JPS6119313Y2 - - Google Patents

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Publication number
JPS6119313Y2
JPS6119313Y2 JP1978056686U JP5668678U JPS6119313Y2 JP S6119313 Y2 JPS6119313 Y2 JP S6119313Y2 JP 1978056686 U JP1978056686 U JP 1978056686U JP 5668678 U JP5668678 U JP 5668678U JP S6119313 Y2 JPS6119313 Y2 JP S6119313Y2
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JP
Japan
Prior art keywords
combustion chamber
secondary combustion
tube
cooling device
opening
Prior art date
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Expired
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JP1978056686U
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Japanese (ja)
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JPS54158487U (en
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Publication of JPS54158487U publication Critical patent/JPS54158487U/ja
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Description

【考案の詳細な説明】 本考案は、下水汚泥、都市塵芥、各種産業廃棄
物等の被処理物を焼却溶融並びに冷却処理するた
めの焼却溶融炉に関し、詳しくは、溶融炉の下向
き開口の下側に二次燃焼室を連設し、その二次燃
焼室に溶融処理物及び高温排ガスを排出するため
の流下筒を連設し、前記開口からの溶融処理物を
前記流下筒を介して下方に配設の直接水冷式の冷
却装置に供給すべく構成し、前記開口からの高温
排ガスを、前記二次燃焼室に連なる煙道を通じて
排出すべく構成した焼却溶融炉に関する。
[Detailed Description of the Invention] The present invention relates to an incinerator and melting furnace for incinerating, melting, and cooling treatment materials such as sewage sludge, urban garbage, and various industrial wastes. A secondary combustion chamber is connected to the side, and a flow tube for discharging the melted product and high-temperature exhaust gas is connected to the secondary combustion chamber, and the melted product from the opening is directed downward through the flow tube. The present invention relates to an incinerator and melting furnace configured to supply high-temperature exhaust gas from the opening to a direct water-cooled cooling device disposed in the combustion chamber, and to discharge high-temperature exhaust gas from the opening through a flue connected to the secondary combustion chamber.

被処理物を焼却溶融して後に冷却処理するに、
従来一般搬には、溶融炉の下向き開口直下に直接
水冷型式の冷却装置を配設すると共に、その溶融
物の流下経路途中に二次燃焼室を設け、もつて前
記二次燃焼室によつて排ガス中の臭気成分を焼却
脱臭すると共に、溶融物を直接水冷によつて固化
して、埋戻しなどに利用するスラグを回収してい
たが、高温の溶融物を直接水冷する事と、二次燃
焼室からの輻射熱による加熱作用とが相俟つて、
直接水冷式の冷却装置において多量の水蒸気が発
生し、この為に二次燃焼室の温度が低下して脱臭
効率の低下や、排ガス廃熱を利用する場合に熱交
換面での悪影響がみられ、あるいはこれを補うた
めに燃料消費量が増大するなどの問題がみられ
る。
When the material to be processed is incinerated and melted and then cooled,
Conventionally, in general transportation, a water cooling type cooling device is installed directly below the downward opening of the melting furnace, and a secondary combustion chamber is installed in the middle of the flow path of the melt. In addition to incinerating and deodorizing the odor components in the exhaust gas, the molten material was solidified by direct water cooling to recover slag for use in backfilling. Combined with the heating effect of radiant heat from the combustion chamber,
A large amount of water vapor is generated in a direct water-cooled cooling system, which lowers the temperature of the secondary combustion chamber, resulting in a decrease in deodorizing efficiency and adverse effects on heat exchange when exhaust gas waste heat is used. Or, to compensate for this, there are problems such as an increase in fuel consumption.

このような不都合を解消する手段として、従来
では、実開昭52−165583号公報に示されるよう
に、溶融物の水槽内への投下に伴つて発生する多
量の水蒸気を、二次燃焼室に達する前に外部へ吸
引導出する手段が用いられていたが、この場合に
は、 (イ) 発生蒸気の吸引導管を二次燃焼室の煙道とは
別に、冷却装置となる水槽と二次燃焼室との間
に設けているために、溶融物の落下経路が長く
なり、装置全体の大型化を逸がれない。
Conventionally, as a means to eliminate such inconveniences, as shown in Japanese Utility Model Application No. 52-165583, a large amount of water vapor generated when the melt is dropped into a water tank is transferred to a secondary combustion chamber. In this case, (a) the suction pipe for the generated steam is separated from the flue of the secondary combustion chamber, and the water tank serving as a cooling device and the secondary combustion Because it is provided between the chamber and the chamber, the falling path of the molten material becomes long, and the overall size of the apparatus cannot be avoided.

(ロ) 溶融処理物を直接冷却するときの衝撃的かつ
急激な処理物の冷却によつて、回収スラグが粉
粒状に細分化してしまう。
(b) When the molten material is directly cooled, the recovered slag is fragmented into powder particles due to the shocking and sudden cooling of the material.

という欠点があつた。There was a drawback.

本考案が解決しようとする技術的課題は、上述
の如き従来技術の欠点を解消するにあたつて、装
置全体の小型化を図るために、二次燃焼室から冷
却装置の水面に至る溶融物落下経路を短かくすれ
ば、熱源となる二次燃焼室と水面との距離が短か
くなつてより一層水蒸気が発生し易くなるとい
う、装置全体の小型化と二次燃焼室内での燃焼温
度の低下を防止する手段とが、互に相反する条件
のもとで成り立つとみられていた困難性を克服し
て、 a 二次燃焼室と水面とを近づけて装置全体の小
型化を図りながらも、水蒸気の発生は抑制して
二次燃焼室内での温度低下を避ける。
The technical problem to be solved by the present invention is to solve the above-mentioned drawbacks of the conventional technology, and to reduce the size of the entire device by reducing the amount of molten material from the secondary combustion chamber to the water surface of the cooling device. By shortening the falling path, the distance between the secondary combustion chamber, which is the heat source, and the water surface becomes shorter, making it easier to generate water vapor. By overcoming the difficulty that was thought to exist under mutually contradictory conditions, the means to prevent the decrease in water level have been overcome, and a. The generation of water vapor is suppressed to avoid a drop in temperature in the secondary combustion chamber.

b 直接水冷式の冷却装置を用いながら溶融物の
細分化を避ける。
b. Avoid fragmentation of the melt while using direct water-cooled cooling equipment.

という目的を達成することができる。This purpose can be achieved.

上記課題を解決するために講じた本考案の技術
手段は、溶融炉の下向き開口の下側に二次燃焼室
を連設し、その二次燃焼室に溶融処理物及び高温
排ガスを排出するための流下筒を連設し前記開口
からの溶融処理物を前記流下筒を介して下方に配
設の直接水冷式の冷却装置に供給すべく構成し、
前記開口からの高温排ガスを、前記二次燃焼室に
連なる煙道を通じ排出すべく構成した焼却溶融炉
であつて、前記流下筒の下端にその流下筒の下方
位置から前記冷却装置の溶融処理物の受入口にわ
たつて、前記冷却装置側に向うほど下降する溶融
処理物受止め面を備えた傾斜供給筒を連設して溶
融処理物の流下経路の全体を屈曲経路に構成し、
前記傾斜供給筒の少なくとも溶融処理物受止め面
を間接鈴却型式に構成すると共に、前記溶融処理
物受止め面に沿つて摺動自在に、かつ、その押出
面を間接冷却型式に構成した押出具を設け、さら
に、前記傾斜供給筒の溶融処理物移送での長さ
を、その傾斜供給筒内での溶融処理物の流れ方向
において、前記流下筒の前記二次燃焼室に対する
開口部の前記流れ方向での上手側の開口縁部分
と、前記流下筒の前記傾斜供給筒に対する開口部
の前記流れ方向での下手側の開口縁部分とを結ぶ
仮想線分の延長線の近くで、かつ、それよりも前
記流れ方向の下手側に前記冷却装置の溶融物受入
口を位置させるに足る長さに設定したことであ
る。
The technical means of the present invention taken to solve the above problems is to provide a secondary combustion chamber below the downward opening of the melting furnace, and to discharge the melted product and high-temperature exhaust gas into the secondary combustion chamber. A flow tube is arranged in series, and the molten material from the opening is supplied to a direct water-cooled cooling device disposed below via the flow tube,
An incinerator and melting furnace configured to discharge high-temperature exhaust gas from the opening through a flue connected to the secondary combustion chamber, the melted product of the cooling device being delivered to the lower end of the downflow tube from a lower position of the downflow tube. A slanted supply tube having a molten material receiving surface that descends toward the cooling device side is arranged in series across the receiving port of the molten material, so that the entire flow path of the molten material is formed into a curved path,
At least the molten material receiving surface of the inclined supply tube is configured to be an indirect cooling type, and the pusher is slidable along the molten material receiving surface, and the extrusion surface is configured to be an indirect cooling type. Further, the length of the slanted supply tube for transferring the molten material is determined by the length of the opening of the downstream tube to the secondary combustion chamber in the flow direction of the molten material in the slanted supply tube. Near an extension line of an imaginary line segment connecting an upper opening edge portion in the flow direction and a lower opening edge portion in the flow direction of the opening for the inclined supply tube of the downstream tube, and The length is set to be sufficient to position the melt receiving port of the cooling device on the downstream side in the flow direction.

上記技術手段を講じたことよつて得られる作用
効果は次の通りである。
The effects obtained by taking the above technical measures are as follows.

すなわち溶融処理物の流下経路を屈曲経路に
構成し、かつ、直接水冷式の冷却装置の溶融処
理物受入口を、二次燃焼室からの輻射熱の作用
範囲から遠ざけるように前記仮想線分よりも溶
融処理物流れ方向の下手側に位置させたことに
より、二次燃焼室と冷却装置とを充分に近づけ
て装置全体の小型化を図ることができながら
も、二次燃焼室からの輻射熱によつて冷却装置
側の水面から多量の水蒸気が発生することを、
屈曲状に形成された流下経路自体で効果的に抑
制し得る利点がある。
In other words, the flow path of the molten material is configured to be a curved path, and the molten material receiving port of the direct water cooling type cooling device is set further away from the range of action of radiant heat from the secondary combustion chamber than the virtual line segment. By locating it on the downstream side in the flow direction of the molten material, it is possible to bring the secondary combustion chamber and the cooling device close enough together to downsize the entire device. Therefore, a large amount of water vapor is generated from the water surface on the cooling equipment side.
There is an advantage that the flow can be effectively suppressed by the curved flow path itself.

また、溶融処理物の流下経路を構成する傾斜
供給筒の溶融処理物受止め面を間接冷却型式に
構成し、かつ、その溶融処理物受止め面に沿つ
て摺動自在な押出し具を設けてあるので、徐冷
効果をもつ間接冷却型式の受止め面によつて溶
融処理物を徐冷することができるのみならず、
前記受止め面の傾斜を緩やかにしてその徐冷効
果を一層助長しようとする場合に、前記溶融処
理物の流動性が低下して受止め面に堆積するこ
とを、前記押出具の押出し作用によつて解消す
ることができるので、前記受止め面の傾斜を一
層緩やかにしてその徐冷効果を充分に活用し、
溶融処理物の細分化を効果的に避けられるもの
であると共に、充分徐冷された後に冷却装置に
投入される溶融処理物が多量の水蒸気を発生す
ることを抑制し得る点で有利であり、さらにま
た、このように受止め面の傾斜を緩やかにする
ことは溶融処理物の流下経路の上下長さをより
一層短かくして装置全体の小型化を図る上でも
有効である。
In addition, the molten material receiving surface of the inclined supply tube that constitutes the flow path of the molten material is configured to be an indirect cooling type, and an extrusion tool that is slidable along the molten material receiving surface is provided. Therefore, not only can the molten material be slowly cooled by the indirect cooling type receiving surface that has a slow cooling effect,
When attempting to further promote the slow cooling effect by making the slope of the receiving surface gentle, the extrusion action of the extrusion tool prevents the fluidity of the melted material from decreasing and depositing on the receiving surface. Therefore, by making the slope of the receiving surface more gentle and making full use of its slow cooling effect,
It is advantageous in that it can effectively avoid fragmentation of the melted material, and it can also suppress the generation of a large amount of water vapor in the melted material that is fed into the cooling device after being sufficiently slowly cooled. Furthermore, making the slope of the receiving surface gentle in this manner is effective in further shortening the vertical length of the flow path of the melted material, thereby reducing the size of the entire apparatus.

以下に、本考案の実施例を図面の記載に基いて
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

都市塵芥や各種産業廃棄物等の被処理物を焼却
溶融並びに冷却処理して、スラグを回収するため
の焼却溶融炉は、被処理物の貯留供給部1と燃焼
溶融室2からなる溶融炉Aと、この溶融炉Aの下
向き開口3を通して溶融処理物と高温排ガスとを
流入して、その排ガス中の臭気成分を焼却脱臭し
て煙道4から排出する二次燃焼室B及び流下溶融
処理物を冷却処理して回収する直接水冷式の冷却
装置Cから構成されている。
The incineration and melting furnace for recovering slag by incinerating, melting and cooling materials to be treated such as urban garbage and various industrial wastes is a melting furnace A consisting of a storage and supply section 1 for materials to be treated and a combustion melting chamber 2. and a secondary combustion chamber B, into which the melted material and high-temperature exhaust gas flow through the downward opening 3 of the melting furnace A, incinerate and deodorize the odor components in the exhaust gas, and discharge the melted material from the flue 4; It consists of a direct water-cooled cooling device C that cools and recovers the water.

前記焼却溶融炉Aは、ホツパー5とダンパー6
とを通して供給される被処理物を、下降供給路を
備える貯留供給部雑から溶融室2の回転炉床7に
横移送供給し、これを下向き燃焼するバーナー8
によつて焼却溶融するもので、溶融処理物は開口
3を通して冷却装置Cに流下供給され、かつ高温
排ガスは、二次燃焼室Bのバーナー9によつて焼
却脱臭されて、その二次燃焼室Bのに連設された
煙道4を通して排出される。
The incinerator melting furnace A includes a hopper 5 and a damper 6.
A burner 8 that horizontally transfers and supplies the material to be processed, which is supplied through the storage and supply section having a downward supply path, to the rotary hearth 7 of the melting chamber 2 and burns it downward.
The molten material is incinerated and melted through the opening 3 and supplied to the cooling device C through the opening 3, and the high-temperature exhaust gas is incinerated and deodorized by the burner 9 in the secondary combustion chamber B. It is discharged through a flue 4 connected to B.

前記溶融処理物の流下経路は、前記二次燃焼室
Bの下端開口に連設される流下筒3Aと、その流
下筒3Aの下端から前記冷却装置Cの溶融処理物
受入口19aにわたつて延設される傾斜供給筒1
0とによつて、その全体を屈曲経路に構成してあ
る。
The flow path for the melted material extends from the lower end of the flow tube 3A connected to the lower end opening of the secondary combustion chamber B to the melted material receiving port 19a of the cooling device C. Inclined supply tube 1 installed
0, the entire path is configured into a curved path.

前記傾斜供給筒10は、その全体が二重壁構造
で、冷却水の供給管11と排出管12とが接続さ
れれ溶融処理物を間接的に冷却するように構成さ
れていて、かつ、少なくとも処理物流下経路範囲
において、その処理物受止め面13に付着した処
理物を傾斜下端側に押出すために押出具14が設
けられている。
The inclined supply cylinder 10 has a double-walled structure as a whole, and is configured to connect a cooling water supply pipe 11 and a discharge pipe 12 so as to indirectly cool the melted product, and has at least A pushing tool 14 is provided in the downstream route range for the treated material to push out the treated material adhering to the treated material receiving surface 13 toward the lower end of the slope.

この押出具14は、前記処理物受止め面13に
沿つて摺動する押出14aと、押出し状態におい
て流下処理物を受止める受受止面14bとを備
え、かつ全体が隔壁を備える二重壁構造で、冷却
水の供給並びに排水の可撓管15,15が連結さ
れ、即ち、間接冷却の構造となつており、人為操
作、あるいは、タイマーなどによつて間歇的に駆
動されるシリンダ16によつて自動的に摺動操作
されるように構成されている。
This extrusion tool 14 includes an extruder 14a that slides along the processed material receiving surface 13, and a receiving surface 14b that receives the flowing material in the extruded state, and has a double wall entirely provided with a partition wall. In this structure, flexible pipes 15, 15 for supplying and discharging cooling water are connected, that is, it has an indirect cooling structure, and a cylinder 16 is operated intermittently by manual operation or a timer. Therefore, the sliding operation is automatically performed.

さらに、前記傾斜供給筒10は、二次燃焼室B
からの輻射熱によつて前記冷却装置Cの水槽19
内に溜められている冷却水の水面が直接的に加熱
されないように、前記流下筒3Aの二次燃焼室B
に対する開口と、その流下筒3Aの傾斜供給筒1
0に対する開口との間において、傾斜供給筒10
内における流れ方向での上手側の開口縁(二次燃
焼室B側の開口)と下手側の開口縁部分傾斜供給
筒10側の開口とを結ぶ仮想線分Xによつて表示
される輻射熱の作用限界の近くで、かつ、それよ
りも前記流れ方向の下手側に前記冷却装置Cの溶
融処理物受入口19aが位置するようにその流れ
方向での長さを設定してある。
Furthermore, the inclined supply pipe 10 is arranged in a secondary combustion chamber B.
The water tank 19 of the cooling device C is
The secondary combustion chamber B of the downstream tube 3A is designed so that the surface of the cooling water stored therein is not directly heated.
and the inclined supply tube 1 of the downstream tube 3A.
0, the inclined supply cylinder 10
The radiant heat represented by the imaginary line segment The length in the flow direction is set so that the molten material receiving port 19a of the cooling device C is located near the action limit and on the downstream side in the flow direction.

前記冷却装置Cは、前記傾斜供給筒10側から
供給される溶融処理物を直接水冷する水槽19
と、冷却固化したスラグを水封状態で回収するバ
ケツトコンベア18とから構成されてる。
The cooling device C includes a water tank 19 that directly cools the melted material supplied from the inclined supply tube 10 side.
and a bucket conveyor 18 that collects the cooled and solidified slag in a water-sealed state.

尚、図中17はスクレーバーで、押出具14の
戻り行程において、その受止面14b、あるいは
更に、両側面に付着した処理物を掻き落すもので
ある。
In the figure, reference numeral 17 denotes a scraper, which scrapes off material to be treated that has adhered to the receiving surface 14b or both side surfaces of the extruder 14 during its return stroke.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本考案に係る焼却溶融炉の実施例を示
し、第1図は全体縦断側面図、第2図は要部の詳
細図である。 A……溶融炉、B……二次燃焼室、C……り冷
却装置、X……仮想線分、3……下向き開口、3
A……流下筒、4……煙道、10……傾斜供給
筒、13……溶融処理物受止め面、14……押出
具、14a……押出面、19a……溶融処理物受
入口。
The drawings show an embodiment of the incinerator and melting furnace according to the present invention, with FIG. 1 being an overall longitudinal side view and FIG. 2 being a detailed view of the main parts. A...Melting furnace, B...Secondary combustion chamber, C...Recooling device, X...Virtual line segment, 3...Downward opening, 3
A... Flow tube, 4... Flue, 10... Inclined supply tube, 13... Melt processed material receiving surface, 14... Extrusion tool, 14a... Extrusion surface, 19a... Melted processed material receiving port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 溶融炉Aの下向き開口3の下側に二次燃焼室B
を連設し、その二次燃焼室Bに溶融処理物及び高
温排ガスを排出するための流下筒3Aを連設し、
前記開口3からの溶融処理物を前記流下筒3Aを
介して下方に配設の直接水冷式の冷却装置Cに供
給すべく構成し、前記開口3からの高温排ガス
を、前記二次燃焼室Bにに連なる煙道4を通じて
排出すべく構成した焼却溶融炉であつて、前記流
下筒3Aの下端にその流下筒3A下方位置から前
記冷却装置Cの溶融融処理物の受入口19aにわ
たつて、前記冷却装置C側に向うほど下降する溶
融処理物受止め面13を備えた傾斜供給筒10を
連設して溶融処理物の流下経路の全体を屈曲経路
に構成し、前記傾斜供給筒10の少なくとも溶融
処理物受止め面13を間接冷却型式に構成すると
共に、前記溶融処理物受止め面13に沿つて摺動
自在に、かつ、その押出面14aを間接冷却型式
に構成した押出具14を設け、さらに、前記傾斜
供給筒10の溶融処理物移送方向での長さを、そ
の傾斜供給筒10内での溶融処理物の流れ方向に
おいて、前記流下筒3Aの前記二次燃焼室Bに対
する開口部の前記流れ方向での上手側の開口縁部
分と、前記流下筒3Aの前記傾斜供給筒10に対
する開口部の前記流れ方向での下手側の開口縁部
分とを結ぶ仮想線分Xの延長線の近くで、かつ、
それよりも前記流れ方向の下手側に前記冷却装置
Cの溶融物受入口19aを位置させるに足る長さ
に設定してある焼却溶融炉。
Secondary combustion chamber B is located below the downward opening 3 of the melting furnace A.
are connected in series, and a downstream cylinder 3A for discharging the melted product and high-temperature exhaust gas is installed in the secondary combustion chamber B,
The structure is such that the molten material from the opening 3 is supplied to a direct water-cooled cooling device C disposed below via the flow tube 3A, and the high-temperature exhaust gas from the opening 3 is supplied to the secondary combustion chamber B. It is an incinerator and melting furnace configured to discharge through a flue 4 that is connected to a pipe, and at the lower end of the downflow tube 3A, from a position below the downflow tube 3A to the reception port 19a of the molten processed material of the cooling device C, Inclined supply cylinders 10 each having a molten material receiving surface 13 that descends toward the cooling device C side are arranged in series to configure the entire flow path of the molten material into a curved path. An extrusion tool 14 is configured such that at least the molten product receiving surface 13 is of an indirect cooling type, and is slidable along the molten product receiving surface 13, and the extrusion surface 14a thereof is configured of an indirect cooling type. Further, the length of the inclined supply tube 10 in the direction of transporting the melted material is set such that the opening of the downstream tube 3A to the secondary combustion chamber B in the flow direction of the melted material within the inclined supply tube 10. An extension line of an imaginary line segment near, and
The incinerator and melting furnace is set to have a length sufficient to position the melt receiving port 19a of the cooling device C on the downstream side in the flow direction.
JP1978056686U 1978-04-27 1978-04-27 Expired JPS6119313Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1978056686U JPS6119313Y2 (en) 1978-04-27 1978-04-27

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1978056686U JPS6119313Y2 (en) 1978-04-27 1978-04-27

Publications (2)

Publication Number Publication Date
JPS54158487U JPS54158487U (en) 1979-11-05
JPS6119313Y2 true JPS6119313Y2 (en) 1986-06-11

Family

ID=28953826

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1978056686U Expired JPS6119313Y2 (en) 1978-04-27 1978-04-27

Country Status (1)

Country Link
JP (1) JPS6119313Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0523940Y2 (en) * 1987-10-06 1993-06-18

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5818593B2 (en) * 1975-05-26 1983-04-13 日立プラント建設株式会社 Smelt Kokeikashiyoriyo Kaitenbanno Reikiyakuhouhou
JPS52165583U (en) * 1976-06-09 1977-12-15

Also Published As

Publication number Publication date
JPS54158487U (en) 1979-11-05

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