JPH10288321A - Electrical resistance melting furnace of refuse incinerated ash - Google Patents

Electrical resistance melting furnace of refuse incinerated ash

Info

Publication number
JPH10288321A
JPH10288321A JP9944797A JP9944797A JPH10288321A JP H10288321 A JPH10288321 A JP H10288321A JP 9944797 A JP9944797 A JP 9944797A JP 9944797 A JP9944797 A JP 9944797A JP H10288321 A JPH10288321 A JP H10288321A
Authority
JP
Japan
Prior art keywords
electrode
molten
furnace
graphite electrode
melting furnace
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.)
Withdrawn
Application number
JP9944797A
Other languages
Japanese (ja)
Inventor
Mutsuo Maki
睦夫 牧
Takeji Nagasato
武治 長里
Yoshifumi Hasegawa
佳史 長谷川
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 JP9944797A priority Critical patent/JPH10288321A/en
Publication of JPH10288321A publication Critical patent/JPH10288321A/en
Withdrawn legal-status Critical Current

Links

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Furnace Details (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the corrosion of electrodes by molten salt and prevent the electric current from the electrodes from flowing to the molten salt and enhance melting efficiency to molten slags. SOLUTION: This melting furnace arranges an electrode 3 to rise and fall freely inside a cylinder-shaped body 4 supported on an upper furnace cover 2 in a refuse incinerated ash melting electrical resistance furnace provided with the graphite electrode 3 by using an electrode lift device while the cylinder- shaped body 4 comprises an insulating refractory in the outer layer and an expandable refractory in the inner layer. In this case, the graphite electrode 3 is arranged to connect an electrode having a specified length.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、都市ごみ、下水汚
泥、産業廃棄物等の廃棄物を焼却した際に発生する焼却
灰を溶融してスラグ化する焼却灰の電気抵抗溶融炉に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an incineration ash electric resistance melting furnace which melts incineration ash generated when incinerating waste such as municipal solid waste, sewage sludge, industrial waste and the like to form slag.

【0002】[0002]

【従来の技術】都市ごみの焼却灰中には、重金属等の有
害物質が多量に含まれているため、都市ごみの焼却灰を
直接埋立て処理したり投棄処理したりすことは有害物質
の溶出等から安全上問題がある。
2. Description of the Related Art Since incinerated ash from municipal waste contains a large amount of harmful substances such as heavy metals, it is difficult to directly dispose of or incinerate municipal incinerated ash by leaching harmful substances. There is a safety problem from the above.

【0003】このため、特開平7−77318号公報に
交流電気抵抗溶融炉により焼却灰を溶融処理してスラグ
化することが提案されている。
[0003] For this reason, Japanese Patent Application Laid-Open No. 7-77318 proposes that slag is formed by melting incinerated ash using an AC electric resistance melting furnace.

【0004】図5は従来の交流電気抵抗溶融炉の全体図
で、炉本体1の上部炉蓋2に3本の黒鉛電極3を設け、
黒鉛電極3の先端を炉の溶融スラグに埋没させ、黒鉛電
極3に交流電圧をかけることにより溶融スラグに交流通
電し、溶解状態になった溶融スラグの電気抵抗に基づく
ジュール熱により灰自体を抵抗体にして電気抵抗熱を発
生させ、その熱でスラグの溶解状態の維持と、溶融スラ
グからの伝熱で灰を加熱、溶融する。炉内に供給された
焼却灰は電気抵抗加熱によって溶融処理され、下層より
溶融メタル、溶融スラグ、溶融塩の各層が生成される。
溶融メタルは前記溶融メタル出湯口1aより出湯され、
同様に溶融スラグは前記溶融スラグ出湯口1bより、溶
融塩は溶融塩出湯口1cより出湯される。
FIG. 5 is an overall view of a conventional AC electric resistance melting furnace, in which three graphite electrodes 3 are provided on an upper furnace lid 2 of a furnace body 1.
The tip of the graphite electrode 3 is immersed in the molten slag of the furnace, AC current is applied to the molten slag by applying an AC voltage to the graphite electrode 3, and the ash itself is resisted by Joule heat based on the electric resistance of the molten slag in a molten state. The body generates electric resistance heat, and the heat keeps the molten state of the slag and heats and melts the ash by the heat transfer from the molten slag. The incineration ash supplied into the furnace is melted by electric resistance heating, and each layer of molten metal, molten slag, and molten salt is generated from the lower layer.
The molten metal is discharged from the molten metal tap hole 1a,
Similarly, the molten slag is discharged from the molten slag outlet 1b, and the molten salt is discharged from the molten salt outlet 1c.

【0005】[0005]

【発明が解決しようとする課題】ごみ焼却炉から発生す
る飛灰中にはKCl,NaCl等の塩類が大量に含まれ
ているため、焼却灰を溶融する際には溶融スラグととも
に溶融塩が生成される。電極は、操業中、溶融塩の2N
++2C1-または2K++2C1-と酸化反応すること
で腐食するという問題がある。
Since fly ash generated from a refuse incinerator contains a large amount of salts such as KCl and NaCl, molten salt is generated together with molten slag when melting the incinerated ash. Is done. During operation, the electrode is
a + + 2C1 - or 2K + + 2C1 - that there is a problem of corrosion by oxidation.

【0006】また、溶融塩は導電度が高いので、電極か
らの電流が低抵抗部分の溶融塩の層に集中して流れて、
溶融スラグにおいて発生するジュール熱が減少し、溶融
スラグが十分加熱されなくなるという問題もある。
Further, since the molten salt has a high conductivity, the current from the electrode flows intensively into the molten salt layer in the low resistance portion,
There is also a problem that Joule heat generated in the molten slag is reduced and the molten slag is not sufficiently heated.

【0007】そこで、本発明は、溶融塩による電極の腐
食を防止するとともに、電極からの電流が溶融塩に流れ
るのを防止して、溶融スラグに対する溶融効率を高める
ことができるごみ焼却灰の電気抵抗溶融炉を提供するも
のである。
Therefore, the present invention provides an electric power generation system for refuse incineration ash which prevents corrosion of an electrode by molten salt and prevents current from the electrode from flowing into the molten salt, thereby improving the melting efficiency of molten slag. A resistance melting furnace is provided.

【0008】[0008]

【課題を解決するための手段】本発明のごみ焼却灰の電
気抵抗溶融炉は、黒鉛電極を備えたごみ焼却灰の電気抵
抗溶融炉において、上部炉蓋に支持された筒状体の内側
に、黒鉛電極が電極昇降装置により昇降自在に配置さ
れ、前記筒状体は外層が絶縁性耐火物で内層が発泡性耐
火物で構成されていることを特徴とする。
According to the present invention, there is provided an electric resistance melting furnace for refuse incineration ash provided with a graphite electrode, wherein the electric resistance melting furnace for refuse incineration ash is provided inside a tubular body supported by an upper furnace lid. The graphite electrode is arranged so as to be able to move up and down by an electrode elevating device, and the cylindrical body has an outer layer made of an insulating refractory and an inner layer made of a foaming refractory.

【0009】黒鉛電極は所定長さの電極を接続して構成
された電極を用いる。
As the graphite electrode, an electrode formed by connecting electrodes of a predetermined length is used.

【0010】[0010]

【発明の実施の形態】図1は本発明の電気抵抗溶融炉の
実施例を示す全体図、図2は図1に示す筒状体と黒鉛電
極の断面図で、図2−(a)は横断面図、図2−(b)
は縦断面図であり、図3は図1に示す筒状体と黒鉛電極
の斜視図である。
FIG. 1 is an overall view showing an embodiment of an electric resistance melting furnace according to the present invention, FIG. 2 is a sectional view of a tubular body and a graphite electrode shown in FIG. 1, and FIG. Cross-sectional view, FIG. 2- (b)
FIG. 3 is a longitudinal sectional view, and FIG. 3 is a perspective view of the tubular body and the graphite electrode shown in FIG.

【0011】図1に示す電気抵抗溶融炉は三相交流電気
抵抗溶融炉で、炉本体1の上部炉蓋2に3本の黒鉛電極
3を設け、各黒鉛電極3は上部炉蓋2に支持された筒状
体4の内側を電極昇降装置5により昇降自在に設けられ
ている。炉本体1には、炉内に形成される溶融メタル、
溶融スラグ及び溶融塩を出湯するため、溶融メタル出湯
口1a、溶融スラグ出湯口1b及び溶融塩を出湯する溶
融塩出湯口1cが設けられている。また、上部炉蓋2に
は、焼却灰を供給する灰供給口2a及び電気炉内で発生
したガスを排出する排ガス出口2bを設ける。
The electric resistance melting furnace shown in FIG. 1 is a three-phase AC electric resistance melting furnace, in which three graphite electrodes 3 are provided on an upper furnace lid 2 of a furnace body 1, and each graphite electrode 3 is supported by the upper furnace lid 2. The inside of the formed cylindrical body 4 is provided so as to be movable up and down by an electrode lifting device 5. Furnace body 1 includes molten metal formed in the furnace,
In order to discharge molten slag and molten salt, a molten metal tapping port 1a, a molten slag tapping port 1b and a molten salt tapping port 1c for tapping molten salt are provided. The upper furnace lid 2 is provided with an ash supply port 2a for supplying incinerated ash and an exhaust gas outlet 2b for discharging gas generated in the electric furnace.

【0012】図2及び図3に示すように、筒状体4は、
外層が絶縁性耐火物4aで内層が発泡性耐火物4bで構
成され、筒状体4は電気炉内の溶融スラグ層に浸漬する
ように下方へ向かって設けられている。外層の絶縁性耐
火物としては、溶融塩に対して絶縁性を有する耐火物、
例えば、珪石れんがまたはマグネシアれんが等を用い
る。また、内層の発泡性耐火物は、膨張する電極と外層
の絶縁性耐火物との間でクッション材として作用する、
例えば、断熱質のプラスチック耐火物等で構成する。
As shown in FIGS. 2 and 3, the cylindrical body 4 is
The outer layer is composed of an insulating refractory 4a and the inner layer is composed of a foaming refractory 4b, and the tubular body 4 is provided downward so as to be immersed in a molten slag layer in an electric furnace. As the insulating refractory of the outer layer, a refractory having an insulating property against molten salt,
For example, silica brick or magnesia brick is used. Further, the foamable refractory of the inner layer acts as a cushioning material between the expanding electrode and the insulating refractory of the outer layer,
For example, it is made of a heat-insulating plastic refractory or the like.

【0013】黒鉛電極3の先端は筒状体4の下端から突
出させる。筒状体4内の黒鉛電極3は所定長さの黒鉛電
極3の端部に形成された雄ねじ3a及び雌ねじ3bによ
り接続されている。
The end of the graphite electrode 3 projects from the lower end of the cylindrical body 4. The graphite electrode 3 in the tubular body 4 is connected by a male screw 3a and a female screw 3b formed at an end of the graphite electrode 3 having a predetermined length.

【0014】前記の構成において、黒鉛電極に交流電圧
を印加することにより溶融スラグに交流通電し、溶解状
態になった溶融スラグの電気抵抗に基づくジュール熱に
より灰自体を抵抗体にして電気抵抗熱を発生させ、その
熱でスラグの溶解状態の維持と、溶融スラグからの伝熱
で灰を加熱、溶融する。灰の溶融により炉内に下層から
溶融メタル層、溶融スラグ層、溶融塩層が生成される。
溶融メタルは溶融メタル出湯口1aより出湯され、同様
に溶融スラグは溶融スラグ出湯口1bより、溶融塩は溶
融塩出湯口1cより出湯される。
In the above configuration, an alternating current is applied to the molten slag by applying an alternating voltage to the graphite electrode, and the ash itself is converted into a resistor by the Joule heat based on the electric resistance of the molten slag in a molten state, thereby obtaining an electric resistance heat. Is generated, and the ash is heated and melted by maintaining the molten state of the slag by the heat and by transferring heat from the molten slag. Due to the melting of the ash, a molten metal layer, a molten slag layer, and a molten salt layer are generated from a lower layer in the furnace.
The molten metal is discharged from the molten metal outlet 1a, the molten slag is discharged from the molten slag outlet 1b, and the molten salt is discharged from the molten salt outlet 1c.

【0015】黒鉛電極3は溶融塩から筒状体4で保護さ
れているため、溶融塩に接しないので、溶融塩により浸
食されることがない。また、黒鉛電極3は生成される溶
融塩より下方の位置までに配設される筒状体4により溶
融塩と電気的に絶縁状態にあるため、黒鉛電極3からの
電流が低抵抗部分の溶融塩層に集中して流れることがな
くなり、溶融スラグ層を流れる電流により溶融スラグが
十分に加熱される。
Since the graphite electrode 3 is protected from the molten salt by the cylindrical body 4 and does not come into contact with the molten salt, it is not eroded by the molten salt. Further, since the graphite electrode 3 is electrically insulated from the molten salt by the tubular body 4 disposed to a position below the generated molten salt, the current from the graphite electrode 3 melts the low-resistance portion. The molten slag is no longer concentrated and flows, and the molten slag is sufficiently heated by the current flowing through the molten slag layer.

【0016】筒状体4から突出している黒鉛電極3の先
端が操業に伴い損耗すると、黒鉛電極3の上端に所定長
さの黒鉛電極3を螺合して接続し、電極昇降装置5で黒
鉛電極3を降下させて筒状体4から突出させる。
When the tip of the graphite electrode 3 protruding from the cylindrical body 4 is worn out during operation, the graphite electrode 3 having a predetermined length is screwed and connected to the upper end of the graphite electrode 3, and the graphite lifting and lowering device 5 is used for the graphite electrode 3. The electrode 3 is lowered to project from the cylindrical body 4.

【0017】図4は本発明の電気抵抗溶融炉の別実施例
を示す全体図で、図4に示す電気抵抗溶融炉は単相交流
電気抵抗溶融炉で、炉本体1の上部炉蓋2に1本の黒鉛
電極3を設け、この黒鉛電極3に対向して炉本体1の炉
底に炉底電極6を設け、黒鉛電極3は上部炉蓋2に支持
された筒状体4の内側を電極昇降装置5により昇降自在
に設けられている。
FIG. 4 is an overall view showing another embodiment of the electric resistance melting furnace of the present invention. The electric resistance melting furnace shown in FIG. One graphite electrode 3 is provided, and a furnace bottom electrode 6 is provided on the furnace bottom of the furnace main body 1 so as to face the graphite electrode 3. The graphite electrode 3 covers the inside of the cylindrical body 4 supported by the upper furnace lid 2. It is provided to be able to move up and down by an electrode lifting device 5.

【0018】本実施例の単相交流電気抵抗溶融炉は炉本
体1、上部炉蓋2、筒状体4の構造は前記実施例と同一
構成なので、その説明は省略する。
In the single-phase AC electric resistance melting furnace of this embodiment, the structures of the furnace main body 1, the upper furnace lid 2, and the cylindrical body 4 are the same as those of the above-described embodiment, and the description thereof will be omitted.

【0019】前記構成において、黒鉛電極と炉底電極間
に交流電圧を印加することにより溶融スラグに交流通電
し、溶解状態になった溶融スラグの電気抵抗に基づくジ
ュール熱によりスラグの溶解状態の維持と、溶融スラグ
からの伝熱で灰を加熱、溶融する。灰の溶融により炉内
に溶融メタル層、溶融スラグ層、溶融塩層が生成され、
溶融メタルは前記溶融メタル出湯口1aより出湯され、
同様に溶融スラグは前記溶融スラグ出湯口1bより、溶
融塩は溶融塩出湯口1cより出湯される。
In the above configuration, an alternating current is applied to the molten slag by applying an alternating voltage between the graphite electrode and the furnace bottom electrode, and the molten state of the slag is maintained by Joule heat based on the electric resistance of the molten slag in the molten state. Then, the ash is heated and melted by the heat transfer from the molten slag. The melting of the ash creates a molten metal layer, a molten slag layer, and a molten salt layer in the furnace,
The molten metal is discharged from the molten metal tap hole 1a,
Similarly, the molten slag is discharged from the molten slag outlet 1b, and the molten salt is discharged from the molten salt outlet 1c.

【0020】黒鉛電極3は溶融塩から筒状体4で保護さ
れているため、溶融塩に接しないので、溶融塩により浸
食されることがない。また、黒鉛電極3は筒状体4によ
り溶融塩と電気的に絶縁状態にあるため、黒鉛電極3か
らの電流が溶融塩層に集中して流れることがなくなり、
溶融スラグ層を流れる電流により溶融スラグが十分に加
熱される。
Since the graphite electrode 3 is protected from the molten salt by the tubular body 4 and does not come into contact with the molten salt, it is not eroded by the molten salt. In addition, since the graphite electrode 3 is electrically insulated from the molten salt by the cylindrical body 4, the current from the graphite electrode 3 does not concentrate on the molten salt layer, and
The molten slag is sufficiently heated by the electric current flowing through the molten slag layer.

【0021】[0021]

【発明の効果】筒状体により黒鉛電極を保護するため、
溶融塩による電極の腐食あるいは電極間の短絡を防止す
ることができるので、電極の消耗頻度を改善できるとと
もに、安定した運転を行なうことができる。
In order to protect the graphite electrode by the cylindrical body,
Since the corrosion of the electrodes due to the molten salt or the short circuit between the electrodes can be prevented, the frequency of consumption of the electrodes can be improved and a stable operation can be performed.

【0022】また、電極は所定長さの電極を接続して送
り出すので、筒状体下端より突出する電極先端が操業に
ともない損耗するが、不足分を送り出すことにより、炉
内に十分な電圧を印加することが可能となる。
Further, since the electrodes are connected and fed out with electrodes of a predetermined length, the electrode tips protruding from the lower end of the cylindrical body are worn by operation, but by sending out the shortage, a sufficient voltage is supplied into the furnace. It becomes possible to apply.

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

【図1】本発明の電気抵抗溶融炉の実施例を示す全体図
である。
FIG. 1 is an overall view showing an embodiment of an electric resistance melting furnace of the present invention.

【図2】図1に示す筒状体と黒鉛電極の断面図で、図2
−(a)は横断面図、図2−(b)は縦断面図である。
FIG. 2 is a sectional view of the tubular body and the graphite electrode shown in FIG.
FIG. 2A is a transverse sectional view, and FIG. 2B is a longitudinal sectional view.

【図3】図1に示す筒状体と黒鉛電極の斜視図である。FIG. 3 is a perspective view of a tubular body and a graphite electrode shown in FIG. 1;

【図4】本発明の電気抵抗溶融炉の別実施例を示す全体
図である。
FIG. 4 is an overall view showing another embodiment of the electric resistance melting furnace of the present invention.

【図5】従来の交流電気抵抗溶融炉の全体図である。FIG. 5 is an overall view of a conventional AC electric resistance melting furnace.

【符号の説明】[Explanation of symbols]

1 炉本体 1a 溶融メタル出湯口 1b 溶融スラグ出湯口 1c 溶融塩出湯口 2 上部炉蓋 2a 灰供給口 2b 排ガス出口 3 黒鉛電極 3a 雄ねじ 3b 雌ねじ 4 筒状体 4a 絶縁性耐火物 4b 発泡性耐火物 5 電極昇降装置 6 炉底電極 DESCRIPTION OF SYMBOLS 1 Furnace main body 1a Molten metal tap 1b Molten slag tap 1c Molten salt tap 2 Upper furnace lid 2a Ash supply port 2b Exhaust gas outlet 3 Graphite electrode 3a Male screw 3b Female screw 4 Cylindrical body 4a Insulating refractory 4b Foaming refractory 5 Electrode lifting device 6 Furnace bottom electrode

───────────────────────────────────────────────────── フロントページの続き (72)発明者 長谷川 佳史 北九州市戸畑区大字中原46−59 日鐵プラ ント設計株式会社内 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Yoshifumi Hasegawa 46-59, Nakahara, Tobata-ku, Kitakyushu City Inside Nippon Steel Plant Design Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 黒鉛電極を備えたごみ焼却灰の電気抵抗
溶融炉において、上部炉蓋に支持された筒状体の内側
に、黒鉛電極が電極昇降装置により昇降自在に配置さ
れ、前記筒状体は外層が絶縁性耐火物で内層が発泡性耐
火物で構成されていることを特徴とするごみ焼却灰の電
気抵抗溶融炉。
In an electric resistance melting furnace for refuse incineration ash provided with graphite electrodes, a graphite electrode is disposed inside a tubular body supported by an upper furnace lid so as to be able to move up and down by an electrode lifting device. An electric resistance melting furnace for refuse incineration ash, wherein the outer layer is made of an insulating refractory and the inner layer is made of a foaming refractory.
【請求項2】 黒鉛電極が所定長さの電極を接続して構
成された電極であることを特徴とする請求項1記載のご
み焼却灰の電気抵抗溶融炉。
2. The electric resistance melting furnace for incinerated ash according to claim 1, wherein the graphite electrode is an electrode formed by connecting electrodes of a predetermined length.
JP9944797A 1997-04-16 1997-04-16 Electrical resistance melting furnace of refuse incinerated ash Withdrawn JPH10288321A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9944797A JPH10288321A (en) 1997-04-16 1997-04-16 Electrical resistance melting furnace of refuse incinerated ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9944797A JPH10288321A (en) 1997-04-16 1997-04-16 Electrical resistance melting furnace of refuse incinerated ash

Publications (1)

Publication Number Publication Date
JPH10288321A true JPH10288321A (en) 1998-10-27

Family

ID=14247624

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9944797A Withdrawn JPH10288321A (en) 1997-04-16 1997-04-16 Electrical resistance melting furnace of refuse incinerated ash

Country Status (1)

Country Link
JP (1) JPH10288321A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100481072B1 (en) * 2002-06-25 2005-04-07 김현상 Melting apparatus using electric resistance and method thereof
JP2006010291A (en) * 2004-06-29 2006-01-12 Nikko Kankyo Kk Ceiling part structure for furnace
CN105466224A (en) * 2015-12-14 2016-04-06 湖南顶立科技有限公司 Heating furnace

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100481072B1 (en) * 2002-06-25 2005-04-07 김현상 Melting apparatus using electric resistance and method thereof
JP2006010291A (en) * 2004-06-29 2006-01-12 Nikko Kankyo Kk Ceiling part structure for furnace
JP4584636B2 (en) * 2004-06-29 2010-11-24 日鉱環境株式会社 How to use industrial waste treatment furnace
CN105466224A (en) * 2015-12-14 2016-04-06 湖南顶立科技有限公司 Heating furnace
CN105466224B (en) * 2015-12-14 2018-01-26 湖南顶立科技有限公司 A kind of heating furnace

Similar Documents

Publication Publication Date Title
JPH10288321A (en) Electrical resistance melting furnace of refuse incinerated ash
JP3377906B2 (en) Method for preventing decrease in fluidity of molten slag in plasma melting furnace
JP3722674B2 (en) Method and apparatus for lowering melting furnace
JP2007071509A (en) Bottom electrode structure for electric melting furnace
JP2001050528A (en) Operation method of electric melting furnace
JP4467769B2 (en) Electric resistance melting furnace
CN218442300U (en) Bottom heating device of melting furnace
JP2004257631A (en) Plasma melting treatment apparatus for waste disposal
JP3977164B2 (en) Plasma melting apparatus and plasma melting method
JP4095774B2 (en) How to restart the plasma ash melting furnace
JP4667665B2 (en) Plasma ash melting furnace and operating method thereof
JPH10292908A (en) Electrical resistance melting furnace for dust incineration ash
JP2955961B2 (en) Waste incineration ash melting furnace
JP3534680B2 (en) Operation method of ash melting furnace
JP3149726B2 (en) Electric resistance type incineration ash melting furnace and its operation method
JP2747983B2 (en) Method and apparatus for melting municipal solid waste incineration ash
JPH09280534A (en) Melting furnace for refuse incineration ash
JPH11237018A (en) Plasma melting furnace, and its operation method
JP3575570B2 (en) Ash melting furnace
CN115200026A (en) Bottom heating device of melting furnace
JP2855265B2 (en) Electric resistance melting furnace
JP4185667B2 (en) Operating method of plasma ash melting furnace
JP3831930B2 (en) Electrode sealing device for ash melting furnace
JPH1019230A (en) Method for melting treatment of refuse inclineration ash and melting furnace therefor
JP2002162010A (en) Waste melting furnace

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20040706