JP3408772B2 - Operation control method and apparatus for plasma melting furnace - Google Patents
Operation control method and apparatus for plasma melting furnaceInfo
- Publication number
- JP3408772B2 JP3408772B2 JP18247299A JP18247299A JP3408772B2 JP 3408772 B2 JP3408772 B2 JP 3408772B2 JP 18247299 A JP18247299 A JP 18247299A JP 18247299 A JP18247299 A JP 18247299A JP 3408772 B2 JP3408772 B2 JP 3408772B2
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- JP
- Japan
- Prior art keywords
- molten metal
- furnace
- discharge
- waste
- plasma
- 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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- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Furnace Charging Or Discharging (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、産業廃棄物、家庭
ごみ等の都市ゴミ及びごみ焼却炉での焼却残渣、主灰、
飛灰等、更には焼却前の廃棄物を溶融処理する溶融炉の
運転制御方法とその装置に係り、特に廃棄物溶融時に炉
内に堆積する溶融メタルの増加を推定し、溶融メタルを
炉外へ取出す出湯時期を検出し、該検出信号に基づいて
出湯操作を行なうプラズマ溶融炉の運転制御方法及びそ
の装置に関する。TECHNICAL FIELD The present invention relates to industrial waste, municipal solid waste such as household waste, and incineration residue in a refuse incinerator, main ash,
The present invention relates to a method and an apparatus for controlling the operation of a melting furnace that melts fly ash and other waste before incineration, and in particular estimates the increase in molten metal that accumulates in the furnace when waste is melted, The present invention relates to an operation control method and apparatus for a plasma melting furnace, which detects a tapping time to be taken out and performs tapping operation based on the detection signal.
【0002】[0002]
【従来の技術】都市ごみや、下水汚泥、産業廃棄物及び
それらの焼却灰、飛灰、残渣(以下単に焼却残渣とい
う)は多くの場合埋立て処理されている。しかし、近年
埋め立て地の確保が次第に困難になっているため、埋め
立てられる焼却灰等の容積を小さくする方法が要望され
ている。また、埋め立てられた焼却灰等からの有機物
質、重金属などの有害物質が雨水、地下水に溶出して、
二次公害を引き起こす問題も懸念されており、これらの
無公害化の技術も要望されている。2. Description of the Related Art Municipal refuse, sewage sludge, industrial waste, and their incinerated ash, fly ash, and residues (hereinafter simply referred to as incineration residues) are often landfilled. However, in recent years, it has become increasingly difficult to secure landfill sites, so there is a demand for a method of reducing the volume of incinerated ash or the like to be landfilled. In addition, organic substances from landfilled incineration ash, harmful substances such as heavy metals, elute into rainwater and groundwater,
There is also concern about the problem of causing secondary pollution, and technologies for making these pollution-free are also required.
【0003】一方、資源の再利用の観点から、従来焼却
灰等として埋め立てられていた物も再利用化の要望があ
る。都市ごみの焼却灰は、磁気やふるい等により選別さ
れ、金属物質は新たな資源として再利用されているが、
残った灰の再利用方法の要望も出されている。このよう
な要望に対し、プラズマ炉、バーナ炉、誘導炉などの溶
融処理炉に焼却灰を投入してこれらを溶融処理する方法
が実現している。これらの方法によれば、焼却灰を高温
で溶融することで、焼却灰中の有害成分を高温分解する
とともに、金属成分を溶融メタル(金属)として溶融ス
ラグから分離することができる。On the other hand, from the viewpoint of reusing resources, there is a demand for reusing materials that were conventionally landfilled as incinerated ash. Incinerated ash of municipal waste is sorted by magnetism and sieving, and metallic substances are reused as new resources.
There is also a demand for a method of reusing the remaining ash. In response to such a demand, a method has been realized in which incineration ash is put into a melting furnace such as a plasma furnace, a burner furnace, an induction furnace and the like is melted and processed. According to these methods, by melting the incinerated ash at a high temperature, the harmful components in the incinerated ash can be decomposed at a high temperature, and the metal component can be separated as molten metal (metal) from the molten slag.
【0004】溶融スラグを固化したものは焼却灰からの
減容率が大きく、且つガラス化状態にあるためにスラグ
中の有害物質は雨水、地下水に溶出しないので、このま
ま埋立てても二次公害の心配はない。また該スラグは、
砂利、小石の代わりにコンクリートの骨材や、ブロック
化して道路のタイルに利用するなどして再利用すること
もできる。一方、近年の溶融炉については、焼却灰等の
溶融だけでなく直接廃棄物を溶融処理する溶融処理炉も
考えられており、これらも途中の廃棄物焼却工程が不要
になるために、有効な廃棄物処理方法である。Solidified molten slag has a large volume reduction rate from incinerated ash, and since it is in a vitrified state, harmful substances in the slag do not elute into rainwater or groundwater. I don't have to worry. Also, the slag is
It can also be reused by using concrete aggregate instead of gravel and pebbles, or by blocking it into road tiles. On the other hand, as a melting furnace in recent years, a melting treatment furnace that directly melts not only the melting of incinerated ash but also waste is considered, and these are also effective because the waste incineration process in the middle is unnecessary. This is a waste treatment method.
【0005】ごみ焼却炉での焼却残渣や飛灰等を溶融処
理する溶融炉の一つであるプラズマ灰溶融炉に関して従
来例を図5に基づいて説明する。溶融炉1は直流電源装
置2を持ち、炉上部から差し込まれたプラズマ電極5を
用いて炉底電極6との間で放電させ高温のプラズマを発
生させる。炉上部に設けた被溶融物供給口7より炉内に
投入された焼却灰は、プラズマの輻射熱とともに、溶融
スラグ9、溶融メタル(金属)10中を通る電流が発生
するジュール熱により熱せられ溶融する。A conventional example of a plasma ash melting furnace which is one of melting furnaces for melting incineration residues and fly ash in a refuse incinerator will be described with reference to FIG. The melting furnace 1 has a DC power supply device 2 and uses a plasma electrode 5 inserted from the upper part of the furnace to generate a high temperature plasma by causing a discharge between the melting electrode 1 and a furnace bottom electrode 6. The incineration ash introduced into the furnace from the melted material supply port 7 provided in the upper part of the furnace is heated by the radiant heat of the plasma and the Joule heat generated by the electric current passing through the molten slag 9 and the molten metal (metal) 10 to be melted. To do.
【0006】そして投入口7より炉内に投入された焼却
灰は、プラズマアーク及び電流がスラグ中を流れる時に
発生するジュール発熱によって発生する高熱(1300
〜2000℃)で溶融されるが、かかるプラズマ溶融炉
において溶融処理する焼却灰中には、溶融スラグ9とな
るシリカ等の成分と、溶融メタル10となる鉄を始めと
する金属成分が含まれている。The incinerator ash charged into the furnace through the charging port 7 has a high heat (1300) generated by Joule heat generated when a plasma arc and an electric current flow in the slag.
The molten slag 9 is melted at a temperature of up to 2000 ° C., but the incineration ash that is melt-processed in the plasma melting furnace contains a component such as silica that forms the molten slag 9 and a metal component such as iron that forms the molten metal 10. ing.
【0007】このため前記炉内で溶融された焼却灰は、
比重の軽い溶融スラグ9が上部に浮上し、溶融メタル1
0が下部に沈んでいき二層に分離されていく。上部層の
溶融スラグ9は出滓樋3より溢れ出るように連続的に流
れ出していき、スラグ搬送コンベヤ8で徐々に空冷して
回収する。また、前記スラグ搬送コンベヤ8で徐冷する
代わりに、大きな冷却用水槽へ落下させ急冷することに
より水砕スラグとして回収する方法もある。Therefore, the incinerated ash melted in the furnace is
Molten slag 9 with a low specific gravity floats to the top, and molten metal 1
Zero sinks to the bottom and separates into two layers. The molten slag 9 in the upper layer continuously flows out so as to overflow from the slag gutter 3 and is gradually cooled by the slag transport conveyor 8 and collected. There is also a method of collecting as water granulated slag by dropping it into a large cooling water tank and rapidly cooling it instead of gradually cooling it by the slag transport conveyor 8.
【0008】このような運転を続けていると、上部層の
溶融スラグ9は連続的に炉外へ排出されていくが、下部
層の溶融メタル10は徐々に蓄積していく。金属成分は
スラグ成分に比べて少量のため蓄積速度は速くはない
が、次第に溶融メタル層が厚くなり、溶融メタル層の液
面が上昇するため、反対に溶融スラグ層が薄くなってく
る。If such an operation is continued, the molten slag 9 in the upper layer is continuously discharged out of the furnace, but the molten metal 10 in the lower layer gradually accumulates. Since the amount of the metal component is smaller than that of the slag component, the accumulation rate is not fast, but the molten metal layer gradually thickens and the liquid level of the molten metal layer rises, so that the molten slag layer becomes thin on the contrary.
【0009】前述の通り、電流が溶融スラグ層を流れる
時に、該スラグ9が抵抗として発生するジュール熱は、
溶融のための熱源の一つである。一方、溶融処理により
その堆積層厚が増大する溶融メタル(金属)10の電気
抵抗値は、溶融スラグ9に比べて非常に小さいので、そ
の発熱量も小さく、溶融メタル層の増大は同一電流で運
転している場合には、発熱量の低下にもつながり炉の運
転としては望ましくない。そのため溶融メタル10が蓄
積されてくると、該溶融メタル10を炉外に排出するた
めに、炉1を傾けて溶融メタル(金属)10を排出する
傾動と呼ばれる操作を断続的に行なっている。As described above, the Joule heat generated by the slag 9 as a resistance when an electric current flows through the molten slag layer is
It is one of the heat sources for melting. On the other hand, since the electric resistance value of the molten metal (metal) 10 whose deposited layer thickness increases due to the melting treatment is much smaller than that of the molten slag 9, its calorific value is also small, and the increase of the molten metal layer is the same current. When operating, this also leads to a decrease in heat generation and is not desirable for operating the furnace. Therefore, when the molten metal 10 is accumulated, an operation called tilting for tilting the furnace 1 to discharge the molten metal (metal) 10 is intermittently performed in order to discharge the molten metal 10 to the outside of the furnace.
【0010】[0010]
【発明が解決しようとする課題】このため前記従来の溶
融設備において、前記傾動操作タイミングを決定するた
めに、被溶融物の溶融に伴い炉内に蓄積される溶融メタ
ル10の量を検出するニーズはあったが、炉内は高温
(1300〜2000℃)で腐食性の高いガスがあるな
ど長期間安定して計測できるセンサが配置できないた
め、従来は運転員の推測によって傾動操作を実施してお
り、個人差、経験の差で判断にばらつきが出るといった
問題があった。Therefore, in the conventional melting equipment, there is a need to detect the amount of the molten metal 10 accumulated in the furnace as the material to be melted is melted in order to determine the tilting operation timing. However, because there is a high temperature (1300 to 2000 ° C) and highly corrosive gas in the furnace, it is not possible to place a sensor that can measure stably for a long period of time. However, there was a problem that judgments varied due to individual differences and differences in experience.
【0011】また、都市ゴミや産業廃棄物はその混入種
別が種々雑多であり、これらの焼却残渣である焼却灰や
飛灰等も当然に物性が安定せず、且つ時間的物性変動が
あるために、このようなものを被溶融物とする場合は、
溶融メタル10の堆積増加速度が変化するために、予め
定めた時間間隔で溶融メタル10の排出を行なうと、場
合によっては傾動タイミングが遅くなって傾動の準備が
間に合わなくなったり、早すぎるという傾動頻度が増し
て溶融時間が短くなるなど、効率的な運転が行なえなく
なるという問題があった。[0011] Further, since various types of municipal waste and industrial waste are mixed, the physical properties of incineration ash, fly ash, etc., which are the incineration residues thereof, are naturally not stable and the physical properties fluctuate with time. In addition, when making such a thing as a melted object,
If the molten metal 10 is discharged at a predetermined time interval because the rate of increase in the deposition of the molten metal 10 changes, the tilting timing may be delayed and the tilting may not be ready in time, or the tilting frequency may be too fast. However, there was a problem that efficient operation could not be performed, such as a decrease in melting time due to an increase in temperature.
【0012】また、特開平9−280536号に開示さ
れているような、溶融部にレベル検出用電極を設ける方
法では、炉内で高温による電極の溶解、溶融物の対流に
よる電極の摩耗や折れ、電極表面へのスラグの付着など
の問題が考えられ、またこれらの電極の損傷状態を外部
より検出することは困難なため、傾動タイミング時期制
御用に長期間安定して検出することに不安があるといっ
た問題があった。Further, in the method of disposing the level detecting electrode in the melting portion as disclosed in Japanese Patent Laid-Open No. 9-280536, the electrode is melted at a high temperature in the furnace, and the electrode is worn or broken due to convection of the melt. There is a problem such as adhesion of slag to the electrode surface, and since it is difficult to detect the damage state of these electrodes from the outside, there is concern about stable detection for a long time for tilt timing timing control. There was a problem like that.
【0013】本発明は、廃棄物溶融炉において溶融メタ
ルが堆積してきたことを、炉内にセンサを設置すること
なく精度良く確実に予測することが可能となり、溶融メ
タルの排出時期を、運転員の経験や勘に頼らずに知るこ
とができる廃棄物溶融炉の運転制御方法とその装置、特
に廃棄物プラズマ溶融処理炉の廃棄物溶融炉の運転制御
方法とその装置を提供することを目的とする。According to the present invention, it is possible to accurately and accurately predict the deposition of molten metal in a waste melting furnace without installing a sensor in the furnace, and to determine the discharge timing of molten metal by an operator. With the aim of providing an operation control method and an apparatus for a waste melting furnace, which can be known without relying on the experience and intuition, especially an operation control method and an apparatus for a waste melting furnace of a waste plasma melting treatment furnace. To do.
【0014】[0014]
【課題を解決するための手段】請求項1記載の発明は、
本発明の第1発明に対応するもので、スラグや溶融メタ
ルを区別する計量は排出サイクル毎に前記溶融スラグ下
方に堆積した溶融メタルを所定手段で排出する廃棄物溶
融処理炉において、直前の溶融メタルの排出時以降の現
サイクルにおける炉内に投入する廃棄物の投入量を計測
し、該計測した現サイクルの廃棄物投入総量が所定の既
定値を超えた場合に、溶融メタルの排出時期が来たと判
断するとともに、前記既定値が各排出サイクル毎に補正
されていることを特徴とする。The invention according to claim 1 is
It corresponds to the first invention of the present invention, and the weighing for distinguishing slag and molten metal is performed immediately before melting in a waste melting treatment furnace that discharges molten metal accumulated under the molten slag by a predetermined means in each discharge cycle. When the amount of waste input into the furnace in the current cycle after metal discharge is measured, and the total amount of waste input in the current cycle exceeds a predetermined preset value, the molten metal discharge timing is When it is judged that it came , the default value is corrected for each discharge cycle
It is characterized by being.
【0015】かかる発明によれば、溶融炉において溶融
メタルが堆積してきたことを、炉内にセンサを設置する
ことなく精度良く確実に予測することが可能となり、こ
れにより炉内より溶融メタルを排出時期を、運転員の経
験や勘に頼らずに知ることができる。尚、本発明は廃棄
物溶融炉の運転制御方法であってプラズマ廃棄物溶融炉
のみには限定されず、他の内部溶融炉、電気アーク炉に
も適用可能である。また、ここでいう廃棄物とは、ごみ
焼却炉での焼却残滓、主灰、飛灰を含み、その他溶融炉
で溶融処理する可能性のある廃棄物等をいう。According to the present invention, it is possible to accurately and surely predict that the molten metal has accumulated in the melting furnace without installing a sensor in the furnace, thereby discharging the molten metal from the furnace. You can know the time without depending on the experience and intuition of the operator. The present invention is a method for controlling the operation of the waste melting furnace and is not limited to the plasma waste melting furnace, but can be applied to other internal melting furnaces and electric arc furnaces. In addition, the term "waste" as used herein refers to waste, etc. that includes incineration residue in a refuse incinerator, main ash, and fly ash, and may be melt-processed in a melting furnace.
【0016】請求項2記載の発明は、請求項1記載の発
明の精度向上を図るために、各サイクル毎に溶融メタル
の排出時における溶融メタル量を計測し、少なくとも現
サイクルの計測値により廃棄物投入量当りの溶融メタル
量を求めることにより、次回溶融メタル排出時期を決め
る前記規定値を補正することを特徴とする。In order to improve the accuracy of the invention described in claim 1, the invention described in claim 2 measures the amount of molten metal at the time of discharging the molten metal in each cycle, and discards the measured value of at least the current cycle. It is characterized in that the specified value for determining the next molten metal discharge time is corrected by obtaining the molten metal amount per the material input amount.
【0017】かかる発明によれば、被溶融物の性状の季
節変動や経時的に変化した場合であっても、排出した溶
融メタル量より補正することができ、精度良い排出時期
を求めることができる。According to this invention, even if the properties of the material to be melted are seasonally changed or change with time, it can be corrected from the amount of molten metal discharged, and an accurate discharge timing can be obtained. .
【0018】請求項3記載の発明は前記請求項1記載の
発明を効果的に実施するための装置に関する発明で、直
前の溶融メタルの排出時以降の現サイクルにおける炉内
に投入する廃棄物の投入量を計測する手段と、該計測し
た現サイクルの廃棄物投入総量が所定の既定値とを比較
する手段と、該比較手段よりの信号に基づいて溶融メタ
ルの排出時期を設定する排出制御手段とを具えるととも
に、前記既定値が各排出サイクル毎に補正されているこ
とを特徴とする。The invention according to claim 3 relates to an apparatus for effectively carrying out the invention according to claim 1, wherein the waste to be charged into the furnace in the current cycle after the immediately preceding discharge of the molten metal is discharged. Means for measuring the input amount, means for comparing the measured total amount of waste input in the present cycle with a predetermined value, and discharge control means for setting the discharge timing of the molten metal based on a signal from the comparing means Tomo and comprises a door
In addition, the predetermined value is corrected for each discharge cycle .
【0019】請求項4記載の発明は前記請求項2記載の
発明を効果的に実施するための装置に関する発明で、各
サイクル毎の溶融メタルの排出時における溶融メタル量
を計測する手段と、各サイクルにおける炉内に投入する
廃棄物の投入量を計測する手段と、前記2つの検出手段
よりの検出信号に基づいて、次回溶融メタル排出時期を
決める前記規定値を補正する補正手段とを具えたことを
特徴とする。The invention according to claim 4 is an invention relating to an apparatus for effectively carrying out the invention according to claim 2, wherein means for measuring the molten metal amount at the time of discharging the molten metal in each cycle, and And a correction unit for correcting the specified value for determining the next molten metal discharge timing based on the detection signals from the two detection units. It is characterized by
【0020】請求項5記載の発明は本発明の第2発明に
対応するもので、定電流制御機能を有する直流電源装置
により定電流を流しながらプラズマ放電により廃棄物を
溶融処理する廃棄物溶融処理炉において、プラズマ電極
と炉底電極間の運転時の電圧変動を監視して、負方向の
瞬時的な電圧変動を検出して計数し、その単位時間当り
の発生回数が所定の規定回数を超える状態が所定の時間
継続した場合に、溶融メタルの排出時期が来たと判断す
ることを特徴とする。A fifth aspect of the present invention corresponds to the second aspect of the present invention, in which the waste is melted by plasma discharge while a constant current is applied by a DC power supply having a constant current control function to melt the waste. In the furnace, the voltage fluctuations during operation between the plasma electrode and the bottom electrode are monitored, and the instantaneous negative voltage fluctuations are detected and counted, and the number of occurrences per unit time exceeds the specified number of times. It is characterized in that when the state continues for a predetermined time, it is judged that the molten metal discharge time has come.
【0021】かかる発明によれば、溶融メタルの出滓重
量等を検知する特別なセンサは必要なく、プラズマ電極
に印加する直流電圧電源の電圧変動の状況より溶融メタ
ルが堆積してきたことを精度良く確実に検出することが
でき、溶融メタルを排出時期を、運転員の経験や勘に頼
らずに知ることができるのみならず、一時的な被溶融物
の性状変動にも対応することが出来、これにより最適な
廃棄物の投入制御や、異常判断等も検知可能となる。According to the present invention, no special sensor for detecting the weight of molten metal slag is required, and it is possible to accurately determine that the molten metal has accumulated due to the voltage fluctuation of the DC voltage source applied to the plasma electrode. It is possible to reliably detect, and not only know the molten metal discharge timing without relying on the experience and intuition of the operator, but it is also possible to deal with temporary changes in the properties of the molten material, This makes it possible to detect optimal waste input control and abnormality determination.
【0022】請求項6記載の発明は前記請求項5記載の
発明を効果的に実施するための装置に関する発明で、プ
ラズマ電極と炉底電極間の運転時の電圧変動を検出する
電圧変動検出手段と、該電圧変動より負方向の瞬時的な
電圧変動を検出して計数する計数手段と、その単位時間
当りの前記瞬時的な電圧変動発生回数が所定の規定回数
を超える状態が所定時間継続した場合に、溶融メタルの
排出時期が来たと判断する判断手段と、を具えたことを
特徴とする。The invention according to claim 6 relates to an apparatus for effectively carrying out the invention according to claim 5, which is a voltage fluctuation detecting means for detecting a voltage fluctuation during operation between the plasma electrode and the furnace bottom electrode. And a counting means for detecting and counting an instantaneous voltage fluctuation in the negative direction from the voltage fluctuation, and a state in which the number of occurrences of the instantaneous voltage fluctuation per unit time exceeds a predetermined prescribed number for a predetermined time. In this case, a determining means for determining that it is time to discharge the molten metal is provided.
【0023】請求項7記載の発明は前記第1発明と第2
発明の要旨を組み合わせてより精度良い溶融メタルの排
出時期を判断するもので、直前の溶融メタルの排出時以
降の現サイクルにおける炉内に投入する廃棄物の投入総
量に基づいて溶融メタルの排出時期を判断する第1の判
定手段と、プラズマ電極と炉底電極間の負方向の瞬時的
な電圧変動により溶融メタルの排出時期を判断する第2
の判定手段とを具え、いずれか一方若しくは両者の判定
信号に基づいて、溶融メタルの排出時期を判断すること
を特徴とする。The invention according to claim 7 is the first invention and the second invention.
A more accurate determination of the molten metal discharge timing is made by combining the gist of the invention, and the molten metal discharge timing is based on the total amount of waste input into the furnace in the current cycle after the immediately preceding molten metal discharge. And a second determining means for determining the discharge timing of the molten metal based on the instantaneous negative voltage fluctuation between the plasma electrode and the furnace bottom electrode.
And determining the discharge timing of the molten metal based on one or both of the determination signals.
【0024】かかる発明によれば、前記2つの発明を組
み合わせて、互いにバックアップ、補完することがで
き、より信頼性の高い排出時期の判断と運転制御装置を
提供することができる。According to this invention, the above two inventions can be combined to back up and complement each other, and it is possible to provide a more reliable discharge timing determination and operation control device.
【0025】[0025]
【発明の実施の形態】以下、本発明を図に示した実施形
態を用いて詳細に説明する。但し、この実施形態に記載
される構成部品の種類、材質、形状、その相対配置、及
び動作手順などは特に特定的な記載が無い限り、この発
明の範囲をそれのみに限定する趣旨ではなく単なる説明
例に過ぎない。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below with reference to the embodiments shown in the drawings. However, unless otherwise specified, the types, materials, shapes, relative arrangements, and operating procedures of the constituent parts described in this embodiment are not intended to limit the scope of the present invention thereto, but are merely It is only an example.
【0026】図1は本発明の第1の実施の形態に係るプ
ラズマ灰溶融炉の運転制御装置の全体構成図で、同図を
基に本発明を説明する。図中で図5と同一符号は同一機
能部品若しくは部位を示し、その部分の詳細な説明は省
略する。図中1は、プラズマ灰溶融炉で、炉内に溶融ス
ラグ9と溶融メタル10が堆積しているとともに、溶融
スラグ9と対応する炉側部に出滓樋3が取り付けられて
いる。8はスラグ搬送コンベヤで、出滓樋3より溢れ出
るように連続的に流れ出した溶融スラグ9を搬送しなが
ら徐々に空冷する。空冷されたスラグや溶融メタル10
は重量計量装置22で計測され、その重量計測信号を溶
融メタル量演算装置に送り、所定の演算と測定を行な
う。FIG. 1 is an overall configuration diagram of an operation control device for a plasma ash melting furnace according to a first embodiment of the present invention. The present invention will be described based on the diagram. In the figure, the same reference numerals as those in FIG. 5 denote the same functional parts or parts, and detailed description of those parts will be omitted. In the figure, reference numeral 1 denotes a plasma ash melting furnace in which molten slag 9 and molten metal 10 are deposited in the furnace, and a slag gutter 3 is attached to the side of the furnace corresponding to the molten slag 9. Reference numeral 8 denotes a slag transporting conveyor, which gradually cools the molten slag 9 that is continuously flowing out so as to overflow from the slag gutter 3 while it is being transported. Air-cooled slag and molten metal 10
Is measured by the weight measuring device 22, and the weight measurement signal is sent to the molten metal amount calculating device to perform predetermined calculation and measurement.
【0027】スラグや溶融メタルを区別する計量は、炉
の傾動の有無より容易に判定できる。即ち、炉1の傾動
開始後、搬送コンベヤ8上に溶融メタル(金属)10が
出たタイミングから、コンベヤ8の送り速度とコンベヤ
長さを考慮することで、溶融メタル(金属)10がコン
ベヤ出口端へ到達する時間が判り、溶融メタル10の計
測開始タイミングを得ることができるので、溶融スラグ
9と区別して計測ができる。また、磁石で選別する磁選
装置や、磁気での金属判定装置、画像処理判別装置など
の溶融メタル選別器を設置して正確に分別すれば、溶融
メタル量をより正確に計量できる。これにより、傾動期
間中に排出された溶融メタル(金属)10の総量を溶融
メタル計量装置38で円滑に求めることができる。The weighing for distinguishing the slag and the molten metal can be easily determined by the presence or absence of tilting of the furnace. That is, after the start of tilting of the furnace 1, the molten metal (metal) 10 is taken out from the conveyor exit by considering the feed speed and the conveyor length of the conveyor 8 from the timing at which the molten metal (metal) 10 comes out on the conveyor 8. Since the time to reach the end can be known and the measurement start timing of the molten metal 10 can be obtained, the measurement can be performed separately from the molten slag 9. Further, the amount of molten metal can be measured more accurately if a magnetic separation device for selecting with a magnet, a metal determination device with magnetism, a molten metal selector such as an image processing determination device is installed and accurately sorted. Thereby, the total amount of the molten metal (metal) 10 discharged during the tilting period can be smoothly obtained by the molten metal measuring device 38.
【0028】25は炉押し上げ機構で、傾動制御装置3
5よりの信号に基づいて操作盤37よりの指示にて所定
タイミングで支点26を中心に炉1の傾動を行なう。2
は直流電源装置で、炉上部より挿設された主電極(プラ
ズマ電極)5と炉底電極6間で、窒素ガス18が充填さ
れた炉内でプラズマ17を放電を行なう(図3参照)。
7は炉上部に設けた灰投入口で、その上部に投入量計測
装置21を介して灰投入装置12が設けられている。傾
動制御装置35には、傾動時期投入量記憶装置32と投
入量積算装置33よりの信号を比較器34で比較してそ
の比較信号により制御される。Reference numeral 25 is a furnace pushing-up mechanism, which is a tilt control device 3
The furnace 1 is tilted around the fulcrum 26 at a predetermined timing according to an instruction from the operation panel 37 based on the signal from the control unit 5. Two
Is a DC power supply device, which discharges plasma 17 in a furnace filled with nitrogen gas 18 between a main electrode (plasma electrode) 5 and a furnace bottom electrode 6 inserted from the upper part of the furnace (see FIG. 3).
Reference numeral 7 denotes an ash charging port provided on the upper part of the furnace, and an ash charging device 12 is provided on the ash charging port via a charging amount measuring device 21. The tilt control device 35 is controlled by the comparison signal obtained by comparing the signals from the tilt timing input amount storage device 32 and the input amount integrating device 33 with the comparator 34.
【0029】傾動時期投入量記憶装置32には手動設定
器31と投入量補正装置39が取り付けられており、こ
れらの信号が該記憶装置32に入力される。尚、図中3
6は表示盤、37は操作盤で、夫々傾動制御装置35に
接続されている。The tilting timing input amount storage device 32 is provided with a manual setting device 31 and an input amount correction device 39, and these signals are input to the storage device 32. In addition, 3 in the figure
Reference numeral 6 is a display panel, and 37 is an operation panel, which are connected to the tilt control device 35, respectively.
【0030】かかる装置において、灰投入量計量装置2
1を灰投入装置12に設置して炉内に投入される灰の量
を計測し、投入量積算装置33で各バッチ(各傾動タイ
ミング間隔)毎の投入総量を計測する。傾動時期投入総
量を設定された傾動時期投入量記憶装置32の設定値
と、投入量積算装置33の積算値を比較器34によって
比較し、積算値が設定値を超えた場合に比較器34は傾
動制御装置35に傾動時期が来たことを通知する。傾動
制御装置35は、表示盤36に傾動時期が来たことを表
示し、運転員は操作盤37より傾動操作指示を出すこと
により傾動作業へ入る。傾動制御装置35は自動的に傾
動操作を行なっても良い。In such a device, the ash input measuring device 2
1 is installed in the ash feeding device 12 to measure the amount of ash charged into the furnace, and the charging amount integration device 33 measures the total charging amount for each batch (each tilting timing interval). The comparator 34 compares the set value of the tilting timing input amount storage device 32 for which the total tilting amount input has been set with the integrated value of the input amount integrating device 33. If the integrated value exceeds the set value, the comparator 34 The tilt control device 35 is notified that the tilt time has come. The tilt control device 35 displays on the display panel 36 that the tilting time has come, and the operator enters the tilting work by issuing a tilting operation instruction from the operation panel 37. The tilt control device 35 may automatically perform the tilting operation.
【0031】傾動時期投入量記憶装置32へ投入量の設
定は手動設定器31により、運転員が手入力により設定
する。設定値は、経験豊かな運転員の経験値によって決
定したり、投入灰を分析して含まれる金属成分から投入
総量を求めることができる。また、運転員は作業計画、
当直人員を考慮してから傾動操作を始めることができる
ように、表示板36に傾動の表示がされても傾動操作に
入るまでに、数時間から1日程度の余裕があるように総
投入量の設定をする必要がある。例えば、夜間に傾動時
期到達の表示が出た場合に、当直人員の多い日中の運転
で傾動操作を行なうなどの判断ができるようにするため
である。しかし、傾動操作を傾動制御装置35により全
自動で行なう場合は、確認のため表示盤36に表示を行
なうが、傾動操作に関しては傾動制御装置35が行なう
ためこの限りではない。The setting of the input amount in the tilting timing input amount storage device 32 is manually performed by the operator using the manual setting device 31. The set value can be determined based on the experience value of an experienced operator, or the input amount can be calculated from the metal components contained by analyzing the input ash. In addition, the operator has a work plan,
So that the tilting operation can be started after considering the shift personnel, even if the tilting is displayed on the display board 36, there is a margin of several hours to one day before the tilting operation is started. It is necessary to set. This is because, for example, when a display indicating that the tilting time has been reached is displayed at night, it is possible to make a judgment such as performing tilting operation during daytime driving with a lot of shift personnel. However, when the tilting control device 35 performs the tilting operation fully automatically, the display is displayed on the display panel 36 for confirmation, but the tilting control device 35 performs the tilting operation.
【0032】傾動作業とは、図2に示すように炉1を傾
けて炉内に蓄積された溶融メタル(金属)10を炉外へ
排出することである。溶融炉底部の片側に動作時の支点
26となる蝶番が具備されており、反対側には油圧ジャ
ッキ、電動シリンダなどで構成される炉押し上げ機構2
5が具備されている。これにより炉1の片側を持ち上げ
ることで支点26を軸に炉1を傾かせることができ、徐
々に炉1を傾けていき、炉1に設定された所定角度(2
0〜40°)まで傾ける。溶融メタル10の排出が終了
したら、炉1を元に戻す。投入量積算装置33へ傾動制
御装置35よりリセット信号を送り、積算計を零に初期
化してから灰投入を開始して溶融運転を再開する。The tilting work is to tilt the furnace 1 as shown in FIG. 2 and discharge the molten metal 10 accumulated in the furnace to the outside of the furnace. A hinge serving as a fulcrum 26 during operation is provided on one side of the bottom of the melting furnace, and a furnace pushing-up mechanism 2 including a hydraulic jack, an electric cylinder, etc. is provided on the other side.
5 are provided. Thus, by lifting one side of the furnace 1, the furnace 1 can be tilted about the fulcrum 26, the furnace 1 is gradually tilted, and the predetermined angle (2
Tilt from 0 to 40 °). After discharging the molten metal 10, the furnace 1 is returned to the original state. The tilt control device 35 sends a reset signal to the charging amount accumulating device 33 to initialize the accumulator to zero, and then starts ash charging and restarts the melting operation.
【0033】傾動により、溶融メタル(金属)10は通
常溶融スラグ9が排出されている出滓樋3を通って冷却
コンベヤ8上へ導かれる。コンベヤ8上で冷却された溶
融メタル(金属)10はコンベヤ端で回収されるが、こ
こに設置された計量装置22によって排出された溶融メ
タル重量を計測することができる。溶融メタル重量の、
溶融スラグ9と区別した精度良い計測は、前記方法によ
り正確に計量できる。これにより、傾動期間中に排出さ
れた溶融メタル10の総重量を溶融メタル計量装置38
で求めることができる。By tilting, the molten metal (metal) 10 is guided onto the cooling conveyor 8 through the slag gutter 3 from which the molten slag 9 is usually discharged. The molten metal (metal) 10 cooled on the conveyor 8 is collected at the end of the conveyor, and the weight of the molten metal discharged by the weighing device 22 installed here can be measured. Of molten metal weight,
The accurate measurement that is distinguished from the molten slag 9 can be accurately measured by the above method. As a result, the total weight of the molten metal 10 discharged during the tilting period is determined by the molten metal measuring device 38.
Can be found at.
【0034】一方、炉1の傾動角度は、炉押し上げ機構
25のリフト量から容易に求められ、この傾動角度と炉
内形状の計算により炉内に残された溶融メタル重量が判
るので、排出された溶融メタル(金属)量と合わせて傾
動直前の炉内の溶融メタル重量を知ることができる。On the other hand, the tilt angle of the furnace 1 can be easily obtained from the lift amount of the furnace pushing-up mechanism 25, and the weight of the molten metal left in the furnace can be known from the calculation of the tilt angle and the shape of the furnace. It is possible to know the weight of molten metal in the furnace immediately before tilting together with the amount of molten metal (metal).
【0035】又、前回傾動時に炉内に残っていた溶融メ
タル重量が判ることから、前回傾動から今回傾動までに
増加した溶融メタル重量も判り、その前回/今回の傾動
タイミング間の灰投入量も灰投入量積算装置33により
判ることから、灰単位重量当りに含まれる金属成分を求
めることができる。Further, since the weight of the molten metal remaining in the furnace at the time of the previous tilting is known, the weight of the molten metal increased from the previous tilting to the current tilting is also known, and the ash input amount between the previous and current tilting timings is also known. The metal component contained in the ash unit weight can be obtained from the ash addition amount integrating device 33.
【0036】廃棄物の焼却灰の場合、そのもととなる廃
棄物の組成は一定でなく、収集される時期や収集先など
の要因で組成が変化することがある為、溶融メタル(金
属)10の増加速度が変ることがある。しかしながら本
実施例によれば、前述のようにして、灰単位重量当りの
金属成分含有量を各傾動タイミングサイクル毎に計測し
て管理することで、各傾動タイミングサイクル間で金属
成分が増加の傾向に有れば傾動時期投入量を減らし、減
少してくれば傾動時期投入量を増加させるような補正を
することも可能である。In the case of waste incineration ash, the composition of the waste that is the source of the ash is not constant, and the composition may change depending on factors such as the time of collection and the collection destination. The rate of increase of 10 may change. However, according to the present embodiment, as described above, by measuring and managing the metal component content per unit weight of ash for each tilt timing cycle, the metal component tends to increase during each tilt timing cycle. It is also possible to make a correction such that the tilting period input amount is decreased if it is, and the tilting period input amount is increased if it is decreasing.
【0037】投入量補正装置39にはかかるロジックを
組込んだ投入量補正回路(プログラム)が組み込まれて
おり、これにより溶融する灰の組成が変化した場合でも
傾動時期を適切に設定できる。The input amount correction device 39 incorporates an input amount correction circuit (program) incorporating such a logic, whereby the tilting timing can be appropriately set even when the composition of the molten ash changes.
【0038】次に図3、図4により、本発明の第二の実
施の形態を示す。図3はプラズマ溶融炉の電極先端付近
を拡大して示した要部構成図(1)と、その右側に電気
的な等価回路(2)を示す。等価回路に示すように、ス
ラグ抵抗Rsは大きく、メタル抵抗Rmは小さい。電極
5の中央にはプラズマ作動ガス18となる不活性ガス
(例えば窒素ガス)が通る穴5aが空いており電極5先
端より吹出している。溶融スラグ9表面はプラズマ流1
7やプラズマ作動ガス18を吹き付けられるだけでな
く、投入される灰が塊となって落ちた場合や、灰中の成
分がプラズマの高熱によりガス化する等の理由により表
面は少なからず波立っている。Next, FIGS. 3 and 4 show a second embodiment of the present invention. FIG. 3 is a main part configuration diagram (1) enlarging and showing the vicinity of the electrode tip of the plasma melting furnace, and an electrical equivalent circuit (2) is shown on the right side thereof. As shown in the equivalent circuit, the slag resistance Rs is large and the metal resistance Rm is small. A hole 5a through which an inert gas (for example, nitrogen gas) serving as the plasma working gas 18 passes is formed in the center of the electrode 5 and is blown out from the tip of the electrode 5. Surface of molten slag 9 is plasma flow 1
7 and the plasma working gas 18 are not only sprayed, but also when the ash that is thrown in falls as a lump, or the components in the ash are gasified due to the high heat of the plasma, the surface is not a little wavy. There is.
【0039】溶融スラグ層9の厚さが薄くなってくる
と、表面が波立った時に溶融スラグ層9の厚さが非常に
薄くなり、時として部分的に溶融メタル(金属)層10
がむき出しに近くなる。この場合、プラズマ電極5から
のプラズマ電流17は直接溶融メタル(金属)10に流
れることとなる。電気回路的には溶融スラグ部分の電気
抵抗Rsが零になったのと等しい。プラズマ溶融炉1の
直流電源装置2が、設定された電流量を流すように制御
する定電流電源装置である場合、回路上の抵抗値(Rc
+Rg+Rs+Rm)が変化すると、一定電流が流れて
いることから、溶融炉に印加されている電圧が変化す
る。(オームの法則:V=I×Rによる)As the thickness of the molten slag layer 9 becomes thinner, the thickness of the molten slag layer 9 becomes extremely thin when the surface is wavy, and sometimes the molten metal (metal) layer 10 partially forms.
It's almost exposed. In this case, the plasma current 17 from the plasma electrode 5 directly flows into the molten metal (metal) 10. In terms of electric circuit, it is equal to the electric resistance Rs of the molten slag portion becoming zero. When the DC power supply device 2 of the plasma melting furnace 1 is a constant current power supply device that controls so that a set amount of current flows, the resistance value (Rc
When + Rg + Rs + Rm) changes, the voltage applied to the melting furnace changes because a constant current flows. (Ohm's law: V = I × R)
【0040】そのため、溶融スラグ層9が薄くなってき
て、溶融スラグ面が波立った場合にプラズマ電極5直下
で溶融メタル(金属)層10部分が液面に顔を出すと、
全抵抗(Rc+Rg+Rs+Rm)でスラグ抵抗Rsが
占める比率は比較的大きい為、急激な電圧低下が発生す
る。しかしこの状態は長く続かずに、波の山の部分が来
ると溶融スラグ層9が間に入り、電圧は上昇して元に戻
るという現象が起きる。このような電圧変化を、以下で
は下方スパイクと呼ぶ。Therefore, when the molten slag layer 9 becomes thinner and the molten slag surface becomes wavy, when the molten metal (metal) layer 10 portion appears directly below the plasma electrode 5,
Since the ratio of the slag resistance Rs to the total resistance (Rc + Rg + Rs + Rm) is relatively large, a sharp voltage drop occurs. However, this state does not last for a long time, and when the peak of the wave comes, the molten slag layer 9 intervenes and the voltage rises and returns to the original state. Hereinafter, such a voltage change is referred to as a downward spike.
【0041】図4に図3(2)の等価回路に基づいて直
流電圧電源の電圧変動を計測した波形グラフ図を示す。
図4(1)は溶融メタル(金属)10が多い場合であ
り、下方スパイクが発生しているのが判る。図4(2)
は溶融メタル(金属)10が少ない場合であり、多少の
変動はあるものの、安定しておりスパイク状の電圧変動
は発生していない。従って、図3(2)の等価回路にお
いて、プラズマ電極5と炉底電極6との間に電圧計40
を介在させて、その検知電圧を電圧変動監視装置41に
送り、該監視装置41で電源電圧の変化を監視し、予め
設定された電圧変動が発生した場合に所定のカウンタ信
号を計数装置42に出すようになっている。FIG. 4 is a waveform graph diagram in which the voltage fluctuation of the DC voltage power supply is measured based on the equivalent circuit of FIG. 3 (2).
FIG. 4 (1) shows a case where the molten metal (metal) 10 is large, and it can be seen that a downward spike is generated. Figure 4 (2)
Indicates a case where the molten metal (metal) 10 is small, and although there is some variation, it is stable and no spike-like voltage variation occurs. Therefore, in the equivalent circuit of FIG. 3 (2), a voltmeter 40 is provided between the plasma electrode 5 and the furnace bottom electrode 6.
Is sent to the voltage fluctuation monitoring device 41, the monitoring device 41 monitors changes in the power supply voltage, and a predetermined counter signal is sent to the counting device 42 when a preset voltage fluctuation occurs. It is supposed to be released.
【0042】本実施例では下方スパイクを検出するため
監視装置41への設定は、電圧の下降値:Vdown[V]以
上、電圧の変化率:dV/dt[v/s]以上、低下時間幅T[s]
以下を設定しておき、この条件に該当する信号変化が有
った場合に信号を出すようになっている。一例として
は、電圧下降値:30[V]以上、電圧の変化率:5[v/s]
以上、低下時間幅15[s]以下があげられる。しかし、
被溶融物の粘性、性状(特に電気抵抗など)、運転電
圧、運転電流量、溶融処理量などによってこれらの値は
変化する為、あくまでもこの値は一例であって本発明を
限定するものではない。In the present embodiment, in order to detect the downward spike, the monitoring device 41 is set so that the voltage drop value: Vdown [V] or more, the voltage change rate: dV / dt [v / s] or more, the fall time width. T [s]
The following is set and a signal is output when there is a signal change corresponding to this condition. As an example, voltage drop value: 30 [V] or more, voltage change rate: 5 [v / s]
As described above, the reduction time width is 15 [s] or less. But,
Since these values change depending on the viscosity and properties of the material to be melted (especially electric resistance), operating voltage, operating current amount, melting treatment amount, etc., these values are merely examples and do not limit the present invention. .
【0043】下方スパイク計数装置42では電圧変動監
視装置41の出力カウンタ信号を各傾動タイミング間隔
毎でカウントして積算していく。傾動時期判断装置43
は下方スパイク計数装置42のカウント値を定期的に取
込み記憶する。取込んだ後、リセット信号を出力して下
方スパイク計数装置42のカウント値を零に戻す。判断
装置43では、運転状況を判断し、通常の灰投入運転中
に時間当りの下方スパイク発生数が所定の値を超えた場
合に傾動時期として判断する。例えば、1時間当りの下
方スパイク発生数が50回を超え、その状態が5時間以
上続いた場合には傾動時期がきたとして判断する(かか
る判断時期本例も本発明を限定するものではない)。こ
の検出信号は傾動制御装置35へ入力され、後の処理は
前記実施例1で説明したものと同様に処理されるので、
ここでは詳しい説明は省略する。The lower spike counter 42 counts and integrates the output counter signal of the voltage fluctuation monitor 41 at each tilt timing interval. Tilt timing determination device 43
Periodically fetches and stores the count value of the lower spike counting device 42. After capturing, a reset signal is output to reset the count value of the lower spike counting device 42 to zero. The determination device 43 determines the operation status, and determines the tilting timing when the number of downward spikes generated per hour during a normal ash charging operation exceeds a predetermined value. For example, when the number of downward spikes generated per hour exceeds 50 times and the state continues for 5 hours or more, it is determined that the tilting timing has come (this determining timing does not limit the present invention). . This detection signal is input to the tilt control device 35, and the subsequent processing is the same as that described in the first embodiment, so
Detailed description is omitted here.
【0044】このような方法を用いることにより、灰投
入量を計測しなくとも傾動時期を検出することができ
る。一時的に金属成分を多く含む灰を溶融した場合に
は、設定された灰投入量に達する前に電圧変動の徴候が
現れるので、遅れることなく傾動時期を検出することが
できる。By using such a method, the tilting timing can be detected without measuring the ash input amount. When the ash containing a large amount of metal components is temporarily melted, a sign of voltage fluctuation appears before the set ash input amount is reached, so that the tilting timing can be detected without delay.
【0045】また、第1の実施例の検出方法と第2の実
施例の検出方法を両方とも組み入れた運転制御装置とす
ることで、互いにバックアップ、補完することができ、
より信頼性の高い判断方法と運転制御装置を提供するこ
とができる。Further, by providing the operation control device incorporating both the detection method of the first embodiment and the detection method of the second embodiment, it is possible to back up and complement each other.
A more reliable determination method and operation control device can be provided.
【0046】本実施例では、被溶融物としてごみ焼却炉
の焼却飛灰、残渣を溶融するプラズマ灰溶融炉を対象と
しているが、焼却残渣、飛灰以外の廃棄物など被溶融物
中に金属成分を含む物質を溶融処理する他の廃棄物のプ
ラズマ溶融炉の場合にも本発明を適用することはでき
る。また、本実施例では、溶融メタルの排出方法として
傾動を対象としたが、タップホールを開け、炉底から出
湯する方式による溶融メタル排出方法など他の排出方法
においても、本発明を適用することができる。In the present embodiment, the incineration fly ash of the refuse incinerator and the plasma ash melting furnace that melts the residue are targeted as the objects to be melted. The present invention can also be applied to the case of another waste plasma melting furnace in which a substance containing components is melt-processed. Further, in the present embodiment, tilting is targeted as the molten metal discharging method, but the present invention can be applied to other discharging methods such as a molten metal discharging method in which a tap hole is opened and tapped from the furnace bottom. You can
【0047】[0047]
【発明の効果】以上記載のごとく本第1発明によれば、
溶融炉において溶融メタルが堆積してきたことを、炉内
にセンサを設置することなく精度良く確実に予測するこ
とが可能となり、これにより炉内より溶融メタルを排出
する傾動作業開始時期を、運転員の経験や勘に頼らずに
知ることができる。この場合、請求項2、4記載の発明
を組み込むことにより、被溶融物の性状の季節変動や経
時的に変化した場合であっても、排出した溶融メタル量
より補正することができ、精度良い傾動開始時期を求め
ることができる。尚、これらの発明はプラズマ廃棄物溶
融炉のみには限定されず、他の内部溶融炉、電気アーク
炉にも適用可能である。As described above, according to the first aspect of the present invention,
It is possible to accurately and accurately predict the deposition of molten metal in the melting furnace without installing a sensor in the furnace, which allows the operator to determine the tilt operation start time for discharging molten metal from the furnace. You can learn without relying on your experience and intuition. In this case, by incorporating the inventions of claims 2 and 4, even if the property of the material to be melted is seasonally changed or changes with time, it can be corrected from the discharged molten metal amount and the accuracy is high. The tilt start time can be calculated. These inventions are not limited to the plasma waste melting furnace, but can be applied to other internal melting furnaces and electric arc furnaces.
【0048】更に第2発明によれば、溶融メタルの出滓
重量等を検知する特別なセンサは必要なく、プラズマ電
極に印加する直流電圧電源の電圧変動の状況より溶融メ
タルが堆積してきたことを精度良く確実に検出すること
ができ、溶融メタルを排出する傾動作業開始時期を、運
転員の経験や勘に頼らずに知ることができるのみなら
ず、一時的な被溶融物の性状変動にも対応することが出
来、これにより最適な廃棄物の投入制御や、異常判断等
も検知可能である。Further, according to the second aspect of the invention, no special sensor for detecting the weight of molten metal slag is required, and the molten metal is deposited due to the voltage fluctuation of the DC voltage power source applied to the plasma electrode. It is possible to detect accurately and reliably, and to know the start time of the tilting operation for discharging molten metal without relying on the experience and intuition of the operator, as well as temporary property changes of the melted object. Therefore, it is possible to detect optimal waste input control and abnormality determination.
【0049】更に第3発明によれば、前記2つの発明を
併用することで、互いにバックアップ、補完することが
でき、より信頼性の高い排出時期の判断と運転制御装置
を提供することができる。Further, according to the third aspect of the present invention, by using the above two aspects together, it is possible to back up and complement each other, and it is possible to provide a more reliable discharge timing determination and operation control device.
【図1】 図1は本発明の第1の実施の形態に係るプラ
ズマ灰溶融炉の運転制御装置の全体構成図である。FIG. 1 is an overall configuration diagram of an operation control device for a plasma ash melting furnace according to a first embodiment of the present invention.
【図2】 炉の傾動動作を示す作用説明図である。FIG. 2 is an operation explanatory view showing a tilting operation of the furnace.
【図3】 本発明の第2の実施形態を説明する図で、
(1)はプラズマ溶融炉の電極先端付近を拡大して示し
た要部構成図、(2)は電気的な等価回路を示す。FIG. 3 is a diagram illustrating a second embodiment of the present invention,
(1) is an enlarged schematic view of the vicinity of the electrode tip of the plasma melting furnace, and (2) shows an electrical equivalent circuit.
【図4】 図3(2)の等価回路に基づいて直流電圧電
源の電圧変動を計測した電圧変動波形のグラフ図を示
し、(1)は溶融メタル(金属)が多い場合、(2)は
溶融メタル(金属)が少ない場合を示す。FIG. 4 shows a graph of a voltage fluctuation waveform obtained by measuring the voltage fluctuation of the DC voltage power supply based on the equivalent circuit of FIG. 3 (2). The case where the amount of molten metal (metal) is small is shown.
【図5】 従来技術の係るプラズマ灰溶融炉の全体構成
図である。FIG. 5 is an overall configuration diagram of a plasma ash melting furnace according to a conventional technique.
1 溶融炉 2 直流電源装置 3 出滓樋 5 主電極(プラズマ電極) 6 炉底電極 7 投入口 8 搬送コンベヤ 9 溶融スラグ 10 溶融メタル(金属) 12 灰投入装置 14 投入量積算表示装置 15 重量表示器 21 投入量計測装置 22 重量計量装置 25 炉押し上げ機構 31 手動設定器 32 傾動時期投入量記憶装置 33 投入量積算装置 34 比較器 35 傾動制御装置 37 操作盤 38 溶融メタル計量装置 39 投入量補正装置 40 電圧計 41 電圧変動監視装置 42 下方スパイク計数装置 43 傾動時期判断装置 1 melting furnace 2 DC power supply 3 Debris gutter 5 Main electrode (plasma electrode) 6 Furnace bottom electrode 7 slot 8 Conveyor 9 Molten slag 10 Molten metal 12 Ash feeding device 14 Input amount integration display 15 Weight indicator 21 Input amount measuring device 22 Weighing device 25 furnace lifting mechanism 31 Manual setting device 32 Tilt timing input amount storage device 33 Input amount integrating device 34 Comparator 35 Tilt control device 37 Operation panel 38 Molten metal measuring device 39 Input amount correction device 40 Voltmeter 41 Voltage fluctuation monitoring device 42 Downward spike counter 43 Tilt timing determination device
フロントページの続き (72)発明者 和田 恭子 神戸市兵庫区和田崎町一丁目1番1号 三菱重工業株式会社神戸造船所内 (56)参考文献 特開 平10−332268(JP,A) 特開 平10−185155(JP,A) 特開 平10−246415(JP,A) 特開 平3−127486(JP,A) 特開 昭60−216112(JP,A) 特開 昭61−168719(JP,A) 特開 昭57−184820(JP,A) 特開 平10−332123(JP,A) 特開 平9−280536(JP,A) (58)調査した分野(Int.Cl.7,DB名) F23G 5/50 F23G 5/00 115 F23J 1/00 F23J 1/08 F27B 3/19 F27B 3/28 Front page continuation (72) Inventor Kyoko Wada 1-1-1, Wadasaki-cho, Hyogo-ku, Kobe Mitsubishi Heavy Industries, Ltd. Kobe Shipyard (56) Reference JP-A-10-332268 (JP, A) JP-A 10-185155 (JP, A) JP 10-246415 (JP, A) JP 3-127486 (JP, A) JP 60-216112 (JP, A) JP 61-168719 (JP, A) JP 57-184820 (JP, A) JP 10-332123 (JP, A) JP 9-280536 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) ) F23G 5/50 F23G 5/00 115 F23J 1/00 F23J 1/08 F27B 3/19 F27B 3/28
Claims (7)
サイクル毎に前記溶融スラグ下方に堆積した溶融メタル
を所定手段で排出する廃棄物溶融処理炉において、 直前の溶融メタルの排出時以降の現サイクルにおける炉
内に投入する廃棄物の投入量を計測し、該計測した現サ
イクルの廃棄物投入総量が所定の既定値を超えた場合
に、溶融メタルの排出時期が来たと判断するとともに、
前記既定値が各排出サイクル毎に補正されていることを
特徴とするプラズマ溶融炉の運転制御方法。1. A waste melting treatment furnace which discharges molten metal accumulated under the molten slag by a predetermined means in each discharge cycle for measuring the difference between slag and molten metal. The amount of waste to be put into the furnace in the cycle is measured, and when the measured total amount of waste input in the current cycle exceeds a predetermined predetermined value, it is determined that the discharge time of the molten metal has come ,
The operation control method for a plasma melting furnace, wherein the predetermined value is corrected for each discharge cycle .
ける溶融メタル量を計測し、少なくとも現サイクルの計
測値により廃棄物投入量当りの溶融メタル量を求めるこ
とにより、次回溶融メタル排出時期を決める前記規定値
を補正することを特徴とする請求項1記載のプラズマ溶
融炉の運転制御方法。2. The next molten metal discharge time is determined by measuring the molten metal amount at the time of discharging the molten metal for each cycle and determining the molten metal amount per waste input amount based on at least the measured value of the current cycle. The operation control method for a plasma melting furnace according to claim 1, wherein the specified value is corrected.
ラグを排出するとともに、任意に設定した排出サイクル
毎に前記溶融スラグ下方に堆積した溶融メタルを所定手
段で排出する廃棄物溶融処理炉において、 直前の溶融メタルの排出時以降の現サイクルにおける炉
内に投入する廃棄物の投入量を計測する手段と、該計測
した現サイクルの廃棄物投入総量が所定の既定値とを比
較する手段と、該比較手段よりの信号に基づいて溶融メ
タルの排出時期を設定する排出制御手段とを具えるとと
もに、前記既定値が各排出サイクル毎に補正されている
ことを特徴とするプラズマ溶融炉の運転制御装置。3. A waste melting treatment in which the waste is melted and the molten slag is discharged from a slag spout, and the molten metal accumulated under the molten slag is discharged by a predetermined means in each arbitrarily set discharge cycle. In the furnace, compare the means to measure the amount of waste input into the furnace in the current cycle after the last molten metal discharge and the measured total amount of waste input in the current cycle to a predetermined value. and means, when comprising a discharge control means for setting a discharge time of the molten metal on the basis of a signal from said comparing means DOO
In addition, the operation control device for a plasma melting furnace , wherein the predetermined value is corrected for each discharge cycle .
ける溶融メタル量を計測する手段と、各サイクルにおけ
る炉内に投入する廃棄物の投入量を計測する手段と、前
記2つの検出手段よりの検出信号に基づいて、次回溶融
メタル排出時期を決める前記規定値を補正する補正手段
とを具えたことを特徴とする請求項3記載のプラズマ溶
融炉の運転制御装置。4. A means for measuring the amount of molten metal at the time of discharging molten metal in each cycle, a means for measuring the amount of waste to be charged into the furnace in each cycle, and the two detection means. The operation control device for a plasma melting furnace according to claim 3, further comprising a correction unit that corrects the specified value that determines the next molten metal discharge timing based on the detection signal.
極間に、定電流制御機能を有する直流電源装置により定
電流を流しながらプラズマ放電により廃棄物を溶融処理
して出滓口より溶融スラグを排出するとともに、任意に
設定した排出サイクル毎に前記溶融スラグ下方に堆積し
た溶融メタルを所定手段で排出する廃棄物溶融処理炉に
おいて、 プラズマ電極と炉底電極間の運転時の電圧変動を監視し
て、負方向の瞬時的な電圧変動を検出して計数し、その
単位時間当りの発生回数が所定の規定回数を超える状態
が所定の時間継続した場合に、溶融メタルの排出時期が
来たと判断することを特徴とするプラズマ溶融炉の運転
制御方法。5. The waste is melted by plasma discharge while being supplied with a constant current by a direct current power supply device having a constant current control function between the plasma electrode inserted from the top of the furnace and the bottom electrode, and melted from the outlet. In the waste melting furnace, which discharges the slag and discharges the molten metal accumulated under the molten slag by a predetermined means in each discharge cycle set arbitrarily, the voltage fluctuation during operation between the plasma electrode and the bottom electrode By monitoring and detecting instantaneous voltage fluctuations in the negative direction and counting, and when the number of occurrences per unit time exceeds the specified number of times for a certain period of time, the molten metal discharge timing comes. A method for controlling the operation of a plasma melting furnace, which is characterized in that
極間に、定電流制御機能を有する直流電源装置により定
電流を流しながらプラズマ放電により廃棄物を溶融処理
して出滓口より溶融スラグを排出するとともに、任意に
設定した排出サイクル毎に前記溶融スラグ下方に堆積し
た溶融メタルを所定手段で排出する廃棄物溶融処理炉に
おいて、 プラズマ電極と炉底電極間の運転時の電圧変動を検出す
る電圧変動検出手段と、該電圧変動より負方向の瞬時的
な電圧変動を検出して計数する計数手段と、その単位時
間当りの前記瞬時的な電圧変動発生回数が所定の規定回
数を超える状態が所定時間継続した場合に、溶融メタル
の排出時期が来たと判断する判断手段と、を具えたこと
を特徴とするプラズマ溶融炉の運転制御装置。6. The waste is melted by plasma discharge while being supplied with a constant current by a direct current power supply device having a constant current control function between the plasma electrode inserted from above the furnace and the bottom electrode, and melted from the outlet. In the waste melting furnace, which discharges the slag and discharges the molten metal accumulated under the molten slag by a predetermined means in each discharge cycle set arbitrarily, the voltage fluctuation during operation between the plasma electrode and the bottom electrode Voltage fluctuation detection means for detecting, counting means for detecting and counting instantaneous voltage fluctuations in the negative direction from the voltage fluctuations, and the number of times of occurrence of the instantaneous voltage fluctuations per unit time exceeds a prescribed number of times. An operation control device for a plasma melting furnace, comprising: a judgment means for judging that a molten metal discharge time has come when the state continues for a predetermined time.
極間に、定電流制御機能を有する直流電源装置により定
電流を流しながらプラズマ放電により廃棄物を溶融処理
して出滓口より溶融スラグを排出するとともに、任意に
設定した排出サイクル毎に前記溶融スラグ下方に堆積し
た溶融メタルを所定手段で排出する廃棄物溶融処理炉に
おいて、 直前の溶融メタルの排出時以降の現サイクルにおける炉
内に投入する廃棄物の投入総量に基づいて溶融メタルの
排出時期を判断する第1の判定手段と、プラズマ電極と
炉底電極間の負方向の瞬時的な電圧変動により溶融メタ
ルの排出時期を判断する第2の判定手段とを具え、いず
れか一方若しくは両者の判定信号に基づいて、溶融メタ
ルの排出時期を判断することを特徴とするプラズマ溶融
炉の運転制御装置。7. The waste material is melted by plasma discharge while being supplied with a constant current by a DC power supply device having a constant current control function between the plasma electrode inserted from above the furnace and the bottom electrode, and melted from the outlet. In a waste melting treatment furnace that discharges slag and discharges the molten metal accumulated under the molten slag by a predetermined means in every discharge cycle set arbitrarily, in the furnace in the current cycle after the last discharge of molten metal The first determination means for determining the discharge timing of the molten metal based on the total amount of waste to be charged into the furnace, and the discharge timing of the molten metal by the instantaneous negative voltage fluctuation between the plasma electrode and the bottom electrode of the furnace. And a second determination means for determining the discharge timing of the molten metal based on the determination signal of either or both of them. Control device.
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JP2008209040A (en) * | 2007-02-23 | 2008-09-11 | Mitsubishi Heavy Ind Ltd | Operation control method and device of plasma melting furnace |
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