JPS6146814A - Slug discharging facility for waste material melting furnace - Google Patents

Slug discharging facility for waste material melting furnace

Info

Publication number
JPS6146814A
JPS6146814A JP16876284A JP16876284A JPS6146814A JP S6146814 A JPS6146814 A JP S6146814A JP 16876284 A JP16876284 A JP 16876284A JP 16876284 A JP16876284 A JP 16876284A JP S6146814 A JPS6146814 A JP S6146814A
Authority
JP
Japan
Prior art keywords
slag
slug
furnace
conduit
metal
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.)
Granted
Application number
JP16876284A
Other languages
Japanese (ja)
Other versions
JPH067006B2 (en
Inventor
Takeyuki Ishibashi
石橋 勇之
Koji Arita
有田 耕二
Takeshi Otani
大谷 断
Katsuo Kawafuchi
河渕 勝夫
Akio Nakamoto
彰夫 中本
Hirotsugu Kubo
博嗣 久保
Toshio Shiina
椎名 利雄
Hachiro Fujishiro
藤城 八郎
Masato Ando
安藤 允人
Yoichi Hosaka
保坂 洋一
Ryoichi Ueno
良一 上野
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.)
JFE Engineering Corp
Tanabe Kakoki Co Ltd
Original Assignee
Tanabe Kakoki Co Ltd
NKK Corp
Nippon Kokan 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 Tanabe Kakoki Co Ltd, NKK Corp, Nippon Kokan Ltd filed Critical Tanabe Kakoki Co Ltd
Priority to JP16876284A priority Critical patent/JPH067006B2/en
Publication of JPS6146814A publication Critical patent/JPS6146814A/en
Publication of JPH067006B2 publication Critical patent/JPH067006B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/085High-temperature heating means, e.g. plasma, for partly melting the waste

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Plasma & Fusion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

PURPOSE:To perform a continuous discharging of slug by a method wherein a slug discharging pipe passing through a furnace wall of a melting furnace is passed through the furnace wall, the slug discharging pipe is inclined upwardly and the slug and/or metal is overflowed and discharged from the slug discharging pipe. CONSTITUTION:A degree of upward inclination of slug discharging pipe 9 and a position of a side end part 9b in a furnace are preferably made such that a thickness Hb from the side end part 9b of the pipe 9 in the furnace to the level LSL of the slug layer is 100-300mm., preferably 200-300mm. and an inclination angle of about 15 deg.. The melting slug 4 may entangle the metal 3 when the slug is discharged from the slug discharging port 9a, the metal level LFe always keeps a position lower than the slug discharging port 9a, thereby a stable slug layer 4 can be formed. With this arrangement, a frequent degree of lifting or descending of the electrodes is reduced, a stable applied power can be attained and a continuous discharging of slug becomes possible.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は都市廃棄物を溶融径廃棄するための溶融炉に係
シ、特にその溶融炉出滓設備に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a melting furnace for disposing of municipal waste, and more particularly to a melting furnace slag extraction facility.

〔従来技術〕[Prior art]

都市とみ等の廃棄物は、焼却後埋立処分する方法が主流
を占めている。然しなから、近年埋立処分するための土
地の確保が困難なため、廃棄物焼却灰を更に減容する廃
棄物の溶融処理法が注目されている。
The mainstream method for municipal waste is to incinerate it and then dispose of it in a landfill. However, in recent years, it has become difficult to secure land for landfill disposal, so waste melting treatment methods that further reduce the volume of waste incineration ash have been attracting attention.

これら廃棄物の溶融処理法としては、アーク炉方式と抵
抗炉方式の;通シがあるが、前者のアーり炉方式の場合
、 1)アーク放電のため電圧、電流が不安定である。
There are two methods for melting and processing these wastes: an arc furnace method and a resistance furnace method; however, in the case of the former method, the arc furnace method has the following problems: 1) Voltage and current are unstable due to arc discharge.

2)アーク放電維持のための電極昇降の頻度が、激しく
その追従がむずかしい。
2) The frequency of raising and lowering the electrode to maintain arc discharge is so intense that it is difficult to follow it.

等の問題点を有している。It has the following problems.

一方後者の抵抗炉方式による処理法においては、従来か
ら合金鉄等の製造用として抵抗炉は用いられておシ、そ
の加熱法は、被熔融物内に電極を埋設させ通電すること
により、ジュール熱を得る電気式溶融炉であるため、前
述のアーク炉のもつ問題点は無い。
On the other hand, in the latter treatment method using a resistance furnace, resistance furnaces have traditionally been used for manufacturing ferroalloys, etc., and the heating method is to embed electrodes in the material to be melted and energize it. Since it is an electric melting furnace that generates heat, it does not have the problems of the above-mentioned arc furnace.

これら抵抗式溶融炉における溶融後の出滓方法には、間
欠式および連続式の二連シがあシ、前者の間欠式出滓方
法は、合金鉄等の製造設備において既に完成された技術
で、焼却灰の実験設備においても良好な運転が確認され
ている。
There are two types of slag extraction methods after melting in these resistance type melting furnaces: intermittent type and continuous type. Good operation has also been confirmed in the incineration ash experimental equipment.

然し、連続出滓に関しては、単味物質を対照とする実例
があるものの、焼却灰等のように、金属及びスラグとい
う性状の全く異なった物質を含んでいる例は無く、また
次のような難点がある。
However, with regard to continuous slag, although there are actual cases in which simple substances are compared, there are no examples of continuous slag containing substances with completely different properties such as metal and slag, such as incineration ash, and the following There are some difficulties.

即ち 1)王として5i01 t A40g * CaO等よ
りなるスラグと金属の物性の相異によル、出滓口の浸食
防止対策を異にする。
That is, 1) Measures to prevent erosion at the slag outlet are different depending on the physical properties of the slag and the metal, which are made of 5i01 t A40g * CaO, etc.

2)焼却量の変動に対する出滓量の追従が困難である。2) It is difficult to follow the amount of slag produced in response to changes in the amount of incineration.

6)補修時間がかかる。6) Repairs take time.

4)出滓口の外気接触による、溶融物の固着現象が生ず
る。
4) Due to contact with the outside air at the slag outlet, a phenomenon of sticking of the molten material occurs.

5)間欠出滓の場合、タップ、閉塞作業の頻度が高い。5) In the case of intermittent slag, tapping and closing operations are required frequently.

一方溶融処理方式は焼却処理方式に比べて、処理物の温
度は500〜700℃−と高く、それだけ危険性も高く
、熟練度を要する。そのため出来るだけ作業量が減少で
きる連続出滓方式に対するニーズが高まっている。
On the other hand, in the melt processing method, the temperature of the processed material is as high as 500 to 700°C, compared to the incineration method, and the danger is correspondingly higher, requiring a higher degree of skill. Therefore, there is a growing need for a continuous slag extraction system that can reduce the amount of work as much as possible.

密閉式アーク炉において、タッピング作業をおこなわず
連続的に出滓をおこなうものとして、特開昭56−77
611号忙は、炉殻の炉床中央部に出滓口を穿設し、こ
の出滓口の上層部を堤防状のせき止め部で囲繞し、出滓
口には気密装置を付設し、炉殻または上記炉蓋忙ガス排
出口と廃棄投入物とを設けた廃棄物処理用アーク炉を提
案している。
Japanese Patent Application Laid-Open No. 56-77 describes a closed arc furnace that continuously extracts slag without tapping.
No. 611 has a slag outlet drilled in the center of the hearth of the hearth, the upper part of this slag outlet is surrounded by an embankment-like dam, an airtight device is attached to the slag outlet, and the furnace An electric arc furnace for waste treatment is proposed which is provided with a shell or a furnace lid with a gas outlet and a waste input.

上記アーク炉の場合、出滓口が炉底部にあるため、アー
ク炉設置位置を高所にする必要があシ、且つシール等の
機構が複離である等の難点がある。
In the case of the above-mentioned arc furnace, since the slag outlet is located at the bottom of the furnace, the arc furnace must be installed at a high place, and there are disadvantages such as the need for separate mechanisms such as seals.

従って、都市廃棄物焼却灰を溶融炉で溶融処理するに当
って、簡単な機構で連続的に出滓する設備の開発が要望
されていた。
Therefore, in melting municipal waste incineration ash in a melting furnace, there has been a demand for the development of equipment that can continuously discharge slag with a simple mechanism.

〔発明の概要〕[Summary of the invention]

本発明は前記従来技術の問題点に鑑みなされたものであ
シ、焼却灰のように、メタル及びスラグ等の成分を含む
廃棄物を電気抵抗式溶融炉で処理するに当夛、その出滓
を連続して行なうことが出来る設備を提供することを目
的とし、作業の合理化並びに安全化を計るものである。
The present invention has been made in view of the problems of the prior art, and is suitable for processing waste materials such as incineration ash containing components such as metal and slag in an electric resistance melting furnace. The purpose is to provide equipment that can perform continuous operations, and to streamline and make the work safer.

本発明は、廃棄物焼却灰を溶融し、スラグ層とメタル層
を形成し、溶融スラグを出滓せしめる電気抵抗式溶融炉
において、該溶融炉々壁を貫通する出滓導管を炉壁周囲
に穿設し、該出滓導管を上方向に傾斜せしめ、前記スラ
グ及び/またはメタルを該出滓導管より溢流排出せしめ
ることを特徴とする廃棄物溶融炉の出滓設備である。
The present invention provides an electric resistance melting furnace that melts waste incineration ash, forms a slag layer and a metal layer, and discharges the molten slag. This slag extraction equipment for a waste melting furnace is characterized in that the slag extraction conduit is bored and the slag extraction conduit is inclined upward, and the slag and/or metal is overflowed and discharged from the slag extraction conduit.

〔発明の実施例〕[Embodiments of the invention]

本発明を実施態様例である図に基いて述べる。 The present invention will be described based on the drawings which are examples of embodiments.

第1図は本発明の実施例装置の説明図である。FIG. 1 is an explanatory diagram of an apparatus according to an embodiment of the present invention.

図において、1は外殻鋼板製、耐火煉瓦、カーボンブロ
ック内張りよる成る電気抵抗式溶融炉であシ、炉上部に
設けた炉蓋2により外気と遮断している。
In the figure, reference numeral 1 denotes an electric resistance melting furnace made of a steel shell, refractory bricks, and carbon block lining, and is isolated from the outside air by a furnace lid 2 provided at the top of the furnace.

被溶融物である焼却灰5は、上部蓋2を貫通して設けた
装入灰シュート7より装入されるが、炉内に均等に分配
できるように複数個設けている。
Incineration ash 5, which is the material to be melted, is charged through a charging ash chute 7 provided through the upper lid 2, and a plurality of ash chutes are provided so as to be evenly distributed in the furnace.

6は加熱用の炭素材より々る電極であ夛、ジュール熱に
より、加熱・溶融できるように押し下げ可能に、被溶融
物層内に埋設している。
Reference numeral 6 denotes an electrode made of a carbon material for heating, which is buried in the layer of the material to be melted so as to be able to be pushed down so that it can be heated and melted by Joule heat.

斯る電気抵抗式溶解炉においては、溶融物は比重差の順
に、炉底部よル重いものから軽いものに層別されて貯ま
る。最下部は最も重い比重6.3〜6.5のメタル層6
、その上部には比重2.6〜2.9のスラグ層4の順と
なる0 8は廃ガスの排出管であり別に設けられた廃ガス処理設
備に導通している。9はスラグ及び/またはメタルの出
滓導管であり、電極6近傍の炉壁周囲に複数個、炉壁を
貫通せしめ、上方向に傾斜し穿設されている。9aは出
滓口、9bは出滓導管の炉内壁側端部である。
In such an electric resistance melting furnace, the molten material is stratified and stored in the order of the difference in specific gravity from heavier to lighter at the bottom of the furnace. The lowest layer is the heaviest metal layer 6 with a specific gravity of 6.3 to 6.5.
, above which is a slag layer 4 having a specific gravity of 2.6 to 2.9, and 08 is a waste gas discharge pipe, which is connected to a separately provided waste gas treatment facility. A plurality of slag and/or metal slag discharge conduits 9 are provided around the furnace wall in the vicinity of the electrode 6, penetrating the furnace wall and slanting upward. 9a is a slag outlet, and 9b is an end of the slag conduit on the furnace inner wall side.

本発明の目的を達成するための出滓導管9の上向き傾斜
度ならびに、炉内壁側端部9bの位置は、出滓導管9の
炉内壁側端部9bからのスラグ層しペk Lst 1で
の厚さHbが100〜300 wa tFf ’Jしく
は200〜300amを条件とし、炉内壁側端部9bか
らの出滓導管内のスラグ及び/又はメタルレベルLaま
での浸漬深さをHaとし、被溶融物のレベルLa5hと
Lstとの装入厚さをHcとし、鉄、スラグ及び被溶融
物の比重を夫々ρFee  PH4+  P @3bと
し走場合 HaX l”y6< HbX P、t+ He ×/’
ashを条件とし決定すればよい。この条件を満足する
ものとして前記Hbが200〜300 ttaにおいて
、出滓導管9は約15°上向き傾斜とすることが好まし
い0 出滓導管9の先端には、交換容易な浸食防止用アタッチ
メント10が付いておシ、11はメタル抜出し口で炉を
停止する時のみ開孔し用いるものであ夛、12は出滓口
9aの開孔用マッドガン、13はオープナである0 次に本発明の出滓設備の作用について述べる。
The upward inclination of the slag conduit 9 and the position of the end 9b on the furnace inner wall side to achieve the object of the present invention are determined by the slag layer from the end 9b of the slag conduit 9 on the furnace inner wall side. The thickness Hb is 100 to 300 wa tFf 'J or 200 to 300 am, and the immersion depth from the furnace inner wall side end 9b to the slag and/or metal level La in the slag conduit is Ha, Let Hc be the charging thickness at the level La5h and Lst of the melted material, and let the specific gravity of iron, slag, and melted material be ρFee PH4+ P @3b, respectively.
It may be determined using ash as a condition. To satisfy this condition, when the Hb is 200 to 300 tta, it is preferable that the slag discharge conduit 9 be inclined upward by about 15 degrees. At the tip of the slag discharge conduit 9, an easily replaceable erosion prevention attachment 10 is provided. Reference numeral 11 is a metal outlet which is used to open the hole only when stopping the furnace, 12 is a mud gun for opening the slag outlet 9a, and 13 is an opener. The function of slag equipment will be described.

本電気抵抗式溶融炉1は、電極6によるジュール加熱の
ため1スラグ層4の厚みを常に200〜60〇−形成し
電極6を浸漬する必要がある。
In this electric resistance type melting furnace 1, it is necessary to always form one slag layer 4 with a thickness of 200 to 600 mm and to immerse the electrode 6 in order to perform Joule heating by the electrode 6.

従来の水平型出滓口では溶融したスラグと未溶融物が同
時に出滓し、スラグ層4を形成することができない。そ
のため、メタルが出滓口レベル近傍に達した時、別の出
滓口よりメタルを抜き出すか、あるいは炉を傾動してメ
タル分を抜き出さねばない欠点があったが、前記の如く
構成された本   1発明の出滓設備に依れば、溶融ス
ラグ4は出滓口9aより出滓する時メタル3をも巻込み
、メタルレベルL1は常に出滓口9a位置より下がった
位置となシ、スラグ層4を安定して形成することができ
る。
In a conventional horizontal slag outlet, molten slag and unmelted material slag simultaneously, and the slag layer 4 cannot be formed. Therefore, when the metal reached near the level of the slag outlet, there was a drawback that the metal had to be extracted from another slag outlet or the metal portion had to be extracted by tilting the furnace. According to the slag extraction equipment of the first invention, when the molten slag 4 is discharged from the slag outlet 9a, it also involves the metal 3, and the metal level L1 is always at a position lower than the position of the slag outlet 9a. The slag layer 4 can be stably formed.

また万一、メタルレベルLyeが出滓口9a より上昇
した場合にもスラグN4及び被溶融物灰層5の荷重によ
りメタル6は出滓口9aから溢流排出されるような出滓
導管9の傾斜となる。
In addition, even if the metal level Lye rises from the slag outlet 9a, the metal 6 will overflow from the slag outlet 9a due to the load of the slag N4 and the ash layer 5 of the melted material. It becomes a slope.

従って常に一定厚以上のスラグ層4が形成されるため電
極6の昇降の頻度が少なくなり、また使用電力が安定し
連続操業を可能とする。
Therefore, since the slag layer 4 is always formed with a certain thickness or more, the frequency of raising and lowering the electrode 6 is reduced, and the power consumption is stable, making continuous operation possible.

出滓導管9の出滓口の断面形状はどんな形状をとっても
よいが円形が望ましく、その断面積(口径)は、最大処
理時にも充分排出できる口径とすることは勿論、スラグ
等の付着の影響を受けない程度の口径までにすることは
可能で、溶融量に応じてオーバ70−する構造となって
いる。
The cross-sectional shape of the slag outlet of the slag conduit 9 may have any shape, but it is preferable to have a circular shape.The cross-sectional area (aperture) should not only be large enough to discharge the slag even during maximum processing, but also be sensitive to the effects of adhesion of slag, etc. It is possible to make the diameter up to the extent that it does not receive any damage, and the structure is such that the diameter exceeds 70 mm depending on the amount of melting.

従って炉内の溶融スラグレベルL8t ヲコントロール
することなく、電力の調整のみで、処理量の大巾な変動
九も追従可能である。出滓口9a は外気と接触するた
め、保温、加温してもよく、また外気と接触しないよう
にパージを行なっても良い。
Therefore, it is possible to follow wide fluctuations in the throughput by simply adjusting the electric power without controlling the molten slag level L8t in the furnace. Since the slag outlet 9a comes into contact with the outside air, it may be kept warm or heated, or may be purged so as not to come into contact with the outside air.

同様出滓導f9を、炉壁周囲の電極6の近傍に複数個穿
設することにより、これら出滓導管を交互に使用するこ
とにより、該出滓導管の補修を、炉を長期間停止するこ
となく連続運転することができる。
By drilling a plurality of similar slag discharge conduits f9 near the electrode 6 around the furnace wall and using these slag discharge conduits alternately, the furnace can be stopped for a long period of time without repairing the slag discharge conduits. It can be operated continuously without any problems.

更に本発明により、出滓口9a変更時のマッドガン12
並にオープナ16を使用することにより、出滓口閉塞及
び開口作業が容易になるものである。
Furthermore, according to the present invention, the mud gun 12 when changing the slag outlet 9a
In addition, by using the opener 16, it becomes easy to close and open the slag outlet.

〔発明の効果〕〔Effect of the invention〕

本発明の廃棄物溶融炉の出滓設備は、都市とみ等の廃棄
物焼却灰を大量に減容し得て、電気抵抗式溶融炉のスラ
グ層が安定して形成されるため、電極の昇降頻度が少な
くなシ使用市力が安定し得て、連続操業を可能にするも
のである。また廃棄物の溶融のみならず、連続出滓を目
途とする産業用電気炉等にも応用可能な有用な設備であ
る。
The slag extraction equipment of the waste melting furnace of the present invention can reduce the volume of waste incineration ash from urban areas, etc. in large quantities, and the slag layer of the electric resistance type melting furnace is stably formed, so that the electrodes can be raised and lowered. This makes it possible to stabilize the city power that is used infrequently and to enable continuous operation. Moreover, it is a useful equipment that can be applied not only to melting waste but also to industrial electric furnaces for continuous slag extraction.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の廃棄物溶融炉の出滓設備の模式図で
ある。 1:電機抵抗式溶融炉、3:メタル、4ニスラグ、5:
被溶融物、7:装入シュート、9:出滓導管、9a:出
滓口、9b:出滓導管炉内側端部、1’ D : 浸食
防止用アタッチメント、11:メタル抜出口、La:出
滓導管のスラグ及び/又はメタルレベル、LBtニスラ
グ層レベル、La5h: M溶融物レベル、Lye:メ
タルレベル。
FIG. 1 is a schematic diagram of the slag extraction equipment of the waste melting furnace of the present invention. 1: Electric resistance melting furnace, 3: Metal, 4 Nisslag, 5:
Material to be melted, 7: Charging chute, 9: Slag outlet, 9a: Slag outlet, 9b: Slag outlet conduit inner end of furnace, 1' D: Attachment for erosion prevention, 11: Metal outlet, La: Outlet Slag and/or metal level of slag conduit, LBt varnish slag layer level, La5h: M melt level, Lye: metal level.

Claims (2)

【特許請求の範囲】[Claims] (1)廃棄物焼却灰を溶融し、スラグ層とメタル層を形
成せしめ、溶融スラグを出滓せしめる電気抵抗式溶融炉
において、該溶融炉々壁を貫通する出滓導管を炉壁周囲
に穿設し、該出滓導管を上方向に傾斜せしめ、前記スラ
グ及び/またはメタルを該出滓導管より溢流排出せしめ
ることを特徴とする廃棄物溶融炉の出滓設備。
(1) In an electric resistance melting furnace that melts waste incineration ash, forms a slag layer and a metal layer, and releases the molten slag, a slag extraction conduit that penetrates the walls of the melting furnaces is bored around the furnace wall. 1. A slag extraction facility for a waste melting furnace, characterized in that the slag extraction conduit is provided and the slag extraction conduit is inclined upward, and the slag and/or metal is overflowed and discharged from the slag extraction conduit.
(2)前記出滓導管を上方向に傾斜せしめ設けるに当り
、該出滓導管の炉内壁側端部の位置及び傾斜度を、 Ha×ρ_F_e<Hb×ρ_s_l+Hc×ρ_a_
s_hHb:100〜300mm ただし Ha:炉内壁側端部からの出滓導管内のスラグ及び/又
はメタルレベル迄の浸漬深さ Hb:出滓導管炉内壁側端部からのスラグ層レベルまで
の厚み Hc:被溶融物の装入厚み ρ_F_e:鉄の比重 ρ_s_l:スラグの比重 ρ_a_s_h:被溶融物の比重 の条件にて決定することを特徴とする特許請求の範囲第
1項記載の廃棄物溶融炉の出滓設備。
(2) When sloping the slag conduit upward, the position and degree of inclination of the end of the slag conduit on the furnace inner wall side are set as follows: Ha×ρ_F_e<Hb×ρ_s_l+Hc×ρ_a_
s_hHb: 100 to 300 mm However, Ha: Immersion depth from the end of the furnace inner wall to the slag and/or metal level in the slag conduit Hb: Thickness Hc of the slag conduit from the end of the furnace inner wall to the slag layer level : Charging thickness of the material to be melted ρ_F_e: Specific gravity of iron ρ_s_l: Specific gravity of slag ρ_a_s_h: The waste melting furnace according to claim 1, characterized in that it is determined based on the conditions of the specific gravity of the material to be melted. Tailing equipment.
JP16876284A 1984-08-14 1984-08-14 Waste melting furnace slag facility Expired - Lifetime JPH067006B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16876284A JPH067006B2 (en) 1984-08-14 1984-08-14 Waste melting furnace slag facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16876284A JPH067006B2 (en) 1984-08-14 1984-08-14 Waste melting furnace slag facility

Publications (2)

Publication Number Publication Date
JPS6146814A true JPS6146814A (en) 1986-03-07
JPH067006B2 JPH067006B2 (en) 1994-01-26

Family

ID=15873967

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16876284A Expired - Lifetime JPH067006B2 (en) 1984-08-14 1984-08-14 Waste melting furnace slag facility

Country Status (1)

Country Link
JP (1) JPH067006B2 (en)

Also Published As

Publication number Publication date
JPH067006B2 (en) 1994-01-26

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