JPS62108918A - Burning and melting device - Google Patents

Burning and melting device

Info

Publication number
JPS62108918A
JPS62108918A JP60248956A JP24895685A JPS62108918A JP S62108918 A JPS62108918 A JP S62108918A JP 60248956 A JP60248956 A JP 60248956A JP 24895685 A JP24895685 A JP 24895685A JP S62108918 A JPS62108918 A JP S62108918A
Authority
JP
Japan
Prior art keywords
furnace body
furnace
molten substance
incineration
supply port
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.)
Granted
Application number
JP60248956A
Other languages
Japanese (ja)
Other versions
JPH0258524B2 (en
Inventor
Haruo Nishino
西野 晴生
Yoshiharu Tanaka
嘉治 田中
Masaharu Matsui
松井 雅治
Madoka Kawakami
川上 円
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.)
Chiyoda Chemical Engineering and Construction Co Ltd
Original Assignee
Chiyoda Chemical Engineering and Construction Co Ltd
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 Chiyoda Chemical Engineering and Construction Co Ltd filed Critical Chiyoda Chemical Engineering and Construction Co Ltd
Priority to JP60248956A priority Critical patent/JPS62108918A/en
Priority to CN85109352.3A priority patent/CN1004224B/en
Priority to US06/812,654 priority patent/US4728081A/en
Priority to FR8519021A priority patent/FR2575271B1/en
Publication of JPS62108918A publication Critical patent/JPS62108918A/en
Publication of JPH0258524B2 publication Critical patent/JPH0258524B2/ja
Granted legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PURPOSE:To make it possible to easily and precisely carry out supply of a molten substance and stop thereof, to arbitrarily set the staying time within the furnace and complete to maintain the processing step in an airtight manner by providing a furnace body provided with a molten substance supply port at a position eccentric from a center axis in a swingable manner with respect to a hood fixed at the side of the molten substance supply port. CONSTITUTION:On the side wall of a furnace body 1 a molten substance supply port 16 to the central axis O-O of the burnace body 1. On another end, a charging port 13 for a material to be processed is provided. Then, the furnace body 1 is placed on a pair of rollers 7 provided with a machine base 30 by setting its longitudinal direction horizontally or inclining slightly. A gear 6 provided around the outer periphery of the furnace body 1 is engaged with a pinion 21 rotating by a motor 8 rotatable in both normal and reverse directions, provided on the machine base 30 separately, and the furnace body 1 is installed in a swingable manner. In this case, the movable range is set to that it is sufficient if the molten substance is picked up from the molten substance supply port provided at least in the furnace body, and its range is selected according to necessity.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、有機物、無機物、金属等を焼却溶融する焼却
溶融装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an incineration and melting apparatus for incinerating and melting organic substances, inorganic substances, metals, and the like.

〔従来技術〕[Prior art]

従来、有機物、無機物、金属等を焼却溶融する焼却溶融
装置としては、例えば金属溶解炉、下水汚泥溶融炉、都
市ごみや産業廃棄物の焼却溶融処理装置および原子力発
電所等から発生する放射性廃棄物の焼却溶融固化処理装
置等がある。
Conventionally, incineration and melting equipment for incinerating and melting organic matter, inorganic matter, metals, etc., has been used for example, metal melting furnaces, sewage sludge melting furnaces, incineration and melting treatment equipment for municipal waste and industrial waste, and radioactive waste generated from nuclear power plants, etc. There are incineration, melting and solidification processing equipment, etc.

この種の焼却溶融装置が具備すべき点としては、特に以
下の3点が挙げられる。
This type of incineration melting device should have the following three points in particular.

+t)  /’fjj融物の出湯および出湯の停止が容
易に行なえ、被処理物の炉内滞留時間を任意に設定する
ことができることが必要である。
+t) /'fjj It is necessary to be able to easily tap and stop tapping the melt, and to be able to arbitrarily set the residence time of the material to be treated in the furnace.

卯ち、高温の熔融物の出湯および出湯の停止が安全、か
つ容易に行なえることが不可欠であり、また炉内の熔融
物の量等に制約されずに、任意に出湯および出湯の停止
を行なうことにより、被処理物に応じた加熱時間、即ち
、被処理物の炉内滞留時間を設定できることが重要であ
る。
It is essential that hot melt can be tapped and stopped safely and easily, and it is also possible to tap or stop tapping at will without being restricted by the amount of melt in the furnace. It is important that by doing this, it is possible to set the heating time depending on the object to be processed, that is, the residence time of the object in the furnace.

(2)  熔融物を炉内から確実に取出すことが必要で
ある。
(2) It is necessary to reliably remove the molten material from the furnace.

特に、熔融物の部分的な風化あるいは未熔融の被処理物
により出湯口が閉塞されるような事態を起してはならな
い。
In particular, the tap hole must not be blocked by partial weathering of the molten material or by unmelted materials.

(3)  被処理物の焼却溶融、出湯、冷却の一連の処
理工程は気密を保った処理装置内で完結することが望ま
しい。
(3) It is desirable that the series of processing steps of incineration melting, tapping, and cooling of the material to be processed be completed in an airtight processing device.

邪ち、被処理物が溶融状態になった時に発生するヒユー
ム、ダスト等の飛散を防止するため、また、被処理物中
に含まれる有害物質が雰囲気中に移行する可能性のある
場合には、その有害物質の飛散を防止するために、処理
装置を気密化することが必要である。
In order to prevent the scattering of fumes, dust, etc. that are generated when the processed material becomes molten, and when there is a possibility that harmful substances contained in the processed material may migrate into the atmosphere. In order to prevent the harmful substances from scattering, it is necessary to make the processing equipment airtight.

そこで従来から知られているこの種装置としては、以下
のような各方式のものがあったが、それぞれ下記するご
とき欠点があった。
Conventionally, there have been various types of devices of this type known as follows, but each of them has the following drawbacks.

(イ) 加熱室の底部に出湯口を設け、その出湯口をス
ライドゲート等によって開閉し、溶融物の出湯および出
湯の停止を行なう方式。
(a) A method in which a tap is provided at the bottom of the heating chamber, and the tap is opened and closed using a slide gate, etc. to tap and stop the tap of the molten material.

この方式では、出湯部の閉塞を起し易く、またスライド
ゲート等の損耗が激しいため、頻繁な保守が必要となる
という欠点があった。
This method has the disadvantage that the hot water outlet is easily clogged, and the slide gate etc. are subject to severe wear and tear, requiring frequent maintenance.

(ロ) 加熱室の側壁または底部に出湯口を設け、出湯
口近傍を強制冷却して溶融物を部分的に固化させること
によって出湯口を閉ざし、出湯する場合には出湯口近傍
を部分的に加熱し、出湯口近傍の固化物を再溶融する方
式。
(b) A tap hole is provided on the side wall or bottom of the heating chamber, and the area near the tap hole is forcedly cooled to partially solidify the molten material, thereby closing the tap hole. A method of heating and remelting the solidified material near the tap.

この方式は、出湯および出湯の停止に要する設備が多大
であり、操作も複雑になるという欠点がある。
This method has the disadvantage that a large amount of equipment is required for tapping and stopping the hot water, and the operation is also complicated.

(ハ) 加熱室の側壁に設けた溢流口から溶融物を溢流
させて取出す方式。
(c) A method in which the molten material is taken out by overflowing from the overflow port provided on the side wall of the heating chamber.

この方式は溢流口の閉塞を起し易く、また被処理物の炉
内滞留時間を制御するためには、被処理物の投入速度、
熔融物の性状等を慎重に制御する必要があるという欠点
がある。
This method tends to cause blockage of the overflow port, and in order to control the residence time of the material to be treated in the furnace, it is necessary to
The disadvantage is that the properties of the melt must be carefully controlled.

(ニ) 容器または鋳型内に投入した被処理物を加熱、
溶融し、そのまま冷却する方式。
(d) Heating the workpiece placed in the container or mold;
A method in which it is melted and then cooled.

この方式は容器または鋳型が加熱源あるいは溶融物から
高い熱を直接受けるので、容器の耐熱、断熱が容易でな
く、また、連続的あるいは半連続的な処理には不向きで
あるという欠点がある。
This method has the disadvantage that the container or mold directly receives high heat from the heating source or the molten material, so it is difficult to provide heat resistance and insulation for the container, and it is not suitable for continuous or semi-continuous processing.

(ホ) 被処理物の層の表層を加熱、溶融し、溶融物を
自重で落下させて加熱室の下部より取出す方式。
(e) A method in which the surface layer of the object to be treated is heated and melted, and the molten material is allowed to fall under its own weight and taken out from the bottom of the heating chamber.

この方式は溶融物の湯だまりを作らない方式のため、被
処理物の炉内滞留時間が短かく、被処理物の溶融が不充
分になり易い欠点がある。
Since this method does not create a pool of molten material, the residence time of the material to be processed in the furnace is short, and the drawback is that the material to be processed tends to be insufficiently melted.

(へ) 被処理物を開放型加熱室にて加熱、溶融した後
、加熱室を傾斜させ内部の溶融物を取出す方式。
(F) A method in which the material to be processed is heated and melted in an open heating chamber, and then the heating chamber is tilted to take out the molten material inside.

この方式は被処理物の炉内滞留時間を任意に設定でき、
かつ溶融物を確実に取出すことができるが、出湯時の気
密化が困難であり、また、連続的あるいは半連続的な処
理には不向きであるという欠点がある。
This method allows you to arbitrarily set the residence time of the material to be processed in the furnace.
Although the molten material can be taken out reliably, it has the disadvantage that it is difficult to make it airtight during tapping, and it is not suitable for continuous or semi-continuous processing.

〔発明の目的〕[Purpose of the invention]

本発明は前記従来方式の欠点を解消し、焼却溶融装置の
溶融物の出湯および出湯の停止ヒが容易に、かつ確実に
行なえ、更に被処理物の炉内滞留時間を任意に設定でき
、かつ一連の処理工程を気密を保ったままで完結できる
焼却溶融装置を提供することを目的としたものである。
The present invention eliminates the drawbacks of the conventional method, and enables easy and reliable tapping and stopping of the melted material in the incineration melting device, as well as the ability to arbitrarily set the residence time of the material to be treated in the furnace. The object of the present invention is to provide an incineration and melting device that can complete a series of processing steps while maintaining airtightness.

〔発明の構成〕[Structure of the invention]

本発明の焼却溶融装置は、中心軸から偏心した位置に出
湯口を設けた炉体を、その出湯口側に固設したフードに
対して揺動自在に設けることにより構成される。
The incineration and melting apparatus of the present invention is constructed by providing a furnace body with a tap hole located at a position eccentric from the central axis so as to be swingable relative to a hood fixed to the tap hole side.

〔実施例〕〔Example〕

以下図面を参照して本発明の詳細な説明するが、第1図
は本発明の実施例1における焼却溶融装置の外観図、第
2図は第1図の炉体およびフードの拡大側断面図、第3
図は第2図の1−1方向の炉体の正断面図である。
The present invention will be described in detail below with reference to the drawings. Fig. 1 is an external view of an incineration and melting apparatus in Embodiment 1 of the present invention, and Fig. 2 is an enlarged side sectional view of the furnace body and hood shown in Fig. 1. , 3rd
The figure is a front sectional view of the furnace body in the direction 1-1 of FIG. 2.

まず、この焼却熔融装置は第1図および第2図に示すご
とく、炉体1およびフード2の主要部分からなり、また
第2図に示すように、中空の炉体lは円筒状金属製の炉
殻10の内壁を耐火・断熱材11で覆ったものであり、
更に、炉体1は必要に応じて強制冷却できるようになっ
ている。
First, as shown in Figures 1 and 2, this incineration and melting equipment consists of the main parts of a furnace body 1 and a hood 2.As shown in Figure 2, the hollow furnace body l is made of cylindrical metal. The inner wall of the furnace shell 10 is covered with a fireproof/insulating material 11,
Furthermore, the furnace body 1 can be forcedly cooled if necessary.

ここで、この強制冷却の方式には、目的に応じて空冷式
または水冷式が用いられるが、被処理物中に塩化ビニー
ルなど焼却時に塩化水素を発生する物質が含まれ、この
塩化水素の凝縮により炉殻10が腐食の想れのある場合
には、塩化水素が凝縮せぬよう炉殻温度を100から2
00°C以上に保ち、かつ炉殻10の機械的強度が低下
せぬように炉殻温度を300から400℃以下に保てる
ように空冷式により炉殻温度を制御することが望ましい
Air-cooling or water-cooling is used for this forced cooling method depending on the purpose, but the material to be treated contains substances that generate hydrogen chloride when incinerated, such as vinyl chloride, and this hydrogen chloride condenses. If the furnace shell 10 is likely to be corroded, the furnace shell temperature should be increased from 100 to 2
It is desirable to control the furnace shell temperature by air cooling so as to maintain the furnace shell temperature at 00°C or higher and at 300 to 400°C or lower so as not to reduce the mechanical strength of the furnace shell 10.

炉体Iの側壁には、炉体lの中心軸0−0から偏心した
位置に出湯口16が設けられており他端には、被処理物
投入口13が設けられている。
A tap hole 16 is provided on the side wall of the furnace body I at a position eccentric from the central axis 0-0 of the furnace body I, and a workpiece inlet 13 is provided at the other end.

ここで、炉体1内での発生ガスをフード2側へ導入する
煙道として、第3図に示すように出湯口16にて煙道を
兼用しても良いが、第5図の実施例2に示すように出湯
口16′とは別に中心軸O−Oと同心に煙道25を設け
ても良い。
Here, as a flue for introducing the gas generated in the furnace body 1 to the hood 2 side, the outlet 16 may also be used as a flue as shown in FIG. 3, but the embodiment shown in FIG. As shown in FIG. 2, a flue 25 may be provided concentrically with the central axis O-O in addition to the tap 16'.

次に、第1図に示すように、炉体1は長さ方向を水平ま
たは若干傾けて、機台30に設けた一対のローラ7上に
例えば回動自在に載面し、その炉体1の外周に設けたギ
ヤー6を、別に機台30上に設けた正逆両方向に回転可
能のモータ8で回転するビニオン21に噛合させており
炉体1が揺動自在に設けられている。この場合可動範囲
は、少なくとも炉体に設けた出湯口から溶融物が取出せ
るようにすればよく、その範囲は必要に応じ選択すれば
よい。
Next, as shown in FIG. 1, the furnace body 1 is rotatably placed, for example, on a pair of rollers 7 provided on a machine stand 30 with the length direction horizontal or slightly inclined. A gear 6 provided on the outer periphery of the furnace body 1 is meshed with a pinion 21 which is rotated by a motor 8 separately provided on a machine base 30 and rotatable in both forward and reverse directions, so that the furnace body 1 is swingably provided. In this case, the movable range may be such that the molten material can be taken out at least from a tap provided in the furnace body, and the range may be selected as necessary.

また、第3図に示すように、炉体l内の被処理物を加熱
するバーナ20および被処理物の焼、  却のための2
次空気送入口23が設けられている。なお、バーナ20
および2次空気送入口23は、第3図の如く円筒形炉体
1の円周方向側面に設けてもよく、また軸方向に設けて
もよい。
In addition, as shown in FIG. 3, there is also a burner 20 for heating the object to be processed in the furnace body l, and a burner 20 for incinerating the object to be processed.
A secondary air inlet 23 is provided. In addition, burner 20
The secondary air inlet 23 may be provided on the side surface in the circumferential direction of the cylindrical furnace body 1 as shown in FIG. 3, or may be provided in the axial direction.

更に、第2図に示すように、固定式のフード2は金属製
殻14の内壁を耐火・断熱材15で覆ったもので、この
フード2は、炉体1と炉体、  1の回動を制限せぬよ
うに連結された状態で固定されており、かつ連結部は炉
体1内での発生ガスが炉外に漏洩せぬようにシールされ
る。
Furthermore, as shown in FIG. 2, the fixed type hood 2 has the inner wall of a metal shell 14 covered with a fireproof/insulating material 15. The connecting portions are fixed in a connected state so as not to restrict the flow, and the connecting portions are sealed to prevent gas generated within the furnace body 1 from leaking outside the furnace.

また、このフード2にはバーナ19が炉体lの出湯口1
6に対向するように設けられており、また、2次空気送
入口24が設けられている。
Also, in this hood 2, a burner 19 is installed at the outlet 1 of the furnace body l.
6, and a secondary air inlet 24 is also provided.

一方、このフード2の上部には煙道22が設けられてお
り、炉体1内で発生したガスは出湯口■6を通り、煙道
22を通して装置外に出される。
On the other hand, a flue 22 is provided in the upper part of the hood 2, and the gas generated within the furnace body 1 passes through the outlet (6) and is discharged to the outside of the apparatus through the flue 22.

ここで、煙道を通ったガスは、他の排ガス処理設備に送
られるが、被処理物を焼却処理する場合に発生する可燃
性ガスや可燃性ダスト等を燃焼させるためには、このフ
ード2に二次燃焼室の作用を持たせ、発生ガスをバーナ
19による助燃によって二次燃焼させた後に装置外に出
されるようにすることが望ましい。
Here, the gas passing through the flue is sent to other exhaust gas treatment equipment, but in order to burn the flammable gas and combustible dust that are generated when the material to be treated is incinerated, this hood 2 It is desirable that the combustion chamber be provided with the function of a secondary combustion chamber so that the generated gas is subjected to secondary combustion through auxiliary combustion by the burner 19 and then discharged to the outside of the apparatus.

フード2の底部には、熔融物の通る通湯口17が設けら
れ、かつこの通湯口17は耐火・断熱材製のスライド式
ダンパー18によって開閉される。
The bottom of the hood 2 is provided with a spout 17 through which the melt passes, and this spout 17 is opened and closed by a sliding damper 18 made of a fireproof and heat insulating material.

また、第1図に示されるように、上記通湯口17に面し
て熔融物を受は入れられる受器3が設置できるようにな
っており、この受器3は油圧ジャンキ等公知の手段によ
ってフード2の方向に押上げられ、通湯口17に面して
フード2に密着されるようになっている。
Further, as shown in FIG. 1, a receiver 3 for receiving the melt can be installed facing the pouring port 17, and this receiver 3 can be installed by a known means such as a hydraulic jack. It is pushed up in the direction of the hood 2 and is brought into close contact with the hood 2 while facing the hot water inlet 17.

ここで、溶融物を受器3内で冷却固化する場合は、上記
実施例1のごと(、受器3を用いれば良く、鋳型内で冷
却固化する場合には鋳型が、そして粒状固化を行なう場
合には水槽が、それぞれ通湯口17に面して設置される
Here, when the molten material is cooled and solidified in the receiver 3, the receiver 3 may be used as in Example 1 above, and when the melt is cooled and solidified in the mold, the mold is In this case, water tanks are installed facing the respective hot water inlets 17.

また、第1図に示すように、炉体lの被処理物投入口1
3側は、炉体lの回動を制限せぬように被処理物供給器
4と連結しているが、この被処理物供給器4としては、
スクリューフィーダ式、ブツシャ式等の公知の方式のも
のが用いられる。
In addition, as shown in FIG.
The third side is connected to the material supply device 4 to be treated so as not to restrict the rotation of the furnace body l.
A known method such as a screw feeder type or a bushing type is used.

以上の構成からなる実施例1の焼却溶融装置における焼
却溶融処理作業について、その各作業状態を示す第4−
A図から第4−D図を参照して説明すると、まず、炉体
1内の内容物が流出しないように出湯口16が、第4−
A図の焼却溶融の状態を示す位置に(るように、可逆式
のモータ8によって炉体lを回動させ、また、フード2
の底部に前記の方法で受器3を圧着させる。
Regarding the incineration and melting processing work in the incineration and melting apparatus of Example 1 having the above-described configuration, Section 4-4 shows each work state.
To explain with reference to FIGS. A to 4-D, first, the tap hole 16 is closed to the
The furnace body l is rotated by the reversible motor 8, and the hood 2
The receiver 3 is crimped onto the bottom of the container 3 using the method described above.

次にバーナ20に点火し、被処理物を被処理物供給器4
によって被処理物投入口13から連続あるいは間欠的に
炉体1内に投入し、焼却溶融するが、この時第4−A図
の矢印Xに示すように可逆式のモータ8を間欠的に正逆
方向に回動させ、炉体1を揺動させて炉体1内の被処理
物を攪拌する。
Next, the burner 20 is ignited, and the workpiece is transferred to the workpiece supply device 4.
The material to be treated is continuously or intermittently introduced into the furnace body 1 through the inlet 13 and incinerated and melted. The furnace body 1 is rotated in the opposite direction, and the object to be processed in the furnace body 1 is stirred.

これにより、被処理物は均一に加熱されるばかりでなく
、被処理物の焼却に必要な酸素が万遍なくいきわたるた
め、完全に焼却させることができる。
Thereby, the object to be processed is not only heated uniformly, but also the oxygen necessary for incineration of the object to be processed is evenly distributed, so that the object can be completely incinerated.

また、溶融物Mが攪拌されるため均一になり、熔融物M
を冷却固化して得られる固化体も均質なものになる。
In addition, since the melt M is stirred, it becomes uniform, and the melt M
The solidified material obtained by cooling and solidifying is also homogeneous.

なお、炉体1内で発生したガスは、煙道を兼ねた出湯口
16、または第5図の実施例2の場合は別個の煙道25
を通して、フード2へ導入されるが、ガス中に可燃性ガ
スやダストが含まれる場合には、バーナ19の助燃によ
ってフード2内で二次燃焼された後、煙道22を通して
他の排ガス処理設備に送られる。
Note that the gas generated in the furnace body 1 is discharged through the outlet 16 which also serves as a flue, or in the case of the second embodiment shown in FIG. 5, a separate flue 25.
However, if the gas contains flammable gas or dust, it is secondary combusted in the hood 2 by auxiliary combustion in the burner 19, and then passed through the flue 22 to other exhaust gas treatment equipment. sent to.

次に、所定の加熱時間が経過した後、第4−B図の出湯
の状態に示すように、まずフード2底部のスライド式ダ
ンパー18を開け、通湯口17を受器3に向けて開口す
る。
Next, after a predetermined heating time has elapsed, first open the slide type damper 18 at the bottom of the hood 2 and open the hot water outlet 17 toward the receiver 3, as shown in the hot water tapping state in Figure 4-B. .

この時、受器3が通湯口17に密着しているため、フー
ド2内の雰囲気が外気にふれることはない。
At this time, since the receiver 3 is in close contact with the hot water inlet 17, the atmosphere inside the hood 2 is not exposed to the outside air.

次に、第4−B図に示すように、出湯口16が炉体1内
の溶融物Mの液面下に位置するように炉体lを回動させ
て止め、溶融物Mを出湯口16、通湯口17を通して受
器3に導入するが、この時、炉体1の回動、停止の制御
によって出湯口16が溶融物Mに触れる位置を制御する
ことにより、出湯速度を制御する。
Next, as shown in Fig. 4-B, the furnace body 1 is rotated and stopped so that the tap hole 16 is located below the liquid level of the molten material M in the furnace body 1, and the molten material M is removed from the tap hole. 16. The molten metal is introduced into the receiver 3 through the inlet 17, and at this time, the tapping speed is controlled by controlling the position where the outlet 16 touches the molten material M by controlling rotation and stopping of the furnace body 1.

また、フード2例のバーナ19によって、炉体1の出湯
口16近傍を加熱することにより、溶融物Mの粘性低下
や凝固による出湯口16の閉塞を防止する。
Further, by heating the vicinity of the tap hole 16 of the furnace body 1 by the burners 19 of the two hoods, the tap hole 16 is prevented from being clogged due to decrease in viscosity or solidification of the molten material M.

所定量の出湯を行なった後に、第4−C図の出湯の停止
状態に示すように、出湯口16が熔融物Mの液面から離
れた位置にくるよ、うに炉体1を回動させ、出湯を停止
する。
After a predetermined amount of melt has been tapped, the furnace body 1 is rotated so that the tap hole 16 is at a position away from the liquid level of the molten material M, as shown in the stopped state of tapping in Figure 4-C. , stop the hot water supply.

この後、更に焼却熔融、出湯、出湯の停止を繰り返して
いけば良く、また受器3を交換する場合には第4−D図
の受器の交換の状態に示すように、スライド式ダンパー
18を閉じ、フード2内の雰囲気を外気と遮断した後に
受器3を交換する。
After this, it is sufficient to repeat the incineration melting, tapping, and stopping of tapping.Also, when replacing the receiver 3, as shown in the state of replacing the receiver in Fig. 4-D, the sliding damper 18 After closing the hood 2 and isolating the atmosphere inside the hood 2 from outside air, the receiver 3 is replaced.

次に、第6図は実施例3の焼却溶融装置を示しており、
実施例1と同じ部品はそれぞれ同じ部品番号で示してい
るが、炉体1に連結したフード2を、煙道33を介して
焼却炉26に連結した点が実施例1と異なる構成となっ
ており、この焼却炉26では、炉体1内で発生する高温
の排ガスを利用して、可燃性被処理物の焼却が行なわれ
る。
Next, FIG. 6 shows the incineration melting apparatus of Example 3,
The same parts as in Example 1 are indicated by the same part numbers, but the configuration differs from Example 1 in that the hood 2 connected to the furnace body 1 is connected to the incinerator 26 via the flue 33. In the incinerator 26, the combustible material to be treated is incinerated using high-temperature exhaust gas generated within the furnace body 1.

一方、炉体1内では、主に難燃物、不燃物の焼却熔融が
行なわれるが、可燃物の焼却は比較的低温で行なえるが
、炉の内容積を大きくすることが必要であり、逆に難燃
物、不燃物の焼却溶融のためには炉の内容積は比較的小
さくて良いが高温に加熱する必要がある。
On the other hand, in the furnace body 1, incineration and melting of retardant and non-combustible materials are mainly performed, and although combustible materials can be incinerated at relatively low temperatures, it is necessary to increase the internal volume of the furnace. On the other hand, in order to incinerate and melt flame retardant and non-combustible materials, the internal volume of the furnace may be relatively small, but it is necessary to heat the furnace to a high temperature.

そこで、炉体1は難燃物、不燃物を高温で焼却溶融し、
ここから発生する排ガスを大きな容積を有する焼却炉2
6に導入し、ここで可燃物の焼却を行なうことにより効
率の良い焼却溶融を行なうことができる。
Therefore, the furnace body 1 incinerates and melts flame retardant and non-combustible materials at high temperature.
Incinerator 2 which has a large volume to collect the exhaust gas generated from this
6 and incinerate the combustible material there, efficient incineration and melting can be performed.

焼却炉26には、被処理物投入口27、煙道28、焼却
灰取出し口31が設けられており、また、助燃用のバー
ナ34、二次空気送入口29が設けられている。
The incinerator 26 is provided with a material inlet 27, a flue 28, and an incineration ash outlet 31, as well as a burner 34 for auxiliary combustion and a secondary air inlet 29.

なお、この焼却炉26はこの実施例3のごとく、竪型固
定床式の他、火格子式環公知の方式のものであっても良
い。
Incidentally, the incinerator 26 may be of a vertical fixed bed type as in the third embodiment, or may be of a known grate type ring type.

以上の構成からなる実施例3の焼却熔融装置を用いた焼
却熔融処理作業は以下のように行なわれる。
The incineration and melting process using the incineration and melting apparatus of Example 3 having the above configuration is performed as follows.

まず、可燃性の被処理物は被処理物投入口27から焼却
炉26内に投入され、炉体1内で発生し、煙道33を通
して焼却炉26内に導入された高温のガスにより加熱さ
れ、焼却される。
First, the combustible material to be treated is put into the incinerator 26 from the material input port 27 and heated by high-temperature gas generated in the furnace body 1 and introduced into the incinerator 26 through the flue 33. , will be incinerated.

スタートアップ時など、炉体1内での発生ガスの温度が
低い場合には、必要に応じてバーナ34による助燃が行
なわれる。
When the temperature of the generated gas in the furnace body 1 is low, such as during startup, auxiliary combustion is performed by the burner 34 as necessary.

焼却灰は焼却炉26の底部にたまり、焼却灰取出口31
からダンパー32を介して行なわれる。
The incinerated ash accumulates at the bottom of the incinerator 26 and is removed from the incinerated ash outlet 31.
This is done through the damper 32.

難燃物、不燃物、更には焼却炉26から取出された焼却
灰は炉体Iに投入され、前記実施例1で説明したと同様
の工程で焼却熔融される。
The incombustible materials, noncombustible materials, and even the incinerated ash taken out from the incinerator 26 are put into the furnace body I, and are incinerated and melted in the same process as described in the first embodiment.

〔発明の効果〕〔Effect of the invention〕

以上に説明した本発明の焼却溶融装置は下記のような顕
著な効果を有する。
The incineration melting apparatus of the present invention described above has the following remarkable effects.

(1)本発明の焼却溶融装置の炉体には、その中心軸か
ら偏心した位置に出湯口を設け、しかも、その炉体を揺
動自在にしているため、炉体を回動し、停止させること
により、容易に、かつ安全に溶融物の出湯および出湯の
停止、更には出湯速度の制御が行なわれるという効果が
ある。
(1) The furnace body of the incineration and melting device of the present invention is provided with a tap outlet at a position eccentric from its central axis, and the furnace body is swingable, so the furnace body can be rotated and stopped. This has the effect of easily and safely dispensing the melt, stopping the dispensing, and controlling the dispensing speed.

(2)炉体内の溶融物の量などに制約されず任意に出湯
および出湯の停止が行なえるため、被処理物の炉内滞留
時間を任意に設定できる。
(2) The residence time of the material to be treated in the furnace can be set arbitrarily because the melt can be tapped and stopped at will without being restricted by the amount of molten material in the furnace.

(3)上記(11のごとく、出湯口を偏心させているの
で、出湯口を上方に向けておいて揺動させると溶融物が
こぼれることがなく、また溶融物を出湯口からフード側
に出す時は、出湯口を下方に向けるだけで容易に出すこ
とができる。
(3) As mentioned in (11) above, the tap is eccentric, so if you keep the tap facing upward and swing it, the melt will not spill out, and the melt will flow out from the tap to the hood side. You can easily release the water by simply pointing the tap downward.

(4)炉体を揺動自在にしているので、炉体内の被処理
物の攪拌が良く行なわれるので、効率良く加熱でき、更
に通風を良くすることができるので、被処理物の焼却を
効率良く行なうことができる。
(4) Since the furnace body can be freely swung, the material to be processed inside the furnace is well agitated, allowing for efficient heating.Furthermore, ventilation can be improved, so the material to be processed can be incinerated efficiently. can do well.

(5)炉体の揺動により溶融物を攪拌混合できるので、
それにより熔融速度を促進でき、また、溶融物を均一に
することができると共に、溶融物の税泡が促進されるた
め、熔融物を冷却して得られる固化体を均質、かつ緻密
なものにすることができる。
(5) Since the molten material can be stirred and mixed by the rocking of the furnace body,
This can accelerate the melting rate, make the melt uniform, and promote the formation of bubbles in the melt, making the solidified material obtained by cooling the melt homogeneous and dense. can do.

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

第1図は本発明の実施例1における焼却溶融装置の外観
側面図、第2図は第1図の炉体およびフードの拡大側断
面図、第3図は第2図の炉体の1−1方向の正断面図、
第4−A図、第4−B図、第4−C図および第4−D図
は第1図の実施例1の焼却溶融装置の焼却溶融処理作業
について一連の状態を示す断面図、第5図は本発明の実
施例2の炉体の正断面図、第6図は本発明の実施例3の
焼却溶融装置の側断面図である。 1・・・炉体、2・・・フード、7・・・ローラ、8・
・・モータ、16.16’・・・出湯口、21・・・ビ
ニオン、M・・・溶融物、0−0・・・中心軸。
FIG. 1 is an external side view of the incineration and melting apparatus in Example 1 of the present invention, FIG. 2 is an enlarged side sectional view of the furnace body and hood of FIG. 1, and FIG. 3 is a 1- A front cross-sectional view in one direction,
4-A, 4-B, 4-C, and 4-D are sectional views showing a series of states regarding the incineration and melting process of the incineration and melting apparatus of Example 1 in FIG. 5 is a front sectional view of a furnace body according to a second embodiment of the present invention, and FIG. 6 is a side sectional view of an incineration and melting apparatus according to a third embodiment of the present invention. 1...furnace body, 2...hood, 7...roller, 8...
... Motor, 16.16'... Tap, 21... Binion, M... Melt, 0-0... Central axis.

Claims (1)

【特許請求の範囲】[Claims] 中心軸から偏心した位置に出湯口を設けた炉体を、その
出湯口側に固設したフードに対して揺動自在に設けた焼
却溶融装置。
An incineration and melting device in which a furnace body with a tap hole located eccentrically from the central axis is swingable relative to a hood fixed to the tap hole side.
JP60248956A 1984-12-24 1985-11-08 Burning and melting device Granted JPS62108918A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP60248956A JPS62108918A (en) 1985-11-08 1985-11-08 Burning and melting device
CN85109352.3A CN1004224B (en) 1984-12-24 1985-12-21 Incinerating and melting appartus
US06/812,654 US4728081A (en) 1984-12-24 1985-12-23 Incinerating and melting apparatus
FR8519021A FR2575271B1 (en) 1984-12-24 1985-12-23 INCINERATION AND FUSION APPARATUS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60248956A JPS62108918A (en) 1985-11-08 1985-11-08 Burning and melting device

Publications (2)

Publication Number Publication Date
JPS62108918A true JPS62108918A (en) 1987-05-20
JPH0258524B2 JPH0258524B2 (en) 1990-12-10

Family

ID=17185902

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60248956A Granted JPS62108918A (en) 1984-12-24 1985-11-08 Burning and melting device

Country Status (1)

Country Link
JP (1) JPS62108918A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS534341A (en) * 1976-07-02 1978-01-14 Tatsunogumi Kk Construction method for concrete side ditch
JPS57117719A (en) * 1981-01-16 1982-07-22 Von Roll Ag Combined combustion for hard dough-like and fluid waste matter - melting furnace

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS534341A (en) * 1976-07-02 1978-01-14 Tatsunogumi Kk Construction method for concrete side ditch
JPS57117719A (en) * 1981-01-16 1982-07-22 Von Roll Ag Combined combustion for hard dough-like and fluid waste matter - melting furnace

Also Published As

Publication number Publication date
JPH0258524B2 (en) 1990-12-10

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