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JP2938693B2 - Method for removing molten slag from incineration ash melting furnace - Google Patents
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JP2938693B2 - Method for removing molten slag from incineration ash melting furnace - Google Patents

Method for removing molten slag from incineration ash melting furnace

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Publication number
JP2938693B2
JP2938693B2 JP4335649A JP33564992A JP2938693B2 JP 2938693 B2 JP2938693 B2 JP 2938693B2 JP 4335649 A JP4335649 A JP 4335649A JP 33564992 A JP33564992 A JP 33564992A JP 2938693 B2 JP2938693 B2 JP 2938693B2
Authority
JP
Japan
Prior art keywords
slag
molten
melting furnace
furnace
molten slag
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
JP4335649A
Other languages
Japanese (ja)
Other versions
JPH06159647A (en
Inventor
正夫 堺
哲夫 明石
一雄 山岸
研一 西村
恒男 山下
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 Corp
Original Assignee
Nippon Kokan Ltd
Tanabe 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 Kokan Ltd, Tanabe Corp filed Critical Nippon Kokan Ltd
Priority to JP4335649A priority Critical patent/JP2938693B2/en
Publication of JPH06159647A publication Critical patent/JPH06159647A/en
Application granted granted Critical
Publication of JP2938693B2 publication Critical patent/JP2938693B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Inorganic Fibers (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】この発明は、都市ごみ焼却灰溶融
炉の溶融スラグを出滓口で閉塞することなく出滓する方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing molten slag from a municipal solid waste incineration ash melting furnace without closing the slag with a slag outlet.

【0002】[0002]

【従来の技術】都市ごみ焼却灰を溶融するための電気炉
式の溶融炉が知られている。図4は従来の電気炉式の焼
却灰溶融炉の1例を示す断面図である。
2. Description of the Related Art There is known an electric furnace type melting furnace for melting municipal waste incineration ash. FIG. 4 is a sectional view showing an example of a conventional electric furnace type incineration ash melting furnace.

【0003】図4に示す従来の電気炉式の焼却灰溶融炉
(以下、「灰溶融炉」という)1においては、炉本体2
内に電極3を上下動自在に設け、炉本体2内に投入され
た焼却灰層4内に電極3を挿入し、焼却灰を溶融して溶
融スラグおよび溶融メタルに液化して溶融スラグ層5お
よび溶融メタル層6を形成する。その後は、電極3の先
端が溶融スラグ層5の湯面から一定の距離を保つように
保持しつつ、電極3と溶融メタル層6との間に発生した
アーク熱により焼却灰を溶融して溶融スラグおよび溶融
メタルに液化する。炉本体2の炉壁の所定位置に出滓口
9が設けられており、溶融スラグおよび溶融メタルは出
滓口9からオーバーフローすることにより排出される
(以下、「先行技術」という)。先行技術は電極3と溶
融メタル層6との間に発生したアーク熱により焼却灰を
溶融するため、溶融スラグ層は可能な限り薄くする必要
がある。このため、出滓口9から随時オーバーフローを
行なっている。
[0003] In a conventional electric furnace type incinerated ash melting furnace (hereinafter referred to as "ash melting furnace") 1 shown in FIG.
The electrode 3 is provided in the furnace body 2 so as to be movable up and down, the electrode 3 is inserted into the incineration ash layer 4 put into the furnace main body 2, the incineration ash is melted and liquefied into molten slag and molten metal, and the molten slag layer 5 And a molten metal layer 6 is formed. Thereafter, while maintaining the tip of the electrode 3 at a certain distance from the surface of the molten slag layer 5, the incinerated ash is melted and melted by the arc heat generated between the electrode 3 and the molten metal layer 6. Liquefies into slag and molten metal. A slag port 9 is provided at a predetermined position on the furnace wall of the furnace body 2, and molten slag and molten metal are discharged by overflowing from the slag port 9 (hereinafter, referred to as “prior art”). In the prior art, since the incinerated ash is melted by the arc heat generated between the electrode 3 and the molten metal layer 6, the molten slag layer needs to be as thin as possible. For this reason, overflow from the slag port 9 is performed at any time.

【0004】都市ごみ焼却灰の溶融スラグの塩基度は、
一般的に0.4 前後であり、溶融温度が高温度領域の場合
であっても粘度が高く、炉外へ出滓する場合に流れにく
い。従って、先行技術においては、補助的な熱源で出滓
部を加熱したり、塩基度をCaO 分等で調整するなどの手
段によって粘度を下げて流れやすくしている。
The basicity of molten slag of municipal solid waste incineration ash is
Generally, it is around 0.4, and the viscosity is high even when the melting temperature is in a high temperature range, and it is difficult to flow when the slag is discharged outside the furnace. Therefore, in the prior art, the viscosity is lowered by means of heating the slag portion with an auxiliary heat source, or adjusting the basicity with CaO content or the like, to facilitate the flow.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
ような対策を実施しない場合は、出滓口が閉塞し灰溶融
炉の運転が不能となる。このように、従来の灰溶融炉に
おいては、補助的な熱源が必要であったり、焼却灰とと
もに塩基度調整剤も溶融処理することでエネルギーを余
分に投入する必要がある。また、塩基度調整剤は高価で
あり、経済的にも不利である。
However, when the above measures are not taken, the smelt outlet is closed and the operation of the ash melting furnace becomes impossible. As described above, in the conventional ash melting furnace, an auxiliary heat source is required, and it is necessary to additionally input energy by melting the basicity adjusting agent together with the incinerated ash. Further, the basicity adjuster is expensive and economically disadvantageous.

【0006】従って、この発明の目的は、補助的な加熱
や塩基度調整剤を使用せずに、出滓口が閉塞することな
く溶融スラグを出滓することができる焼却灰溶融炉の溶
融スラグ出滓方法を提供することにある。
Accordingly, an object of the present invention is to provide a molten slag of an incineration ash melting furnace capable of discharging molten slag without closing a slag outlet without using auxiliary heating or a basicity adjusting agent. It is to provide a slag removal method.

【0007】この発明は、溶融炉内に配置された電極に
通電し、発生するジュール熱によって投入された焼却灰
を溶融して形成された溶融スラグ層内に前記電極を挿入
して塩基度が0.6以下である高粘度の溶融スラグ層お
よび溶融メタル層を形成する電気式の焼却灰溶融炉の溶
融スラグ出滓方法であって、前記溶融メタル層の液面よ
り上方となるように前記溶融炉の炉壁に出滓口を設けて
おき、前記出滓口の開度および/または焼却灰の投入量
を調整することによって前記溶融スラグ層の湯面を前記
出滓口から200mm以上の高さに保ちながら、前記出
滓口から溶融スラグを直接炉外に排出することに特徴を
有するものである。
The present invention relates to an electrode arranged in a melting furnace.
Incineration ash injected by Joule heat generated when electricity is supplied
Insert the electrode into the molten slag layer formed by melting
And a high viscosity molten slag layer with a basicity of 0.6 or less
Of an electric incineration ash melting furnace forming a molten metal layer
A method for removing molten slag, comprising:
A slag port is provided on the furnace wall of the melting furnace so that
The opening of the slag outlet and / or the amount of incinerated ash
The molten metal surface of the molten slag layer by adjusting
While maintaining a height of 200 mm or more from the slag outlet,
It is characterized in that the molten slag is discharged directly from the slag port to the outside of the furnace .

【0008】[0008]

【作用】都市ごみ焼却灰の溶融炉として、発明者等によ
り、ジュール熱を利用した電気溶融炉が既に開発されて
いる。本発明においては、このジュール熱を利用した電
気溶融炉を利用する。即ち、先ず、炉内に投入された焼
却灰層内に電極を挿入し、焼却灰を溶融して溶融スラグ
および溶融メタルに液化する。これにより、溶融スラグ
層および溶融メタル層が形成される。その後は、電極の
先端を溶融スラグ層内に挿入し、ジュール熱によって焼
却灰を溶融する。炉内に溜まった溶融スラグ層はジュー
ル熱を利用するため所定の厚さを形成させる。炉の高さ
方向中間部の炉壁には出滓口が設けられており、溶融ス
ラグ層の湯面と出滓口との間に一定の高低差が確保さ
れ、この高低差によりもたらされる溶融スラグの圧力
(ヘッド圧)によって溶融スラグが押し出され出滓口か
ら排出する。塩基度が0.6 以下の粘度の高い溶融スラグ
であっても出滓口が閉塞することなく連続で出滓可能で
ある。溶融スラグの湯面と出滓口との高低差が常に一定
となるように、出滓口からの溶融スラグ排出量または焼
却灰投入量等を制御して溶融スラグの湯面の位置を常に
一定に保持する。
The present inventors have already developed an electric melting furnace utilizing Joule heat as a melting furnace for municipal waste incineration ash. In the present invention, an electric melting furnace utilizing this Joule heat is used. That is, first, an electrode is inserted into the incineration ash layer charged into the furnace, and the incineration ash is melted and liquefied into molten slag and molten metal. Thereby, a molten slag layer and a molten metal layer are formed. Thereafter, the tip of the electrode is inserted into the molten slag layer, and the incinerated ash is melted by Joule heat. The molten slag layer accumulated in the furnace has a predetermined thickness in order to utilize Joule heat. A slag port is provided on the furnace wall in the middle of the furnace in the height direction, and a certain level difference is secured between the molten metal surface of the molten slag layer and the slag port. The molten slag is extruded by the pressure of the slag (head pressure) and discharged from the slag port. Even with a highly viscous molten slag having a basicity of 0.6 or less, the slag can be continuously discharged without closing the slag opening. Control the amount of molten slag discharged from the slag port or the amount of incinerated ash to keep the level of the molten slag level so that the height difference between the molten slag surface and the slag outlet is always constant. To hold.

【0009】[0009]

【実施例】次に、この発明を図面を参照しながら説明す
る。図1はこの発明の実施例を示す電気炉式の都市ごみ
焼却灰溶融炉の断面図、図2は出滓口を説明する断面
図、図3は同正面図である。
Next, the present invention will be described with reference to the drawings. FIG. 1 is a cross-sectional view of an electric furnace type municipal waste incineration ash melting furnace showing an embodiment of the present invention, FIG. 2 is a cross-sectional view illustrating a slag outlet, and FIG. 3 is a front view of the same.

【0010】図1に示すように、電気炉式の都市ごみ焼
却灰溶融炉(灰溶融炉)1の炉本体2内には電極3が上
下動自在に設けられている。炉本体2の高さ方向中間部
の炉壁には出滓口7が設けられている。電極3を焼却灰
層4内に挿入して焼却灰を溶融して溶融スラグおよび溶
融メタルに液化する。これにより、溶融スラグ層および
溶融メタル層が形成される。その後は、溶融スラグ層5
内に電極3の先端を挿入し、ジュール熱によって焼却灰
を溶融し溶融スラグおよび溶融メタルに液化する。本発
明に利用する溶融炉はジュール熱を利用するため、炉内
に溜まった溶融スラグ層は所定の厚さを有する。出滓口
7と溶融スラグ層5の湯面との間に所定の高低差を確保
できるように湯面の位置を調整する。溶融スラグはその
ヘッド圧により出滓口7から排出する。
As shown in FIG. 1, an electrode 3 is vertically movable within a furnace body 2 of an electric furnace type municipal waste incineration ash melting furnace (ash melting furnace) 1. A slag port 7 is provided in a furnace wall at an intermediate portion in the height direction of the furnace main body 2. The electrode 3 is inserted into the incineration ash layer 4 to melt the incineration ash and liquefy it into molten slag and molten metal. Thereby, a molten slag layer and a molten metal layer are formed. After that, the molten slag layer 5
The incineration ash is melted by Joule heat and liquefied into molten slag and molten metal. Since the melting furnace used in the present invention utilizes Joule heat, the molten slag layer accumulated in the furnace has a predetermined thickness. The position of the molten metal level is adjusted so that a predetermined height difference can be secured between the slag outlet 7 and the molten metal level of the molten slag layer 5. The molten slag is discharged from the slag port 7 by the head pressure.

【0011】出滓口7には、図1〜図3に示すように、
出滓口開閉機構8が設けられている。出滓口開閉機構8
は、炉本体2の外側の出滓口7の出口に設けられた環状
の基部8bと、基部8bの外側に基部8bの開口を閉塞可能に
設けられた、上下にスライド移動自在のゲート8aとから
なっている。出滓口開閉機構8の開度調整により溶融ス
ラグの出滓量が制御される。10はゲート8aおよび基部8b
を水冷するための冷却水11の入出口である。出滓口開閉
機構8によって焼却灰の溶融処理量とバランスするよう
に出滓量を制御し、溶融スラグ層5の湯面の位置を一定
に保持し、溶融スラグ層5の湯面と出滓口7との間に一
定の高低差を維持しヘッド圧を常時確保する。
As shown in FIG. 1 to FIG.
A slag opening / closing mechanism 8 is provided. Outlet opening and closing mechanism 8
An annular base 8b provided at the outlet of the slag port 7 outside the furnace body 2, and a gate 8a slidable up and down provided outside the base 8b so as to close the opening of the base 8b. Consists of By adjusting the opening degree of the slag opening / closing mechanism 8, the amount of slag discharged from the molten slag is controlled. 10 is gate 8a and base 8b
This is an inlet / outlet of cooling water 11 for water-cooling. The amount of slag is controlled by the slag opening / closing mechanism 8 so as to balance the amount of incineration ash that is melted, the level of the molten surface of the molten slag layer 5 is kept constant, Maintain a constant head pressure by maintaining a constant height difference with the mouth 7.

【0012】また、溶融スラグ層5の湯面の位置を一定
に保持する方法として、炉内に投入する焼却灰の量を制
御する方法を使用してもよい。
Further, as a method of keeping the position of the molten metal surface of the molten slag layer 5 constant, a method of controlling the amount of incinerated ash to be charged into the furnace may be used.

【0013】先行技術に示すように、従来の灰溶融炉で
は、溶融スラグは溶融メタルとともにオーバーフロー方
式により自重落下することで炉外に排出されていた。実
施例においては、出滓口7と溶融スラグの湯面との間の
距離が(図1中に示すAの距離が)200mm 以上となるよ
うに溶融スラグの湯面を調整し、出滓口7より溶融スラ
グをそのヘッド圧を利用して押し出している。これによ
り、塩基度が0.6 以下の粘度の高い溶融スラグであって
も出滓口7が閉塞することなく連続して出滓可能であ
る。従って、塩基度調整剤および補助的な加熱手段は不
要である。
As shown in the prior art, in the conventional ash melting furnace, the molten slag was discharged out of the furnace by falling under its own weight together with the molten metal by an overflow method. In the embodiment, the molten metal surface of the molten slag is adjusted such that the distance between the molten metal outlet 7 and the molten metal surface of the molten slag (the distance A shown in FIG. 1) is 200 mm or more. 7, the molten slag is extruded using the head pressure. Thereby, even if the molten slag has a high basicity of 0.6 or less, the slag can be continuously discharged without closing the slag opening 7. Therefore, a basicity adjuster and auxiliary heating means are not required.

【0014】[0014]

【発明の効果】以上説明したように、この発明によれ
ば、以下のような工業上有用な効果がもたらされる。 塩基度が0.6 以下の粘度の高い溶融スラグでも、出
滓部の加熱、塩基度調整剤の使用等の補助的な手段を採
らずに、出滓口が閉塞することなく出滓できる。 出滓部の加熱、塩基度調整剤を使用する必要がない
ため、電力原単位を悪くすることがなく経済的に有利で
ある。
As described above, the present invention has the following industrially useful effects. Even with high viscosity molten slag having a basicity of 0.6 or less, slag can be removed without blocking the slag opening without using auxiliary means such as heating of the slag portion and use of a basicity adjusting agent. Since there is no need to heat the slag portion and use a basicity adjuster, it is economically advantageous without deteriorating the power consumption unit.

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

【図1】この発明の実施例を示す電気炉式の都市ごみ焼
却灰溶融炉の断面図
FIG. 1 is a sectional view of an electric furnace type municipal waste incineration ash melting furnace showing an embodiment of the present invention.

【図2】出滓口を説明する断面図FIG. 2 is a cross-sectional view illustrating a slag port.

【図3】出滓口を説明する正面図FIG. 3 is a front view illustrating a slag port.

【図4】従来の電気炉式の焼却灰溶融炉の1例を示す断
面図。
FIG. 4 is a sectional view showing an example of a conventional electric furnace type incineration ash melting furnace.

【符号の説明】[Explanation of symbols]

1 電気炉式の都市ごみ焼却灰溶融炉 2 炉本体 3 電極 4 焼却灰層 5 溶融スラグ層 6 溶融メタル層 7 出滓口 8 出滓口開閉機構 8a ゲート 8b 基部 9 出滓口 10 冷却水入出口 11 冷却水。 DESCRIPTION OF SYMBOLS 1 Electric furnace type municipal refuse incineration ash melting furnace 2 Furnace main body 3 Electrode 4 Incineration ash layer 5 Molten slag layer 6 Molten metal layer 7 Slag outlet 8 Slag opening and closing mechanism 8a Gate 8b Base 9 Slag outlet 10 Cooling water inlet Exit 11 cooling water.

フロントページの続き (72)発明者 西村 研一 新潟県糸魚川市一の宮5−7−12 (72)発明者 山下 恒男 新潟県糸魚川市上刈1−1−7 (56)参考文献 特開 昭61−168719(JP,A) (58)調査した分野(Int.Cl.6,DB名) F23J 1/08 F23J 1/00 F27B 3/08 F27B 3/19 Continuation of the front page (72) Inventor Kenichi Nishimura 5-7-12 Ichinomiya, Itoigawa-shi, Niigata (72) Inventor Tsuneo Yamashita 1-1-7, Kamigari, Itoigawa-shi, Niigata (56) References JP-A-61-168719 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) F23J 1/08 F23J 1/00 F27B 3/08 F27B 3/19

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】溶融炉内に配置された電極に通電し、発生
するジュール熱によって投入された焼却灰を溶融して形
成された溶融スラグ層内に前記電極を挿入して塩基度が
0.6以下である高粘度の溶融スラグ層および溶融メタ
ル層を形成する電気式の焼却灰溶融炉の溶融スラグ出滓
方法であって、前記溶融メタル層の液面より上方となる
ように前記溶融炉の炉壁に出滓口を設けておき、前記出
滓口の開度および/または焼却灰の投入量を調整するこ
とによって前記溶融スラグ層の湯面を前記出滓口から2
00mm以上の高さに保ちながら、前記出滓口から溶融
スラグを直接炉外に排出することを特徴とする焼却灰
融炉の溶融スラグ出滓方法。
1. An electric current is applied to an electrode disposed in a melting furnace to generate electricity.
Melts the incinerated ash injected by Joule heat
Inserting the electrode into the formed molten slag layer,
High viscosity molten slag layer and molten metal of 0.6 or less
Of molten slag from electric incineration ash melting furnace that forms slag layer
A method wherein the liquid metal layer is above the liquid level
A slag port is provided on the furnace wall of the melting furnace so that
Adjust the opening of the slag and / or the amount of incinerated ash.
And the molten metal surface of the molten slag layer is
Melt from the slag port while maintaining the height at least 00 mm
A method for discharging molten slag from an incineration ash melting furnace, wherein the slag is directly discharged outside the furnace .
JP4335649A 1992-11-20 1992-11-20 Method for removing molten slag from incineration ash melting furnace Expired - Lifetime JP2938693B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4335649A JP2938693B2 (en) 1992-11-20 1992-11-20 Method for removing molten slag from incineration ash melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4335649A JP2938693B2 (en) 1992-11-20 1992-11-20 Method for removing molten slag from incineration ash melting furnace

Publications (2)

Publication Number Publication Date
JPH06159647A JPH06159647A (en) 1994-06-07
JP2938693B2 true JP2938693B2 (en) 1999-08-23

Family

ID=18290966

Family Applications (1)

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JP4335649A Expired - Lifetime JP2938693B2 (en) 1992-11-20 1992-11-20 Method for removing molten slag from incineration ash melting furnace

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JPH067007B2 (en) * 1985-01-23 1994-01-26 日本鋼管株式会社 Waste melting furnace slag facility

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