JP2000028123A - Secondary combustion control device of garbage incinerator - Google Patents
Secondary combustion control device of garbage incineratorInfo
- Publication number
- JP2000028123A JP2000028123A JP10192607A JP19260798A JP2000028123A JP 2000028123 A JP2000028123 A JP 2000028123A JP 10192607 A JP10192607 A JP 10192607A JP 19260798 A JP19260798 A JP 19260798A JP 2000028123 A JP2000028123 A JP 2000028123A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen concentration
- concentration
- secondary combustion
- exhaust gas
- combustion
- 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.)
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Links
Landscapes
- Incineration Of Waste (AREA)
Abstract
(57)【要約】
【課題】 二次燃焼制御における排ガスに含まれる一酸
化炭素濃度と窒素酸化物濃度を同時に低減すべく二次燃
焼後の排ガス含有酸素濃度を制御するための目標酸素濃
度を短時間に演算可能なゴミ焼却炉の二次燃焼制御装置
を提供する。
【解決手段】 ゴミ焼却炉40の燃焼状態に対応して変
化する所定のプロセスデータと二次燃焼後の排ガス含有
酸素濃度を入力データとし、当該燃焼状態において二次
燃焼後の排ガス含有窒素酸化物濃度及び一酸化炭素濃度
を出力データとする排ガス濃度模擬手段1と、その入力
データである酸素濃度を所定範囲内で変化させて、その
出力データである窒素酸化物濃度及び一酸化炭素濃度の
所定の評価値が最低となる酸素濃度を目標酸素濃度とし
て出力する目標酸素濃度設定手段2と、酸素濃度変化の
所定範囲をその制御範囲全体の一部として所定のプロセ
スデータの値に対応して設定する酸素濃度範囲設定手段
3とを備える。
(57) [Problem] To provide a target oxygen concentration for controlling the concentration of oxygen contained in exhaust gas after secondary combustion in order to simultaneously reduce the concentration of carbon monoxide and nitrogen oxide contained in exhaust gas in secondary combustion control. Provided is a secondary combustion control device for a refuse incinerator that can be operated in a short time. SOLUTION: Predetermined process data that changes according to the combustion state of a refuse incinerator 40 and oxygen concentration in exhaust gas after secondary combustion are input data, and nitrogen oxides in exhaust gas after secondary combustion in the combustion state. Exhaust gas concentration simulation means 1 using the concentration and the carbon monoxide concentration as output data, and changing the oxygen concentration as the input data within a predetermined range to determine the nitrogen oxide concentration and the carbon monoxide concentration as the output data. Target oxygen concentration setting means 2 for outputting the oxygen concentration with the lowest evaluation value as the target oxygen concentration, and setting a predetermined range of the oxygen concentration change as a part of the entire control range corresponding to the value of predetermined process data. And an oxygen concentration range setting means 3 for performing the operation.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、排ガス中の一酸化
炭素濃度、及び、窒素酸化物濃度の低減を図るゴミ焼却
炉の二次燃焼制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a secondary combustion control device for a refuse incinerator for reducing the concentration of carbon monoxide and the concentration of nitrogen oxides in exhaust gas.
【0002】[0002]
【従来の技術】従来より、ゴミ焼却炉の燃焼制御は、燃
焼状態に応じた適切な目標酸素濃度を設定し、その目標
酸素濃度を維持するように二次燃焼空気量を制御するこ
とで窒素酸化物及び一酸化炭素の発生を抑制している。
従って、ゴミ焼却炉の二次燃焼制御装置としては、装入
廃棄物を焼却処理する移動式火床を備えた火炉から排出
された燃焼排ガスを二次燃焼させる煙道上流に設けた二
次燃焼空気供給機構と、二次燃焼後の排ガス含有酸素濃
度を測定するガス検出機構と、前記ガス検出機構による
検出酸素濃度を前記目標酸素濃度に調整すべく前記二次
燃焼空気供給機構による空気供給量をPID制御する空
気供給量制御手段を備えて構成したものがある。また、
前記目標酸素濃度を決定する手段として、ゴミ焼却炉の
燃焼状態に対応して変化する所定のプロセスデータと前
記酸素濃度を入力データとし、当該燃焼状態において二
次燃焼後の排ガス含有窒素酸化物濃度及び一酸化炭素濃
度を出力データとする窒素酸化物及び一酸化炭素発生に
係るプロセスモデルを、ニューラルネットワーク等を利
用して実炉の実績データを学習させることによって作成
し、燃焼状態の変化に応じた適切な目標酸素濃度を設定
する方法として、特定の燃焼状態下において、そのとき
の前記所定のプロセスデータを前記プロセスモデルに入
力するとともに、残りの入力データである前記酸素濃度
を、例えば、厚生省の示す所定の基準値(6%以上)を
含む制御範囲(6%〜11%)内で変化させて、前記プ
ロセスモデルから出力される窒素酸化物濃度及び一酸化
炭素濃度を評価して、その所定の評価値が最低となる前
記酸素濃度を前記目標酸素濃度として設定していたもの
がある。2. Description of the Related Art Conventionally, the combustion control of a refuse incinerator has been carried out by setting an appropriate target oxygen concentration according to the combustion state and controlling the amount of secondary combustion air to maintain the target oxygen concentration. It suppresses the generation of oxides and carbon monoxide.
Therefore, as a secondary combustion control device of a garbage incinerator, a secondary combustion provided upstream of a flue for secondary combustion of flue gas discharged from a furnace having a movable grate for incineration of charged waste is provided. An air supply mechanism, a gas detection mechanism for measuring the oxygen concentration in the exhaust gas after the secondary combustion, and an air supply amount by the secondary combustion air supply mechanism to adjust the oxygen concentration detected by the gas detection mechanism to the target oxygen concentration. Is provided with an air supply amount control means for performing PID control on the air supply. Also,
As means for determining the target oxygen concentration, predetermined process data that changes in accordance with the combustion state of the refuse incinerator and the oxygen concentration are used as input data, and in the combustion state, the concentration of the nitrogen oxides in the exhaust gas after the secondary combustion. And a process model for nitrogen oxide and carbon monoxide generation using carbon monoxide concentration as output data by learning the actual data of actual furnaces using a neural network etc., and responding to changes in combustion conditions. As a method of setting an appropriate target oxygen concentration, under a specific combustion state, the predetermined process data at that time is input to the process model, and the oxygen concentration as the remaining input data is, for example, Is changed within a control range (6% to 11%) including a predetermined reference value (6% or more) indicated by Evaluating the force concentration of nitrogen oxides and carbon monoxide concentrations, there is the oxygen concentration evaluation value of the predetermined becomes minimum that has been set as the target oxygen concentration.
【0003】[0003]
【発明が解決しようとする課題】上記した従来のゴミ焼
却炉の二次燃焼制御装置の場合、前記目標酸素濃度を設
定する度に、前記酸素濃度を予め設定した制御範囲の全
範囲で変化させていたため、前記プロセスモデルの演算
処理に長時間を要し、前記目標酸素濃度をきめ細かく調
整するのが困難であるという問題があった。In the above-described conventional secondary combustion control device for a refuse incinerator, the oxygen concentration is changed over the entire range of the preset control range every time the target oxygen concentration is set. Therefore, there is a problem that it takes a long time to perform the arithmetic processing of the process model, and it is difficult to finely adjust the target oxygen concentration.
【0004】本発明は、かかる実情に鑑みてなされたも
のであり、その目的は、上述の問題点を解消し、二次燃
焼制御における排ガスに含まれる一酸化炭素濃度と窒素
酸化物濃度を同時に低減可能な目標酸素濃度を短時間の
演算処理で設定でき、きめ細かく且つ効率的に一酸化炭
素濃度と窒素酸化物濃度の制御が可能なゴミ焼却炉の二
次燃焼制御装置を提供する点にある。The present invention has been made in view of the above circumstances, and an object of the present invention is to solve the above-mentioned problems and to simultaneously reduce the concentration of carbon monoxide and the concentration of nitrogen oxide contained in exhaust gas in secondary combustion control. It is an object of the present invention to provide a secondary combustion control device for a refuse incinerator that can set a target oxygen concentration that can be reduced by a short-time calculation process and that can precisely and efficiently control a carbon monoxide concentration and a nitrogen oxide concentration. .
【0005】[0005]
【課題を解決するための手段】この目的を達成するため
の本発明に係るゴミ焼却炉の二次燃焼制御装置の第一の
特徴構成は、特許請求の範囲の欄の請求項1に記載した
通り、装入廃棄物を焼却処理する移動式火床を備えた火
炉から排出された燃焼排ガスを二次燃焼させる煙道上流
に設けた二次燃焼空気供給機構と、二次燃焼後の排ガス
含有酸素濃度を測定するガス検出機構と、前記ガス検出
機構による検出酸素濃度を目標酸素濃度に調整すべく前
記二次燃焼空気供給機構による空気供給量を制御する空
気供給量制御手段とを備えてなるゴミ焼却炉の二次燃焼
制御装置であって、前記ゴミ焼却炉の燃焼状態に対応し
て変化する所定のプロセスデータと前記酸素濃度を入力
データとし、当該燃焼状態において二次燃焼後の排ガス
含有窒素酸化物濃度及び一酸化炭素濃度を出力データと
する排ガス濃度模擬手段と、前記排ガス濃度模擬手段の
入力データである前記酸素濃度を所定範囲内で変化させ
て、前記排ガス濃度模擬手段の出力データである前記窒
素酸化物濃度及び前記一酸化炭素濃度の所定の評価値が
その所定範囲内で最低となる酸素濃度を前記目標酸素濃
度として出力する目標酸素濃度設定手段と、前記酸素濃
度変化の前記所定範囲をその制御範囲全体の一部として
前記所定のプロセスデータの値に対応して設定する酸素
濃度範囲設定手段とを備えてなる点にある。Means for Solving the Problems A first characteristic configuration of a secondary combustion control device for a refuse incinerator according to the present invention for achieving this object is described in claim 1 of the claims. As shown in the figure, a secondary combustion air supply mechanism installed upstream of the flue for secondary combustion of combustion exhaust gas discharged from a furnace equipped with a mobile grate for incineration of charged waste, and exhaust gas after secondary combustion A gas detection mechanism for measuring the oxygen concentration; and an air supply control means for controlling an air supply amount by the secondary combustion air supply mechanism to adjust the oxygen concentration detected by the gas detection mechanism to a target oxygen concentration. A secondary combustion control device for a refuse incinerator, wherein predetermined process data and the oxygen concentration that change in accordance with the combustion state of the refuse incinerator are input data, and the exhaust gas content after the secondary combustion in the combustion state is included. Nitrogen oxide concentration And an exhaust gas concentration simulating means having carbon monoxide concentration as output data; and the nitrogen being an output data of the exhaust gas concentration simulating means by changing the oxygen concentration which is input data of the exhaust gas concentration simulating means within a predetermined range. Target oxygen concentration setting means for outputting, as the target oxygen concentration, an oxygen concentration at which a predetermined evaluation value of the oxide concentration and the carbon monoxide concentration is the lowest within the predetermined range, and setting the predetermined range of the oxygen concentration change to An oxygen concentration range setting means for setting as a part of the entire control range in accordance with the value of the predetermined process data is provided.
【0006】同第二の特徴構成は、特許請求の範囲の欄
の請求項2に記載した如く、上記第一の特徴構成に加え
て、前記ゴミ焼却炉が前記火炉の出口部の排ガス温度を
検出する温度検出機構と、前記移動式火床の燃切位置を
検出する燃切位置検出機構とを備え、前記プロセスデー
タが、前記温度検出機構による検出温度と前記燃切位置
検出機構による検出燃切位置である点にある。[0006] The second characteristic configuration is that, in addition to the first characteristic configuration, the refuse incinerator controls the exhaust gas temperature at the outlet of the furnace as described in claim 2 of the claims. A temperature detection mechanism for detecting the temperature of the movable grate; and a burn-off position detection mechanism for detecting a burn-off position of the movable grate. It is at the point that is the cutting position.
【0007】同第三の特徴構成は、特許請求の範囲の欄
の請求項3に記載した如く、上記第一または第二の特徴
構成に加えて、前記ゴミ焼却炉の燃焼状態に応じて得ら
れる所定のプロセスデータを入力データとして当該燃焼
状態において二次燃焼後の排ガス含有窒素酸化物濃度及
び一酸化炭素濃度の両方が同時に低下する二次燃焼後の
排ガスに含まれる適正酸素濃度を演算出力する適正酸素
濃度演算手段を備え、前記酸素濃度範囲設定手段が、前
記適正酸素濃度演算手段が出力する適正酸素濃度を前記
所定範囲内に含むように、前記所定範囲を設定する点に
ある。[0007] The third characteristic configuration may be obtained according to the combustion state of the refuse incinerator in addition to the first or second characteristic configuration, as described in claim 3 of the claims. The calculated predetermined process data is used as input data to calculate and output the appropriate oxygen concentration contained in the exhaust gas after the secondary combustion in which both the nitrogen oxide concentration and the carbon monoxide concentration in the exhaust gas after the secondary combustion are simultaneously reduced in the combustion state. The oxygen concentration range setting means sets the predetermined range such that the appropriate oxygen concentration output by the appropriate oxygen concentration calculation means is included in the predetermined range.
【0008】同第四の特徴構成は、特許請求の範囲の欄
の請求項4に記載した如く、上記第三の特徴構成に加え
て、前記適正酸素濃度演算手段がファジィ推論モデルで
構成されている点にある。[0008] In a fourth feature configuration, in addition to the third feature configuration, the appropriate oxygen concentration calculating means is configured by a fuzzy inference model in addition to the third feature configuration. There is in the point.
【0009】以下に作用を説明する。上記第一の特徴構
成によれば、前記酸素濃度範囲設定手段が、前記所定範
囲として前記酸素濃度の制御範囲全体から前記所定のプ
ロセスデータに応じてそのときの燃焼状態に対応した目
標酸素濃度を含む部分的な酸素濃度範囲を設定するた
め、前記目標酸素濃度設定手段は前記酸素濃度を前記制
御範囲全体に比べて狭い範囲で変化させることになり、
前記目標酸素濃度を設定するまでに前記排ガス濃度模擬
手段及び前記目標酸素濃度設定手段の演算処理に要する
処理時間を短縮できるのである。この結果、燃焼状態の
変化に対して前記目標酸素濃度をきめ細かく追従させる
ことができ、排ガスに含まれる窒素酸化物濃度及び一酸
化炭素濃度の両方をより効果的に低減することができる
のである。The operation will be described below. According to the first characteristic configuration, the oxygen concentration range setting means sets the target oxygen concentration corresponding to the combustion state at that time according to the predetermined process data from the entire control range of the oxygen concentration as the predetermined range. In order to set a partial oxygen concentration range including, the target oxygen concentration setting means will change the oxygen concentration in a narrower range than the entire control range,
The processing time required for the arithmetic processing of the exhaust gas concentration simulating means and the target oxygen concentration setting means before setting the target oxygen concentration can be reduced. As a result, the target oxygen concentration can be made to closely follow the change in the combustion state, and both the nitrogen oxide concentration and the carbon monoxide concentration contained in the exhaust gas can be reduced more effectively.
【0010】ところで、既存のゴミ焼却炉における火炉
出口部の燃焼排ガス温度(炉出口温度ともいう)と、移
動式火床を構成する燃焼帯における燃切点のそれぞれに
対する、二次燃焼後の排ガス含有酸素濃度と一酸化炭素
濃度、窒素酸化物濃度の関係を調べると、以下の理由か
ら、一酸化炭素濃度と窒素酸化物濃度の同時低減のため
の適性な排ガス酸素濃度が、炉出口温度と燃切点に応じ
て変化することが判明する。つまり、同一燃切域に対し
て炉出口温度が高いときと低いときを調べると、図4に
示すように、炉出口温度の低いときは、炉出口温度の高
いときと比べて、一酸化炭素低減のための適性排ガス酸
素濃度域が全体的に狭くなるとともに上昇すること、同
一炉出口温度域に対して燃切点が上流側にあるときと下
流側にあるときを調べると、図5に示すように、燃切点
が上流側にあるときには、燃切点が下流側にあるときと
比べて一酸化炭素低減のための適性排ガス酸素濃度域下
限が上昇し、適性排ガス酸素濃度域全体が狭くなるこ
と、図4及び図5に示すように、窒素酸化物は、排ガス
酸素濃度と正の相関、一酸化炭素と負の相関にあり、排
ガス酸素濃度を低くするほど窒素酸化物濃度が低減する
ことによる。即ち、煙道における燃焼状態は、炉出口温
度条件、燃切位置の両条件と非線形な関係にあり、燃切
位置条件は火炉内における燃焼排ガスの攪拌混合条件を
示すもので、燃切点が上流側にあればそれだけ攪拌混合
が不十分であることが推測される。By the way, the exhaust gas after the secondary combustion with respect to each of the combustion exhaust gas temperature at the furnace outlet of the existing refuse incinerator (furnace outlet temperature) and the burn-off point in the combustion zone constituting the movable grate is also shown. Examining the relationship between the oxygen content, the carbon monoxide concentration, and the nitrogen oxide concentration, the appropriate exhaust gas oxygen concentration for simultaneous reduction of the carbon monoxide concentration and the nitrogen oxide concentration depends on the furnace outlet temperature and It turns out that it changes according to the burn-off point. That is, when the furnace outlet temperature is high and when the furnace outlet temperature is low for the same burn-off area, as shown in FIG. 4, the carbon monoxide is lower when the furnace outlet temperature is lower than when the furnace outlet temperature is higher. Fig. 5 shows that the appropriate exhaust gas oxygen concentration range for reduction becomes narrower and higher as a whole, and that the burn-off point is on the upstream side and the downstream side with respect to the same furnace outlet temperature range. As shown, when the burn-off point is on the upstream side, the lower limit of the suitable exhaust gas oxygen concentration range for reducing carbon monoxide is higher than when the burn-off point is on the downstream side, and the entire suitable exhaust gas oxygen concentration range is As shown in FIGS. 4 and 5, the nitrogen oxides have a positive correlation with the exhaust gas oxygen concentration and a negative correlation with the carbon monoxide. The lower the exhaust gas oxygen concentration, the lower the nitrogen oxide concentration. By doing. That is, the combustion state in the flue has a non-linear relationship with both the furnace exit temperature condition and the burn-off position condition, and the burn-off position condition indicates the stirring and mixing conditions of the combustion exhaust gas in the furnace. It is presumed that the stirring and mixing are inadequate for the upstream side.
【0011】従って、上記第二の特徴構成によれば、前
記排ガス濃度模擬手段の入力データとして炉出口温度、
燃切点を使用するため、一酸化炭素濃度と窒素酸化物濃
度を同時且つ効果的に低下する二次燃焼制御が可能とな
る。この場合において、入力データに炉出口温度を取り
入れることにより、二次燃焼の重要条件である二次燃焼
エリアでの滞留時間(燃焼時間に相当)・燃焼温度・攪
拌混合のうちの燃焼温度条件が加味され、入力データに
燃切点を取り入れることにより、攪拌混合条件が加味さ
れるのである。ここに、燃切点を取り入れることの意義
は、二次燃焼エリアよりも上流側の火炉内部における燃
焼排ガスの攪拌混合条件が加味される点にあり、これに
より適切な、つまり、より少量の二次燃焼空気量で、一
酸化炭素濃度と窒素酸化物濃度を同時に低減することが
可能になるのである。尚、上述の滞留時間条件は、二次
燃焼エリアの炉形状という設計配慮により向上しうるも
のである。Therefore, according to the second characteristic configuration, the furnace exit temperature, the furnace outlet temperature,
Since the burn-off point is used, it is possible to perform secondary combustion control in which the concentrations of carbon monoxide and nitrogen oxide are simultaneously and effectively reduced. In this case, by incorporating the furnace outlet temperature into the input data, the combustion temperature conditions of the residence time (corresponding to the combustion time) in the secondary combustion area, the combustion temperature, and the stirring and mixing, which are the important conditions of the secondary combustion, are obtained. The stirring and mixing conditions are taken into account by incorporating the burn-off point into the input data. The significance of introducing the burn-off point here is that the stirring and mixing conditions of the combustion exhaust gas inside the furnace upstream of the secondary combustion area are taken into consideration, and this makes it appropriate, that is, a smaller amount of fuel gas is used. It is possible to simultaneously reduce the concentration of carbon monoxide and the concentration of nitrogen oxide by the amount of the next combustion air. The above residence time condition can be improved by design consideration of the furnace shape of the secondary combustion area.
【0012】また、上記第三の特徴構成によれば、前記
適正酸素濃度演算手段が前記所定のプロセスデータで特
定される燃焼状態下における前記窒素酸化物濃度と前記
一酸化炭素濃度の両方を同時に低減可能な適正酸素濃度
を求め、その適正酸素濃度を直接に前記目標酸素濃度と
はせずに、その適正酸素濃度を含むように前記所定範囲
を設定することで、その設定範囲を狭く維持しながらも
前記目標酸素濃度を確実にその範囲内に得られるのであ
る。また、前記適正酸素濃度演算手段が演算した前記適
正酸素濃度を直接に前記目標酸素濃度とする場合は、前
記適正酸素濃度を高速且つ高精度に演算処理可能に前記
適正酸素濃度演算手段を構成する必要があるが、本特徴
構成によれば、前記適正酸素濃度演算手段の演算精度を
単独で使用する場合に比べ低く設定できるのである。Further, according to the third characteristic configuration, the appropriate oxygen concentration calculating means simultaneously determines both the nitrogen oxide concentration and the carbon monoxide concentration under a combustion state specified by the predetermined process data. A suitable oxygen concentration that can be reduced is determined, and the predetermined range is set so as to include the appropriate oxygen concentration without directly setting the appropriate oxygen concentration as the target oxygen concentration. However, the target oxygen concentration can be reliably obtained within the range. In the case where the appropriate oxygen concentration calculated by the appropriate oxygen concentration calculating means is directly used as the target oxygen concentration, the appropriate oxygen concentration calculating means is configured so that the appropriate oxygen concentration can be processed at high speed and with high accuracy. Although it is necessary, according to this characteristic configuration, the calculation accuracy of the appropriate oxygen concentration calculation means can be set lower than when used alone.
【0013】上記第四の特徴構成によれば、一酸化炭素
濃度と窒素酸化物濃度が共に適性なときの炉出口温度、
燃切点等の前記所定のプロセスデータと排ガス酸素濃度
の関係が非線形であるため、非線形なモデリングに有効
なファジィ推論を前記適正酸素濃度演算手段に使うこと
により、前記所定のプロセスデータに対応する適性な排
ガス酸素濃度を容易に推定できるのである。According to the fourth feature, the furnace outlet temperature when both the concentration of carbon monoxide and the concentration of nitrogen oxide are appropriate,
Since the relationship between the predetermined process data such as the burn-off point and the exhaust gas oxygen concentration is non-linear, the fuzzy inference effective for non-linear modeling is used for the appropriate oxygen concentration calculation means to correspond to the predetermined process data. An appropriate exhaust gas oxygen concentration can be easily estimated.
【0014】[0014]
【発明の効果】以上説明したように、本発明に係るゴミ
焼却炉の二次燃焼制御装置によれば、二次燃焼制御にお
ける目標酸素濃度の設定が高速且つ高精度に処理できる
ため、制御可能な範囲を広くでき、且つ、排ガスに含ま
れる一酸化炭素濃度、及び、窒素酸化物濃度の効果的な
低減が可能な、周辺環境保護に極めて優れたゴミ焼却炉
を実現できるとともに、種々の排ガス処理装置の大型化
を回避して設備費の高騰を防止しうるという優れた効果
を発揮するものである。As described above, according to the secondary combustion control system for a refuse incinerator according to the present invention, the setting of the target oxygen concentration in the secondary combustion control can be performed at high speed and with high accuracy, so that control is possible. Garbage incinerator, which can greatly reduce the carbon monoxide concentration and the concentration of nitrogen oxides contained in the exhaust gas, and which is extremely excellent in environmental protection. The present invention has an excellent effect that it is possible to prevent the processing equipment from increasing in size and to prevent a rise in equipment costs.
【0015】[0015]
【発明の実施の形態】以下に本発明の実施の形態を図面
に基づいて説明する。図1に示すように、ゴミ焼却炉
(プラント)40は、多段に配置されたストーカの前後
移動によりゴミを搬送しながら燃焼させる移動式火床1
4を備えた火炉30と、前記火炉30から排出された燃
焼排ガスを二次燃焼させる煙道31と、前記煙道31か
らの排ガス保有熱で蒸気を生成する廃熱ボイラ17とを
備え、前記ボイラ17を通過した排ガスを排ガス処理装
置18で浄化処理した後、煙突から排気するように構成
してあり、ゴミピット10に集積され、クレーン装置1
1で搬送された都市ゴミはゴミホッパ12に投入され、
前記ゴミホッパ12の下部に設けた給塵装置13で前記
火炉30に装入される。前記移動式火床14に供給され
たゴミは、下方及び側壁から供給される一次燃焼空気に
より、上流側から乾燥・ガス化・ガス燃焼・固体燃焼に
各過程を経て灰ピットに搬送され、主に乾燥・ガス化さ
れる火床が乾燥帯、主にガス燃焼から固体燃焼される火
床が燃焼帯、主に固体燃焼から灰化される火床が後燃焼
帯となる。前記火炉30で生じた燃焼排ガス中の一酸化
炭素等の未燃焼有害物質を完全燃焼させるために二次燃
焼空気を供給する二次燃焼空気供給機構16、つまり、
二次燃焼空気供給ノズルと該ノズルへの空気供給量を調
節するダンパ機構を備えた供給管を、前記煙道31上流
の火炉出口部に設けてある。尚、設備内で消費する電力
は、ガスタービン発電機20と、前記廃熱ボイラ17で
生成された蒸気が供給される蒸気タービン発電機19を
備えたコンバインド発電システムで賄われる。Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, a garbage incinerator (plant) 40 is a movable grate 1 that burns while transporting garbage by moving stokers arranged in multiple stages back and forth.
A furnace 30 provided with an exhaust gas 4, a flue 31 for secondary combustion of the combustion exhaust gas discharged from the furnace 30, and a waste heat boiler 17 for generating steam by using heat retained by the exhaust gas from the flue 31, The exhaust gas passing through the boiler 17 is purified by an exhaust gas treatment device 18 and then exhausted from a chimney.
The municipal garbage transported in 1 is thrown into the garbage hopper 12,
The dust is supplied to the furnace 30 by a dust supply device 13 provided below the dust hopper 12. The refuse supplied to the movable grate 14 is conveyed from the upstream side to the ash pit via primary combustion air supplied from below and from the side wall, through drying, gasification, gas combustion, and solid combustion. The grate that is dried and gasified is a dry zone, the grate that is mainly solid-fired from gas combustion is the combustion zone, and the grate that is mainly incinerated from solid combustion is the post-combustion zone. A secondary combustion air supply mechanism 16 for supplying secondary combustion air to completely burn unburned harmful substances such as carbon monoxide in the combustion exhaust gas generated in the furnace 30;
A supply pipe having a secondary combustion air supply nozzle and a damper mechanism for adjusting the amount of air supplied to the nozzle is provided at the furnace outlet upstream of the flue 31. The power consumed in the facility is provided by a combined power generation system including a gas turbine generator 20 and a steam turbine generator 19 to which steam generated by the waste heat boiler 17 is supplied.
【0016】図1及び図2に示すように、二次燃焼制御
装置は、前記煙道31の上流に設けた二次燃焼空気供給
機構16と、二次燃焼後の排ガス含有酸素濃度を測定す
るガス検出機構34と、前記ガス検出機構34による検
出酸素濃度を目標酸素濃度に調整すべく前記二次燃焼空
気供給機構16による空気供給量を制御する空気供給量
制御手段6を備えて構成してある。As shown in FIGS. 1 and 2, the secondary combustion control device measures the secondary combustion air supply mechanism 16 provided upstream of the flue 31 and the concentration of oxygen contained in exhaust gas after secondary combustion. A gas detection mechanism, and air supply amount control means 6 for controlling an air supply amount by the secondary combustion air supply mechanism 16 so as to adjust the oxygen concentration detected by the gas detection mechanism to a target oxygen concentration. is there.
【0017】前記空気供給量制御手段6は、前記ゴミ焼
却炉40の燃焼状態に対応して変化する所定のプロセス
データと酸素濃度を入力データとし、当該燃焼状態にお
いて二次燃焼後の排ガス含有窒素酸化物濃度及び一酸化
炭素濃度を出力データとする排ガス濃度模擬手段1と、
前記排ガス濃度模擬手段1の入力データである前記酸素
濃度を所定範囲内で変化させて、前記排ガス濃度模擬手
段1の出力データである前記窒素酸化物濃度及び前記一
酸化炭素濃度の所定の評価値がその所定範囲内で最低と
なる酸素濃度を前記目標酸素濃度として出力する目標酸
素濃度設定手段2と、前記所定のプロセスデータを入力
データとして当該燃焼状態において前記窒素酸化物濃度
と前記一酸化炭素濃度の両方が同時に低下するときの適
正酸素濃度を演算する適正酸素濃度演算手段4と、前記
適正酸素濃度演算手段4が出力する適正酸素濃度を前記
所定範囲内に含むように、前記所定範囲を前記酸素濃度
の制御範囲全体の一部として、前記所定のプロセスデー
タの値に対応して設定する酸素濃度範囲設定手段3と、
前記検出酸素濃度を前記目標酸素濃度に調整すべく前記
二次燃焼空気供給機構16による空気供給量を制御(つ
まり、前記ダンパの開度を調節)するPID制御部5と
で構成されている。The air supply amount control means 6 uses predetermined process data and oxygen concentration, which change in accordance with the combustion state of the refuse incinerator 40, as input data. Exhaust gas concentration simulation means 1 using the oxide concentration and the carbon monoxide concentration as output data;
A predetermined evaluation value of the nitrogen oxide concentration and the carbon monoxide concentration which are output data of the exhaust gas concentration simulating means 1 by changing the oxygen concentration which is input data of the exhaust gas concentration simulating means 1 within a predetermined range. A target oxygen concentration setting means 2 for outputting the lowest oxygen concentration within the predetermined range as the target oxygen concentration, and the nitrogen oxide concentration and the carbon monoxide in the combustion state using the predetermined process data as input data. The appropriate oxygen concentration calculating means 4 for calculating the appropriate oxygen concentration when both of the concentrations are simultaneously reduced, and the predetermined range is set so that the appropriate oxygen concentration output by the appropriate oxygen concentration calculating means 4 is included in the predetermined range. An oxygen concentration range setting means 3 that is set as a part of the entire oxygen concentration control range in accordance with the value of the predetermined process data;
The PID control unit 5 controls the air supply amount by the secondary combustion air supply mechanism 16 (that is, adjusts the opening degree of the damper) to adjust the detected oxygen concentration to the target oxygen concentration.
【0018】前記排ガス濃度模擬手段1及び前記適正酸
素濃度演算手段4の入力データである前記所定のプロセ
スデータとしては、前記火炉30の出口部の排ガス温度
(以下、炉出口温度という。)と前記移動式火床14の
燃切位置を採用する。このため、前記炉出口温度を検出
する温度検出機構33が前記出口部に設けられており、
また、前記移動式火床14の燃切位置を検出する燃切位
置検出機構32が、前記火炉30の後方側壁から前記移
動式火床14を臨むように設置された産業用テレビカメ
ラと、該カメラで撮影された燃焼火炎を画像処理して、
ガス燃焼から固体燃焼へ移行する位置を燃切点として抽
出する画像処理手段と、前記燃焼帯の最上流位置から最
下流位置までの間のどの位置に在るかを0%から100
%の数値で出力する演算手段とで構成してある。The predetermined process data as input data of the exhaust gas concentration simulating means 1 and the appropriate oxygen concentration calculating means 4 include an exhaust gas temperature at the outlet of the furnace 30 (hereinafter referred to as a furnace outlet temperature) and the furnace exhaust gas temperature. The burn-off position of the movable grate 14 is adopted. Therefore, a temperature detection mechanism 33 for detecting the furnace outlet temperature is provided at the outlet portion,
Further, an industrial television camera provided with a burn-off position detecting mechanism 32 for detecting a burn-off position of the movable grate 14 facing the movable grate 14 from the rear side wall of the furnace 30; Image processing of the burning flame taken by the camera,
Image processing means for extracting a position at which gas combustion shifts to solid combustion as a burn-off point; and 0% to 100% of a position between the most upstream position and the most downstream position of the combustion zone.
And an arithmetic means for outputting a numerical value of%.
【0019】次に、前記空気供給量制御手段6の各部の
動作について説明する。前記適正酸素濃度演算手段4
は、前記炉出口温度と前記燃切位置を入力データとして
前記適正酸素濃度を逐次演算する。前記酸素濃度範囲設
定手段3は、その適正酸素濃度が入力されると、例え
ば、その適正酸素濃度を中心として±1%を、前記排ガ
ス濃度模擬手段1の入力データとして変化させるための
酸素濃度範囲として出力する。前記目標酸素濃度設定手
段2は、前記酸素濃度範囲設定手段3が設定した前記酸
素濃度範囲に基づいて、その最小値から最大値まで所定
の刻み幅で前記排ガス濃度模擬手段1に対して酸素濃度
を出力し、前記酸素濃度範囲設定手段3はその各酸素濃
度が入力される毎に、別に入力された前記炉出口温度と
前記燃切位置と予め設定された演算アルゴリズムに従っ
て、当該条件下での前記窒素酸化物濃度及び前記一酸化
炭素濃度を演算し、逐次その結果を前記目標酸素濃度設
定手段2に出力する。前記目標酸素濃度設定手段2は前
記各酸素濃度毎の前記窒素酸化物濃度及び前記一酸化炭
素濃度を受信すると、それらの所定の評価値(例えば、
単純平均値或いは加重平均値)を前記各酸素濃度毎に算
出し、その内の最小値を与える酸素濃度を前記目標酸素
濃度として前記PID制御部5へ出力する。前記PID
制御部5は、周知のPID制御により前記ガス検出機構
34で検出される前記検出酸素濃度を前記目標酸素濃度
に調整すべく前記二次燃焼空気供給機構16による空気
供給量を制御する。本実施形態では、前記目標酸素濃度
を演算するために必要な前記排ガス濃度模擬手段1の演
算回数が、前記酸素濃度の変化幅に比例するため、前記
排ガス濃度模擬手段1の演算時間は、例えば、前記酸素
濃度の変化幅を6%〜11%としていた従来例と比較し
て2.5倍の改善が図れることになる。Next, the operation of each part of the air supply amount control means 6 will be described. The appropriate oxygen concentration calculating means 4
Calculates the appropriate oxygen concentration sequentially using the furnace outlet temperature and the burn-off position as input data. When the appropriate oxygen concentration is input, the oxygen concentration range setting means 3 sets an oxygen concentration range for changing ± 1% around the appropriate oxygen concentration as input data of the exhaust gas concentration simulation means 1, for example. Output as Based on the oxygen concentration range set by the oxygen concentration range setting means 3, the target oxygen concentration setting means 2 sends an oxygen concentration to the exhaust gas concentration simulating means 1 at a predetermined interval from a minimum value to a maximum value. The oxygen concentration range setting means 3 outputs the oxygen concentration range setting means 3 under the conditions according to the furnace exit temperature and the burn-off position which are separately inputted and the preset operation algorithm every time the oxygen concentration is inputted. The nitrogen oxide concentration and the carbon monoxide concentration are calculated, and the results are sequentially output to the target oxygen concentration setting means 2. When the target oxygen concentration setting means 2 receives the nitrogen oxide concentration and the carbon monoxide concentration for each of the oxygen concentrations, the target oxygen concentration setting means 2 sets a predetermined evaluation value (for example,
A simple average value or a weighted average value) is calculated for each of the oxygen concentrations, and the oxygen concentration giving the minimum value is output to the PID control unit 5 as the target oxygen concentration. The PID
The controller 5 controls the amount of air supplied by the secondary combustion air supply mechanism 16 to adjust the detected oxygen concentration detected by the gas detection mechanism 34 to the target oxygen concentration by well-known PID control. In the present embodiment, the number of calculations of the exhaust gas concentration simulation means 1 required to calculate the target oxygen concentration is proportional to the width of change of the oxygen concentration. Thus, an improvement of 2.5 times can be achieved as compared with the conventional example in which the variation range of the oxygen concentration is 6% to 11%.
【0020】前記目標酸素濃度設定手段2と前記酸素濃
度範囲設定手段3の演算処理は、簡単な演算処理である
ため、前記排ガス濃度模擬手段1の演算処理時間と比較
して演算時間の増大は無視できる範囲である。また、前
記適正酸素濃度演算手段4が演算する適正酸素濃度に対
する演算精度が酸素濃度換算で±1%以内であれば、前
記排ガス濃度模擬手段1及び前記目標酸素濃度設定手段
2によって最終的な目標酸素濃度が演算され、正確な目
標酸素濃度を得ることができるため、この演算精度をあ
る程度犠牲にして前記適正酸素濃度演算手段4の演算時
間を短縮することができ、前記排ガス濃度模擬手段1の
演算時間に対して大幅な演算時間の増大とはならず、前
記最終的な目標酸素濃度演算までの総演算時間の短縮が
図れるのである。Since the arithmetic processing of the target oxygen concentration setting means 2 and the oxygen concentration range setting means 3 is a simple arithmetic processing, an increase in the arithmetic processing time as compared with the arithmetic processing time of the exhaust gas concentration simulating means 1 is not considered. It can be ignored. If the calculation accuracy of the appropriate oxygen concentration calculated by the appropriate oxygen concentration calculation means 4 is within ± 1% in terms of oxygen concentration, the final target concentration is set by the exhaust gas concentration simulation means 1 and the target oxygen concentration setting means 2. Since the oxygen concentration is calculated and an accurate target oxygen concentration can be obtained, the calculation time of the appropriate oxygen concentration calculating means 4 can be shortened by sacrificing the calculation accuracy to some extent, and the exhaust gas concentration simulating means 1 can be reduced. The calculation time does not increase significantly with respect to the calculation time, and the total calculation time until the final target oxygen concentration calculation can be reduced.
【0021】ところで、前記排ガス濃度模擬手段1は、
前記炉出口温度と前記燃切位置と前記酸素濃度を入力変
数とするプロセスモデルをコンピュータ演算処理する構
成とすればよいが、本実施形態では、前記プロセスモデ
ルを公知のニューラルネットワークで構成している。こ
れにより、複雑なプロセスに対する高精度なプロセスモ
デルを、前記ニューラルネットワークの学習によって自
動生成することができる。Incidentally, the exhaust gas concentration simulating means 1 comprises:
The process model using the furnace outlet temperature, the burn-off position, and the oxygen concentration as input variables may be configured to be processed by a computer, but in the present embodiment, the process model is configured by a known neural network. . Thereby, a highly accurate process model for a complicated process can be automatically generated by learning the neural network.
【0022】また、前記適正酸素濃度演算手段4は、前
記炉出口温度と前記燃切位置を入力データとし、所定の
ファジィルールに基づいて推論処理して二次燃焼後の適
正な排ガス含有酸素濃度を出力データとして出力するよ
うに構成してある。より詳しくは、図3に示すように、
炉出口温度と燃切点を前件部とし、目標酸素濃度を後件
部とする複数のファジィルール22と、前記ファジィル
ール22に従って所要の目標酸素濃度を演算導出するフ
ァジィ推論手段21とで構成してあり、前記ファジィル
ール22を、実炉の所要の燃焼条件を満足した前記入出
力データを教師信号とするニューロ的学習により自動的
にチューニングする自動調整機構23を備えて構成して
ある。The appropriate oxygen concentration calculating means 4 uses the furnace outlet temperature and the burn-out position as input data, performs inference processing based on a predetermined fuzzy rule, and performs an appropriate exhaust gas-containing oxygen concentration after secondary combustion. Is output as output data. More specifically, as shown in FIG.
A plurality of fuzzy rules 22 having a furnace outlet temperature and a burn-off point as antecedents and a target oxygen concentration as a consequent, and fuzzy inference means 21 for calculating and deriving a required target oxygen concentration in accordance with the fuzzy rules 22. The fuzzy rule 22 is provided with an automatic adjustment mechanism 23 that automatically tunes by a neural learning using the input / output data satisfying the required combustion conditions of the actual furnace as a teacher signal.
【0023】前記ファジィルール22は、ルールの出力
が入力変数の一次式で表される高木・菅野の方式を採用
する。つまり、入力ファジィ変数をx1 (炉出口温度;
『高い』『適性』『低い』の3段階),x2 (燃切点;
『上流』『適性』『下流』の3段階)とし、出力をy
(目標酸素濃度)とすれば、ルールは数1に示す一連の
演算式で表される。但し、ωi1,i2 は数2で表され、A
i1,1,Ai2,2は前件部のメンバシップ関数であり、数3
に示すシグモイド関数で表される。The fuzzy rule 22 employs the Takagi-Sugeno method in which the output of the rule is represented by a linear expression of an input variable. That is, the input fuzzy variable is x 1 (furnace outlet temperature;
3 levels of “High”, “Aptitude” and “Low”), x 2 (Burning point;
"Upstream", "Aptitude", "Downstream") and output y
Assuming (target oxygen concentration), the rule is represented by a series of arithmetic expressions shown in Expression 1. Here, ω i1 and i2 are expressed by Expression 2, and A
i1,1 and A i2,2 are membership functions of the antecedent part.
It is represented by the sigmoid function shown in
【0024】[0024]
【数1】if x1 =Ai1,1 & x2 =Ai2,2 th
en y=ωi1,i2 ## EQU1 ## if x 1 = A i1,1 & x 2 = A i2,2 th
en y = ω i1, i2
【数2】ωi1,i2 =ai1,i2 ・x1 +bi1,i2 ・x2 +
ci1,i2 ;i=1,……,nΩ i1, i2 = a i1, i2 × 1 + b i1, i2 × 2 +
c i1, i2 ; i = 1,..., n
【数3】 Aij(x)=1/(1+exp(−a(x−b)))A ij (x) = 1 / (1 + exp (−a (x−b)))
【0025】そして、最終的にファジィ推論手段21に
より、前記ファジィ推論出力y* は、数4によって求め
られる。但し、μi1,i2 は数5で表される前件部の適合
度である。Finally, the fuzzy inference means 21 obtains the fuzzy inference output y * by the following equation (4). Here, μ i1 and i2 are the degrees of conformity of the antecedent part expressed by Expression 5.
【数4】y* =Σ(μi1,i2 ・ωi1,i2 )/Σμi1,i2 [Equation 4] y * = Σ (μ i1, i2 · ω i1, i2 ) / Σμ i1, i2
【数5】μi1,i2 =Ai1,1(x1 )・Ai2,2(x2 )## EQU5 ## μ i1, i2 = A i1,1 (x 1 ) · A i2,2 (x 2 )
【0026】図3に示すように、前記自動調整機構23
は、後述の基準で決定された炉出口温度と燃切点でなる
入力教師信号24を前記ファジィ推論手段21に入力し
て得られた目標酸素濃度y* と、同じく後述の基準で決
定された酸素濃度yr でなる出力教師信号25との誤差
を表す数6に示す評価関数Eを、ニューロ的学習、つま
り、例えば、最急降下法を用いてメンバシップ関数とル
ール後件部のパラメータa,b,cを調整演算するもの
である。As shown in FIG. 3, the automatic adjustment mechanism 23
Is a target oxygen concentration y * obtained by inputting an input teacher signal 24 consisting of a furnace outlet temperature and a burn-off point determined on the basis described later to the fuzzy inference means 21, and also determined on the basis described later. The evaluation function E shown in Expression 6 representing the error from the output teacher signal 25 consisting of the oxygen concentration y r is represented by a neural learning, that is, a membership function and a parameter a, b and c are adjusted and calculated.
【0027】[0027]
【数6】E=1/2・(y* −yr )2 [6] E = 1/2 · (y * -y r) 2
【0028】即ち、3次元の入力データ(x1 ,x2 ,
yr )が与えられる毎にa,b,cについての偏微分演
算によりEの最急降下ベクトルを求め、その値がゼロと
なるように繰り返すのである。この方法は、一般的なバ
ックプロパゲーション方式ニューラルネットの学習方法
と同様である。That is, three-dimensional input data (x 1 , x 2 ,
Every time y r ) is given, the steepest descent vector of E is obtained by partial differential operation on a, b, and c, and the calculation is repeated so that the value becomes zero. This method is the same as a general back propagation neural network learning method.
【0029】以下に、別実施形態を説明する。 〈1〉上記の実施形態では、前記排ガス濃度模擬手段1
及び前記適正酸素濃度演算手段4の入力データである前
記所定のプロセスデータとして、前記炉出口温度と前記
燃切位置を採用したが、他のプロセスデータを使用して
も構わない。また、前記炉出口温度と前記燃切位置に対
して排ガス総流量に対する二次燃焼空気流量比率を入力
データに加えて、二次燃焼後の排ガス含有酸素濃度を出
力するように構成することにより、より適切な二次燃焼
空気供給制御が可能となる。例えば、破砕ゴミ等のよう
に燃えやすいゴミの場合、火床下部より供給する一次燃
焼空気を絞りながら焼却処理する場合があるが、この場
合、一酸化炭素濃度が上昇し易くなる。炉出口温度と燃
切点が等しくとも、一次燃焼空気の供給量によっては一
酸化炭素濃度の発生程度が異なるため、二次燃焼空気流
量比率を入力データに加えることにより、ゴミ質の変動
に対しても効果的な制御が可能になるのである。Hereinafter, another embodiment will be described. <1> In the above embodiment, the exhaust gas concentration simulation means 1
The furnace outlet temperature and the burn-off position are adopted as the predetermined process data as input data of the appropriate oxygen concentration calculating means 4, but other process data may be used. Further, by adding the ratio of the secondary combustion air flow rate to the total exhaust gas flow rate for the furnace outlet temperature and the burn-off position to the total exhaust gas flow rate to the input data, to output the exhaust gas-containing oxygen concentration after the secondary combustion, More appropriate secondary combustion air supply control becomes possible. For example, in the case of flammable garbage such as crushed garbage, incineration may be performed while squeezing the primary combustion air supplied from the lower part of the grate, in which case the concentration of carbon monoxide tends to increase. Even if the furnace outlet temperature and burn-out point are equal, the degree of carbon monoxide concentration varies depending on the supply amount of primary combustion air, so by adding the secondary combustion air flow rate ratio to the input data, Even so, effective control becomes possible.
【0030】〈2〉前記排ガス濃度模擬手段1の前記プ
ロセスモデルは必ずしもニューラルネットワークで構成
されていなくても、前記所定のプロセスデータを入力変
数とする一般的な状態方程式等で表した数式モデルであ
っても構わない。また、前記適正酸素濃度演算手段4の
前記ファジィルール22は、ファジィルール出力が実数
値とする簡略化ファジィ推論であってもよく、マムダニ
の方式を採用するものであってもよい。また、前記ファ
ジィルール22は必ずしもニューロ的学習により自動的
にチューニングするものでなくてもよい。<2> Even though the process model of the exhaust gas concentration simulating means 1 is not necessarily configured by a neural network, it is a mathematical model expressed by a general state equation using the predetermined process data as an input variable. It does not matter. Further, the fuzzy rule 22 of the appropriate oxygen concentration calculating means 4 may be a simplified fuzzy inference in which the fuzzy rule output is a real value, or may adopt a mamdani method. Further, the fuzzy rule 22 does not necessarily have to be automatically tuned by neuro-learning.
【図1】ゴミ焼却炉のブロック構成図FIG. 1 is a block diagram of a refuse incinerator.
【図2】ゴミ焼却炉の二次燃焼制御装置のブロック構成
図FIG. 2 is a block diagram of a secondary combustion control device of the refuse incinerator.
【図3】ファジィ推論部のブロック構成図FIG. 3 is a block diagram of a fuzzy inference unit.
【図4】燃切点一定で炉出口温度が変化したときの排ガ
スO2濃度に対するCO,NOx濃度の特性図FIG. 4 is a characteristic diagram of CO and NOx concentrations with respect to exhaust gas O 2 concentration when the furnace outlet temperature changes at a constant burn-off point.
【図5】炉出口温度一定で燃切点が変化したときの排ガ
スO2濃度に対するCO,NOx濃度の特性図FIG. 5 is a characteristic diagram of the CO and NOx concentrations with respect to the exhaust gas O 2 concentration when the burn-out point changes at a constant furnace outlet temperature.
1 排ガス濃度模擬手段 2 目標酸素濃度設定手段 3 酸素濃度範囲設定手段 4 適正酸素濃度演算手段 5 PID制御部 6 空気供給量制御手段 16 二次燃焼空気供給機構 30 火炉 31 煙道 32 燃切位置検出機構 33 温度検出機構 34 ガス検出機構 40 ゴミ焼却炉(プラント) DESCRIPTION OF SYMBOLS 1 Exhaust gas concentration simulation means 2 Target oxygen concentration setting means 3 Oxygen concentration range setting means 4 Appropriate oxygen concentration calculation means 5 PID control unit 6 Air supply amount control means 16 Secondary combustion air supply mechanism 30 Furnace 31 Stack 32 Detection of burn-off position Mechanism 33 Temperature detection mechanism 34 Gas detection mechanism 40 Garbage incinerator (plant)
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3K062 AA02 AB01 AC01 AC19 BA02 CA01 CB08 DA01 DA22 DA23 DA25 DA40 DB08 3K078 AA06 BA03 BA22 BA24 CA03 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 3K062 AA02 AB01 AC01 AC19 BA02 CA01 CB08 DA01 DA22 DA23 DA25 DA40 DB08 3K078 AA06 BA03 BA22 BA24 CA03
Claims (4)
備えた火炉から排出された燃焼排ガスを二次燃焼させる
煙道上流に設けた二次燃焼空気供給機構と、二次燃焼後
の排ガス含有酸素濃度を測定するガス検出機構と、前記
ガス検出機構による検出酸素濃度を目標酸素濃度に調整
すべく前記二次燃焼空気供給機構による空気供給量を制
御する空気供給量制御手段とを備えてなるゴミ焼却炉の
二次燃焼制御装置であって、 前記ゴミ焼却炉の燃焼状態に対応して変化する所定のプ
ロセスデータと前記酸素濃度を入力データとし、当該燃
焼状態において二次燃焼後の排ガス含有窒素酸化物濃度
及び一酸化炭素濃度を出力データとする排ガス濃度模擬
手段と、 前記排ガス濃度模擬手段の入力データである前記酸素濃
度を所定範囲内で変化させて、前記排ガス濃度模擬手段
の出力データである前記窒素酸化物濃度及び前記一酸化
炭素濃度の所定の評価値がその所定範囲内で最低となる
酸素濃度を前記目標酸素濃度として出力する目標酸素濃
度設定手段と、 前記酸素濃度変化の前記所定範囲をその制御範囲全体の
一部として前記所定のプロセスデータの値に対応して設
定する酸素濃度範囲設定手段とを、備えてなるゴミ焼却
炉の二次燃焼制御装置。1. A secondary combustion air supply mechanism provided upstream of a flue for secondary combustion of combustion exhaust gas discharged from a furnace provided with a movable grate for incinerating charged waste, and after secondary combustion. A gas detection mechanism for measuring the concentration of oxygen contained in the exhaust gas, and air supply amount control means for controlling an air supply amount by the secondary combustion air supply mechanism to adjust the oxygen concentration detected by the gas detection mechanism to a target oxygen concentration. A secondary combustion control device for a refuse incinerator, comprising: predetermined process data that changes in accordance with the combustion state of the refuse incinerator and the oxygen concentration as input data, and after secondary combustion in the combustion state. Exhaust gas concentration simulating means having the exhaust gas-containing nitrogen oxide concentration and carbon monoxide concentration as output data, and changing the oxygen concentration which is input data of the exhaust gas concentration simulating means within a predetermined range, Target oxygen concentration setting means for outputting, as the target oxygen concentration, an oxygen concentration at which a predetermined evaluation value of the nitrogen oxide concentration and the carbon monoxide concentration, which are output data of gas concentration simulation means, is the lowest within the predetermined range. An oxygen concentration range setting means for setting the predetermined range of the oxygen concentration change as a part of the entire control range in accordance with the value of the predetermined process data, the secondary combustion control of a refuse incinerator comprising: apparatus.
ガス温度を検出する温度検出機構と、前記移動式火床の
燃切位置を検出する燃切位置検出機構とを備え、前記プ
ロセスデータが、前記温度検出機構による検出温度と前
記燃切位置検出機構による検出燃切位置である請求項1
記載のゴミ焼却炉の二次燃焼制御装置。2. The refuse incinerator includes a temperature detection mechanism for detecting an exhaust gas temperature at an outlet of the furnace, and a burn-off position detection mechanism for detecting a burn-off position of the movable grate, wherein the process data Are the temperature detected by the temperature detecting mechanism and the burn-off position detected by the burn-off position detecting mechanism.
A secondary combustion control device for a garbage incinerator according to the above.
れる所定のプロセスデータを入力データとして当該燃焼
状態において二次燃焼後の排ガス含有窒素酸化物濃度及
び一酸化炭素濃度の両方が同時に低下する二次燃焼後の
排ガスに含まれる適正酸素濃度を演算出力する適正酸素
濃度演算手段を備え、 前記酸素濃度範囲設定手段が、前記適正酸素濃度演算手
段が出力する適正酸素濃度を前記所定範囲内に含むよう
に、前記所定範囲を設定することを特徴とする請求項1
または2記載のゴミ焼却炉の二次燃焼制御装置。3. Using predetermined process data obtained according to the combustion state of the refuse incinerator as input data, in the combustion state, both the nitrogen oxide concentration and the carbon monoxide concentration in the exhaust gas after the secondary combustion simultaneously decrease. An appropriate oxygen concentration calculating means for calculating and outputting an appropriate oxygen concentration contained in the exhaust gas after the secondary combustion, wherein the oxygen concentration range setting means sets the appropriate oxygen concentration output by the appropriate oxygen concentration calculating means within the predetermined range. The said predetermined range is set so that it may contain.
Or the secondary combustion control device for a refuse incinerator according to 2.
論モデルで構成されている請求項3記載のゴミ焼却炉の
二次燃焼制御装置。4. The secondary combustion control device for a refuse incinerator according to claim 3, wherein said proper oxygen concentration calculating means is constituted by a fuzzy inference model.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10192607A JP2000028123A (en) | 1998-07-08 | 1998-07-08 | Secondary combustion control device of garbage incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10192607A JP2000028123A (en) | 1998-07-08 | 1998-07-08 | Secondary combustion control device of garbage incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000028123A true JP2000028123A (en) | 2000-01-25 |
Family
ID=16294084
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10192607A Pending JP2000028123A (en) | 1998-07-08 | 1998-07-08 | Secondary combustion control device of garbage incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000028123A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018151771A (en) * | 2017-03-10 | 2018-09-27 | 荏原環境プラント株式会社 | Process management support apparatus and method |
| JP2019007702A (en) * | 2017-06-27 | 2019-01-17 | 川崎重工業株式会社 | Secondary combustion gas mixed state estimation method, combustion state estimation method, automatic combustion control method and waste incinerator |
| CN113074379A (en) * | 2021-03-30 | 2021-07-06 | 龙南鑫坤无机新材料有限公司 | Equipment for removing nitrogen oxide at high temperature |
| JP2022010199A (en) * | 2017-03-10 | 2022-01-14 | 荏原環境プラント株式会社 | Process management support device and method |
| JP7250205B1 (en) | 2022-11-25 | 2023-03-31 | 東京瓦斯株式会社 | Learning model generation method, learning model generation device, combustion prediction method, combustion prediction device, and program |
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1998
- 1998-07-08 JP JP10192607A patent/JP2000028123A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018151771A (en) * | 2017-03-10 | 2018-09-27 | 荏原環境プラント株式会社 | Process management support apparatus and method |
| JP2022010199A (en) * | 2017-03-10 | 2022-01-14 | 荏原環境プラント株式会社 | Process management support device and method |
| JP2019007702A (en) * | 2017-06-27 | 2019-01-17 | 川崎重工業株式会社 | Secondary combustion gas mixed state estimation method, combustion state estimation method, automatic combustion control method and waste incinerator |
| CN113074379A (en) * | 2021-03-30 | 2021-07-06 | 龙南鑫坤无机新材料有限公司 | Equipment for removing nitrogen oxide at high temperature |
| JP7250205B1 (en) | 2022-11-25 | 2023-03-31 | 東京瓦斯株式会社 | Learning model generation method, learning model generation device, combustion prediction method, combustion prediction device, and program |
| JP2024076635A (en) * | 2022-11-25 | 2024-06-06 | 東京瓦斯株式会社 | Learning model generation method, learning model generation device, combustion prediction method, combustion prediction device, and program |
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