JP2011021834A - Method of controlling vapor content in waste melting furnace and vapor content control device for waste melting furnace facility - Google Patents

Method of controlling vapor content in waste melting furnace and vapor content control device for waste melting furnace facility Download PDF

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JP2011021834A
JP2011021834A JP2009167993A JP2009167993A JP2011021834A JP 2011021834 A JP2011021834 A JP 2011021834A JP 2009167993 A JP2009167993 A JP 2009167993A JP 2009167993 A JP2009167993 A JP 2009167993A JP 2011021834 A JP2011021834 A JP 2011021834A
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melting furnace
exhaust gas
waste
amount
boiler
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JP5472847B2 (en
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Kazuhiro Kuribayashi
和浩 栗林
Kazutaka Manako
一隆 真名子
Yuichi Shinoda
裕一 篠田
Nobuhiro Tanigaki
信宏 谷垣
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Nippon Steel Engineering Co Ltd
Nippon Steel Environmental and Energy Solutions Corp
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Nippon Steel Engineering Co Ltd
Nippon Steel Environmental Plant Solutions Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To suppress fluctuation of vapor content by controlling scattering amounts of a combustible gas and char after thermal decomposition, through detection of a thermal decomposition state in a waste melting furnace by selecting a fluctuation state of the highest fluctuation speed among fluctuation states of the waste melting furnace, and through adjustment of an amount of air distributed to a tuyere. <P>SOLUTION: The vapor content of the waste melting furnace facilities is controlled, the facilities which are constituted to treat an exhaust gas after recovering sensible heat by an exhaust gas treatment device 7 in a boiler 6 recovering the sensible heat of the exhaust gas generated in a combustion chamber 5 for burning the combustible gas and combustible residue generated in the waste melting furnace 1, and discharging the exhaust gas after the treatment from a chimney 9 through an induced draft fan 8. A waste charging level 14 in the waste melting furnace, a vapor generation amount 15 in the boiler, an operation load 16 of the induced draft fan, and an exhaust gas amount 17 in an outlet of the chimney are measured, and supply amounts of oxygen source from tuyeres 3, 4 are adjusted on the basis of the measurement value of highest fluctuation value among results of the measurements to control the vapor generation amount in the boiler 6. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、廃棄物溶融炉処理設備において、廃棄物を溶融処理する廃棄物溶融炉から発生する可燃ガス及び可燃残渣(チャー)を燃焼室で燃焼させ、燃焼後の排ガスで蒸気を発生させて熱回収するボイラの蒸気量の制御に関する。   In the waste melting furnace processing facility, the present invention burns combustible gas and combustible residue (char) generated from a waste melting furnace for melting waste in a combustion chamber, and generates steam from the exhaust gas after combustion. The present invention relates to the control of the steam amount of a boiler that recovers heat.

一般廃棄物、産業廃棄物、シュレッダーダスト等の廃棄物を廃棄物溶融炉で溶融処理する際に発生する可燃ガス及びチャーを含有する排ガスは、廃棄物溶融炉の後段に設置されている燃焼室に導入して燃焼させ、排出される燃焼排ガスはボイラで熱回収が行われる(特許文献1、2参照)。   An exhaust gas containing combustible gas and char generated when general waste, industrial waste, shredder dust and other waste are melted in the waste melting furnace is a combustion chamber installed at the rear stage of the waste melting furnace The combustion exhaust gas that is introduced into and burned into the exhaust gas is recovered by a boiler (see Patent Documents 1 and 2).

廃棄物溶融炉に投入される廃棄物のごみ質は一定でなく変動するため、廃棄物溶融炉から排出される排ガス中の可燃ガスの成分やチャーの量などが変動する。例えば、自動車シュレッダーダスト(ASR)等のプラスチック含有廃棄物のような粒径が小さくかつプラスチック類が多く急速熱分解が起こりやすい廃棄物が廃棄物溶融炉に投入されて処理される場合、熱分解後の可燃ガス及びチャーが飛散して燃焼室に導入されて急激に燃焼室の温度が上昇する。燃焼室の温度が急上昇すると、燃焼室後段のボイラにおける蒸発量が大きく変動する状況が見られた。   Since the waste quality of the waste introduced into the waste melting furnace is not constant and fluctuates, the combustible gas components and the amount of char in the exhaust gas discharged from the waste melting furnace fluctuate. For example, when waste containing a small particle size, such as waste containing plastic such as automobile shredder dust (ASR), and containing a large amount of plastics, which is susceptible to rapid thermal decomposition, is put into a waste melting furnace and processed. Later combustible gas and char are scattered and introduced into the combustion chamber, and the temperature of the combustion chamber rises rapidly. When the temperature of the combustion chamber rose rapidly, the evaporation amount in the boiler at the rear stage of the combustion chamber was greatly fluctuated.

特開平8−94035号公報JP-A-8-94035 特開平8−159436号公報JP-A-8-159436

従来は廃棄物溶融炉から排出する熱分解後の可燃ガス及びチャーが急増し、ボイラ蒸気量が大幅に上昇した際に、オペレータ操作で対応していたため、変動幅が大きすぎて変動に追従できなかった場合はボイラ蒸気温度上限値を超過し、プラント非常停止に至る状況も見られた。   Conventionally, when the pyrolysis combustible gas and char discharged from the waste melting furnace increased rapidly, and the boiler steam volume increased significantly, it was handled by operator operation, so the fluctuation range was too large to follow the fluctuation. If not, the boiler steam temperature upper limit was exceeded, leading to an emergency shutdown of the plant.

そこで、本発明は、廃棄物溶融炉の変動状況から変化が最も速いものを選択して廃棄物溶融炉内の熱分解状況を速やかに検知し、それに応じて羽口への送風空気量を調整することで熱分解後の可燃ガス及びチャーの飛散量をコントロールして蒸気量の変動を抑制する廃棄物溶融炉設備のボイラの蒸気量制御方法及び装置を提供するものである。   Therefore, the present invention selects the fastest change from the fluctuation state of the waste melting furnace, quickly detects the thermal decomposition state in the waste melting furnace, and adjusts the amount of air blown to the tuyere accordingly Thus, the present invention provides a steam amount control method and apparatus for a boiler of a waste melting furnace facility that controls the amount of scattered flammable gas and char after pyrolysis to suppress fluctuations in the amount of steam.

本発明の請求項1の発明は、炉上部から廃棄物を投入し、炉下部に配設した複数段の羽口から酸素源を供給して、廃棄物中の灰分及び非燃焼物を溶融し、溶融物を炉底部から排出する廃棄物溶融炉で発生する可燃ガス及び可燃残渣を燃焼する燃焼室と燃焼室で発生した排ガスの顕熱を回収するボイラとボイラで顕熱回収後の排ガスを排ガス処理装置で処理して、処理後の排ガスを誘引通風機を介して排出する煙突より構成する廃棄物溶融炉設備の蒸気量制御方法において、廃棄物溶融炉内の廃棄物の充填レベル、ボイラの発生蒸気量、誘引通風機の運転負荷および煙突出口の排ガス量を測定し、これらの測定結果の変動値が最も大きい測定値に基づいて前記上段羽口からの酸素源供給量を調整してボイラでの発生蒸気量を制御することを特徴とする。   According to the first aspect of the present invention, waste is introduced from the upper part of the furnace, and an oxygen source is supplied from a plurality of tuyere arranged at the lower part of the furnace to melt the ash and non-combustibles in the waste. , Flammable gas generated in a waste melting furnace that discharges molten material from the bottom of the furnace, combustion chamber that burns flammable residue, boiler that recovers sensible heat of exhaust gas generated in the combustion chamber, and exhaust gas after sensible heat recovery in the boiler In a method for controlling the amount of steam in a waste melting furnace facility comprising a chimney that is processed by an exhaust gas treatment device and exhausts the treated exhaust gas through an induction fan, the waste filling level in the waste melting furnace, boiler The amount of steam generated, the operating load of the induction fan and the amount of exhaust gas at the smoke outlet are measured, and the oxygen source supply amount from the upper tuyere is adjusted based on the measured value with the largest variation of these measurement results. Controlling the amount of steam generated in the boiler To.

本発明の請求項2の発明は、炉上部から廃棄物を投入し、炉下部に配設した複数段の羽口から酸素源を供給して、廃棄物中の灰分及び非燃焼物を溶融し、溶融物を炉底部から排出する廃棄物溶融炉と、廃棄物溶融炉で発生する可燃ガス及び可燃残渣を燃焼する燃焼室と、燃焼室で発生した排ガスの顕熱を回収するボイラと、ボイラで顕熱回収後の排ガスの排ガス処理装置と処理後の排ガスを誘引通風機を介して排出する煙突より構成する廃棄物溶融炉設備の蒸気量制御設備において、前記廃棄物溶融炉に設置した廃棄物溶融炉内の廃棄物の充填レベルを測定する充填レベル測定装置と、前記ボイラに設置したボイラの発生蒸気量を測定する発生蒸気量測定装置と、前記誘引通風機の運転負荷を測定する誘引通風機運転負荷測定装置と、前記煙突の出口の排ガス量を測定する排ガス量測定装置と、前記各測定装置からの測定結果が入力され、これらの測定結果の変動値が最も大きい測定値に基づいて前記羽口への送風量を演算し、前記羽口へ送風する送風量を調整する流量調節弁へ弁の開度を調整する制御信号を出力する空気供給制御装置とを備えたことを特徴とする。   According to the second aspect of the present invention, waste is introduced from the upper part of the furnace, and an oxygen source is supplied from a plurality of tuyeres arranged in the lower part of the furnace to melt the ash and non-combustibles in the waste. A waste melting furnace for discharging the melt from the bottom of the furnace, a combustion chamber for burning the combustible gas and combustible residue generated in the waste melting furnace, a boiler for recovering sensible heat of the exhaust gas generated in the combustion chamber, and a boiler In the steam control equipment of the waste melting furnace facility composed of an exhaust gas treatment device for exhaust gas after sensible heat recovery and a chimney that discharges the treated exhaust gas through an induction fan, the waste installed in the waste melting furnace A filling level measuring device for measuring the filling level of waste in the melting furnace, a generated steam amount measuring device for measuring a generated steam amount of a boiler installed in the boiler, and an attraction for measuring an operating load of the induction fan Ventilator operating load measuring device and the smoke The exhaust gas amount measuring device that measures the exhaust gas amount at the outlet of the air and the measurement results from each of the measuring devices are input, and the air flow rate to the tuyere is calculated based on the measured value with the largest fluctuation value of these measurement results And an air supply control device that outputs a control signal for adjusting the opening degree of the valve to a flow rate adjusting valve that adjusts the amount of air sent to the tuyere.

本発明は、熱分解が急速に進むと、ごみレベルの急低下、ボイラ蒸気量の急増、誘引通風機の運転負荷の急増、排ガス流量の急増があるため、廃棄物溶融炉内の廃棄物の充填レベル、ボイラの発生蒸気量、誘引通風機の負荷および煙突出口の排ガス量を測定し、いずれかの検出端データのうち、変動値が最も大きい測定値に基づいて溶融炉内の熱分解状況を早期に検知して送風空気量を自動的に調整することで、ボイラ蒸気量の変動が大きくなる前の時点での調整が可能となり、ボイラ蒸気量を適正範囲内に維持管理することが可能となる。また、廃棄物溶融炉の安定溶融状況を維持できる送風量バランスを保ちながら送風流量調節して確実にボイラ蒸気量の変動の抑制が可能となる。   In the present invention, when pyrolysis progresses rapidly, there is a sudden decrease in the dust level, a rapid increase in the amount of boiler steam, a sudden increase in the operating load of the induction fan, and a rapid increase in the exhaust gas flow rate. Measure the filling level, the amount of steam generated from the boiler, the load of the induction fan and the amount of exhaust gas from the smoke outlet, and the pyrolysis status in the melting furnace based on the measured value with the largest fluctuation value of any of the detection end data Can be adjusted at the time before the fluctuation of the boiler steam volume becomes large, and the boiler steam volume can be maintained within an appropriate range. It becomes. In addition, it is possible to reliably suppress fluctuations in the boiler steam amount by adjusting the air flow rate while maintaining the air flow balance that can maintain the stable melting state of the waste melting furnace.

本発明の蒸気量制御方法を適用する廃棄物溶融炉設備の概略全体図である。1 is a schematic overall view of a waste melting furnace facility to which a steam amount control method of the present invention is applied. 本発明による溶融炉の上段羽口の配置を示し、(a)はA−Aの上段羽口、(b)はB−Bの中段羽口の配置図である。The arrangement | positioning of the upper tuyeres of the melting furnace by this invention is shown, (a) is an upper stage tuyeres of AA, (b) is an arrangement plan of the middle tuyeres of BB. 上段羽口及び中段羽口の空気量とボイラ蒸気量の関係を示すグラフである。It is a graph which shows the relationship between the air quantity and boiler steam quantity of an upper stage tuyere and a middle stage tuyere.

本発明の実施例について図面を参照しながら説明する。   Embodiments of the present invention will be described with reference to the drawings.

図1において、シャフト炉式廃棄物溶融炉1の炉上部より、廃棄物、副原料の石灰石とともにコークスが装入される。炉底部の下段羽口2から酸素含有ガス又は酸素富化ガス、その上方の中段羽口3、上段羽口4からなる上部羽口から空気が吹き込まれる。コークスや熱分解によって生じた炭素質を高温炉床において高温度で燃焼させ、炉内の乾燥帯、熱分解帯及び燃焼溶融帯を順次降下させて溶融スラグ化する。   In FIG. 1, coke is charged from the upper part of the shaft furnace type waste melting furnace 1 together with waste and auxiliary limestone. Air is blown from an upper tuyere composed of an oxygen-containing gas or an oxygen-enriched gas and a middle tuyere 3 and an upper tuyere 4 above the lower tuyere 2 at the bottom of the furnace. The carbonaceous material generated by coke and pyrolysis is burned at a high temperature in the high-temperature hearth, and the drying zone, pyrolysis zone, and combustion melting zone in the furnace are sequentially lowered to form molten slag.

溶融炉1から排出される可燃ガス及びチャーを含有する排ガスは、燃焼室5で燃焼され、高温の燃焼排ガスはボイラ6で熱回収が行われ、ボイラ6の排ガスは排ガス処理設備7の冷却塔で冷却され、消石灰等の中和剤で中和され、集じん機で固気分離され、誘引通風機8を経て煙突9から排出される。廃棄物溶融炉1、燃焼室5、ボイラ6、排ガス処理設備7、誘引通風機8は、それぞれダクト10〜13により順次接続されている。   The exhaust gas containing the combustible gas and char discharged from the melting furnace 1 is combusted in the combustion chamber 5, the high-temperature combustion exhaust gas is recovered by the boiler 6, and the exhaust gas from the boiler 6 is used as a cooling tower of the exhaust gas treatment facility 7. Then, it is neutralized with a neutralizing agent such as slaked lime, solid-gas separated by a dust collector, and discharged from the chimney 9 through the induction fan 8. The waste melting furnace 1, the combustion chamber 5, the boiler 6, the exhaust gas treatment facility 7, and the induction ventilator 8 are sequentially connected by ducts 10 to 13, respectively.

溶融炉1にはごみレベルを、ボイラにはボイラ蒸気量を、誘引通風機には運転負荷(電流値)、煙突の出口には排ガス流量をそれぞれ測定する測定装置14〜17が設置されている。   The melting furnace 1 is provided with measuring devices 14 to 17 for measuring the dust level, the boiler for the amount of boiler steam, the induction fan for operating load (current value), and the exhaust gas flow rate for the outlet of the chimney. .

溶融炉1の上部羽口は、図2(a)に示す上段羽口4と図2(b)に示す中段羽口3が上下方向において重ならないように溶融炉1の円周方向にずらして配置することにより、吹き込む空気量が炉内で偏らないで均一に流れるようにしている。   The upper tuyere of the melting furnace 1 is shifted in the circumferential direction of the melting furnace 1 so that the upper tuyere 4 shown in FIG. 2A and the middle tuyere 3 shown in FIG. By arranging it, the amount of air blown is made to flow uniformly without being biased in the furnace.

上段羽口4、中段羽口3及び下段羽口2には、送風機18の酸素源供給配管19から分岐した上段羽口用ヘッダ20、中段羽口用ヘッダ21及び下段羽口用ヘッダ22にそれぞれ接続されている上段羽口空気供給管23、中段羽口空気供給管24及び下段羽口空気供給管25から空気が供給される。各空気供給管23,24,25には、それぞれ流量調整弁26,27,28が設けられている。   The upper tuyere 4, the middle tuyere 3 and the lower tuyere 2 are respectively connected to the upper tuyere header 20, the middle tuyere header 21 and the lower tuyere header 22 branched from the oxygen source supply pipe 19 of the blower 18. Air is supplied from the connected upper tuyere air supply pipe 23, middle tuyere air supply pipe 24, and lower tuyere air supply pipe 25. The air supply pipes 23, 24, 25 are provided with flow rate adjusting valves 26, 27, 28, respectively.

各計測装置14〜17で計測された計測信号は、空気供給制御装置29に入力されて、各流量調整弁26,27へ流量調節制御信号が出力される。空気供給制御装置29には、上段羽口4、中段羽口3のそれぞれについてごみレベル、ボイラ蒸気量、誘引通風機負荷あるいは煙突の排ガス流量の変動量に対して個別の流量調節弁の調節量が設定されており、計測されたごみレベル、ボイラ蒸気量、誘引通風機負荷あるいは煙突の排ガス流量に対して流量調節弁の調節量の設定値を流量調節弁へ制御信号として出力する。   Measurement signals measured by the measurement devices 14 to 17 are input to the air supply control device 29, and flow rate control signals are output to the flow rate adjustment valves 26 and 27. The air supply control device 29 includes an adjustment amount of an individual flow rate control valve for each of the upper tuyere 4 and the middle tuyere 3 with respect to the fluctuation level of the dust level, the boiler steam amount, the induction fan load or the exhaust gas flow rate of the chimney. Is set, and the set value of the adjustment amount of the flow rate control valve is output as a control signal to the flow rate control valve with respect to the measured dust level, boiler steam amount, induction ventilator load or chimney exhaust gas flow rate.

図3(b)のグラフに示すように、空気供給制御装置29に入力される、ごみレベル、ボイラ蒸気量、誘引通風機負荷あるいは煙突の排ガス流量の計測信号のうち、溶融炉内の熱分解が急速に進んで、最も速く選択された計測信号がボイラ蒸気量30であった場合、温度制御装置29では上段羽口送風空気量31、中段羽口送風空気量32のそれぞれの設定に応じて各流量調整弁4、3の調整量の制御信号が出力されて減調整されることで、ボイラ蒸気量30の上昇が抑制される。   As shown in the graph of FIG. 3B, among the measurement signals of the dust level, boiler steam amount, induction ventilator load or chimney exhaust gas flow rate input to the air supply control device 29, the thermal decomposition in the melting furnace. If the measurement signal selected the fastest is the boiler steam amount 30, the temperature control device 29 responds to the settings of the upper tuyere blown air amount 31 and the middle tuyere blown air amount 32, respectively. The control signal of the adjustment amount of each flow regulating valve 4 and 3 is output and is adjusted to be reduced, so that an increase in the boiler steam amount 30 is suppressed.

(1)ごみレベルの急低下、(2)ボイラ蒸気量の急増、(3)誘引通風機の運転負荷の急増、あるいは(4)排ガス流量の急増のいずれかの時には、溶融炉内の熱分解が急速に進んでいるため、いずれかの検出信号が空気供給制御装置に入力されると、上段羽口あるいは中段羽口の流量調整弁を調整して送風空気量を減らして熱分解を速やかに抑える。この抑制により、ボイラ蒸気量の変動幅が大きくなることはなく、確実にボイラ蒸気量の変動を抑制できるようになった。 Thermal decomposition in the melting furnace occurs when either (1) a sharp drop in dust level, (2) a rapid increase in boiler steam volume, (3) a sudden increase in operating load of the induction fan, or (4) a sudden increase in exhaust gas flow rate Therefore, when any detection signal is input to the air supply control device, the flow adjustment valve at the upper tuyere or the middle tuyere is adjusted to reduce the amount of blown air and to quickly perform thermal decomposition. suppress. By this suppression, the fluctuation range of the boiler steam amount is not increased, and the fluctuation of the boiler steam amount can be surely suppressed.

1:溶融炉
2:下段羽口
3:中段羽口
4:上段羽口
5:燃焼室
6:ボイラ
7:排ガス処理設備
8:誘引通風機
9:煙突10〜13:ダクト
14:計測装置(ごみレベル)
15:計測装置(ボイラ蒸気量)
16:計測装置(誘引通風機負荷)
17:計測装置(排ガス流量)
18:送風機
19:酸素源供給配管
20:上段羽口用ヘッダ
21:中段羽口用ヘッダ
22:下段羽口用ヘッダ
23:上段羽口空気供給管
24:中段羽口空気供給管
25:下段羽口空気供給管
26:流量調整弁
27:流量調整弁
28:流量調整弁
29:空気供給制御装置
30:ボイラ蒸気量
31:上段羽口送風空気量
32:中段羽口送風空気量
1: Melting furnace 2: Lower tuyere 3: Middle tuyere 4: Upper tuyere 5: Combustion chamber 6: Boiler 7: Exhaust gas treatment equipment 8: Induction ventilator 9: Chimney 10-13: Duct 14: Measuring device (garbage) level)
15: Measuring device (boiler steam volume)
16: Measuring device (attracting ventilator load)
17: Measuring device (exhaust gas flow rate)
18: Blower 19: Oxygen source supply pipe 20: Upper tuyere header 21: Middle tuyere header 22: Lower tuyere header 23: Upper tuyere air supply pipe 24: Middle tuyere air supply pipe 25: Lower tuyere Mouth air supply pipe 26: Flow rate adjustment valve 27: Flow rate adjustment valve 28: Flow rate adjustment valve 29: Air supply control device 30: Boiler steam amount 31: Upper tuyere blown air amount 32: Middle stage tuyere blown air amount

Claims (2)

炉上部から廃棄物を投入し、炉下部に配設した複数段の羽口から酸素源を供給して、廃棄物中の灰分及び非燃焼物を溶融し、溶融物を炉底部から排出する廃棄物溶融炉で発生する可燃ガス及び可燃残渣を燃焼する燃焼室と燃焼室で発生した排ガスの顕熱を回収するボイラとボイラで顕熱回収後の排ガスを排ガス処理装置で処理して、処理後の排ガスを誘引通風機を介して排出する煙突より構成する廃棄物溶融炉設備の蒸気量制御方法において、
廃棄物溶融炉内の廃棄物の充填レベル、ボイラの発生蒸気量、誘引通風機の運転負荷および煙突出口の排ガス量を測定し、
これらの測定結果の変動値が最も大きい測定値に基づいて前記上段羽口からの酸素源供給量を調整してボイラでの発生蒸気量を制御することを特徴とする廃棄物溶融炉設備の蒸気量制御方法。
Disposal in which waste is introduced from the top of the furnace, oxygen sources are supplied from a plurality of tuyeres arranged at the bottom of the furnace, ash and non-combustibles in the waste are melted, and the melt is discharged from the bottom of the furnace Combustion gas that burns combustible gas and combustion residue generated in a material melting furnace and boiler that recovers sensible heat of exhaust gas generated in the combustion chamber In the method for controlling the amount of steam in a waste melting furnace facility comprising a chimney that discharges the exhaust gas through an induction ventilator,
Measure the filling level of waste in the waste melting furnace, the amount of steam generated by the boiler, the operating load of the induction fan and the amount of exhaust gas from the smoke outlet,
The steam of the waste melting furnace equipment is characterized in that the amount of steam generated in the boiler is controlled by adjusting the oxygen source supply amount from the upper tuyere based on the measurement value having the largest fluctuation value of these measurement results. Quantity control method.
炉上部から廃棄物を投入し、炉下部に配設した複数段の羽口から酸素源を供給して、廃棄物中の灰分及び非燃焼物を溶融し、溶融物を炉底部から排出する廃棄物溶融炉と、廃棄物溶融炉で発生する可燃ガス及び可燃残渣を燃焼する燃焼室と、燃焼室で発生した排ガスの顕熱を回収するボイラと、ボイラで顕熱回収後の排ガスの排ガス処理装置と処理後の排ガスを誘引通風機を介して排出する煙突より構成する廃棄物溶融炉設備の蒸気量制御設備において、
前記廃棄物溶融炉に設置した廃棄物溶融炉内の廃棄物の充填レベルを測定する充填レベル測定装置と、
前記ボイラに設置したボイラの発生蒸気量を測定する発生蒸気量測定装置と、
前記誘引通風機の運転負荷を測定する誘引通風機運転負荷測定装置と、
前記煙突の出口の排ガス量を測定する排ガス量測定装置と、
前記各測定装置からの測定結果が入力され、これらの測定結果の変動値が最も大きい測定値に基づいて前記羽口への送風量を演算し、前記羽口へ送風する送風量を調整する流量調節弁へ弁の開度を調整する制御信号を出力する空気供給制御装置とを備えたことを特徴とする廃棄物溶融炉設備の蒸気量制御装置。
Disposal in which waste is introduced from the top of the furnace, oxygen sources are supplied from a plurality of tuyeres arranged at the bottom of the furnace, ash and non-combustibles in the waste are melted, and the melt is discharged from the bottom of the furnace Waste melting furnace, combustion chamber for burning combustible gas and combustible residue generated in waste melting furnace, boiler for recovering sensible heat of exhaust gas generated in combustion chamber, and exhaust gas treatment of exhaust gas after sensible heat recovery in boiler In the facility for controlling the amount of steam of the waste melting furnace facility comprising the device and the chimney that discharges the exhaust gas after treatment through the induction fan,
A filling level measuring device for measuring the filling level of the waste in the waste melting furnace installed in the waste melting furnace;
A generated steam amount measuring device for measuring a generated steam amount of a boiler installed in the boiler;
An induction fan operating load measuring device for measuring an operation load of the induction fan; and
An exhaust gas amount measuring device for measuring the exhaust gas amount at the exit of the chimney;
A flow rate for inputting the measurement results from each of the measuring devices, calculating the air flow rate to the tuyere based on the measurement value having the largest fluctuation value of these measurement results, and adjusting the air flow rate sent to the tuyere An apparatus for controlling the amount of steam in a waste melting furnace, comprising: an air supply control device that outputs a control signal for adjusting the opening of the valve to a control valve.
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