989-03-27 1990-10-15
JPH0450119U (en) * 1990-08-30 1992-04-28
JPH07116461A (en) * 1993-10-22 1995-05-09 Ishikawajima Harima Heavy Ind Co Ltd Apparatus for controlling injection amount of ammonia into denitration reactor

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6119290B2 (en) * 1978-12-01 1986-05-16 Hitachi Ltd
JPS5952515A (en) * 1982-09-21 1984-03-27 Babcock Hitachi Kk Method for controlling flow rate of ammonia in waste gas denitration apparatus
JPS5965729U (en) * 1982-10-27 1984-05-02 三菱重工業株式会社 Denitration equipment
JPS60216829A (en) * 1984-04-13 1985-10-30 Mitsubishi Heavy Ind Ltd Denitration apparatus
JPS6187519U (en) * 1984-11-15 1986-06-07
JPS62227426A (en) * 1986-03-31 1987-10-06 Babcock Hitachi Kk Ammonia pouring control device
JPH02251223A (en) * 1989-03-24 1990-10-09 Ishikawajima Harima Heavy Ind Co Ltd Controller of nox in exhaust gas
JPH02124556U (en) * 1989-03-27 1990-10-15
JPH0450119U (en) * 1990-08-30 1992-04-28
JPH07116461A (en) * 1993-10-22 1995-05-09 Ishikawajima Harima Heavy Ind Co Ltd Apparatus for controlling injection amount of ammonia into denitration reactor

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