JP3361198B2 - Circular fixed melting furnace - Google Patents

Circular fixed melting furnace

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Publication number
JP3361198B2
JP3361198B2 JP28374894A JP28374894A JP3361198B2 JP 3361198 B2 JP3361198 B2 JP 3361198B2 JP 28374894 A JP28374894 A JP 28374894A JP 28374894 A JP28374894 A JP 28374894A JP 3361198 B2 JP3361198 B2 JP 3361198B2
Authority
JP
Japan
Prior art keywords
furnace body
melted
storage chamber
combustion chamber
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.)
Expired - Fee Related
Application number
JP28374894A
Other languages
Japanese (ja)
Other versions
JPH08145327A (en
Inventor
政信 志垣
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.)
Takuma KK
Original Assignee
Takuma KK
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 Takuma KK filed Critical Takuma KK
Priority to JP28374894A priority Critical patent/JP3361198B2/en
Publication of JPH08145327A publication Critical patent/JPH08145327A/en
Application granted granted Critical
Publication of JP3361198B2 publication Critical patent/JP3361198B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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、都市ごみ等の焼却灰や
下水汚泥等の被溶融物を溶融処理する為の円形固定式溶
融炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a circular fixed type melting furnace for melting and treating incinerated ash of municipal solid waste and sewage sludge.

【0002】[0002]

【従来の技術】一般に、都市ごみ等の焼却灰はその多く
が埋め立て処理されている。しかし、近年、埋め立て地
の確保が年々困難になりつつあり、焼却灰の有効利用や
減容化が要請されている。ところで、都市ごみ等は、焼
却することによりその容積が1/15〜1/20程度に
減容し、更にその焼却灰を溶融処理してスラグにすると
約1/3位に減容する。又、焼却灰を溶融処理してスラ
グにすると、単に容積が減少するばかりでなく、重金属
の溶出がなくなり、骨材や路盤材等への有効利用が可能
となる。従って、最近は焼却灰の溶融処理が行われるよ
うになりつつある。又、焼却灰のみならず、汚泥の溶融
処理も行われつつある。
2. Description of the Related Art Generally, most of the incinerated ash of municipal solid waste is landfilled. However, in recent years, it has become difficult to secure landfills year by year, and there is a demand for effective utilization and volume reduction of incinerated ash. By the way, the volume of municipal solid waste is reduced to about 1/15 to 1/20 by incineration, and the volume is reduced to about 1/3 when the incinerated ash is melt-processed into slag. Further, when the incinerated ash is melt-processed into slag, not only the volume is reduced, but also heavy metals are not eluted and it can be effectively used as an aggregate or a roadbed material. Therefore, recently, incineration ash is being melted. Further, not only incineration ash but also sludge melting treatment is being performed.

【0003】従来、焼却灰や下水汚泥等(以下被溶融物
と云う)を溶融処理する装置としては、表面溶融炉が広
く利用されて居り、これには角形固定式溶融炉と円形回
転式溶融炉とがある。
Conventionally, a surface melting furnace has been widely used as an apparatus for melting and treating incinerated ash, sewage sludge and the like (hereinafter referred to as melted matter), and a square fixed type melting furnace and a circular rotary type melting furnace are used. There is a furnace.

【0004】前記角形固定式溶融炉は、図8に示す如
く、被溶融物供給路20a及びスラグ排出口20bを有
する炉本体20と、炉底20cに設けられた供給プッシ
ャー21と、天井壁20dに設けられたバーナ22等か
ら構成されて居り、炉内に供給された被溶融物23をバ
ーナ22の燃焼熱により表面から溶融するようにしたも
のである。尚、図8に於いて、24はホッパ、25は冷
却水槽、26は水封式スラグコンベヤである。
As shown in FIG. 8, the square fixed melting furnace has a furnace body 20 having a melted material supply path 20a and a slag discharge port 20b, a supply pusher 21 provided on a furnace bottom 20c, and a ceiling wall 20d. The burner 22 and the like are provided in the furnace, and the melted material 23 supplied into the furnace is melted from the surface by the combustion heat of the burner 22. In FIG. 8, 24 is a hopper, 25 is a cooling water tank, and 26 is a water-sealed slag conveyor.

【0005】而して、ホッパ24から被溶融物供給路2
0aに投入された被溶融物23は、供給プッシャー21
により炉内へ順次送り込まれ、表面が傾斜面となった状
態で炉底20cに堆積される。炉底20cに堆積した被
溶融物23は、バーナ22の燃焼熱によりその表面がフ
ィルム状に溶融してスラグとなり、傾斜面を流下してス
ラグ排出口20bから冷却水槽25内に落下する。尚、
溶融スラグが傾斜面を流下することによって、傾斜面に
は次々に未溶融状態の被溶融物23が露出することにな
り、この露出した被溶融物23はバーナ22の燃焼熱に
より順次溶融されて行く。冷却水槽25内に落下したス
ラグは、冷却固化されて黒色粒状の砂状物となり、水封
式スラグコンベヤ26により取り出される。そして、溶
融の進行に伴って溶融した傾斜面が後退すると、供給プ
ッシャー21により新しい被溶融物23が炉内へ送り込
まれる。
Thus, the molten material supply path 2 from the hopper 24.
The material 23 to be melted put in
Are sequentially fed into the furnace by the above, and are deposited on the furnace bottom 20c in a state where the surface is an inclined surface. The material 23 to be melted deposited on the furnace bottom 20c is melted into a slag by its surface being melted into a film by the combustion heat of the burner 22, and flows down the inclined surface and falls into the cooling water tank 25 from the slag discharge port 20b. still,
As the molten slag flows down the inclined surface, the unmelted melted material 23 is successively exposed on the sloped surface, and the exposed melted material 23 is sequentially melted by the combustion heat of the burner 22. go. The slag that has fallen into the cooling water tank 25 is cooled and solidified into a black granular sandy substance, which is taken out by the water-sealed slag conveyor 26. Then, when the melted inclined surface recedes as the melting progresses, a new material 23 to be melted is fed into the furnace by the supply pusher 21.

【0006】この角形固定式溶融炉は、炉本体20が固
定されている為に構造的に極めてシンプルで、故障が殆
どなくてメンテナンスも簡単に行え、又、供給プッシャ
ー21により被溶融物23の定量供給を確実に行える等
の利点がある。
Since this furnace is fixed, the furnace main body 20 is fixed, so that it is structurally very simple, there is almost no failure, and maintenance can be performed easily. There are advantages such as reliable supply of a fixed amount.

【0007】一方、円形回転式溶融炉は、図9に示す如
く、底壁27a中央部にスラグ排出口27bを有し、回
転自在に支持された有底筒状の炉本体27と、炉本体2
7内に昇降自在に配設され、炉本体27との間に被溶融
物28の貯留室29及び燃焼室30を形成する天井壁3
1と、天井壁31に設けられたバーナ32等から構成さ
れて居り、燃焼室30内にすり鉢状で且つ環状に堆積さ
れた被溶融物28をバーナ32の燃焼熱により表面から
溶融するようにしたものである。尚、図9に於いて、3
3は炉本体27の支持ローラ、34は炉本体27の回転
駆動装置、35は天井壁31の昇降駆動装置、36は被
溶融物28の供給装置、37はシール機構、38は冷却
水ジャケット、39は二次燃焼室、40は二次燃焼室用
バーナ、41は煙道、42は水封式スラグコンベヤであ
る。
On the other hand, the circular rotary melting furnace, as shown in FIG. 9, has a slag discharge port 27b at the center of a bottom wall 27a, and has a bottomed cylindrical furnace main body 27 and a furnace main body 27 rotatably supported. Two
Ceiling wall 3 which is arranged in a movable manner up and down in 7 and forms a storage chamber 29 and a combustion chamber 30 for the melted material 28 with the furnace body 27.
1 and a burner 32 and the like provided on the ceiling wall 31, so that the mortar-shaped and annularly deposited melted substance 28 in the combustion chamber 30 is melted from the surface by the combustion heat of the burner 32. It was done. In addition, in FIG.
3 is a support roller for the furnace body 27, 34 is a rotation drive device for the furnace body 27, 35 is a lift drive device for the ceiling wall 31, 36 is a supply device for the melted material 28, 37 is a sealing mechanism, 38 is a cooling water jacket, 39 is a secondary combustion chamber, 40 is a burner for a secondary combustion chamber, 41 is a flue, and 42 is a water-sealed slag conveyor.

【0008】而して、供給装置36により環状の貯留室
29の一個所に供給された被溶融物28は、炉本体27
が回転していることとも相俟って燃焼室30内にすり鉢
状で且つ環状に堆積される。燃焼室30内に堆積した被
溶融物28は、バーナ32の燃焼熱によりその表面がフ
ィルム状に溶融してスラグとなり、すり鉢状の表面を流
下してスラグ排出口27bから二次燃焼室39を経て水
封式スラグコンベヤ42に落下し、黒色粒状の砂状物と
なって排出される。そして、溶融の進行に伴って溶融面
のレベルが後退すると、被燃焼物28が環状の貯留室2
9から順次落下して溶融面に供給される。
Thus, the material to be melted 28 supplied to one portion of the annular storage chamber 29 by the supply device 36 is transferred to the furnace body 27.
Together with the rotation, the particles are accumulated in the combustion chamber 30 in a mortar shape and in an annular shape. The material to be melted 28 deposited in the combustion chamber 30 melts into a slag by melting its surface into a film due to the combustion heat of the burner 32, and flows down the mortar-shaped surface to the secondary combustion chamber 39 from the slag discharge port 27b. After that, it falls on the water-sealed slag conveyor 42 and is discharged as a black granular sandy substance. Then, when the level of the melting surface recedes as the melting progresses, the burned material 28 is stored in the annular storage chamber 2
It is sequentially dropped from 9 and supplied to the melting surface.

【0009】この円形回転式溶融炉は、被溶融物28に
よって燃焼室30周囲に環状の層を形成し、炉壁を覆う
ようにしている為、炉壁からの熱損失が極めて少なく、
又、溶融炉にありがちな炉壁の耐火物の溶損を防止でき
る等、優れた利点がある。
In this circular rotary type melting furnace, the material to be melted 28 forms an annular layer around the combustion chamber 30 to cover the furnace wall, so that the heat loss from the furnace wall is extremely small,
In addition, there are excellent advantages such as preventing melting of refractory material on the furnace wall, which is often found in melting furnaces.

【0010】[0010]

【発明が解決しようとする課題】然し乍ら、前記各溶融
炉にも解決すべき問題点が残されている。即ち、角形固
定式溶融炉に於いては、炉壁の三方が煉瓦積みで且つ露
出している為、炉壁からの熱損失が極めて大きいうえ、
炉壁の一部分に溶融スラグが接触して炉壁の煉瓦が溶損
すると云う問題がある。
However, there are still some problems to be solved in each of the melting furnaces. That is, in the square fixed melting furnace, since three sides of the furnace wall are brick-laid and exposed, heat loss from the furnace wall is extremely large, and
There is a problem that the molten slag contacts a part of the furnace wall and the bricks of the furnace wall are melted and damaged.

【0011】一方、円形回転式溶融炉に於いては、溶融
面への被溶融物28の供給を、被溶融物28の安息角
(すり鉢状の傾斜面と水平面とのなす角度)による自然
崩落に頼っている為、図10に示すように被溶融物28
の層の表面が実線位置から破線位置まで溶け込まない
と、被溶融物28の崩落が望めなく、このような状態に
なると、炉底27aが露出して炉底27aの耐火物が溶
損すると云う問題がある。そこで、このような現象を防
止する為に従来の円形回転式溶融炉では、天井壁31を
昇降駆動装置35により昇降させて溶融面への被溶融物
28の供給が容易に行われるようにしている。ところ
が、天井壁31を運転中に昇降させると、バーナ32へ
の燃料供給管や燃焼用空気供給管、炉本体27や天井壁
31の冷却水ジャケット38への冷却水の供給・排出装
置等を全てフレキシブルにする必要があり、溶融炉自体
の構造が極めて複雑化すると云う問題がある。然も、天
井壁31を昇降駆動し、炉本体も回転駆動するようにし
ている為、多数のシール機構37が必要になって構造が
より一層複雑になる。更に、環状の貯留室29に供給さ
れた被溶融物28は、圧縮状態で堆積される為、炉本体
27や天井壁31が回転・昇降運動しているにも拘わら
ず、溶融面のレベルが低下しても被溶融物28が崩落し
難くかったり、或いは崩落しないことがあった。その結
果、被溶融物28を溶融面へ均一且つ円滑に供給できな
いと云う問題があった。
On the other hand, in the circular rotary type melting furnace, the material to be melted 28 is supplied to the melting surface by the natural collapse due to the angle of repose of the material to be melted 28 (the angle formed by the mortar-shaped inclined surface and the horizontal plane). As shown in FIG. 10, the material to be melted 28
If the surface of the layer does not melt from the solid line position to the broken line position, collapse of the melted material 28 cannot be expected, and in such a state, the furnace bottom 27a is exposed and the refractory material of the furnace bottom 27a is said to melt. There's a problem. Therefore, in order to prevent such a phenomenon, in the conventional circular rotary melting furnace, the ceiling wall 31 is moved up and down by the lifting drive device 35 so that the material to be melted 28 can be easily supplied to the melting surface. There is. However, when the ceiling wall 31 is moved up and down during operation, the fuel supply pipe and the combustion air supply pipe to the burner 32, the cooling water supply / discharge device for the furnace body 27 and the cooling water jacket 38 of the ceiling wall 31, etc. There is a problem that the structure of the melting furnace itself becomes extremely complicated because it is necessary to make it all flexible. However, since the ceiling wall 31 is driven to move up and down and the furnace body is also driven to rotate, a large number of sealing mechanisms 37 are required, which further complicates the structure. Further, since the material to be melted 28 supplied to the annular storage chamber 29 is accumulated in a compressed state, the level of the melting surface is high even though the furnace body 27 and the ceiling wall 31 are rotating and moving up and down. Even if the temperature was lowered, the material to be melted 28 was difficult to collapse or sometimes did not collapse. As a result, there is a problem that the melted material 28 cannot be uniformly and smoothly supplied to the melting surface.

【0012】本発明は、このような問題点に鑑みて為さ
れたものであり、炉壁からの熱損失や炉壁の溶損を防止
できると共に、溶融炉自体の構造の簡略化を図れ、然
も、燃焼室内へ被溶融物を均一且つ円滑に供給できる円
形固定式溶融炉を提供するにある。
The present invention has been made in view of these problems, and can prevent heat loss from the furnace wall and melting loss of the furnace wall, and can simplify the structure of the melting furnace itself. Still, it is still another object of the present invention to provide a circular fixed melting furnace that can uniformly and smoothly supply a material to be melted into a combustion chamber.

【0013】[0013]

【課題を解決するための手段】上記目的を達成する為
に、本発明の請求項1の円形固定式溶融炉は、固定状態
で設置され、底壁中央部にスラグ・ガス排出口を形成し
た略有底筒状の炉本体と、炉本体の上方開口部に固定状
態で配置され、炉本体との間に燃焼室を形成すると共
に、炉本体の周壁との間に環状の貯留室を形成する天井
壁と、天井壁に設けられたバーナと、環状の貯留室に配
設され、貯留室の一個所に供給された焼却灰等の被溶融
物を貯留室に均一に分配する分配供給装置と、炉本体の
底壁外周縁部に等角度毎に配設され、貯留室から供給さ
れた被溶融物を燃焼室中央側へ定量宛押し出して燃焼室
内にすり鉢状で且つ環状の被溶融物の層を形成する複数
の供給プッシャーと、隣接する供給プッシャー間に配置
され、供給プッシャー間に供給された被溶融物が自然に
供給プッシャー側へ滑り落ちるように被溶融物の安息角
以上の傾斜を有する耐火物により三角錐形状に形成され
複数のガイド体とを具備して成る。
In order to achieve the above object, the circular fixed melting furnace according to claim 1 of the present invention is installed in a fixed state, and a slag / gas discharge port is formed in the center of the bottom wall. A substantially bottomed cylindrical furnace body and a fixedly arranged upper opening of the furnace body, which forms a combustion chamber between the furnace body and an annular storage chamber between the furnace body and the peripheral wall of the furnace body. Distributing and feeding device that is disposed in a ceiling wall, a burner provided on the ceiling wall, and an annular storage chamber, and that evenly melts a material to be melted, such as incineration ash, that is supplied to one location of the storage chamber, to the storage chamber And, the molten material supplied from the storage chamber is extruded in a fixed amount to the outer peripheral edge of the bottom wall of the furnace main body toward the central side of the combustion chamber to form a mortar-shaped and annular molten material in the combustion chamber. A plurality of feed pushers that form a layer of The melt supplied is formed in a triangular pyramid shape by refractory having a slope greater than the angle of repose of the melt as sliding down the natural feeding pusher side
And a plurality of guide bodies.

【0014】又、本発明の請求項2の円形固定式溶融炉
は、前記円形固定式溶融炉に於いて、ガイド体に替えて
回転数を自由に制御できる複数のスクリューフィーダー
を配設し、供給プッシャー間に供給された被溶融物をス
クリューフィーダーにより燃焼室中央側へ移送するよう
にしたものである。
The circular fixed melting furnace according to claim 2 of the present invention is the same as the circular fixed melting furnace, except that a guide member is used.
A plurality of screw feeders whose rotation speed can be freely controlled are arranged, and the melted material supplied between the supply pushers is transferred to the center of the combustion chamber by the screw feeder.

【0015】更に、本発明の請求項3の円形固定式溶融
炉は、固定状態で設置され、底壁中央部にスラグ・ガス
排出口を形成した略有底筒状の炉本体と、炉本体の上方
開口部に固定状態で配置され、炉本体との間に燃焼室を
形成すると共に、炉本体の周壁との間に環状の貯留室を
形成する天井壁と、天井壁に設けられたバーナと、環状
の貯留室に配設され、貯留室の一個所に供給された焼却
灰等の被溶融物を貯留室に均一に分配する分配供給装置
と、炉本体の底壁外周縁部に等角度毎に配設され、貯留
室から供給された被溶融物を燃焼室中央側へ定量宛移送
して燃焼室内にすり鉢状で且つ環状の被溶融物の層を形
成すると共に回転数を自由に制御できる複数のスクリュ
ーフィーダーとを具備して成るものである。
Further, the circular fixed type melting furnace according to claim 3 of the present invention is installed in a fixed state, and has a substantially bottomed cylindrical furnace body having a slag / gas discharge port formed at the center of the bottom wall, and the furnace body. A ceiling wall that is fixedly arranged in the upper opening of the furnace to form a combustion chamber with the furnace body and also forms an annular storage chamber with the peripheral wall of the furnace body, and a burner provided on the ceiling wall. And a distribution supply device that is disposed in the annular storage chamber and evenly distributes the material to be melted such as incinerated ash supplied to one location of the storage chamber to the storage chamber, and the outer peripheral edge of the bottom wall of the furnace body. Arranged at each angle, the melted material supplied from the storage chamber is quantitatively transferred to the center of the combustion chamber to form a mortar-shaped and annular layer of melted material in the combustion chamber, and the rotation speed is freely set. It comprises a plurality of controllable screw feeders.

【0016】[0016]

【作用】環状の貯留室の一個所に供給された焼却灰等の
被溶融物は、分配供給装置により貯留室に均一に分配さ
れる。貯留室に均一に分配された被溶融物は、供給プッ
シャーやスクリューフィーダーにより燃焼室中央側へ押
し込まれ、燃焼室内にすり鉢状で且つ環状に堆積され
る。このとき、供給プッシャー間に位置する被溶融物
は、供給プッシャー間に配設した三角錐形状のガイド体
に案内されて供給プッシャー側へ滑り落ち、該供給プッ
シャーにより燃焼室中央側へ押し込まれたり、或いは供
給プッシャー間に配設したスクリューフィーダーにより
燃焼室中央側へ移送されて行く。燃焼室内に堆積した被
溶融物は、バーナの燃焼熱によりその表面がフィルム状
に溶融してスラグとなり、すり鉢状の傾斜面を流下して
スラグ・ガス排出口から排出される。又、スラグ・ガス
排出口からは燃焼室内の高温の燃焼ガスも排出される。
尚、溶融スラグが傾斜面を流下することによって、傾斜
面には次々に未溶融状態の被溶融物が露出することにな
り、この露出した被溶融物はバーナの燃焼熱により順次
溶融されて行く。そして、溶融の進行に伴って溶融面が
後退すると、各供給プッシャーやスクリューフィーダー
が被溶融物を定量宛燃焼室中央側へ押し出し、燃焼室内
に常に燃焼状態に応じた適正な被溶融物の層を形成す
る。即ち、燃焼室内には常時一定量の被溶融物が供給さ
れて理想的な被溶融物の層が形成されることになり、被
溶融物の溶融処理が良好且つ円滑に行われる。
The molten material such as incinerated ash supplied to one portion of the annular storage chamber is uniformly distributed to the storage chamber by the distribution supply device. The material to be melted, which is uniformly distributed in the storage chamber, is pushed toward the center of the combustion chamber by the supply pusher and the screw feeder, and is accumulated in the combustion chamber in a mortar shape and in an annular shape. At this time, the material to be melted located between the supply pushers slides down toward the supply pusher side by being guided by the triangular pyramidal guide body arranged between the supply pushers, and is pushed into the center of the combustion chamber by the supply pushers. Alternatively, it is transferred to the center of the combustion chamber by a screw feeder arranged between the supply pushers. The material to be melted deposited in the combustion chamber is melted into a slag by its surface being melted into a film by the heat of combustion of the burner, and flows down the mortar-shaped inclined surface and is discharged from the slag / gas discharge port. Further, the high temperature combustion gas in the combustion chamber is also discharged from the slag / gas discharge port.
In addition, as the molten slag flows down the inclined surface, the unmelted molten material is exposed one after another on the inclined surface, and the exposed molten material is sequentially melted by the combustion heat of the burner. . Then, as the melting surface recedes as the melting progresses, each supply pusher and screw feeder push the material to be melted toward the fixed amount of the combustion chamber toward the center side, and the appropriate layer of the material to be melted according to the combustion state is always provided in the combustion chamber. To form. That is, a constant amount of the material to be melted is constantly supplied into the combustion chamber to form an ideal layer of the material to be melted, and the melting process of the material to be melted is performed smoothly and smoothly.

【0017】この溶融炉は、炉本体の周壁近傍及び底壁
に被溶融物の層を形成し、周壁及び底壁が露出しないよ
うにしている為、炉壁からの放熱が少なくなる。その結
果、燃料消費量が少なくて済むうえ、炉壁の耐火物の寿
命も延びることになる。又、炉本体や天井壁を固定式に
している為、炉本体等の駆動装置を省略できるうえ、バ
ーナへの燃料供給管や燃焼用空気供給管等を全てフレキ
シブルにしたりする必要もなく、溶融炉自体の構造を大
幅に簡略化でき、メンテナンスも極めて容易になる。更
に、分配供給装置によって被溶融物を環状の貯留室に均
一に分配し、貯留室から供給された被溶融物を供給プッ
シャーやスクリューフィーダーにより燃焼室中央側へ定
量宛送り込んでいる為、被溶融物を燃焼室内へ均一且つ
円滑に供給することができ、燃焼室内に常に燃焼状態に
応じた被溶融物の層を形成することができる。その結
果、被溶融物の溶融処理を効率良く行える。
In this melting furnace, a layer of the material to be melted is formed in the vicinity of the peripheral wall and the bottom wall of the furnace body so that the peripheral wall and the bottom wall are not exposed, so that heat radiation from the furnace wall is reduced. As a result, less fuel is consumed and the life of the refractory material on the furnace wall is extended. In addition, because the furnace body and ceiling wall are fixed, the drive unit such as the furnace body can be omitted, and there is no need to make all the fuel supply pipes and combustion air supply pipes to the burner flexible. The structure of the furnace itself can be greatly simplified, and maintenance becomes extremely easy. Furthermore, the material to be melted is evenly distributed to the annular storage chamber by the distribution supply device, and the material to be melted supplied from the storage chamber is sent to the central side of the combustion chamber by a supply pusher or screw feeder. The substance can be uniformly and smoothly supplied into the combustion chamber, and a layer of the material to be melted can be always formed in the combustion chamber according to the combustion state. As a result, the melting process of the material to be melted can be performed efficiently.

【0018】[0018]

【実施例】以下、本発明の実施例を図面に基づいて詳細
に説明する。図1は本発明の実施例に係る円形固定式溶
融炉の概略縦断面図であり、1は炉本体、2は天井壁、
3はバーナ、4は分配供給装置、5は供給プッシャー、
6はガイド体、7はホッパ、8はフレーム、9は水冷式
スラグカッター、10は水槽、11は水封式フライトコ
ンベヤ、12は水噴霧ノズル、13は煙道である。
Embodiments of the present invention will now be described in detail with reference to the drawings. FIG. 1 is a schematic vertical sectional view of a circular fixed melting furnace according to an embodiment of the present invention, in which 1 is a furnace body, 2 is a ceiling wall,
3 is a burner, 4 is a distributor and feeder, 5 is a supply pusher,
6 is a guide body, 7 is a hopper, 8 is a frame, 9 is a water-cooled slag cutter, 10 is a water tank, 11 is a water-sealed flight conveyor, 12 is a water spray nozzle, and 13 is a flue.

【0019】前記炉本体1は、図1に示すように有底筒
状を呈して居り、内周面が耐火煉瓦等の耐火物で覆われ
た周壁1aと、内面が同じく耐火煉瓦等の耐火物で覆わ
れ、表面がすり鉢状の緩やかな傾斜面となった底壁1b
とから成る。又、底壁1bの中央部には、スラグ並びに
燃焼ガスを排出する為のスラグ・ガス排出口1cが形成
されている。尚、スラグ・ガス排出口1cの近傍位置に
は、冷却水ジャケット(図示省略)が埋設されている。
そして、炉本体1は、床面に立設したフレーム8に水平
姿勢で設置固定されている。
As shown in FIG. 1, the furnace body 1 has a bottomed tubular shape, and has a peripheral wall 1a whose inner peripheral surface is covered with a refractory material such as refractory bricks, and an inner surface which is fire resistant such as refractory bricks. The bottom wall 1b is covered with objects and has a mortar-like gently sloping surface.
It consists of and. A slag / gas discharge port 1c for discharging slag and combustion gas is formed at the center of the bottom wall 1b. A cooling water jacket (not shown) is buried in the vicinity of the slag / gas discharge port 1c.
The furnace body 1 is installed and fixed in a horizontal posture on a frame 8 standing on the floor.

【0020】前記天井壁2は、耐火煉瓦等の耐火物で形
成されて居り、炉本体1の上方開口部に配置され、フレ
ーム8に固定支持されている。これによって、炉本体1
と天井壁2との間に燃焼室14が形成されると共に、炉
本体1の周壁1a上端部と天井壁2の周縁部との間に環
状の貯留室15が形成されることになる。尚、天井壁2
の上面には、冷却水ジャケット(図示省略)が設置され
ている。
The ceiling wall 2 is made of a refractory material such as refractory brick, is arranged in the upper opening of the furnace body 1, and is fixedly supported by the frame 8. As a result, the furnace body 1
The combustion chamber 14 is formed between the upper end of the peripheral wall 1a of the furnace body 1 and the peripheral edge of the ceiling wall 2 between the upper end of the furnace body 1 and the ceiling wall 2. The ceiling wall 2
A cooling water jacket (not shown) is installed on the upper surface of the.

【0021】前記バーナ3は、天井壁2の中央部に設け
られている。本実施例では、スラグ・ガス排出口1cが
バーナ3の直下に位置している為、バーナ3には重油を
燃料とする広角旋回流バーナが使用されて居り、火炎が
充分に広がって焼却灰等の被溶融物16の表面に沿って
流れるようにしている。尚、バーナ3にはガスバーナを
使用しても良い。
The burner 3 is provided at the center of the ceiling wall 2. In this embodiment, since the slag / gas discharge port 1c is located directly below the burner 3, a wide-angle swirl flow burner using heavy oil as fuel is used for the burner 3, and the flame spreads sufficiently to incinerate ash. It is made to flow along the surface of the material 16 to be melted. A gas burner may be used as the burner 3.

【0022】前記分配供給装置4は、貯留室15の上方
位置に配設され、ホッパ7から貯留室15の一個所に供
給された被溶融物16を貯留室15に均一に分配するも
のである。即ち、分配供給装置4は、図1及び図2に示
す如く、環状の貯留室15の上方位置に配置され、貯留
室15に沿って回転する外側環状フレーム4a及び内側
環状フレーム4bと、両環状フレーム4a,4b間に等
間隔毎に取り付けられ、環状の貯留室15の一個所に供
給された被溶融物16を貯留室15に均一に分配する作
用をする複数枚の分配用ベーン4cと、外側環状フレー
ム4aの外周面に配置された調整ローラ4dと、外側環
状フレーム4aの外周面に形成されたラック4eと、ラ
ック4eに噛合するピニオン4fと、ピニオン4fを回
転駆動させる歯車機構4g及びモータ4h等から成り、
ピニオン4fが回転すると、各環状フレーム4a,4b
が回転し、分配用ベーン4cが環状の貯留室15の一個
所に供給された被溶融物16を貯留室15に均一に分配
するようになっている。
The distribution and supply device 4 is arranged above the storage chamber 15 and uniformly distributes the melted material 16 supplied from the hopper 7 to one portion of the storage chamber 15 to the storage chamber 15. . That is, as shown in FIGS. 1 and 2, the distribution and supply device 4 is disposed above the annular storage chamber 15 and rotates along the storage chamber 15 with an outer annular frame 4a and an inner annular frame 4b, and both annular. A plurality of distribution vanes 4c, which are mounted at equal intervals between the frames 4a and 4b, and have a function of uniformly distributing the melted material 16 supplied to one location of the annular storage chamber 15 to the storage chamber 15, An adjusting roller 4d arranged on the outer peripheral surface of the outer annular frame 4a, a rack 4e formed on the outer peripheral surface of the outer annular frame 4a, a pinion 4f meshing with the rack 4e, and a gear mechanism 4g for rotationally driving the pinion 4f, It consists of a motor 4h,
When the pinion 4f rotates, the respective annular frames 4a, 4b
Is rotated so that the distribution vane 4c uniformly distributes the melted material 16 supplied to one portion of the annular storage chamber 15 to the storage chamber 15.

【0023】前記供給プッシャー5は、炉本体1の底壁
1b外周縁部に等角度毎に配設されて居り、貯留室15
から供給された被溶融物16を燃焼室14中央側へ定量
宛押し出し、燃焼室14内に常に理想的な被溶融物16
の層が形成されるようにするものである。本実施例で
は、供給プッシャー5は、図1及び図3に示す如く、炉
本体1の底壁1b外周縁部に等角度毎で且つ進退移動自
在に配設された複数のプッシャー5aと、各プッシャー
5aを進退移動させる流体圧シリンダ5b等から成る。
又、プッシャー5aには、スラグ・ガス排出口1cの直
径と略同一の幅を有するプッシャー5aが多数(本実施
例では八つ)使用されている。尚、スラグ・ガス排出口
1cの直径と略同一の幅を有するプッシャー5aを多数
使用したのは、これらのプッシャー5aを多数用いるこ
とにより被溶融物16の層を正確に調整できることが経
験により知られているからである。そして、各プッシャ
ー5aは、自動的に一定の時間を置いて順番に進退移動
するように駆動制御されている。
The supply pushers 5 are arranged on the outer peripheral edge of the bottom wall 1b of the furnace body 1 at equal angles, and the storage chamber 15
The melted material 16 supplied from the unit is extruded in a fixed amount to the center side of the combustion chamber 14, and the ideal melted material 16 is always fed into the combustion chamber 14.
Is to be formed. In the present embodiment, as shown in FIGS. 1 and 3, the supply pusher 5 includes a plurality of pushers 5a which are arranged on the outer peripheral edge of the bottom wall 1b of the furnace body 1 at equal angles and are movable back and forth. It is composed of a fluid pressure cylinder 5b for moving the pusher 5a forward and backward.
In addition, a large number of pushers 5a (eight in this embodiment) having a width substantially the same as the diameter of the slag / gas discharge port 1c are used as the pushers 5a. It should be noted that the fact that a large number of pushers 5a having a width substantially the same as the diameter of the slag / gas discharge port 1c are used is known from experience that the layer of the melted material 16 can be accurately adjusted by using a large number of these pushers 5a. It is because it is being done. Then, each pusher 5a is drive-controlled so as to automatically advance and retreat in order with a fixed time.

【0024】前記ガイド体6は、耐火煉瓦等の耐火物に
より三角錐形状に形成されて居り、隣接する各プッシャ
ー5a間に配置されている。又、各ガイド体6の傾斜面
6aは、貯留室15に供給された被溶融物16が自然に
供給プッシャー5側へ滑り落ちるように被溶融物16の
安息角以上の傾斜を有している。
The guide body 6 is formed of a refractory material such as refractory bricks into a triangular pyramid shape, and is arranged between the adjacent pushers 5a. Further, the inclined surface 6a of each guide body 6 has an inclination equal to or greater than the repose angle of the melted material 16 so that the melted material 16 supplied to the storage chamber 15 will naturally slide down to the supply pusher 5 side.

【0025】次に、前記円形固定式溶融炉の作用につい
て説明する。ホッパ7から環状の貯留室15の一個所に
供給された焼却灰等の被溶融物16は、分配供給装置4
により貯留室15に均一に分配される。即ち、被溶融物
16は、分配供給装置4の回転自在な各環状フレーム4
a,4bに設けた分配用ベーン4cにより貯留室15に
均一に分配される。
Next, the operation of the circular fixed melting furnace will be described. The material 16 to be melted, such as incinerated ash, which is supplied from the hopper 7 to one portion of the annular storage chamber 15, is distributed by the distribution supply device 4
Are evenly distributed to the storage chamber 15. That is, the material 16 to be melted is rotated by each of the rotatable annular frames 4 of the feeder 4.
It is uniformly distributed to the storage chamber 15 by the distribution vanes 4c provided on the a and 4b.

【0026】貯留室15に均一に分配された被溶融物1
6は、供給プッシャー5により燃焼室14中央側へ押し
込まれ、燃焼室14内にすり鉢状で且つ環状に堆積され
る。このとき、プッシャー5a間に位置する被溶融物1
6は、ガイド体6に案内されてプッシャー5a側へ滑り
落ちる為、燃焼室14中央側へ良好且つ確実に押し込ま
れて行く。
The melted material 1 uniformly distributed in the storage chamber 15
6 is pushed toward the center of the combustion chamber 14 by the supply pusher 5 and is deposited in the combustion chamber 14 in a mortar shape and in an annular shape. At this time, the melted material 1 located between the pushers 5a
6 is guided by the guide body 6 and slides down to the pusher 5a side, so that it is pushed into the center of the combustion chamber 14 satisfactorily and surely.

【0027】燃焼室14内に堆積した被溶融物16は、
バーナ3の燃焼熱によりその表面がフィルム状に溶融し
てスラグとなり、すり鉢状の傾斜面を流下してスラグ・
ガス排出口1cから排出され、水槽10内に落下する。
尚、溶融スラグが傾斜面を流下することによって、傾斜
面には次々に未溶融状態の被溶融物16が露出すること
になり、この露出した被溶融物16はバーナ3の燃焼熱
により順次溶融されて行く。又、スラグがスラグ・ガス
排出口1cから流下するときにつらら状になることがあ
るが、この場合にはスラグカッター9を進退移動させて
つらら状のスラグを切り落とす。これによって、スラグ
の排出が円滑に行われる。
The melted substance 16 deposited in the combustion chamber 14 is
The combustion heat of the burner 3 melts its surface into a film, forming slag, which flows down the mortar-shaped inclined surface to form slag.
The gas is discharged from the gas discharge port 1c and falls into the water tank 10.
As the molten slag flows down the inclined surface, the unmelted molten material 16 is successively exposed on the inclined surface, and the exposed molten material 16 is sequentially melted by the combustion heat of the burner 3. Go away. Also, when the slag flows down from the slag / gas discharge port 1c, it may become icicle-shaped. In this case, the slag cutter 9 is moved forward and backward to cut off the icicle-shaped slag. As a result, the slag is discharged smoothly.

【0028】冷却水槽10内へ落下した溶融スラグは、
水槽10内で冷却固化されて黒色粒状の砂状物となった
後、水封式フライトコンベヤ11により排出される。
The molten slag dropped into the cooling water tank 10 is
After being cooled and solidified in the water tank 10 to form a black granular sand-like material, it is discharged by the water-sealed flight conveyor 11.

【0029】一方、燃焼室14内の高温の燃焼ガスは、
スラグ・ガス排出口1cから排出され、煙道13を通過
中に水噴霧ノズル12からの噴霧により減温されて大気
中に排出される。
On the other hand, the high temperature combustion gas in the combustion chamber 14 is
It is discharged from the slag / gas discharge port 1c, is cooled by the spray from the water spray nozzle 12 while passing through the flue 13, and is discharged into the atmosphere.

【0030】そして、溶融の進行に伴って溶融面が後退
すると、各供給プッシャー5が被溶融物16を定量宛燃
焼室14中央側へ押し出し、燃焼室14内に常に燃焼状
態に応じた適正な被溶融物16の層を形成する。又、プ
ッシャー5a間に位置する被溶融物16は、ガイド体6
に案内されてプッシャー5a側へ滑り落ち、プッシャー
5aによって燃焼室14中央側へ良好且つ確実に押し込
まれて行く。その結果、燃焼室14内には常時一定量の
被溶融物16が供給されて理想的な被溶融物16の層が
形成されることになり、被溶融物16の溶融処理が良好
且つ円滑に行われる。
When the melting surface retreats as the melting progresses, each supply pusher 5 pushes the material 16 to be melted toward the central portion of the combustion chamber 14 to a fixed amount, and the inside of the combustion chamber 14 is always kept in an appropriate state depending on the combustion state. A layer of the melted material 16 is formed. Further, the melted material 16 located between the pushers 5a is the guide body 6
Is pushed down to the side of the pusher 5a, and is pushed into the center of the combustion chamber 14 favorably and surely by the pusher 5a. As a result, a constant amount of the material to be melted 16 is constantly supplied into the combustion chamber 14 to form an ideal layer of the material to be melted 16, and the melting process of the material to be melted 16 is performed smoothly and smoothly. Done.

【0031】この溶融炉は、炉本体1の周壁1a近傍及
び底壁1bに被溶融物16の層を形成し、周壁1a及び
底壁1bが露出しないようにしている為、炉壁からの放
熱が少なくなる。その結果、燃料消費量が少なくて済む
うえ、炉壁の耐火物の寿命も延びることになる。又、炉
本体1や天井壁2を固定式にしている為、炉本体1等の
駆動装置を省略できるうえ、バーナ3への燃料供給管や
燃焼用空気供給管等を全てフレキシブルにしたりする必
要もなく、溶融炉自体の構造を大幅に簡略化でき、メン
テナンスも極めて容易になる。更に、分配供給装置4に
よって被溶融物16を環状の貯留室15に均一に分配
し、貯留室15から供給された被溶融物16を供給プッ
シャー5により燃焼室14中央側へ定量宛送り込んでい
る為、被溶融物16を燃焼室内へ均一且つ円滑に供給す
ることができ、溶融処理を効率良く行える。
In this melting furnace, a layer of the melted material 16 is formed in the vicinity of the peripheral wall 1a and the bottom wall 1b of the furnace body 1 so that the peripheral wall 1a and the bottom wall 1b are not exposed. Is less. As a result, less fuel is consumed and the life of the refractory material on the furnace wall is extended. Further, since the furnace body 1 and the ceiling wall 2 are fixed, the drive device for the furnace body 1 and the like can be omitted, and it is necessary to make the fuel supply pipes and combustion air supply pipes to the burner 3 all flexible. In addition, the structure of the melting furnace itself can be greatly simplified, and maintenance becomes extremely easy. Further, the material to be melted 16 is uniformly distributed to the annular storage chamber 15 by the distribution and supply device 4, and the material to be melted 16 supplied from the storage chamber 15 is sent to the central side of the combustion chamber 14 by the supply pusher 5 in a fixed amount. Therefore, the material 16 to be melted can be uniformly and smoothly supplied into the combustion chamber, and the melting process can be efficiently performed.

【0032】図4は本発明の他の実施例を示し、これは
上記第1実施例の円形固定式溶融炉のガイド体6に替え
て隣接する供給プッシャー5間にスクリューフィーダー
17を配設し、該スクリューフィーダー17により供給
プッシャー5間に供給された被溶融物16を燃焼室14
中央側へ移送するようにしたものである。即ち、各スク
リューフィーダー17は、炉本体1の底壁1b外周縁部
に等角度毎で且つ片持ち状態で回転自在に配設された円
錐状の回転軸17aと、回転軸17aに巻き付けられた
同一高さのねじ羽根17bとから成り、回転数を自由に
制御できるように構成されている。又、各スクリューフ
ィーダー17は、駆動装置(図示省略)により単独若し
くは複数組で駆動されるように構成されている。尚、そ
の他の構成(炉本体1、天井壁2、バーナ3、分配供給
装置4及び供給プッシャー5等)は、上記第1実施例の
ものと全く同一構造に構成されている。この円形回転式
溶融炉も、上記第1実施例の円形回転式溶融と同様の作
用効果を奏することができる。特に、供給プッシャー5
間に供給された被溶融物16をスクリューフィーダー1
7により燃焼室14中央側へ強制的に移送するようにし
ている為、供給プッシャー5間の被溶融物16を確実に
燃焼室14中央側へ送り込むことができる。
FIG. 4 shows another embodiment of the present invention in which a screw feeder 17 is provided between adjacent feed pushers 5 instead of the guide body 6 of the circular fixed melting furnace of the first embodiment. The melted material 16 supplied between the supply pushers 5 by the screw feeder 17 is transferred to the combustion chamber 14
It is designed to be transferred to the center side. That is, each screw feeder 17 is wound around the conical rotation shaft 17a, which is rotatably arranged in the cantilevered state at equal angular intervals on the outer peripheral edge of the bottom wall 1b of the furnace body 1, and the rotation shaft 17a. It is composed of screw blades 17b having the same height, and is configured so that the rotation speed can be freely controlled. Further, each screw feeder 17 is configured to be driven alone or in a plurality of sets by a driving device (not shown). The other structures (the furnace body 1, the ceiling wall 2, the burner 3, the distribution supply device 4, the supply pusher 5, etc.) have the same structure as that of the first embodiment. This circular rotary melting furnace can also achieve the same effects as the circular rotary melting of the first embodiment. In particular, supply pusher 5
The material 16 to be melted supplied between the screw feeder 1
Since it is forcibly transferred to the center side of the combustion chamber 14 by 7, it is possible to reliably send the melted substance 16 between the supply pushers 5 to the center side of the combustion chamber 14.

【0033】図5乃至図7は本発明の更に他の実施例に
係る円形固定式溶融炉の概略縦断面図であり、当該円形
固定式溶融炉は、炉本体1、天井壁2、バーナ3、分配
供給装置4、スクリューフィーダー17、ホッパ7、フ
レーム8、水冷式スラグカッター9、水槽10、水封式
フライトコンベヤ11、水噴霧ノズル12及び煙道13
等から構成されて居り、上記第1実施例の円形固定式溶
融炉の供給プッシャー5及びガイド体6に替えてスクリ
ューフィーダー17を配設したものである。尚、その他
の構成(炉本体1、天井壁2、バーナ3及び分配供給装
置4等)は、上記第1実施例のものと同一構造に構成さ
れて居り、第1実施例のものと同一の部材には同じ参照
番号を付している。
5 to 7 are schematic vertical sectional views of a circular fixed melting furnace according to still another embodiment of the present invention. The circular fixed melting furnace includes a furnace body 1, a ceiling wall 2 and a burner 3. , Distribution feeder 4, screw feeder 17, hopper 7, frame 8, water-cooled slag cutter 9, water tank 10, water-sealed flight conveyor 11, water spray nozzle 12 and flue 13
And the like, and the screw feeder 17 is provided in place of the feed pusher 5 and the guide body 6 of the circular fixed melting furnace of the first embodiment. The other structures (furnace body 1, ceiling wall 2, burner 3, distribution supply device 4, etc.) are the same as those of the first embodiment, and are the same as those of the first embodiment. Parts are given the same reference numbers.

【0034】前記スクリューフィーダー17は、炉本体
1の底壁1b外周縁部に等角度毎に配設されて居り、貯
留室15から供給された被溶融物16を燃焼室14中央
側へ定量宛移送するものである。即ち、スクリューフィ
ーダー17は、炉本体1の底壁1b外周縁部に等角度毎
で且つ片持ち状態で回転自在に配設された円錐状の回転
軸17aと、回転軸17aに巻き付けられた同一高さの
ねじ羽根17bとから成り、回転数を自由に制御できる
ように構成されている。又、各スクリューフィーダー1
7は、駆動装置(図示省略)により単独若しくは複数組
で駆動されるように構成されている。尚、ねじ羽根17
bを同一高さとすることにより被溶融物16を略均一に
送ることができ、又、回転数を無段変速とすることによ
り被溶融物16の送り量を任意に調整することができ
る。
The screw feeders 17 are arranged at equal angles on the outer peripheral edge of the bottom wall 1b of the furnace body 1, and the melted material 16 supplied from the storage chamber 15 is delivered to the center of the combustion chamber 14 in a fixed amount. It is to be transferred. That is, the screw feeder 17 is a conical rotating shaft 17a that is rotatably arranged in the outer peripheral edge portion of the bottom wall 1b of the furnace body 1 at equal angles and in a cantilever state, and the same rotating shaft 17a wound around the rotating shaft 17a. It is composed of a screw blade 17b having a height and is configured so that the rotation speed can be freely controlled. Also, each screw feeder 1
7 is configured to be driven by a driving device (not shown) alone or in plural sets. In addition, the screw blade 17
By setting b to be the same height, the melted material 16 can be fed substantially uniformly, and by setting the number of revolutions to continuously variable speed, the feed amount of the melted material 16 can be arbitrarily adjusted.

【0035】この円形回転式溶融炉は、上記第1実施例
の円形回転式溶融と同様の作用効果を奏することができ
る。然も、被溶融物16を連続的に送り込むことができ
ると共に、被溶融物16の送り込み量も調整することが
できる為、燃焼室14内に常に燃焼状態に応じた適正な
被溶融物16の層を確実に形成することができ、被溶融
物16の溶融処理をより一層効率良く行える。
This circular rotary melting furnace can achieve the same effects as the circular rotary melting of the first embodiment. Needless to say, since the melted material 16 can be continuously fed and the amount of the melted material 16 fed can also be adjusted, a proper melted material 16 that always corresponds to the combustion state can be provided in the combustion chamber 14. The layer can be reliably formed, and the melting process of the melted material 16 can be performed more efficiently.

【0036】上記各実施例に於いては、炉本体1及び天
井壁2を平面視に於いて円形に形成したが、他の実施例
に於いては、炉本体1及び天井壁2を多角形に形成する
ようにしても良い。
In each of the above-mentioned embodiments, the furnace body 1 and the ceiling wall 2 are formed in a circular shape in a plan view, but in other embodiments, the furnace body 1 and the ceiling wall 2 are polygonal. It may be formed in.

【0037】上記各実施例に於いては、ホッパ7から貯
留室15内へ被溶融物16を供給するようにしたが、他
の実施例に於いては、貯留室15の上方位置にロータリ
ーフィーダー等の定量供給装置(図示省略)を配設し、
貯留室15内へ被溶融物16を定量宛供給するようにし
ても良い。
In each of the above embodiments, the material 16 to be melted is supplied from the hopper 7 into the storage chamber 15. However, in other embodiments, the rotary feeder is located above the storage chamber 15. A fixed amount supply device (not shown) such as
The melted material 16 may be supplied in a fixed amount into the storage chamber 15.

【0038】[0038]

【発明の効果】上述の通り、本発明の請求項1の円形固
定式溶融炉は、分配供給装置及び供給プッシャーによっ
て炉本体の炉壁を覆う被溶融物の層を形成し、この被溶
融物の層を表面側から溶融するようしている為、炉壁の
露出を防止することができる。その結果、炉壁からの放
熱が少なくなり、燃料消費量が少なくて済むうえ、炉壁
の耐火物の寿命も延びることになる。又、炉本体及び天
井壁を固定式にしている為、炉本体の回転駆動装置や天
井壁の昇降駆動装置等を省略できるうえ、バーナへの燃
料供給管や燃焼用空気供給管等を全てフレキシブルにし
たりする必要もない。その結果、溶融炉自体の構造を大
幅に簡略化できると共に、メンテナンスも極めて容易に
なる。更に、分配供給装置によって被溶融物を環状の貯
留室に均一に分配し、貯留室から供給された被溶融物を
複数の供給プッシャーにより燃焼室中央側へ定量宛送り
込んでいる為、被溶融物を燃焼室内へ均一且つ円滑に供
給することができ、燃焼室内に常に理想的な被溶融物の
層を形成することができる。その結果、被溶融物の溶融
処理を効率良く行える。そのうえ、隣接する供給プッシ
ャー間にガイド体を配設し、供給プッシャー間に位置す
る被溶融物がガイド体により供給プッシャー側へ滑り落
ちるようにしている為、環状の貯留室に供給された被溶
融物は、燃焼室中央側へ良好且つ確実に押し込まれて行
く。
As described above, the circular fixed melting furnace according to claim 1 of the present invention forms a layer of the melted material covering the furnace wall of the furnace body by the distribution supply device and the supply pusher, and the melted material is formed. Since the layer is melted from the surface side, it is possible to prevent the furnace wall from being exposed. As a result, less heat is radiated from the furnace wall, less fuel is consumed, and the life of the refractory material on the furnace wall is extended. Also, because the furnace body and ceiling wall are fixed, the rotation drive device for the furnace body and the lift drive device for the ceiling wall can be omitted, and all fuel supply pipes and combustion air supply pipes to the burner are flexible. There is no need to turn it on. As a result, the structure of the melting furnace itself can be greatly simplified, and maintenance becomes extremely easy. Furthermore, since the material to be melted is evenly distributed to the annular storage chamber by the distribution and supply device, and the material to be melted supplied from the storage chamber is sent to the central side of the combustion chamber by a plurality of supply pushers, the material to be melted Can be uniformly and smoothly supplied into the combustion chamber, and an ideal melted material layer can always be formed in the combustion chamber. As a result, the melting process of the material to be melted can be performed efficiently. Moreover, since the guide body is arranged between the adjacent supply pushers and the melted material located between the supply pushers is slid down toward the supply pusher side by the guide body, the melted material supplied to the annular storage chamber. Is satisfactorily and surely pushed into the center of the combustion chamber.

【0039】本発明の請求項2〜3の円形固定式溶融炉
にあっては、上記効果に加えて、更に次のような効果を
奏し得る。即ち、請求項2の溶融炉にあっては、隣接す
る供給プッシャー間にスクリューフィーダーを配設し、
供給プッシャー間に供給された被溶融物をスクリューフ
ィーダーにより強制的に移送するようにしている為、供
給プッシャー間の被溶融物は確実に燃焼室中央側へ押し
込まれて行く。又、請求項3の溶融炉にあっては、炉本
体の底壁に、貯留室から供給された被溶融物を燃焼室中
央側へ定量宛移送する複数のスクリューフィーダーを配
設している為、被溶融物を燃焼室内へ連続的に送り込む
ことができると共に、被溶融物の送り込み量も調整する
ことができる。その結果、燃焼室内に常に燃焼状態に応
じた適正な被溶融物の層を確実に形成することができ、
被溶融物の溶融処理をより一層効率良く行える。
In the circular fixed type melting furnace according to the second to third aspects of the present invention, the following effects can be obtained in addition to the above effects. That is, in the melting furnace of claim 2, the screw feeder is provided between the adjacent supply pushers,
Since the melted material supplied between the supply pushers is forcibly transferred by the screw feeder, the melted material between the supply pushers is reliably pushed toward the center of the combustion chamber. Further, in the melting furnace of claim 3, a plurality of screw feeders for quantitatively transferring the melted material supplied from the storage chamber to the central side of the combustion chamber are arranged on the bottom wall of the furnace body. The molten material can be continuously fed into the combustion chamber, and the amount of the molten material fed can be adjusted. As a result, it is possible to reliably form an appropriate layer of the material to be melted according to the combustion state in the combustion chamber,
The melting process of the material to be melted can be performed more efficiently.

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

【図1】本発明の実施例に係る円形固定式溶融炉の概略
縦断面図である。
FIG. 1 is a schematic vertical sectional view of a circular fixed melting furnace according to an embodiment of the present invention.

【図2】分配供給装置の概略平面図である。FIG. 2 is a schematic plan view of a distribution and supply device.

【図3】炉本体の底壁部分の概略横断面図である。FIG. 3 is a schematic cross-sectional view of a bottom wall portion of a furnace body.

【図4】本発明の他の実施例を示し、炉本体の底壁部分
の概略横断面図である。
FIG. 4 is a schematic cross-sectional view of the bottom wall portion of the furnace body showing another embodiment of the present invention.

【図5】本発明の更に他の実施例に係る円形固定式溶融
炉の概略縦断面図である。
FIG. 5 is a schematic vertical sectional view of a circular fixed melting furnace according to still another embodiment of the present invention.

【図6】分配供給装置の概略平面図である。FIG. 6 is a schematic plan view of a distribution and supply device.

【図7】炉本体の底壁部分の概略横断面図である。FIG. 7 is a schematic cross-sectional view of the bottom wall portion of the furnace body.

【図8】従来の角形固定式溶融炉の概略縦断面図であ
る。
FIG. 8 is a schematic vertical sectional view of a conventional square fixed melting furnace.

【図9】従来の円形回転式溶融炉の概略縦断面図であ
る。
FIG. 9 is a schematic vertical sectional view of a conventional circular rotary melting furnace.

【図10】円形回転式溶融炉の要部の縦断面図である。FIG. 10 is a vertical sectional view of a main part of a circular rotary melting furnace.

【符号の説明】[Explanation of symbols]

1は炉本体、1aは周壁、1bは底壁、1cはスラグ・
ガス排出口、2は天井壁、3はバーナ、4は分配供給装
置、6はカッター体、14燃焼室、15は貯留室、16
は被溶融物、17はスクリューフィーダー。
1 is a furnace body, 1a is a peripheral wall, 1b is a bottom wall, 1c is a slag,
Gas discharge port, 2 ceiling wall, 3 burner, 4 distribution supply device, 6 cutter body, 14 combustion chamber, 15 storage chamber, 16
Is a melted material, and 17 is a screw feeder.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23J 1/00 B09B 3/00 C02F 11/10 F23G 3/00 115 F27B 3/18 ─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields surveyed (Int.Cl. 7 , DB name) F23J 1/00 B09B 3/00 C02F 11/10 F23G 3/00 115 F27B 3/18

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 固定状態で設置され、底壁(1b)中央
部にスラグ・ガス排出口(1c)を形成した略有底筒状
の炉本体(1)と、炉本体(1)の上方開口部に固定状
態で配置され、炉本体(1)との間に燃焼室(14)を
形成すると共に、炉本体(1)の周壁(1a)との間に
環状の貯留室(15)を形成する天井壁(2)と、天井
壁(2)に設けられたバーナ(3)と、環状の貯留室
(15)に配設され、貯留室(15)の一個所に供給さ
れた焼却灰等の被溶融物(16)を貯留室(15)に均
一に分配する分配供給装置(4)と、炉本体(1)の底
壁(1b)外周縁部に等角度毎に配設され、貯留室(1
5)から供給された被溶融物(16)を燃焼室(14)
中央側へ定量宛押し出して燃焼室(14)内にすり鉢状
で且つ環状の被溶融物(16)の層を形成する複数の供
給プッシャー(5)と、隣接する供給プッシャー(5)
間に配置され、供給プッシャー(5)間に供給された被
溶融物(16)が自然に供給プッシャー(5)側へ滑り
落ちるように被溶融物(16)の安息角以上の傾斜を有
する耐火物により三角錐形状に形成された複数のガイド
体(6)とを具備したことを特徴とする円形固定式溶融
炉。
1. A substantially bottomed cylindrical furnace body (1) which is fixedly installed and has a slag / gas discharge port (1c) formed at the center of the bottom wall (1b), and above the furnace body (1). A combustion chamber (14) is formed between the furnace body (1) and the furnace body (1) in a fixed state, and an annular storage chamber (15) is formed between the furnace body (1) and the peripheral wall (1a). The incineration ash that is arranged in the ceiling wall (2) to be formed, the burner (3) provided in the ceiling wall (2), and the annular storage chamber (15) and is supplied to one location of the storage chamber (15). A distribution supply device (4) for uniformly distributing the melted material (16) to the storage chamber (15), and the distribution supply device (4) at the outer peripheral edge of the bottom wall (1b) of the furnace body (1) at equal angles, Storage chamber (1
5) the material to be melted (16) supplied from the combustion chamber (14)
A plurality of feed pushers (5) that push out a fixed amount toward the center side to form a layer of the mortar-shaped and to-be-melted substance (16) in the combustion chamber (14), and adjacent feed pushers (5)
Refractory having an inclination equal to or greater than the repose angle of the melted material (16) so that the melted material (16) disposed between the supply pushers (5) slides down to the supply pusher (5) side naturally . And a plurality of guide bodies (6) formed in the shape of a triangular pyramid .
【請求項2】 固定状態で設置され、底壁(1b)中央
部にスラグ・ガス排出口(1c)を形成した略有底筒状
の炉本体(1)と、炉本体(1)の上方開口部に固定状
態で配置され、炉本体(1)との間に燃焼室(14)を
形成すると共に、炉本体(1)の周壁(1a)との間に
環状の貯留室(15)を形成する天井壁(2)と、天井
壁(2)に設けられたバーナ(3)と、環状の貯留室
(15)に配設され、貯留室(15)の一個所に供給さ
れた焼却灰等の被溶融物(16)を貯留室(15)に均
一に分配する分配供給装置(4)と、炉本体(1)の底
壁(1b)外周縁部に等角度毎に配設され、貯留室(1
5)から供給された被溶融物(16)を燃焼室(14)
中央側へ定量宛押し出して燃焼室(14)内にすり鉢状
で且つ環状の被溶融物(16)の層を形成する複数の供
給プッシャー(5)と、隣接する供給プッシャー(5)
間に配置され、供給プッシャー(5)間に供給された被
溶融物(16)を燃焼室(14)中央側へ移送すると共
に回転数を自由に制御できる複数のスクリューフィーダ
ー(17)とを具備したことを特徴とする円形固定式溶
融炉。
2. A furnace body (1) having a substantially bottomed shape, which is installed in a fixed state and has a slag / gas discharge port (1c) formed in the center of the bottom wall (1b), and above the furnace body (1). A combustion chamber (14) is formed between the furnace body (1) and the furnace body (1) in a fixed state, and an annular storage chamber (15) is formed between the furnace body (1) and the peripheral wall (1a). The incineration ash that is arranged in the ceiling wall (2) to be formed, the burner (3) provided in the ceiling wall (2), and the annular storage chamber (15) and is supplied to one location of the storage chamber (15). A distribution supply device (4) for uniformly distributing the melted material (16) to the storage chamber (15), and the distribution supply device (4) at the outer peripheral edge of the bottom wall (1b) of the furnace body (1) at equal angles, Storage chamber (1
5) the material to be melted (16) supplied from the combustion chamber (14)
A plurality of feed pushers (5) that push out a fixed amount toward the center side to form a layer of the mortar-shaped and to-be-melted substance (16) in the combustion chamber (14), and adjacent feed pushers (5)
The melted material (16), which is arranged between the feed pushers (5) and is fed to the center of the combustion chamber (14), is commonly used.
A circular fixed melting furnace, characterized in that it is provided with a plurality of screw feeders (17) whose rotation speed can be freely controlled .
【請求項3】 固定状態で設置され、底壁(1b)中央
部にスラグ・ガス排出口(1c)を形成した略有底筒状
の炉本体(1)と、炉本体(1)の上方開口部に固定状
態で配置され、炉本体(1)との間に燃焼室(14)を
形成すると共に、炉本体(1)の周壁(1a)との間に
環状の貯留室(15)を形成する天井壁(2)と、天井
壁(2)に設けられたバーナ(3)と、環状の貯留室
(15)に配設され、貯留室(15)の一個所に供給さ
れた焼却灰等の被溶融物(16)を貯留室(15)に均
一に分配する分配供給装置(4)と、炉本体(1)の底
壁(1b)外周縁部に等角度毎に配設され、貯留室(1
5)から供給された被溶融物(16)を燃焼室(14)
中央側へ定量宛移送して燃焼室(14)内にすり鉢状で
且つ環状の被溶融物(16)の層を形成すると共に回転
数を自由に制御できる複数のスクリューフィーダー(1
7)とを具備したことを特徴とする円形固定式溶融炉。
3. A substantially bottomed cylindrical furnace body (1) installed in a fixed state and having a slag / gas discharge port (1c) formed at the center of the bottom wall (1b), and above the furnace body (1). A combustion chamber (14) is formed between the furnace body (1) and the furnace body (1) in a fixed state, and an annular storage chamber (15) is formed between the furnace body (1) and the peripheral wall (1a). The incineration ash that is arranged in the ceiling wall (2) to be formed, the burner (3) provided in the ceiling wall (2), and the annular storage chamber (15) and is supplied to one location of the storage chamber (15). A distribution supply device (4) for uniformly distributing the melted material (16) to the storage chamber (15), and the distribution supply device (4) at the outer peripheral edge of the bottom wall (1b) of the furnace body (1) at equal angles, Storage chamber (1
5) the material to be melted (16) supplied from the combustion chamber (14)
Transferring a fixed amount to the center side to form a mortar-shaped and annular layer of the melted material (16) in the combustion chamber (14) and rotate it.
Multiple screw feeder that can be freely control the number (1
7) A circular fixed type melting furnace comprising:
JP28374894A 1994-11-17 1994-11-17 Circular fixed melting furnace Expired - Fee Related JP3361198B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28374894A JP3361198B2 (en) 1994-11-17 1994-11-17 Circular fixed melting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28374894A JP3361198B2 (en) 1994-11-17 1994-11-17 Circular fixed melting furnace

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JPH08145327A JPH08145327A (en) 1996-06-07
JP3361198B2 true JP3361198B2 (en) 2003-01-07

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Publication number Priority date Publication date Assignee Title
TW468021B (en) * 1998-03-27 2001-12-11 Mitsubishi Heavy Ind Ltd Ash melting furnace and ash melting method thereof
JP5627998B2 (en) * 2010-11-10 2014-11-19 株式会社チサキ Raw material heat treatment equipment
KR101889153B1 (en) * 2016-08-31 2018-08-17 주식회사 포스코 Combustor

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