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JP3060197B2 - Incineration ash melting equipment - Google Patents
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JP3060197B2 - Incineration ash melting equipment - Google Patents

Incineration ash melting equipment

Info

Publication number
JP3060197B2
JP3060197B2 JP5337564A JP33756493A JP3060197B2 JP 3060197 B2 JP3060197 B2 JP 3060197B2 JP 5337564 A JP5337564 A JP 5337564A JP 33756493 A JP33756493 A JP 33756493A JP 3060197 B2 JP3060197 B2 JP 3060197B2
Authority
JP
Japan
Prior art keywords
incineration ash
ash
melting
gas
flame
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
JP5337564A
Other languages
Japanese (ja)
Other versions
JPH07190328A (en
Inventor
義明 小長谷
新一 三宅
宏次 関
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.)
Taiyo Nippon Sanso Corp
Original Assignee
Nippon Sanso Corp
Nippon Sanso Holdings 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 Nippon Sanso Corp, Nippon Sanso Holdings Corp filed Critical Nippon Sanso Corp
Priority to JP5337564A priority Critical patent/JP3060197B2/en
Publication of JPH07190328A publication Critical patent/JPH07190328A/en
Application granted granted Critical
Publication of JP3060197B2 publication Critical patent/JP3060197B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • 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、焼却灰溶融装置に関
し、詳しくは、都市ごみ,下水汚泥,その他の廃棄物を
焼却炉で焼却することにより発生する焼却灰、特に微粉
状態の焼却灰を溶融処理する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an incineration ash melting apparatus, and more particularly to an incineration ash generated by incineration of municipal solid waste, sewage sludge, and other wastes in an incinerator, particularly in the form of fine powder. The present invention relates to an apparatus for performing a melting process.

【0002】[0002]

【従来の技術】近年、都市ごみ,下水汚泥,その他の廃
棄物を焼却することにより発生する焼却灰は増加傾向に
あり、埋立処分地の確保が困難になってきている。この
ため、焼却灰の溶融処理による無公害化,減容化,資源
化が行われつつある。
2. Description of the Related Art In recent years, incinerated ash generated by incinerating municipal solid waste, sewage sludge, and other waste has been increasing, and it has become difficult to secure landfill sites. For this reason, non-pollution, volume reduction, and resource recycling are being performed by incineration ash melting.

【0003】特に、焼却炉に設けられた電気集塵機等に
捕集される微粉状態の焼却灰(微粉焼却灰)には、重金
属粒子が含まれていることが多いため、無公害化のため
にも溶融処理を行うことが求められており、このような
微粉焼却灰を溶融処理する方法としては、アーク炉法,
オイルバーナー法,プラズマ法等が実用化されている。
[0003] In particular, since incineration ash in the form of fine powder (fine incineration ash) collected by an electric dust collector or the like provided in an incinerator often contains heavy metal particles, it is necessary to eliminate pollution. It is also required to perform a melting treatment. As a method of melting such a fine powder incinerated ash, an arc furnace method,
An oil burner method, a plasma method and the like have been put to practical use.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記微
粉焼却灰は、溶融炉に投入した際に微粉のため再飛散し
やすいこと、微粉の堆積物は熱伝導度が低いことから、
表面からの加熱は効率が低い等、溶融処理が難しい状況
にある。
However, when the above-mentioned incinerated ash is introduced into a melting furnace, the ash is liable to be scattered because of the fine powder, and the deposit of the fine powder has low thermal conductivity.
Melting treatment is difficult due to low efficiency of heating from the surface.

【0005】また、従来の処理方法であるアーク炉法
は、焼却灰中の水分の管理が厳しいために操業方法が難
しく、オイルバーナー法では、表面溶融炉が実用化され
ているが、焼却灰中の空缶等の金属類まで完全溶融する
のは困難な状況にある。さらに、プラズマ法は、焼却灰
を金属成分を含めて完全溶融できるが、焼却灰1t当た
り800kWh以上の電力を必要とし、通常、ごみ発電
で発生した電力を充当しているが、ごみ発電電力の外販
環境が整備されつつある現在では、経済的な問題点を有
している。
[0005] The arc furnace method, which is a conventional treatment method, is difficult to operate due to strict control of the moisture in the incineration ash. In the oil burner method, a surface melting furnace has been put into practical use. It is difficult to completely melt metals such as empty cans inside. Furthermore, the plasma method can completely melt incineration ash including metal components, but requires power of 800 kWh or more per ton of incineration ash, and usually uses the power generated by refuse power generation. Now that the external sales environment is improving, it has economic problems.

【0006】そこで本発明は、再飛散することで処理が
困難であった微粉焼却灰を効率的に溶融処理することが
できる焼却灰溶融装置を提供することを目的としてい
る。
Accordingly, an object of the present invention is to provide an incineration ash melting apparatus capable of efficiently melting fine incineration ash which has been difficult to treat by re-scattering.

【0007】[0007]

【課題を解決するための手段】上記した目的を達成する
ため、本発明の焼却灰溶融装置は、焼却炉から発生する
焼却灰を溶融炉で溶融処理する装置において、前記溶融
炉に、酸素又は酸素富化ガスを支燃性ガスとする少なく
とも1個の溶射バーナーを、炉壁に火炎が投射されるよ
うに設けるとともに、前記焼却灰の少なくとも一部を前
記溶射バーナーの火炎中に投入する経路を設けたことを
特徴としている。
Means for Solving the Problems In order to achieve the above-mentioned object, an incineration ash melting apparatus according to the present invention is an apparatus for melting and processing incineration ash generated from an incinerator in a melting furnace. less the oxygen-enriched gas and combustion-supporting gas
With one spray burner, a flame is projected on the furnace wall
And a path for introducing at least a part of the incineration ash into the flame of the thermal spray burner is provided.

【0008】また、本発明は、上記構成において、前記
溶融炉の排ガス経路に、前記酸素又は酸素富化ガス、あ
るいは前記焼却灰を前記溶射バーナーの火炎中に搬送す
るガスを予熱する装置を設けたことを特徴としている。
Further, according to the present invention, in the above structure, an apparatus for preheating the oxygen or the oxygen-enriched gas or the gas for conveying the incinerated ash into the flame of the thermal spray burner is provided in the exhaust gas path of the melting furnace. It is characterized by that.

【0009】なお、焼却灰を溶射バーナーの火炎中に供
給する手段は、搬送ガスによる他、スクリューフィーダ
ー等により直接バーナーに供給してもよい。また、溶射
バーナーの燃料は、気体,液体,固体のいずれでもよ
く、最も経済的に入手できる燃料を適宜選択すればよ
い。
The means for supplying the incinerated ash into the flame of the thermal spray burner may be supplied directly to the burner by a screw feeder or the like, instead of using a carrier gas. Further, the fuel for the thermal spray burner may be any of gas, liquid and solid, and the most economically available fuel may be appropriately selected.

【0010】[0010]

【作 用】前記溶射バーナーの火炎中に投入された焼却
灰は、該溶射バーナーの火炎中で溶融軟化し、溶射バー
ナー正面の炉壁に付着した後、下流に流れて排出され
る。また、溶射バーナー正面の炉壁には、溶融した焼却
灰(溶融灰)が付着しているので、火炎中で溶融しない
粒子は、この溶融灰で捕捉されるので、飛散することが
ない。
[Operation] The incineration ash introduced into the flame of the above-mentioned thermal spray burner melts and softens in the flame of the thermal spray burner, adheres to the furnace wall in front of the thermal spray burner, and then flows downstream to be discharged. In addition, since molten incineration ash (molten ash) adheres to the furnace wall in front of the thermal spray burner, particles that do not melt in the flame are captured by the molten ash and do not scatter.

【0011】さらに、前記溶射バーナーに供給される酸
素又は酸素富化ガス、あるいは微粉焼却灰を搬送するガ
スを、前記溶融炉からの排ガスが有する熱エネルギーで
予熱することにより、溶射バーナーで発生する火炎温度
を上昇させることができ、焼却灰の溶融処理能力を向上
できる。
Further, oxygen or an oxygen-enriched gas supplied to the spraying burner or a gas carrying fine powder incineration ash is preheated by thermal energy of exhaust gas from the melting furnace, and is generated by the spraying burner. The flame temperature can be raised, and the melting processing capacity of incinerated ash can be improved.

【0012】なお、粗大な焼却灰は、通常の方法で溶融
炉内に投入され、前記溶射バーナーあるいは別のバーナ
ー等の熱源により溶融処理することができる。
The coarse incineration ash can be put into a melting furnace by a usual method and can be melted by a heat source such as the above-mentioned thermal spray burner or another burner.

【0013】[0013]

【実施例】以下、本発明を、図面に示す一実施例に基づ
いてさらに詳細に説明する。図1に示す焼却灰溶融装置
は、焼却灰を溶融するための溶射バーナー1を備えた溶
融炉2と、前記溶射バーナー1に燃料,支燃性ガス及び
微粉焼却灰をそれぞれ供給するための燃料供給経路3、
支燃性ガス供給経路4及び焼却灰供給経路5と、該溶融
炉2で溶融した焼却灰(溶融灰,溶融スラグ)を取出す
溶融灰取出口6と、溶融炉2で発生した燃焼ガスを排出
する排ガス経路7とにより構成されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in more detail with reference to an embodiment shown in the drawings. The incineration ash melting apparatus shown in FIG. 1 includes a melting furnace 2 having a spraying burner 1 for melting incineration ash, and a fuel for supplying a fuel, a combustion supporting gas, and fine powder incineration ash to the spraying burner 1, respectively. Supply route 3,
A combustion supporting gas supply path 4 and an incineration ash supply path 5, a molten ash outlet 6 for taking out incinerated ash (molten ash and molten slag) melted in the melting furnace 2, and discharging a combustion gas generated in the melting furnace 2. Exhaust gas path 7.

【0014】前記溶射バーナー1は、炉壁21に火炎が
投射されるように、噴射口の正面が炉壁21に対向して
溶融炉2に設置されており、該炉壁21は、炉壁21部
分に付着した溶融灰が炉下部の溶融灰取出口6方向に自
然流下するように形成されている。
The spraying burner 1 has a flame on the furnace wall 21.
In order to be projected, the front of the injection port is installed in the melting furnace 2 so as to face the furnace wall 21, and the furnace wall 21 is configured such that molten ash adhering to the furnace wall 21 portion is located in the lower part of the furnace. It is formed so as to flow naturally in the direction of the molten ash outlet 6.

【0015】前記燃料供給経路3は、液体燃料(重油
等)を使用する場合には、図に示すように燃料貯槽31
及び燃料ポンプ32により構成されるもので、他の気体
燃料,固体燃料を使用する場合には、それぞれ最適な構
成で形成される。
When a liquid fuel (heavy oil or the like) is used, the fuel supply path 3 has a fuel storage tank 31 as shown in FIG.
And other fuel pumps 32. When other gaseous fuels and solid fuels are used, they are formed with optimal configurations.

【0016】前記支燃性ガス供給経路4は、酸素供給設
備41と熱交換器8とにより構成されており、前記酸素
供給設備41から供給される支燃性ガス、即ち酸素ガス
あるいは酸素富化ガスは、熱交換器8で排ガスと熱交換
して昇温した後に前記溶射バーナー1に供給される。
The combustion supporting gas supply path 4 comprises an oxygen supply facility 41 and a heat exchanger 8. The combustion supporting gas supplied from the oxygen supply facility 41, that is, oxygen gas or oxygen-enriched gas is supplied. The gas is heat-exchanged with the exhaust gas in the heat exchanger 8 to be heated and then supplied to the thermal spray burner 1.

【0017】前記焼却灰供給経路5は、微粉焼却灰を定
量供給するためのフィーダー51と、焼却灰搬送用の搬
送ガスとなる空気を供給する圧縮機52とを備えてお
り、前記フィーダー51から供給される微粉焼却灰は、
圧縮機52で昇圧され、前記熱交換器8で排ガスと熱交
換して昇温した搬送ガスに同伴されて前記溶射バーナー
1に供給される。
The incineration ash supply path 5 includes a feeder 51 for supplying a constant amount of fine incineration ash, and a compressor 52 for supplying air serving as a carrier gas for incineration ash conveyance. The supplied fine powder incineration ash is
The pressure is increased by the compressor 52, the heat is exchanged with the exhaust gas by the heat exchanger 8, and the carrier gas is supplied to the spraying burner 1 while being accompanied by the heated carrier gas.

【0018】燃料供給経路3から溶射バーナー1に供給
される燃料は、支燃性ガス供給経路4から供給される支
燃性ガスと混合して燃焼し、高温の火炎を発生する。そ
して、焼却灰供給経路5から溶射バーナー1に供給さ
れ、前記火炎中に投入された微粉焼却灰は、該火炎中で
溶融軟化してバーナー正面の炉壁21に付着する。ま
た、火炎中で溶融しなかった微粉焼却灰は、火炎に同伴
されて炉壁21に投射され、該炉壁21に付着している
溶融灰に捕捉され、ここで溶融する。
The fuel supplied from the fuel supply path 3 to the thermal spray burner 1 mixes with the oxidizing gas supplied from the oxidizing gas supply path 4 and burns to generate a high-temperature flame. The fine powder incineration ash supplied from the incineration ash supply path 5 to the thermal spray burner 1 and introduced into the flame melts and softens in the flame and adheres to the furnace wall 21 in front of the burner. Further, the fine powder incineration ash that has not been melted in the flame is projected on the furnace wall 21 accompanying the flame, is captured by the molten ash attached to the furnace wall 21, and is melted here.

【0019】溶融炉2内で溶融した焼却灰、即ち溶融灰
は、炉壁21から炉下部に流れて炉底部の溶融灰取出口
6を介して取出され、適宜な手段で粉砕されて骨材等と
して利用される。また、炉内で発生したガスは、前記排
ガス経路7から排出される。
The incinerated ash melted in the melting furnace 2, that is, the molten ash flows from the furnace wall 21 to the lower part of the furnace, is taken out through the molten ash outlet 6 at the furnace bottom, is pulverized by appropriate means, and is aggregated. Used as etc. The gas generated in the furnace is discharged from the exhaust gas path 7.

【0020】排ガス経路7は、集塵器71,排風機72
及び排ガス温度を必要に応じて調節するための空気吸入
口73,74を備えるとともに、前記支燃性ガス及び搬
送ガスを加熱するための前記熱交換器8を備えている。
溶融炉2から排出された排ガスは、まず、空気吸入口7
3から流量調節用のダンパー73aを介して吸入した空
気と混合し、所定の温度、例えば前記熱交換器8が耐え
られる温度となって熱交換器8に導入され、前記支燃性
ガス及び搬送ガスを昇温する。
The exhaust gas path 7 includes a dust collector 71 and an exhaust fan 72.
And air inlets 73 and 74 for adjusting the exhaust gas temperature as required, and the heat exchanger 8 for heating the combustion supporting gas and the carrier gas.
The exhaust gas discharged from the melting furnace 2 is first supplied to the air inlet 7
3 and mixed with air sucked through a flow control damper 73a, and is introduced into the heat exchanger 8 at a predetermined temperature, for example, a temperature that the heat exchanger 8 can withstand. Raise the temperature of the gas.

【0021】上記熱交換器8を導出した排ガスは、さら
に空気吸入口74から流量調節用のダンパー74aを介
して吸入した空気と混合し、前記集塵器71の耐熱温度
以下になって集塵器71に導入され、該排ガスに同伴さ
れている微粉を分離した後、排風機72から排出され
る。なお、集塵器71で捕集した微粉は、再度溶射バー
ナー1に供給して溶融処理してもよいが、この微粉は、
一度溶融した球状品であるので、そのまま有効利用する
ことも可能である。
The exhaust gas discharged from the heat exchanger 8 is further mixed with air sucked through an air inlet 74 through a damper 74a for adjusting the flow rate, and when the temperature of the exhaust gas falls below the heat-resistant temperature of the dust collector 71, the dust is collected. After being introduced into the exhaust device 71 and separating fine powder accompanying the exhaust gas, the exhaust gas is discharged from the exhaust fan 72. The fine powder collected by the dust collector 71 may be supplied again to the thermal spray burner 1 and subjected to a melting treatment.
Since it is a spherical product once melted, it can be effectively used as it is.

【0022】また、焼却灰供給経路5から供給される微
粉焼却灰以外の塊状の焼却灰は、通常の手段により溶融
炉2内に供給し、前記溶射バーナー1あるいは別に設け
た溶融用バーナー(図示せず)により加熱溶融すること
ができる。
In addition, lump incineration ash other than the fine powder incineration ash supplied from the incineration ash supply path 5 is supplied into the melting furnace 2 by ordinary means, and is supplied to the spraying burner 1 or a separately provided melting burner (see FIG. (Not shown).

【0023】なお、溶融炉2の形状は、上記実施例に限
定されるものではなく、例えば、図2に示すように、溶
射バーナー1を取付けた焼却灰溶融部22の一側に上下
方向に通路23を設け、該通路23の上方に排ガス導出
口を、下方に溶融灰取出口をそれぞれ設けるようにして
もよく、図3に示すように、上方に排ガス導出口を、下
方に溶融灰取出口をそれぞれ設けた上下方向の通路24
の側壁に火炎が投射されるように溶射バーナー1を取付
けるようにしてもよい。
The shape of the melting furnace 2 is not limited to the above embodiment. For example, as shown in FIG. A passage 23 may be provided, and an exhaust gas outlet may be provided above the passage 23 and a molten ash outlet may be provided below the passage 23. As shown in FIG. Up and down passages 24 each having an outlet
The spraying burner 1 may be attached so that the flame is projected on the side wall of the nozzle.

【0024】[0024]

【0025】[0025]

【発明の効果】以上説明したように、本発明の焼却灰溶
融装置は、炉壁に火炎が投射されるように溶融炉に設け
た溶射バーナーの火炎中に、焼却灰を投入するように構
成したので、溶射バーナーの火炎中に投入された焼却灰
は、溶射バーナーの火炎中で溶融軟化し、溶射バーナー
正面の炉壁に付着した後、下流に流れて排出され、しか
も、火炎中で溶融しきれない焼却灰は、炉壁に付着した
溶融灰に捕捉され、従来、再飛散することで処理が困難
であった微粉焼却灰を効率的に溶融処理することができ
る。
As described above, the incineration ash melting apparatus of the present invention is provided in a melting furnace so that a flame is projected on the furnace wall.
Since the incineration ash was injected into the flame of the thermal spray burner, the incineration ash injected into the flame of the thermal spray burner
Melts and softens in the flame of the spray burner,
After adhering to the front furnace wall, it flows downstream and is discharged,
But the incineration ash that could not be melted in the flame adhered to the furnace wall
Difficult to treat by being trapped by molten ash and re-scattering conventionally
Was able to efficiently melt the fine powder incineration ash
You.

【0026】さらに、本発明の焼却灰溶融装置は、酸素
又は酸素富化ガスを支燃性ガスとする溶射バーナーを用
いているので、2500℃以上の高温の火炎を得ること
が可能であり、金属類迄含めた完全溶融処理を行うこと
ができる。しかも、完全溶融処理ベースで比較すると、
従来のプラズマ法等と比べて経済的な運転を行うことが
できる。
Further, since the incineration ash melting apparatus of the present invention uses a thermal spray burner using oxygen or an oxygen-enriched gas as a supporting gas, a high-temperature flame of 2500 ° C. or more can be obtained. A complete melting process including metals can be performed. Moreover, when compared on a complete melting treatment basis,
Economical operation can be performed as compared with a conventional plasma method or the like.

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

【図1】 本発明の焼却灰溶融装置の一実施例を示す系
統図である。
FIG. 1 is a system diagram showing one embodiment of an incineration ash melting device of the present invention.

【図2】 溶融炉の他の実施例を示す概略断面図であ
る。
FIG. 2 is a schematic sectional view showing another embodiment of the melting furnace.

【図3】 溶融炉のさらに他の実施例を示す概略断面図
である。
FIG. 3 is a schematic sectional view showing still another embodiment of the melting furnace.

【符号の説明】[Explanation of symbols]

1…溶射バーナー、2…溶融炉、3…燃料供給経路、4
…支燃性ガス供給経路、5…焼却灰供給経路、6…溶融
灰取出口、7…排ガス経路、8…熱交換器
DESCRIPTION OF SYMBOLS 1 ... Thermal spray burner, 2 ... Melting furnace, 3 ... Fuel supply path, 4
... combustible gas supply path, 5 ... incineration ash supply path, 6 ... molten ash outlet, 7 ... exhaust gas path, 8 ... heat exchanger

フロントページの続き (56)参考文献 特開 平2−298714(JP,A) 特表 平3−504463(JP,A) (58)調査した分野(Int.Cl.7,DB名) F23J 1/00 - 1/02 F23G 7/00 F23G 5/00 Continuation of the front page (56) References JP-A-2-298714 (JP, A) JP-A-3-504463 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F23J 1 / 00-1/02 F23G 7/00 F23G 5/00

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 焼却炉から発生する焼却灰を溶融炉で溶
融処理する装置において、前記溶融炉に、酸素又は酸素
富化ガスを支燃性ガスとする少なくとも1個の溶射バー
ナーを、炉壁に火炎が投射されるように設けるととも
に、前記焼却灰の少なくとも一部を前記溶射バーナーの
火炎中に投入する経路を設けたことを特徴とする焼却灰
溶融装置。
1. A device for melt processing in a melting furnace the ash generated from the incinerator, the melting furnace, at least one spray burners using oxygen or oxygen-enriched gas and combustion-supporting gas, the furnace wall To be able to project a flame on
The incinerated ash melting device, characterized in that at least a portion of the ash is provided a path to be introduced into the flame of the thermal spray burner.
【請求項2】 前記溶融炉の排ガス経路に、前記支燃性
ガスを予熱する装置を設けたことを特徴とする請求項1
記載の焼却灰溶融装置。
2. An apparatus for preheating the combustion-supporting gas in an exhaust gas path of the melting furnace.
The incinerated ash melting device as described.
【請求項3】 前記焼却灰を搬送ガスで搬送して前記溶
射バーナーの火炎中に投入するよう構成するとともに、
前記溶融炉の排ガス経路に、前記搬送ガスを予熱する装
置を設けたことを特徴とする請求項1記載の焼却灰溶融
装置。
3. A configuration in which the incinerated ash is conveyed by a carrier gas and injected into the flame of the thermal spray burner.
The incineration ash melting device according to claim 1, wherein a device for preheating the carrier gas is provided in an exhaust gas path of the melting furnace.
JP5337564A 1993-12-28 1993-12-28 Incineration ash melting equipment Expired - Lifetime JP3060197B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5337564A JP3060197B2 (en) 1993-12-28 1993-12-28 Incineration ash melting equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5337564A JP3060197B2 (en) 1993-12-28 1993-12-28 Incineration ash melting equipment

Publications (2)

Publication Number Publication Date
JPH07190328A JPH07190328A (en) 1995-07-28
JP3060197B2 true JP3060197B2 (en) 2000-07-10

Family

ID=18309835

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5337564A Expired - Lifetime JP3060197B2 (en) 1993-12-28 1993-12-28 Incineration ash melting equipment

Country Status (1)

Country Link
JP (1) JP3060197B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4095136B2 (en) * 1997-06-17 2008-06-04 大陽日酸株式会社 Glass melting method and apparatus
JP4624971B2 (en) * 2006-10-18 2011-02-02 大同特殊鋼株式会社 Glass melting equipment
JP2011037706A (en) * 2010-09-17 2011-02-24 Daido Steel Co Ltd Glass melting apparatus

Also Published As

Publication number Publication date
JPH07190328A (en) 1995-07-28

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