JPH0630754B2 - How to put waste in the waste melting furnace - Google Patents

How to put waste in the waste melting furnace

Info

Publication number
JPH0630754B2
JPH0630754B2 JP61079400A JP7940086A JPH0630754B2 JP H0630754 B2 JPH0630754 B2 JP H0630754B2 JP 61079400 A JP61079400 A JP 61079400A JP 7940086 A JP7940086 A JP 7940086A JP H0630754 B2 JPH0630754 B2 JP H0630754B2
Authority
JP
Japan
Prior art keywords
waste
furnace
melting
charging
level
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.)
Expired - Lifetime
Application number
JP61079400A
Other languages
Japanese (ja)
Other versions
JPS62237985A (en
Inventor
俊治 古川
友伸 石田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP61079400A priority Critical patent/JPH0630754B2/en
Priority to US06/900,894 priority patent/US4697532A/en
Publication of JPS62237985A publication Critical patent/JPS62237985A/en
Publication of JPH0630754B2 publication Critical patent/JPH0630754B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は廃棄物溶融処理炉の廃棄物投入方法に関するも
のである。さらに詳しくは、電極に対する電力負荷の平
均化を目的とした廃棄物溶融処理炉の廃棄物投入方法に
係わるものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention relates to a method for charging waste in a waste melting treatment furnace. More specifically, the present invention relates to a method for charging waste in a waste melting treatment furnace for the purpose of averaging the electric power load on the electrodes.

[従来の技術] 都市ゴミのような廃棄物を焼却炉により、焼却処理する
際に発生する焼却灰、ダスト等の廃棄物には、例えばク
ロム、ニッケル、マンガン、カドミウム、水銀、銅等人
体や生物に有害な重金属を含むものがあり、その廃棄処
理については国家的規制措置がとられていることは知ら
れている。
[Prior Art] Waste such as incineration ash and dust generated when incinerating waste such as municipal waste in an incinerator includes, for example, human body such as chromium, nickel, manganese, cadmium, mercury, copper and the like. It is known that some of them contain heavy metals that are harmful to living organisms, and that their disposal is subject to national regulatory measures.

これら廃棄物は従来、地中に直接埋立て処分したり、重
金属類を、活性炭に吸着させたり、アルカリを加えて水
酸化物として沈降分離したり、イオン交換樹脂に結合さ
せたりして捕捉除去後、地中に埋立処分する方法がとら
れてきた。しかし、いずれの場合も、埋立地の確保が次
第に困難になりつつあるばかりでなく、直接埋立処分す
る場合は重金属類が地中に溶出して周辺を汚染する恐れ
があり、また重金属類を捕捉後埋立処分する方法は、生
成する重金属吸着活性炭、重金属水酸化物、重金属結合
イオン交換樹脂などを含有するスラッジの処理をどうす
るかが問題となり、その廃棄の仕方如何によっては、二
次公害発生の危険性がある。本問題解決にあたっては、
たとえば燃料を用いて溶融処理する提案もあるが本出願
人は、叙上のような問題点を解決するものとして特開昭
52−143965に示す方法を提案した。この方法
は、電気アーク炉中で溶融したベースメタル、例えば鉄
よりなる金属湯に、還元雰囲気下、産業廃棄物等の処理
の結果生ずる重金属含有焼却残渣或いはスラッジを添加
して重金属類をベースメタル中に溶解させると共に、ベ
ースメタル上に浮遊する溶融スラグ中にも捕捉固定する
ものである。
These wastes have been captured and removed by direct landfill disposal in the ground, adsorption of heavy metals on activated carbon, sedimentation as hydroxide by adding alkali, and binding to ion exchange resin. Later, the method of landfilling underground has been adopted. However, in both cases, not only is it becoming increasingly difficult to secure landfill sites, but when direct landfill disposal, heavy metals may elute into the ground and contaminate the surrounding area. The problem with the method of landfilling after disposal is how to treat the sludge containing the generated heavy metal-adsorbed activated carbon, heavy metal hydroxide, and heavy metal-bonded ion-exchange resin. There is a risk. In solving this problem,
For example, there is a proposal to perform melt processing using fuel, but the present applicant has proposed a method shown in Japanese Patent Laid-Open No. 52-143965 as a solution to the above problems. This method involves adding heavy metal-containing incineration residue or sludge resulting from the treatment of industrial waste, etc. to a base metal melted in an electric arc furnace, for example, a metal hot water made of iron, in a reducing atmosphere to add heavy metals to the base metal. In addition to being dissolved in it, it is also captured and fixed in the molten slag floating on the base metal.

このような溶融処理に用いられる炉として、長手方向直
方体の形をしたサブマージドアーク炉が知られている。
この炉は密閉構造で、上部から炉蓋を貫通してアーク熱
発生用の人造黒鉛製電極が長手方向直線上に複数本装入
され、炉内には、適当な抵抗値を有する溶融開始剤を投
入しておき、ジュール熱により溶融し、いわゆる湯溜り
層を形成させる。湯溜り層は温度1450〜1550℃
の高温溶融状態を保っておき、前記電極と交互に位置し
て設けられる複数個の投入口により廃棄物、例えば都市
ゴミ焼却灰を投入して溶融する。湯溜り層及びその下の
ベースメタル層は炉の運転初期のジュール熱、アーク熱
発生源となると同時に、上記焼却灰溶融の熱源にもな
り、又焼却灰中の鉄分その他の各種重金属類吸収母体の
機能も備えている。焼却灰中の大部分を占める無機物質
は、溶融スラグとなりベースメタル上に浮遊し鉄を始め
Cr、Niなどの重金属類の大部分はベースメタル中に
移行して、一部はスラグ中に固定され、炉体に設けられ
た複数個の出滓口より炉外へ排出される。なお、溶融過
程で、炉内では若干のガスが発生し、排気口より排出さ
れる。ここに長手方向に直方体の形をした溶融処理炉
は、電極揚降装置を炉本体の裏側に一直線に配設できる
ので増設の際の設計が楽であるし、又、電極の消耗によ
る継ぎ足し、取替え等のメンテナンスが容易である。ま
た溶融処理されるべき廃棄物の搬入系設備配置が簡素化
される。そして、焼却残渣投入口は1炉当り、複数個設
置されているので、投入口1個当りの投入負荷を分散軽
減せしめることができる。更に、排気物投入口は、その
各々の位置が電極をはさむように、言い換えれば電極と
電極との間に配置されるので、溶融エネルギーの最も大
きい電極間に排気物が投入されることになり、溶融処理
効率がよい。又、出滓口を一側面に開口させた構造とし
てなるので、溶融スラグの排出作業が容易であるという
利点がある。
As a furnace used for such a melting process, a submerged arc furnace having a shape of a rectangular parallelepiped in the longitudinal direction is known.
This furnace has a closed structure, and a plurality of artificial graphite electrodes for arc heat generation are inserted in a straight line in the longitudinal direction from the top through the furnace lid, and a melting initiator having an appropriate resistance value is placed in the furnace. Is charged and melted by Joule heat to form a so-called pool layer. The temperature of the water pool is 1450 to 1550 ° C
The high temperature molten state is maintained, and waste, for example, municipal waste incineration ash is charged and melted through a plurality of charging ports provided alternately with the electrodes. The basin layer and the base metal layer thereunder serve as Joule heat and arc heat generation source in the initial stage of operation of the furnace, and at the same time serve as a heat source for melting the incineration ash, and also as an iron or other heavy metal absorbing matrix in the incineration ash. It also has the function of. Most of the inorganic substances in the incinerated ash become molten slag and float on the base metal, and most of heavy metals such as iron, Cr, Ni, etc. migrate to the base metal, and some of them are fixed in the slag. And is discharged to the outside of the furnace through a plurality of outlets provided in the furnace body. In the melting process, some gas is generated in the furnace and discharged from the exhaust port. In the melting process furnace in the shape of a rectangular parallelepiped in the longitudinal direction, since the electrode lifting device can be arranged in a straight line on the back side of the furnace body, the design at the time of expansion is easy, and the addition due to the consumption of the electrodes, Easy maintenance such as replacement. In addition, the arrangement of equipment for carrying in wastes to be melt-processed is simplified. Since a plurality of incineration residue charging ports are installed per furnace, the charging load per charging port can be dispersed and reduced. Further, since the exhaust material inlet is disposed so that each position sandwiches the electrode, in other words, between the electrodes, the exhaust material is injected between the electrodes having the largest melting energy. The melt processing efficiency is good. Further, since the outlet is formed on one side surface, there is an advantage that the work of discharging the molten slag is easy.

上記溶融処理炉では複数の廃棄物投入口が設けられてい
るので、投入口直下毎の廃棄物堆積層高さがほぼ平らに
なるようにする必要から、投入口開閉ダンパーの開時間
をタイマーで制御して、各投入口からの投入量が調節さ
れる。また、炉内に廃棄物の堆積層高さを検出するレベ
ル計を投入口の個数に応じた数だけ設け、レベル計の検
知信号に基く投入電力量制御による堆積層高さの均一化
などが行なわれる。
Since the above-mentioned melting treatment furnace is equipped with multiple waste input ports, it is necessary to make the height of the waste accumulation layer almost flat just below each input port. By controlling, the input amount from each input port is adjusted. In addition, the number of level meters that detect the height of the deposited layer of waste is provided in the furnace according to the number of input ports, and the level of the deposited layer can be made uniform by controlling the input electric energy based on the detection signal of the level meter. Done.

[発明が解決しようとする問題点] しかし、投入口開閉ダンパーのタイマーによる開閉制御
に基づく廃棄物の投入量の調節は、炉内における廃棄物
の堆積層高さが均一にならない場合もあった。また投入
電力制御による方法は、投入電力の不平衡、電力タップ
の消耗等があって適切な方法とはいえない。そしていず
れの方法も、廃棄物(例えば、都市ゴミ焼却灰)のよう
に物性に偏りのあるものは、溶融特性に局部的な差異が
あって、溶融継続中に炉内廃棄物の堆積高さが不均一に
なる。加えて、後者の方法は、都市ゴミ焼却灰溶融処理
炉の場合、ゴミ焼却による生ずる廃熱利用の発電電力を
用いるものであるから、その発電負荷の60〜70%を
消費することとなり、発電系の負荷が大きい。
[Problems to be Solved by the Invention] However, the adjustment of the amount of waste input based on the opening / closing control by the timer of the opening / closing damper of the inlet may not always make the height of the deposited layer of the waste uniform in the furnace. . In addition, the method based on input power control cannot be said to be an appropriate method because of imbalance in input power and consumption of power taps. In any of the methods, if the physical properties are uneven, such as waste (for example, municipal waste incineration ash), there is a local difference in the melting characteristics, and the deposition height of in-core waste during melting continues. Becomes uneven. In addition, in the latter method, in the case of an urban refuse incineration ash melting treatment furnace, since power generated by utilizing waste heat generated by waste incineration is used, 60 to 70% of the power generation load is consumed, and power generation The system load is large.

[問題を解決するための手段] 本発明は以上のような問題を解決するために、種々検討
の結果、達成されたもので、炉内に設けた廃棄物堆積高
さ検知用のレベラー計のうち2コ以上のレベラー計の検
出値に基いて、廃棄物投入口の投入口ダンパー開度を制
御し、廃棄物堆積高さの均一化を図るための廃棄物投入
方法を提供するものである。即ち、本発明は、複数個の
廃棄物投入口を備え、炉内に堆積する廃棄物のレベルを
複数個のレベル計によって検出し、その検出値に基いて
廃棄物投入量を制御する廃棄物溶融処理炉の廃棄物投入
方法において、各レベル計が検出した検出値のうち、最
大値と最小値の差が予め設定した値を越えたとき、最小
値を示したレベル計の近傍に廃棄物を投入して、炉内に
おける廃棄物の堆積層高さを平均化することを特徴とす
る廃棄物溶融処理炉への廃棄物投入方法を要旨とするも
のである。
[Means for Solving the Problems] The present invention has been achieved as a result of various studies in order to solve the above problems, and has been achieved by a leveler meter for detecting the height of waste accumulation provided in a furnace. Based on the detected values of two or more levelers, the opening degree of the dumper of the waste dumper is controlled to provide a waste dumping method for achieving uniform waste pile height. . That is, the present invention has a plurality of waste input ports, detects the level of waste accumulated in the furnace by a plurality of level meters, and controls the waste input amount based on the detected values. When the difference between the maximum value and the minimum value among the detection values detected by each level meter exceeds the preset value in the waste injection method of the melting furnace, the waste is placed near the level meter showing the minimum value. The present invention has a gist of a method for charging a waste into a furnace for melting waste, which is characterized in that the height of a deposited layer of the waste in the furnace is averaged by charging.

以下、本発明を図面に基いて説明する。第1図〜第3図
は、本発明の適用される長手方向に直方体の形をしたサ
ブマージドアーク加熱溶融処理炉の1例で、第1図は概
略正面図、第2図は概略平面図、第3図は第2図のX−
X′線における部分断面図である。図中1は耐火材料か
らなる炉本体で上部には蓋体2が設けられる。蓋体2に
は、ガス排出口3のほか、Y直線上に電極4A〜4Fが
貫通し、また、これらの間にはさまれて、複数の廃棄物
投入口5A〜5Eが並設される。さらに、電極と廃棄物
投入口とにはさまれた位置に、投入された廃棄物の堆積
高さを検知する複数のレベル計6A〜6Fが設けられ
る。各廃棄物投入口の投入シュート途中には、廃棄物a
の投入量を調節する開閉ダンパー7A〜7Eが開閉自在
に内装されている。これらダンパーは各々駆動装置8A
〜8Eにより回動される。9はレベル計6A〜6Fから
の検知信号に基き、駆動装置8A〜8Eに、ダンパー7
A〜7Eの開閉を指令する制御装置である。10は、炉
本体1に設けられる溶融スラグの出滓口、11は出滓口
カバー、bは溶融スラグ、cは炉本体底部に形成されて
いるベースメタルである。12は電極支持アーム、13
は電極揚降装置、14は保守点検用扉、15は炉体を補
強する枠組である。
Hereinafter, the present invention will be described with reference to the drawings. 1 to 3 show an example of a rectangular parallelepiped submerged arc heating and melting treatment furnace to which the present invention is applied. FIG. 1 is a schematic front view, and FIG. 2 is a schematic plan view. , Fig. 3 is X- in Fig. 2.
It is a fragmentary sectional view in the X'line. In the figure, reference numeral 1 denotes a furnace body made of a refractory material, and a lid 2 is provided on the upper portion thereof. In addition to the gas discharge port 3, the lid 4 is penetrated by electrodes 4A to 4F on the Y straight line, and sandwiched between these electrodes, a plurality of waste input ports 5A to 5E are arranged in parallel. . Furthermore, a plurality of level meters 6A to 6F for detecting the height of the deposited waste deposited are provided at a position sandwiched between the electrode and the waste inlet. During the charging chute of each waste charging port, waste a
Opening / closing dampers 7A to 7E for adjusting the input amount are opened and closed. Each of these dampers is a drive device 8A.
Rotated by ~ 8E. 9 is based on the detection signal from the level meters 6A to 6F, and is connected to the drive devices 8A to 8E and the damper 7
It is a control device that commands opening and closing of A to 7E. Reference numeral 10 is a molten slag outlet provided in the furnace body 1, 11 is a outlet cover, b is molten slag, and c is a base metal formed on the bottom of the furnace body. 12 is an electrode support arm, 13
Is an electrode lifting device, 14 is a maintenance inspection door, and 15 is a framework for reinforcing the furnace body.

廃棄物の溶融処理を上記の型式のサブマージドアーク炉
を用いて本発明方法により実施するには、前記のとお
り、まず炉本体1内に溶融開始剤等を投入して溶融さ
せ、1450〜1550℃の高温溶融状態の湯溜り層を
形成させる。次に、投入口5A〜5Eより、ダンパー7
A〜7Eを開とし、廃棄物aを同等投入しアーク加熱す
る。廃棄物aの溶融が進むに従って形成される溶融スラ
グbは、逐次出滓口10から排出される。このとき、各
投入口5A〜5E直下における廃棄物aの堆積層高さ
は、廃棄物物性の偏り、堆積層密度差等の差異により各
投入口毎にばらつき、不均一になる。
In order to carry out the melting treatment of the waste by the method of the present invention using the submerged arc furnace of the above-mentioned type, as described above, first, a melting initiator or the like is charged into the furnace body 1 to melt, and 1450 to 1550. A hot water pool layer at a high temperature of ℃ is formed. Next, from the insertion ports 5A to 5E, the damper 7
A to 7E are opened, waste a is equally charged, and arc heating is performed. The molten slag b formed as the melting of the waste a progresses, is sequentially discharged from the outlet 10. At this time, the heights of the deposited layers of the waste a immediately below the respective inlets 5A to 5E are uneven and uneven among the respective inlets due to the unevenness of the physical properties of the waste and the difference in the density of the deposited layers.

本発明は、この不均一を、廃棄物投入口近傍に位置して
設けられる各レベル計がそれぞれ検知するので、そのば
らばらの検出値のうち、最大値と最小値の差が予め定め
た設定値を超えた場合は、最小の検出値を示したレベル
計の最も近傍の廃棄物投入口におけるダンパーをタイマ
ーにより一定時間開いて、廃棄物の投入を行い、溶融処
理中、堆積層高さがほぼ平らな形を維持しようとするも
のである。尚この場合のレベル計の最大および最小の検
出値の差の設定は、適用する炉の特性値として、経験的
に求められるものである。
According to the present invention, each level meter provided near the waste input port detects this non-uniformity, and therefore the difference between the maximum value and the minimum value among the scattered detection values is a preset value. If the value exceeds the limit, the damper at the waste input port closest to the level meter showing the minimum detection value is opened for a certain period of time by a timer to input the waste, and the height of the deposited layer is almost It tries to maintain a flat shape. The setting of the difference between the maximum and minimum detection values of the level meter in this case is empirically determined as the characteristic value of the furnace to be applied.

以上は、次のような制御機構により行うこともできる。
即ち第3図に一点鎖線の伝達経路で示すように、各レベ
ル計6A〜6Eがそれぞれ炉内における廃棄物aの堆積
高さを一定時間毎に検出し、検出信号を制御装置9に伝
達する。そして制御装置9には、各レベル計の検出値
から最大検出値と最小検出値との差を演算し、予め設定
した検出値と比較するプログラム、検出値差が設定し
た検出値を超えているときは、最小検出値を示したレベ
ル計の近傍にある1〜2個の廃棄物投入口のダンパーを
タイマーにより一定時間開とすることをダンパー開閉駆
動装置に指令するプログラムの両者を入力しておく方法
である。尚レベル計の検出作動は、一定時間毎に行うよ
うにすればよい。
The above can also be performed by the following control mechanism.
That is, as indicated by the chain-dotted transmission path in FIG. 3, the level meters 6A to 6E detect the deposition height of the waste a in the furnace at regular intervals, and transmit the detection signal to the controller 9. . Then, in the control device 9, a program for calculating the difference between the maximum detection value and the minimum detection value from the detection values of the respective level meters and comparing it with the preset detection value, the detection value difference exceeds the set detection value. In this case, input both programs of the damper opening / closing drive device instructing the damper opening / closing drive to open the damper of one or two waste inlets near the level meter showing the minimum detection value for a certain period of time by a timer. It is a way to put. The detection operation of the level meter may be performed at regular time intervals.

[作用] 複数個のレベル計の検出する検出値のうち最大値と最小
値とが比較され、最小値を示すレベラー計の近傍に廃棄
物を投入するので、炉全体における堆積レベルの不均一
が修正される。従って、溶融処理中もほぼ水平な廃棄物
堆積レベルが確保される。
[Operation] The maximum value and the minimum value among the detection values detected by a plurality of level meters are compared, and the waste is injected in the vicinity of the leveler meter showing the minimum value. Will be fixed. Therefore, a substantially horizontal waste accumulation level is ensured during the melting process.

[実施例] 炉床面積が3.3Mの第1図に示すようなサブマージ
ドアーク加熱溶融処理炉に都市ゴミ焼却灰(含水率10
%)を廃棄物投入口5A〜5Eからダンパー開時間を同
じにして同量投入し、溶融処理した。即ち、投入口5A
〜5Eまで4分サイクルで、各ダンパー7A〜7Eは3
0秒間のタイマー設定とした。レベル計6A〜6Eによ
る廃棄物の堆積高さの検出は、5分に1回の割合で行っ
た。レベル計の設定は下限30cmで上限を35cm、上上
限を45cmとした。
[Example] A municipal solid waste incineration ash (water content: 10) was placed in a submerged arc heating and melting treatment furnace having a hearth area of 3.3 M 2 as shown in FIG.
%) Was charged from the waste input ports 5A to 5E with the same damper opening time, and melted. That is, input port 5A
4 minutes cycle up to 5E, each damper 7A-7E is 3
The timer was set to 0 seconds. The detection of the height of waste accumulated by the level meters 6A to 6E was performed once every 5 minutes. The level meter was set so that the lower limit was 30 cm, the upper limit was 35 cm, and the upper limit was 45 cm.

通常の物性の都市ゴミ焼却灰を処理する際はどのレベル
計も30〜35cm(溶融スラグ上面よりレベル計の接触
焼却灰上面までの距離)の堆積高さを検出値として示し
た。しかし、物性の大きく偏った都市ゴミ焼却灰を処理
したときの時間経過と、各レベル計6A〜6Eの検出値
は第1表の通りとなった。すなわち炉内における廃棄物
の堆積高さに変動が生じたので、第3図のような制御装
置により各レベル計が下限の30cmを下回る検出値を検
出した時には、その近くのダンパーを5分間開として廃
棄物高さを調節して処理した。なお比較のために制御装
置を作動させないで処理した場合も第1表に併せて示
す。
When treating municipal solid waste incineration ash with normal physical properties, the deposition height of 30 to 35 cm (distance from the upper surface of the molten slag to the upper surface of the contact incineration ash of the level meter) was shown as the detected value for all level meters. However, Table 1 shows the lapse of time when the municipal waste incineration ash whose physical properties are largely deviated and the detected values of the level meters 6A to 6E are shown. In other words, the height of waste piled up in the furnace fluctuated, so when each level meter detected a detection value below the lower limit of 30 cm by the control device shown in Fig. 3, the damper near it was opened for 5 minutes. As a result, the height of the waste was adjusted and treated. For comparison, Table 1 also shows the case of processing without operating the control device.

上記の結果より制御装置ありの本発明によれば、次の
〜が達成できることがわかった。
From the above results, it was found that the following items (1) to (2) can be achieved according to the present invention with a control device.

各投入口原料(焼却灰)の内容変化による投入スピ
ードの変化への迅速的対応。
Prompt response to changes in input speed due to changes in the contents of each input material (incineration ash).

焼却灰の溶融スピードに応じた各セレクション別投
入スピードへの迅速的な対応。
Prompt response to the input speed for each selection according to the melting speed of incinerated ash.

焼却灰層の量の一定化による電圧、電力、条件の安
定化と溶融スラグ熱放散の減少。
Stabilization of voltage, power and conditions and reduction of molten slag heat dissipation by stabilizing the amount of incineration ash layer.

[効果] 本発明は、以上のべたように、廃棄物投入口を複数個備
えた長手方向直方体形の溶融処理炉において、炉内に投
入された堆積する廃棄物レベルのばらつきを修正し溶融
継続中、ほぼ水平に保持しもって、安定した電力をはか
るもので、廃棄物処理分野に大きく寄与することができ
る。
[Effect] As described above, the present invention corrects the variation in the level of the deposited waste introduced into the furnace in the melting process furnace of a rectangular parallelepiped shape in the longitudinal direction having a plurality of waste input ports and continues the melting. Since it keeps almost horizontal inside, it provides stable power and can greatly contribute to the field of waste treatment.

【図面の簡単な説明】[Brief description of drawings]

図面は本発明方法の適用される溶融処理炉の1例を示す
もので、第1図は、概略正面図、第2図は概略平面図、
第3図は第2図のx−x′線における部分断面図であ
る。 1……炉本体、2……炉蓋 3……ガス排出口 4A,B,C,D,E,F……電極 5A,B,C,D,E……廃棄物投入口 6A,B,C,D,E……レベル計 7A,B,C,D,E……ダンパ 8A,B,C,D,E……ダンパー開閉駆動装置 9……制御装置、10……出滓口
The drawings show one example of a melting processing furnace to which the method of the present invention is applied. FIG. 1 is a schematic front view, FIG. 2 is a schematic plan view,
FIG. 3 is a partial sectional view taken along the line xx ′ in FIG. 1 ... Furnace body, 2 ... Furnace lid 3 ... Gas discharge port 4A, B, C, D, E, F ... Electrode 5A, B, C, D, E ... Waste input port 6A, B, C, D, E ... Level meter 7A, B, C, D, E ... Damper 8A, B, C, D, E ... Damper opening / closing drive device 9 ... Control device, 10 ... Outlet opening

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】複数個の廃棄物投入口を備え、炉内に堆積
する廃棄物のレベルを複数個のレベル計によって検出
し、その検出値に基いて廃棄物投入量を制御する廃棄物
溶融処理炉の廃棄物投入方法において、各レベル計が検
出した検出値のうちの最大値と最小値の差が予め設定し
た値を越えたとき、最小値の値を示したレベル計の近傍
に廃棄物を投入して、炉内における廃棄物の堆積層高さ
を平均化することを特徴とする廃棄物溶融処理炉への廃
棄物投入方法。
1. A waste melting system comprising a plurality of waste input ports, detecting the level of waste accumulated in a furnace by a plurality of level meters, and controlling the waste input amount based on the detected values. When the difference between the maximum value and the minimum value among the detection values detected by each level meter exceeds the preset value in the waste disposal method of the processing furnace, discard it in the vicinity of the level meter showing the minimum value. A method for charging waste into a waste melting treatment furnace, characterized in that the height of the deposited layer of the waste in the furnace is averaged by charging the waste.
【請求項2】廃棄物が都市ゴミ焼却灰である特許請求の
範囲第1項記載の廃棄物溶融処理炉への廃棄物投入方
法。
2. The method of charging waste into a waste melting and processing furnace according to claim 1, wherein the waste is incineration ash of municipal waste.
【請求項3】廃棄物溶融処理炉が、サブマージドアーク
炉である特許請求の範囲第1項記載の廃棄物溶融処理炉
への廃棄物投入方法。
3. The method for charging waste into the waste melting treatment furnace according to claim 1, wherein the waste melting treatment furnace is a submerged arc furnace.
JP61079400A 1985-08-27 1986-04-07 How to put waste in the waste melting furnace Expired - Lifetime JPH0630754B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP61079400A JPH0630754B2 (en) 1986-04-07 1986-04-07 How to put waste in the waste melting furnace
US06/900,894 US4697532A (en) 1985-08-27 1986-08-27 Operating method for a refuse processing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61079400A JPH0630754B2 (en) 1986-04-07 1986-04-07 How to put waste in the waste melting furnace

Publications (2)

Publication Number Publication Date
JPS62237985A JPS62237985A (en) 1987-10-17
JPH0630754B2 true JPH0630754B2 (en) 1994-04-27

Family

ID=13688801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61079400A Expired - Lifetime JPH0630754B2 (en) 1985-08-27 1986-04-07 How to put waste in the waste melting furnace

Country Status (1)

Country Link
JP (1) JPH0630754B2 (en)

Also Published As

Publication number Publication date
JPS62237985A (en) 1987-10-17

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