JP2001082719A5 - - Google Patents
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- JP2001082719A5 JP2001082719A5 JP1999262571A JP26257199A JP2001082719A5 JP 2001082719 A5 JP2001082719 A5 JP 2001082719A5 JP 1999262571 A JP1999262571 A JP 1999262571A JP 26257199 A JP26257199 A JP 26257199A JP 2001082719 A5 JP2001082719 A5 JP 2001082719A5
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- amount
- combustion
- correction amount
- value
- driving speed
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- 238000002485 combustion reaction Methods 0.000 claims 56
- 239000000428 dust Substances 0.000 claims 17
- 238000000034 method Methods 0.000 claims 16
- 238000004056 waste incineration Methods 0.000 claims 11
- 238000001035 drying Methods 0.000 claims 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims 2
- 229910052760 oxygen Inorganic materials 0.000 claims 2
- 239000001301 oxygen Substances 0.000 claims 2
- 239000002699 waste material Substances 0.000 claims 2
Claims (12)
ごみ焼却プラントにおける各種のセンサから、蒸気量プロセス値を含む各種のプロセス値を読み込むステップと、
読み込まれた蒸気量プロセス値と予め設定された蒸気量設定値との差を演算し、該差がゼロとなるように、燃焼空気量の設定値を決定するステップと、
外乱が生じたか否かを判定するステップと、
外乱が生じたときに、予め構築されたニューロモデルを用いて、発生される蒸気量の所定時間後の予測値を演算するステップと、
蒸気量予測値と蒸気量設定値との差、及び読み込まれた各種のプロセス値に基づき、蒸気量予測値と蒸気量設定値との差が最小となるように、燃焼空気量設定値を補正するための補正値を演算するステップと、
燃焼空気量を補正値により補正するステップと、
補正された燃焼空気量を供給するステップと
からなることを特徴とする燃焼制御方法。In the combustion control method of the waste incineration plant,
Reading various process values, including steam volume process values, from various sensors in a waste incineration plant;
Calculating a difference between the read steam amount process value and a preset steam amount setting value, and determining a set value of the combustion air amount so that the difference becomes zero;
Determining whether a disturbance has occurred;
When a disturbance occurs, using a neuro model built in advance, calculating a predicted value after a predetermined time of the generated steam amount; and
Based on the difference between the predicted steam volume value and the steam volume setting value and the various process values that have been read, the combustion air volume setting value is corrected so that the difference between the predicted steam volume value and the steam volume setting value is minimized. Calculating a correction value for
Correcting the amount of combustion air with a correction value;
A step of supplying a corrected amount of combustion air.
ごみ焼却プラントはストーカ式のものであって、上記燃焼空気量は、燃焼1帯及び燃焼2帯へ供給される主燃焼空気量であり、
燃焼制御方法はさらに、焼却炉内の燃焼完結点のプロセス値に基づき、乾燥帯及び後燃焼帯への空気量を決定するステップと、主燃焼空気量と乾燥帯及び後燃焼帯への空気量との和である一次燃焼空気量の設定値に基づき、焼却炉出口への空気量である二次燃焼空気量を演算するステップとを含んでいる
ことを特徴とする燃焼制御方法。The combustion control method according to claim 1,
The waste incineration plant is of the stoker type, and the amount of combustion air is the amount of main combustion air supplied to the combustion 1 zone and the combustion 2 zone,
The combustion control method further includes determining the amount of air to the drying zone and the post-combustion zone based on the process value of the combustion completion point in the incinerator, and the amount of air to the main combustion air and the drying zone and the post-combustion zone. And a step of calculating a secondary combustion air amount that is an air amount to the incinerator outlet based on a set value of the primary combustion air amount that is the sum of the above and the combustion control method.
読み込まれた各種のプロセス値を用いて学習することにより、ニューロモデルを更新するステップ
を含んでいることを特徴とする燃焼制御方法。The combustion control method according to claim 1 or 2, further comprising:
A combustion control method comprising a step of updating a neuro model by learning using various read process values.
ごみ焼却プラントにおける各種のセンサから各種のプロセス値を読み込むステップと、
読み込まれた各種のプロセス値に基づき、ごみ性状の変動に応じて調整すべき給じん機の駆動速度の補正量を演算するステップと、
ホッパへのごみの投入時点で、給じん機の駆動速度を演算された補正量だけ変化させるステップと
からなることを特徴とする燃焼制御方法。In the combustion control method of the waste incineration plant,
Reading various process values from various sensors in a waste incineration plant;
A step of calculating a correction amount of the driving speed of the dust feeder to be adjusted according to fluctuations in dust properties based on the various process values read;
And a step of changing the driving speed of the dust feeder by the calculated correction amount at the time of putting garbage into the hopper.
ごみ性状の変動に応じて調整すべきストーカの駆動速度の補正量を演算するステップと、
ホッパへのごみの投入時点で、ストーカの駆動速度を演算された補正量だけ変化させるステップと
を含んでいることを特徴とする燃焼制御方法。The combustion control method according to claim 4, wherein the waste incineration plant is a stoker type, and the method further comprises:
A step of calculating a correction amount of the driving speed of the stalker to be adjusted according to a change in the garbage property;
And a step of changing the driving speed of the stalker by the calculated correction amount at the time when the garbage is put into the hopper.
発生蒸気量に応じて調整すべき給じん機及びストーカの駆動速度それぞれの補正量を演算し、所定の周期で、その時点で得られた補正量でそれぞれの駆動速度を変化させるステップと、
ごみの層厚に応じて調整すべき給じん機及びストーカの駆動速度それぞれの補正量を演算し、所定の周期で、その時点で得られた補正量でそれぞれの駆動速度を変化させるステップと、
焼却炉内の酸素濃度が所定の範囲を外れたときに、調整すべき給じん機及びストーカの駆動速度それぞれの補正量を演算し、かつその時点で、得られた補正量でそれぞれの駆動速度を変化させるステップと、
主燃焼空気量が所定の範囲を外れたときに、調整すべき給じん機及びストーカの駆動速度それぞれの補正量を演算し、かつその時点で、得られた補正量でそれぞれの駆動速度を変化させるステップと、
燃焼完結点の所定の範囲から外れたときに、調整すべき給じん機及びストーカの駆動速度それぞれの補正量を演算し、かつその時点で、得られた補正量でそれぞれの駆動速度を変化させるステップと
を含んでいることを特徴とする燃焼制御方法。6. The combustion control method according to claim 5, further comprising:
Calculating a correction amount for each of the driving speeds of the dust feeder and the stalker to be adjusted according to the amount of generated steam, and changing each driving speed by a correction amount obtained at that time in a predetermined cycle; and
Calculating a correction amount for each of the driving speeds of the dust feeder and the stalker to be adjusted according to the layer thickness of the dust, and changing each driving speed by a correction amount obtained at that time in a predetermined cycle; and
When the oxygen concentration in the incinerator is out of the specified range, the correction amount of each of the driving speeds of the dust feeder and the stalker to be adjusted is calculated, and at that time, the respective correction speeds obtained are the respective driving speeds. A step of changing
When the amount of main combustion air is out of the specified range, calculate the correction amount of the driving speed of the dust feeder and stalker to be adjusted, and change the driving speed by the obtained correction amount at that time Step to
When the combustion completion point is out of the predetermined range, the correction amount for each of the driving speeds of the feeder and stalker to be adjusted is calculated, and at that time, the respective driving speeds are changed by the obtained correction amount. A combustion control method comprising: steps.
ごみを燃焼プラントにおける各種のセンサから、蒸気量プロセス値を含む各種のプロセス値を読み込むステップと、読み込まれた蒸気量プロセス値と予め設定された蒸気量設定値との差を演算し、該差がゼロとなるように、燃焼空気量の設定値を決定するステップと、外乱が生じたか否かを判定するステップと、外乱が生じたと判定したときに、予め構築されたニューロモデルを用いて、発生される蒸気量の所定時間後の予測値を演算するステップと、蒸気量予測値と蒸気量設定値との差、及び読み込まれた各種のプロセス値に基づき、蒸気量予測値と蒸気量設定値との差が最小となるように、燃焼空気量設定値を補正するための補正値を演算するステップと、燃焼空気量を補正値により補正させるステップと、補正された燃焼空気量を供給させるステップとを実行する燃焼制御装置
を備えていることを特徴とするごみを燃焼プラント。In a waste incineration plant equipped with a dust feeder for extruding garbage from a hopper to an incinerator and a combustion furnace for burning the garbage,
The step of reading various process values including the steam amount process value from various sensors in the combustion plant is calculated, and the difference between the read steam amount process value and a preset steam amount set value is calculated. When determining that the disturbance has occurred, a step of determining the set value of the combustion air amount so as to be zero, a step of determining whether or not a disturbance has occurred, Based on the step of calculating the predicted value of the generated steam volume after a predetermined time, the difference between the steam volume predicted value and the steam volume setting value, and various read process values, the steam volume predicted value and the steam volume setting A correction value for correcting the combustion air amount setting value, a step of correcting the combustion air amount by the correction value, and a corrected combustion air amount are supplied so that the difference from the value is minimized. Combustion plants dust, characterized in that it comprises a combustion control device for executing the steps of.
ごみ焼却プラントはストーカ式のものであって、上記燃焼空気量は、燃焼1帯及び燃焼2帯へ供給される主燃焼空気量であり、
燃焼制御装置はさらに、焼却炉内の燃焼完結点のプロセス値に基づき、乾燥帯及び後燃焼帯への空気量を決定するステップと、主燃焼空気量と乾燥帯及び後燃焼帯への空気量との和である一次燃焼空気量の設定値に基づき、焼却炉出口への空気量である二次燃焼空気量を演算するステップとを実行するよう構成されている
ことを特徴とするごみを燃焼プラント。In the combustion plant,
The waste incineration plant is of the stoker type, and the amount of combustion air is the amount of main combustion air supplied to the combustion 1 zone and the combustion 2 zone,
The combustion control device further determines the amount of air to the dry zone and the post-combustion zone based on the process value of the combustion completion point in the incinerator, and the main combustion air amount and the air amount to the dry zone and the post-combustion zone And the step of calculating the amount of secondary combustion air that is the amount of air to the incinerator outlet based on a set value of the amount of primary combustion air that is the sum of plant.
ごみを燃焼プラントにおける各種のセンサから、各種のプロセス値を読み込むステップと、読み込まれた各種のプロセス値に基づき、ごみ性状のの変動に応じて調整すべき給じん機の駆動速度の補正量を演算するステップと、ホッパへのごみの投入時点で、給じん機の駆動速度を演算された補正量だけ変化させるステップとを実行する燃焼制御装置
を備えていることを特徴とするごみを燃焼プラント。In a waste incineration plant equipped with a dust feeder for extruding garbage from a hopper to an incinerator and a combustion furnace for burning the garbage,
The step of reading various process values from various sensors in the combustion plant and the correction amount of the drive speed of the dust feeder to be adjusted according to the fluctuation of the garbage properties based on the various process values read Combustion control device for executing a step of calculating and a step of changing the driving speed of the feeder by the calculated correction amount at the time when the waste is put into the hopper is provided. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26257199A JP3856994B2 (en) | 1999-09-16 | 1999-09-16 | Combustion control method for waste incineration plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26257199A JP3856994B2 (en) | 1999-09-16 | 1999-09-16 | Combustion control method for waste incineration plant |
Publications (3)
Publication Number | Publication Date |
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JP2001082719A JP2001082719A (en) | 2001-03-30 |
JP2001082719A5 true JP2001082719A5 (en) | 2004-12-24 |
JP3856994B2 JP3856994B2 (en) | 2006-12-13 |
Family
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Family Applications (1)
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JP26257199A Expired - Lifetime JP3856994B2 (en) | 1999-09-16 | 1999-09-16 | Combustion control method for waste incineration plant |
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Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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JP4276146B2 (en) * | 2004-08-02 | 2009-06-10 | 株式会社神戸製鋼所 | Control method and apparatus for pyrolysis gasification melting treatment plant, and program |
JP4486628B2 (en) * | 2006-09-25 | 2010-06-23 | 株式会社神戸製鋼所 | Incinerator control method and apparatus, and program |
JP2008249214A (en) * | 2007-03-29 | 2008-10-16 | Kobe Steel Ltd | Control method, device and program for incinerator |
KR101480130B1 (en) * | 2013-06-28 | 2015-01-07 | (주) 태종 엔이씨 | Incineration facility for heat calculate, design program and operator(Operater) analysis of the operation of the form and diagnosis and control of solid fuel boilers and equipment life-cycle management system and method |
JP7178814B2 (en) * | 2018-07-11 | 2022-11-28 | 日鉄エンジニアリング株式会社 | Stoker type waste power generation system and method for stabilizing waste power generation amount |
JP7256016B2 (en) * | 2019-01-25 | 2023-04-11 | 日立造船株式会社 | Predictive model generation device, prediction model generation method by prediction model generation device, and prediction device |
JP7054094B2 (en) * | 2019-05-21 | 2022-04-13 | 学校法人東京電機大学 | Combustion control method, waste incinerator power generation equipment |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS58195707A (en) * | 1982-05-11 | 1983-11-15 | Kawasaki Heavy Ind Ltd | Combustion control method for refuse incinerator |
JPS61143617A (en) * | 1984-12-14 | 1986-07-01 | Kawasaki Heavy Ind Ltd | Method of controlling combustion in refuse incinerator |
JPS63113215A (en) * | 1986-10-29 | 1988-05-18 | Purantetsuku:Kk | Method of controlling combustion of incinerator |
JPS63273716A (en) * | 1987-04-30 | 1988-11-10 | Ebara Infilco Co Ltd | Combustion control method of incinerator |
JPH0526420A (en) * | 1991-07-19 | 1993-02-02 | Sanki Eng Co Ltd | Dust combustion method in dust incinerator |
JPH06332501A (en) * | 1993-05-24 | 1994-12-02 | Ishikawajima Harima Heavy Ind Co Ltd | Feedback controller and incinerator using the feedback controller |
JP3030614B2 (en) * | 1996-08-08 | 2000-04-10 | 住友重機械工業株式会社 | Estimation method of waste layer thickness index and combustion control method of waste incinerator using the method |
JP3351323B2 (en) * | 1997-06-26 | 2002-11-25 | 日本鋼管株式会社 | Waste incineration apparatus and method for suppressing generation of dioxins |
-
1999
- 1999-09-16 JP JP26257199A patent/JP3856994B2/en not_active Expired - Lifetime
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