JP2629108B2 - Waste melting furnace - Google Patents

Waste melting furnace

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Publication number
JP2629108B2
JP2629108B2 JP4087364A JP8736492A JP2629108B2 JP 2629108 B2 JP2629108 B2 JP 2629108B2 JP 4087364 A JP4087364 A JP 4087364A JP 8736492 A JP8736492 A JP 8736492A JP 2629108 B2 JP2629108 B2 JP 2629108B2
Authority
JP
Japan
Prior art keywords
tap hole
waste
gas
tap
forehearth
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 - Fee Related
Application number
JP4087364A
Other languages
Japanese (ja)
Other versions
JPH05288332A (en
Inventor
弘之 小畑
邦博 渡辺
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.)
Nippon Steel Corp
Nippon Steel Plant Designing Corp
Original Assignee
Nittetsu Plant Designing Corp
Nippon Steel Corp
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 Nittetsu Plant Designing Corp, Nippon Steel Corp filed Critical Nittetsu Plant Designing Corp
Priority to JP4087364A priority Critical patent/JP2629108B2/en
Publication of JPH05288332A publication Critical patent/JPH05288332A/en
Application granted granted Critical
Publication of JP2629108B2 publication Critical patent/JP2629108B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、コークスのような塊状
炭素系可燃物質を熱源として、都市ごみ、各種産業廃棄
物、又はそれらを乾燥、焼却、破砕処理等によって得ら
れた中間処理物を加熱溶融して、土木用資材、コンクリ
ート細骨材、表面化粧用骨材用スラグ材として回収する
溶融炉、特に、その出湯口部分の構造に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to municipal solid waste, various industrial wastes, or intermediate products obtained by drying, incineration, crushing, etc., using a massive carbon-based combustible material such as coke as a heat source. The present invention relates to a melting furnace that is heated and melted to recover as civil engineering material, concrete fine aggregate, and slag material for surface decorative aggregate, and more particularly to a structure of a tap hole portion thereof.

【0002】[0002]

【従来の技術】この廃棄物溶融炉は、塩基度調整剤とし
て石灰石,珪石とともにコークスを配合した廃棄物を炉
の頂部から装入し、羽口から酸素含有ガスあるいは酸素
富化ガスを炉内に吹込んでコークスを高温度で燃焼さ
せ、炉内の乾燥帯,乾留ガス化帯及び燃焼溶融帯を順次
降下して溶融スラグ化する構造を有する。
2. Description of the Related Art In this waste melting furnace, waste containing a coke blended with limestone and silica stone as a basicity adjusting agent is charged from the top of the furnace, and an oxygen-containing gas or an oxygen-enriched gas is supplied from a tuyere into the furnace. And the coke is burned at a high temperature, and the drying zone, the carbonization gasification zone and the combustion melting zone in the furnace are sequentially lowered to form molten slag.

【0003】廃棄物溶融炉においては、廃棄物の性状が
変化するために、溶融物の性状も変化し粘性も変化す
る。とくに粘性が高くなると出湯口からの溶融物排出が
困難となり、極端な場合には出湯口の閉塞に追い込まれ
る。
[0003] In a waste melting furnace, the properties of the waste change, so that the properties of the melt change and the viscosity also changes. In particular, when the viscosity is high, it becomes difficult to discharge the melt from the tap hole, and in an extreme case, the melt port is blocked.

【0004】そのため、出湯口としては、溶融物の安定
的な出湯のためには、出湯口先端で溶融物が流路から落
下するまでの過程で、溶融物温度が低下し流動性が悪化
して、流路に固着成長する現象を抑制する必要がある。
さらに、溶融物とともに噴出されるCOを多量に含む可
燃ガスの無害な導出を考慮した構造とする必要があり、
さらには作業者による保守点検に際しての作業環境を良
好に保つことが必要である。
[0004] Therefore, as for the tap hole, in order for the melt to drop stably from the flow path at the tip of the tap hole, the temperature of the melt drops and the fluidity deteriorates in order to stabilize the tapping of the melt. Therefore, it is necessary to suppress the phenomenon of sticking and growing in the flow channel.
In addition, it is necessary to consider the harmless derivation of flammable gas containing a large amount of CO ejected with the melt,
Further, it is necessary to maintain a good working environment for maintenance and inspection by the operator.

【0005】従来、この廃棄物溶融炉の出湯口の構造と
して、実開昭58−58240号公報には、噴出ガスを
下方に案内するカバーを設け、これによって溶融物の保
温とともに、噴出した可燃ガスを系外に案内するように
した構造のものが開示されている。
Conventionally, as a structure of a tap hole of this waste melting furnace, Japanese Utility Model Application Laid-Open No. 58-58240 discloses a cover for guiding a jet gas downward, thereby keeping the heat of the melt and the combustible A structure in which a gas is guided out of the system is disclosed.

【0006】ところが、案内カバーのみによる溶融物の
保温は不充分であり、そのため、溶融物の流動性が悪く
なり、出湯口が閉塞気味となり極端な場合には完全に閉
塞してしまうこともある。さらには、出湯口から噴出し
た可燃ガスは、案内カバー内では酸素が存在せず、案内
カバーから出た所で始めて大気と接触するため、出湯口
流路上の溶融物を保温できない。また、大気との混合が
完全ではなく不完全燃焼を起こし、環境を良好に保つこ
とが困難であった。
However, the heat retention of the melt by the guide cover alone is insufficient, so that the fluidity of the melt deteriorates, and the tap hole tends to be clogged, and may be completely clogged in extreme cases. . Furthermore, since the combustible gas ejected from the tap hole has no oxygen in the guide cover and comes into contact with the atmosphere only when it comes out of the guide cover, the molten material on the tap hole channel cannot be kept warm. In addition, mixing with the atmosphere was not complete, but incomplete combustion occurred, making it difficult to maintain a good environment.

【0007】また、実公昭61−43070号公報で
は、とくに出湯口近傍に熱をつけるために、出湯口近傍
に羽口を追加し、出湯口流路内側近傍の温度を上げてい
るが、炭素系可燃物質充填層内であるため、この羽口で
燃焼した燃焼排ガスはCOガスを含む可燃ガスとして出
湯口から排出される。よって、必要以上に塊状炭素系可
燃物質を消費することになる。また、炉内出湯口近傍が
局部的に高温となるために、局部的な耐火物の損耗が発
生する。さらに、溶融物は、出湯口出口にてとくに温度
降下を起こすために、その対策にはなっていない。
In Japanese Utility Model Publication No. Sho 61-43070, a tuyere is added in the vicinity of the tap hole to increase the temperature in the vicinity of the tap hole, and the temperature in the vicinity of the inside of the tap hole is increased. Since it is in the system flammable substance packed bed, the combustion exhaust gas burned at the tuyere is discharged from the tap as a flammable gas containing CO gas. Therefore, the massive carbon combustible material is consumed more than necessary. In addition, since the temperature near the taphole in the furnace becomes locally high, refractory wear occurs locally. Furthermore, the melt does not take measures as it causes a temperature drop especially at the tap hole outlet.

【0008】さらに、特公平2−606号公報では、出
湯口からの噴出ガスを燃焼させることなく、ダクトで主
排ガス管に接続する構造が示されているが、溶融物の急
冷防止のための格別の対策は講じられていない。
Further, Japanese Patent Publication No. 2-606 discloses a structure in which a gas discharged from a tap is connected to a main exhaust gas pipe by a duct without burning the gas. No special measures have been taken.

【0009】[0009]

【発明が解決しようとする課題】本発明の目的は、抽出
する溶融物に良好な流動状態を維持せしめて、炉の安定
操業を実現させるために、噴出する可燃ガスを有効利用
する出湯口構造を有する廃棄物溶融炉を提供することに
ある。
SUMMARY OF THE INVENTION It is an object of the present invention to maintain a good flow state in a melt to be extracted, and to realize a stable operation of a furnace, a tap hole structure for effectively utilizing a combustible gas to be jetted out. The object of the present invention is to provide a waste melting furnace having:

【0010】[0010]

【課題を解決するための手段】本発明は、廃棄物に塩基
度調整剤と塊状炭素質燃料を頂部から装入し、下部に設
けた羽口から燃焼用ガスを吹込んで、装入廃棄物を溶融
スラグ化して、前記羽口より下方位置に設けた出湯口か
ら溶融物を抽出する廃棄物溶融炉において、前記出湯口
を炉体側方に、横向きに設け、前記出湯口を囲繞して抽
出溶融物を受ける前炉を配置し、同前炉内に前記出湯口
の周りに逆U字型に形成したヘッダーをU字の開口を下
向きにして設け、該ヘッダーに前記出湯口を指向して
数の燃焼用ガス吹付ノズルを配置したことを特徴とす
る。
SUMMARY OF THE INVENTION According to the present invention, a waste material is charged with a basicity adjuster and a bulk carbonaceous fuel from the top, and a combustion gas is blown from a tuyere provided at a lower portion. the was melted slag, the waste melting furnace to extract the molten material from hot water port formed in a lower position than the tuyere, the tap hole
The furnace side direction, sideways provided a forehearth for receiving the extract melts and surrounds the outflow position is arranged, the tap hole in the front furnace
U-shaped header around U-shaped opening
Provided in the orientation, double directed to the tap hole in the header
A number of combustion gas spray nozzles are arranged.

【0011】[0011]

【作用】出湯口から噴出するガスは、可燃成分であるC
Oを約30%含んでおり、これを燃焼させることによ
り、そのガス輻射にて溶融物が落下する出湯口先端部付
近の保熱を行うことが可能となる。
[Effect] The gas ejected from the tap is a combustible component C
O is contained in about 30%, and by burning this, it becomes possible to keep heat near the tip of the tap hole where the melt falls by the gas radiation.

【0012】また、前炉を設けることで、ガス輻射に加
え前炉内壁の固体輻射により、保熱効果をより一段と高
めることが可能である。一旦出湯口先端部から離れ、下
方空間へ落下し始めると、溶融物の温度が多少低下して
も固着成長は起こらない。
Further, by providing the forehearth, it is possible to further enhance the heat retention effect by solid radiation on the inner wall of the forehearth in addition to gas radiation. Once separated from the tip of the taphole and begins to fall into the lower space, no sticking growth occurs even if the temperature of the melt is slightly lowered.

【0013】さらに、燃焼用酸素含有ガスをノズルから
強制的に吹込むために、噴出ガスとの混合も促進され完
全燃焼も可能になるとともに、前炉は完全に大気と遮断
することが可能となり、作業環境も改善される。
Further, since the oxygen-containing gas for combustion is forcibly blown from the nozzle, the mixing with the ejected gas is promoted to enable complete combustion, and the forehearth can be completely shut off from the atmosphere. The environment is also improved.

【0014】[0014]

【実施例】図1は、本発明の溶融炉の全体構造を示す。FIG. 1 shows the entire structure of a melting furnace according to the present invention.

【0015】図1において、廃棄物溶融炉10は、上部
分の径を燃焼排ガスの空塔速度が低減するように、二段
の羽口1,2の中の上段羽口1の断面部分の径の5倍に
拡大した形状とし、内面下方を20〜80mm径のコー
クスを用いた場合の安息角以上の傾斜角度70度を持た
せた中空錐体形状の炉体3からなる。
In FIG. 1, a waste melting furnace 10 has a diameter of an upper portion which is a cross section of the upper tuyere 1 in two tuyeres 1 and 2 so that the superficial velocity of the flue gas is reduced. It has a hollow cone-shaped furnace body 3 having a shape enlarged to five times the diameter and having an inclination angle of 70 degrees or more at the repose angle when coke having a diameter of 20 to 80 mm is used below the inner surface.

【0016】炉体の羽口1,2は、炉体周囲にそれぞれ
6本ずつ設置され、上段羽口1、下段羽口2からは、炉
内コークスを燃焼させて高温雰囲気の火格子を形成する
ように、予熱された空気を吹き込む。
The tuyeres 1 and 2 of the furnace body are provided around the furnace body, each having six tuyeres. The upper tuyeres 1 and the lower tuyeres 2 burn the coke in the furnace to form a grate in a high-temperature atmosphere. Blow in preheated air as you do.

【0017】さらに、炉体3下部には、廃棄物の灰分,
不燃分やコークス,石灰石の灰分が高温で溶融,混合さ
れ、塩基度調整が行われた溶融スラグを排出する出湯口
4を設けている。
Further, the ash content of the waste,
A tap hole 4 is provided for discharging molten slag in which incombustible components, coke, and limestone are melted and mixed at a high temperature, and the basicity of which is adjusted.

【0018】その炉体3の天井の中央から廃棄物Aとコ
ークスBと溶融物の塩基度を調整する石灰石Cを装入す
る装入筒5が装着されている。
A charging cylinder 5 for charging waste A, coke B, and limestone C for adjusting the basicity of the melt is mounted from the center of the ceiling of the furnace body 3.

【0019】この装入筒5からの装入物は、廃棄物Aと
コークスBの40〜80%を層状にして、あるいは混合
して、石灰石Cとともに装入する。さらに、コークスB
を篩分けし、粒径大のものを装入筒5に、粒径小のもの
を周辺コークス装入口6に装入するようにコークスの粒
径を変更してもよい。この周辺コークス装入口6は外周
上面の4個所で内面天井に開口している。7は炉体3の
天井の一側に設けられたガス排気管を示し、ダスト堆積
がないよう垂直に接続している。また、このガス排気管
7は廃棄物装入筒5にも設けることができる。
The charge from the charging cylinder 5 is charged together with the limestone C in the form of a layer or a mixture of 40 to 80% of the waste A and the coke B. Furthermore, coke B
May be changed, and the particle size of the coke may be changed so that the large particle size is charged into the charging cylinder 5 and the small particle size is charged into the peripheral coke charging inlet 6. The peripheral coke inlet 6 is open to the inner ceiling at four locations on the outer peripheral upper surface. Reference numeral 7 denotes a gas exhaust pipe provided on one side of the ceiling of the furnace body 3, which is connected vertically so as not to accumulate dust. Further, the gas exhaust pipe 7 can be provided also in the waste charging cylinder 5.

【0020】8は装入口6から装入されたコークスBに
よって炉内周辺部に形成されたコークス充填域を示す。
9は炉底付近の中心部から中央の装入筒5の直下に形成
された高温炉床域を示し、その上方位置には装入筒5に
よって装入される廃棄物AとコークスBと石灰石Cとの
混合物からなる廃棄物充填域11が形成され、廃棄物A
とコークスB及び石灰石Cを装入する装入筒5の下端は
廃棄物充填域11の中に埋設されている。
Reference numeral 8 denotes a coke filling area formed in the furnace inside by the coke B charged from the charging inlet 6.
Reference numeral 9 denotes a high-temperature hearth region formed immediately below the central charging cylinder 5 from the center near the furnace bottom, and above the waste A, coke B, and limestone charged by the charging cylinder 5 are located above the high temperature hearth area. C, a waste-filled area 11 composed of a mixture with
The lower end of the charging cylinder 5 for charging the coke B and the limestone C is buried in the waste filling area 11.

【0021】さらに、12はコークス充填域8と炉天井
との間に形成された空間域であって、この空間域12の
形成によって、ガス排気管7から排出される排ガス中の
ダストの低減とガス排出をスムーズに行なうことができ
る。
Further, reference numeral 12 denotes a space formed between the coke filling region 8 and the furnace ceiling. The formation of this space 12 reduces the dust in the exhaust gas discharged from the gas exhaust pipe 7 and reduces the amount of dust. Gas can be discharged smoothly.

【0022】破線は、燃焼排ガスEの処理系を示し、炉
に設けられたガス排気管7より二次燃焼室13、空気予
熱器14、ガス冷却機15、集塵機16、洗煙装置1
7、誘引送風機18、煙突19を経て排出される例を示
しているが、可燃ガスとしての回収系とすることもでき
る。20は羽口1、2に空気予熱器14によって予熱さ
れた空気を送り込む送風ファンである。
A broken line indicates a processing system for the flue gas E, and a secondary combustion chamber 13, an air preheater 14, a gas cooler 15, a dust collector 16, and a smoke cleaning device 1 are connected through a gas exhaust pipe 7 provided in the furnace.
7. Although an example is shown in which the air is discharged through the induction blower 18 and the chimney 19, a recovery system as combustible gas may be used. Reference numeral 20 denotes a blower fan for sending air preheated by the air preheater 14 to the tuyeres 1 and 2.

【0023】21は、出湯口4を囲繞する前炉であっ
て、この前炉21には、流量調節弁22を介して導入箱
23からの燃焼用空気を出湯口4に吹き付けて、可燃性
の排気ガスEを燃焼するノズル部24が設けられ、これ
によって、溶融物Mの温度を約1450℃に維持し、出
湯口4の閉塞を防止するとともに、前炉21を加熱し、
さらに流下する溶融物Mは前炉の図示しない底部から、
製品化のための処理装置に搬出される。この間の溶融物
は大気と遮断され、周囲の環境を良好に維持することが
可能となる。また、25は前炉21内の排ガスを排出す
るための排気口であって、この排気ガスは炉体3からの
排気ガスと混合し、ガス処理される。
Reference numeral 21 denotes a forehearth which surrounds the tap hole 4. The forehearth 21 blows combustion air from the introduction box 23 through the flow control valve 22 to the tap hole 4 so as to be flammable. Is provided, which keeps the temperature of the melt M at about 1450 ° C., prevents the tap hole 4 from being clogged, and heats the forehearth 21;
Further, the melt M flowing down from the bottom (not shown) of the forehearth
It is carried out to a processing device for commercialization. During this time, the melt is shut off from the atmosphere, and the surrounding environment can be maintained well. Reference numeral 25 denotes an exhaust port for discharging exhaust gas in the forehearth 21, and this exhaust gas is mixed with exhaust gas from the furnace body 3 and subjected to gas treatment.

【0024】図2および図3は、図1に示す前炉の構造
の詳細を示す。
2 and 3 show details of the structure of the forehearth shown in FIG.

【0025】図2は、図1に示すノズル部24の拡大図
であって、図3は図2のA−A線から見た正面図であ
る。
FIG. 2 is an enlarged view of the nozzle section 24 shown in FIG. 1, and FIG. 3 is a front view as viewed from the line AA in FIG.

【0026】これらの図において、炉体3の底部に傾斜
して設けられた出湯口4の前面には燃焼用空気ヘッダー
26が出湯口4の孔41の上部を覆う逆U字形に形成さ
れ、このヘッダー26には、出湯口の孔41の上方を指
向して複数のノズル27が配置され、空気導入管28か
らの空気を吹き付けて出湯口4から溶融物とともに噴出
する可燃性ガスを効果的に燃焼する。
In these figures, a combustion air header 26 is formed in an inverted U-shape to cover the upper part of the hole 41 of the tap hole 4 on the front surface of the tap hole 4 provided at the bottom of the furnace body 3 at an angle. A plurality of nozzles 27 are arranged on the header 26 so as to be directed above the hole 41 of the tap hole, and blow air from the air inlet pipe 28 to effectively combustible gas ejected from the tap hole 4 together with the melt. Burns.

【0027】[0027]

【発明の効果】本発明によって以下の効果を奏する。According to the present invention, the following effects can be obtained.

【0028】(1)高温炉床を確実に形成し、高温炉床
から排出される溶融物の安定出湯を維持しつつ、経済的
な廃棄物溶融炉を実現できる。
(1) An economical waste melting furnace can be realized while reliably forming a high-temperature hearth and maintaining a stable tapping of the melt discharged from the high-temperature hearth.

【0029】(2)前炉を設置し、出湯口から噴出する
可燃ガスを燃焼させることにより、出湯口先端部の溶融
物の保温が可能となり、閉塞等を回避できる。
(2) By installing a forehearth and burning the combustible gas spouted from the tap, it is possible to keep the melt at the tip of the tap and to avoid clogging and the like.

【0030】(3)前炉を設置し、燃焼用空気を強制的
に吹き込むことで、周囲の作業環境を良好に維持すると
ともに、可燃ガスとの混合性が良好となり、完全燃焼が
可能となる。
(3) By installing a forehearth and forcibly blowing in the combustion air, the surrounding working environment is maintained well, the mixing with the combustible gas is improved, and complete combustion becomes possible. .

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

【図1】 本発明を適用した廃棄物溶融炉の全体構造を
示す。
FIG. 1 shows the entire structure of a waste melting furnace to which the present invention is applied.

【図2】 図1に示す前炉の構造の拡大図である。FIG. 2 is an enlarged view of the structure of the forehearth shown in FIG.

【図3】 図2をA−A線から見た正面図である。FIG. 3 is a front view of FIG. 2 as seen from line AA.

【符号の説明】[Explanation of symbols]

A 廃棄物 B コークス C 石灰石 D 送風空気 E 燃焼排ガス M 溶融物 1 上段羽口 2 下段羽口 3 炉体 4 出湯口 5 装入筒 6 コークス装入口 7 ガス排気管 8 コークス充填域 9 高温炉床域 10 溶融炉 11 廃棄物充填域 12 上部空間 13 二次燃焼室 14 空気予熱器 15 ガス冷却機 16 集塵機 17 洗煙装置 18 誘引送風機 19 煙突 20 送風ファン 21 前炉 22 流量調節弁 23 空気導入箱 24 ノズル部 25 前炉の排気口 26 燃焼用空気ヘ
ッダー 27 ノズル 28 空気導入管 41 出湯口の孔
Reference Signs List A waste B coke C limestone D blast air E flue gas M melt 1 upper tuyere 2 lower tuyere 3 furnace body 4 tap hole 5 charging cylinder 6 coke charging inlet 7 gas exhaust pipe 8 coke filling area 9 high temperature hearth Area 10 Melting furnace 11 Waste filling area 12 Upper space 13 Secondary combustion chamber 14 Air preheater 15 Gas cooler 16 Dust collector 17 Smoke washing device 18 Induction blower 19 Chimney 20 Ventilation fan 21 Forehearth 22 Flow control valve 23 Air introduction box 24 Nozzle part 25 Exhaust port of forehearth 26 Air header for combustion 27 Nozzle 28 Air introduction pipe 41 Hole of tap hole

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−5611(JP,A) 実開 昭53−111574(JP,U) 特公 昭41−11038(JP,B1) 特公 昭51−42433(JP,B2) ──────────────────────────────────────────────────続 き Continued on the front page (56) References JP-A-3-5611 (JP, A) JP-A-53-111574 (JP, U) JP-B-41-11038 (JP, B1) JP-B-51- 42433 (JP, B2)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 廃棄物に塩基度調整剤と塊状炭素質燃料
を頂部から装入し、下部に設けた羽口から燃焼用ガスを
吹込んで、装入廃棄物を溶融スラグ化して、前記羽口よ
り下方位置に設けた出湯口から溶融物を抽出する廃棄物
溶融炉において、前記出湯口を炉体側方に、横向きに設
け、前記出湯口を囲繞して抽出溶融物を受ける前炉を配
置し、同前炉内に前記出湯口の周りに逆U字型に形成し
たヘッダーをU字の開口を下向きにして設け、該ヘッダ
ーに前記出湯口を指向して複数の燃焼用ガス吹付ノズル
を配置した廃棄物溶融炉。
1. A basicity adjuster and a massive carbonaceous fuel are charged into waste from the top, and combustion gas is blown from a tuyere provided at a lower portion to convert the charged waste into a molten slag to form said wings. In a waste melting furnace for extracting molten material from a tap hole provided below the tap, the tap port is provided laterally on the side of the furnace body.
A forehearth surrounding the tap hole and receiving the extracted melt is formed in the forehearth in an inverted U-shape around the tap hole.
Header with the U-shaped opening facing down,
Waste melting furnace in which a plurality of combustion gas blowing nozzle directed to the tap hole to chromatography.
JP4087364A 1992-04-08 1992-04-08 Waste melting furnace Expired - Fee Related JP2629108B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4087364A JP2629108B2 (en) 1992-04-08 1992-04-08 Waste melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4087364A JP2629108B2 (en) 1992-04-08 1992-04-08 Waste melting furnace

Publications (2)

Publication Number Publication Date
JPH05288332A JPH05288332A (en) 1993-11-02
JP2629108B2 true JP2629108B2 (en) 1997-07-09

Family

ID=13912843

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4087364A Expired - Fee Related JP2629108B2 (en) 1992-04-08 1992-04-08 Waste melting furnace

Country Status (1)

Country Link
JP (1) JP2629108B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5525434B2 (en) * 1974-10-09 1980-07-05
JPS53111574U (en) * 1977-02-10 1978-09-06
JPH035611A (en) * 1989-05-30 1991-01-11 Nippon Steel Corp Waste melting furnace

Also Published As

Publication number Publication date
JPH05288332A (en) 1993-11-02

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