JPH0118323B2 - - Google Patents
Info
- Publication number
- JPH0118323B2 JPH0118323B2 JP56166958A JP16695881A JPH0118323B2 JP H0118323 B2 JPH0118323 B2 JP H0118323B2 JP 56166958 A JP56166958 A JP 56166958A JP 16695881 A JP16695881 A JP 16695881A JP H0118323 B2 JPH0118323 B2 JP H0118323B2
- Authority
- JP
- Japan
- Prior art keywords
- clinker
- waste
- temperature
- exhaust gas
- temperature hearth
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/085—High-temperature heating means, e.g. plasma, for partly melting the waste
Landscapes
- Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明は、下水汚泥などの各種の産業廃棄物
や、あるいはそれらを必要に応じて予め乾燥焼却
や粉砕処理した中間処理物を、埋立てに使用した
時に重金属が流出しないようにしたり、あるいは
建設骨材に利用できるようにする等のために焼
却、溶融する方法に関し、詳しくは、産業廃棄物
あるいはその中間処理物を、炭素系可燃物質によ
つて形成した高温炉床に供給して、焼却溶融さ
せ、燃焼排ガスを前記高温炉床の上方に形成した
上昇流路に排出させる廃棄物溶融方法に関し、そ
の目的は、上昇流路の内面に付着したクリンカー
を、簡単な操作で、しかも、短時間で、そのう
え、十分に除去させることができるようにせんと
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is designed to prevent heavy metals from flowing out when various industrial wastes such as sewage sludge, or intermediately processed products obtained by drying, incinerating or pulverizing them as necessary, are used in landfills. Regarding the method of incinerating and melting industrial waste or its intermediate products to prevent it from burning or to make it usable as construction aggregate, etc. Regarding a waste melting method, the waste is supplied to a bed, incinerated and melted, and the combustion exhaust gas is discharged into an ascending channel formed above the high-temperature hearth, the purpose of which is to easily remove clinker attached to the inner surface of the ascending channel. The aim is to enable sufficient removal in a short time and with a simple operation.
さらに詳述すると、上記廃棄物溶融方法におい
て、上昇流路の内面にクリンカーが付着堆積する
のを抑制する手段として、燃焼排ガスを冷却させ
たり、あるいは、上昇流路の横断面積を増大させ
て燃焼排ガスの線速度を低下させる等の手段が考
えられるが、これらの場合、熱エネルギーを有効
利用できない経済面での不利があり、実用し難い
ものである。このため、従来では、付着したクリ
ンカーを人為的に破砕、除去するようにしている
が、この場合、危険な高所で作業しなければなら
ず、しかも、作業ができる温度に炉温を一旦低下
させ、クリンカー除去作業後再び炉温を上昇させ
なければならないために、クリンカー除去作業に
際して長時間に亘つて廃棄物溶融作業を停止しな
ければならず、その上、クリンカー全体を適確に
除去することが困難である等、各種の欠点があ
り、本発明はかかる欠点を一挙に解消することを
目的とする。 More specifically, in the above waste melting method, as a means to suppress clinker from adhering and accumulating on the inner surface of the ascending channel, combustion exhaust gas is cooled or the cross-sectional area of the ascending channel is increased. Although measures such as lowering the linear velocity of the exhaust gas can be considered, these methods have an economical disadvantage in that thermal energy cannot be used effectively, and are therefore difficult to put into practical use. For this reason, in the past, adhering clinker was manually crushed and removed, but in this case, the work had to be done at a dangerous height, and the furnace temperature had to be lowered to a temperature where the work could be done. Because the furnace temperature must be raised again after the clinker removal work, the waste melting work must be stopped for a long time during the clinker removal work, and in addition, the entire clinker must be removed properly. There are various drawbacks, such as the fact that it is difficult to do so, and it is an object of the present invention to eliminate these drawbacks all at once.
次に、例示図により本発明の実施態様を説明す
る。 Next, embodiments of the present invention will be described with reference to illustrative figures.
キユポラタイプの溶融炉1に、炭素系可燃物質
から成る高温炉床2を形成し、ホツパー3から高
温炉床2に、ダンパー4a,4bを交互に開閉し
て、産業廃棄物あるいはその中間処理物を、炭素
系可燃物質と混合状態であるいは交互に供給し、
炭素系可燃物質と産業廃棄物あるいはその中間処
理物の充填層5を高温炉床2上に形成し、そし
て、下方の第1羽口6から高温炉床2に空気等の
酸素含有ガスを供給して、高温炉床2の上部にお
いて産業廃棄物あるいはその中間処理物を燃焼、
溶融し、そして、燃焼排ガスを高温炉床2の上方
に形成した上昇流路7と高温炉床2の下部に接続
した下部流路8とに排出させるようにし、そし
て、溶融物を前記下部流路8を通して炉外へ取出
し、そして、高温炉床2から発生した燃焼排ガス
を、充填層5を通過する際に生成される臭気成分
及び有害成分を燃焼分解させるよう、上昇流路7
内において、第2羽口9から供給される空気等の
酸素含有ガスによつて後燃焼させるようにし、更
に、高温炉床2部分に対する側壁を2重管構造に
して水冷ジヤケツト10構成してある。 A high-temperature hearth 2 made of carbon-based combustible material is formed in a cupola-type melting furnace 1, and dampers 4a and 4b are alternately opened and closed to transfer industrial waste or its intermediate processed materials from a hopper 3 to the high-temperature hearth 2. , supplied in a mixed state or alternately with carbon-based combustible materials,
A packed bed 5 of carbon-based combustible substances and industrial waste or intermediate treatment thereof is formed on the high-temperature hearth 2, and oxygen-containing gas such as air is supplied to the high-temperature hearth 2 from the first tuyere 6 below. Then, industrial waste or its intermediate treatment is burnt in the upper part of the high-temperature hearth 2.
The combustion exhaust gas is discharged into an ascending passage 7 formed above the high-temperature hearth 2 and a lower passage 8 connected to the lower part of the high-temperature hearth 2, and the molten material is discharged into the lower flow passage 7. The combustion exhaust gas generated from the high-temperature hearth 2 is taken out of the furnace through the passage 8, and the ascending passage 7 is configured to combust and decompose odor components and harmful components generated when the combustion exhaust gas is passed through the packed bed 5.
After-combustion is carried out inside the furnace by oxygen-containing gas such as air supplied from the second tuyere 9, and the side wall for the two portions of the high-temperature hearth is constructed with a double pipe structure to form a water-cooled jacket 10. .
前記上昇流路7からの燃焼排ガスを、炉頂部に
接続した排気ダクト11、ダスト除去用サイクロ
ン12、熱交換器13、第1ブロワ14を通して
大気中に放出させるようにし、さらに、前記第
1、第2羽口6,9に対して第2ブロワ15にて
供給する酸素含有ガスを、前記熱交換器13にて
加温させるようにしてある。 The combustion exhaust gas from the ascending passage 7 is discharged into the atmosphere through an exhaust duct 11 connected to the top of the furnace, a dust removal cyclone 12, a heat exchanger 13, and a first blower 14, and further, the first The oxygen-containing gas supplied to the second tuyeres 6 and 9 by the second blower 15 is heated by the heat exchanger 13.
又、前記高温炉床2への産業廃棄物あるいはそ
の中間処理物の供給を停止又は減少させた状態に
おいて、第1、第2羽口6,9の夫々と第2ブロ
ワ15との間に設けた流量制御弁V1,V2の調節、
及び、高温炉床2への炭素系可燃物質の供給速度
の調節等によつて、高温炉床2を、それから上昇
流路7内に排出される燃焼排ガスの温度が上昇流
路7の内面に付着したクリンカーの溶流点(1000
℃乃至1210℃)プラス50℃乃至100℃となる状態
で、30分乃至1時間、燃焼させ、上昇流路7の内
面に付着したクリンカーを溶融流下させるように
してある。 Further, in a state where the supply of industrial waste or its intermediate treated product to the high-temperature hearth 2 is stopped or reduced, a Adjustment of flow control valves V 1 and V 2 ,
By adjusting the supply rate of the carbon-based combustible material to the high-temperature hearth 2, etc., the temperature of the combustion exhaust gas discharged from the high-temperature hearth 2 into the ascending channel 7 is lowered to the inner surface of the ascending channel 7. Melting point of attached clinker (1000
The clinker adhering to the inner surface of the ascending flow path 7 is melted and flowed down by burning for 30 minutes to 1 hour at a temperature of 50 to 100 degrees Celsius (1210 degrees Celsius) plus 50 degrees Celsius.
要するに、上昇流路7の内面に付着したクリン
カーを、高温炉床2を上記の如く燃焼させるだけ
の簡単な操作で除去でき、しかも、炉温を低下さ
せずにクリンカー除去を行なえるので、クリンカ
ー除去作業に際して廃棄物溶融作業を長時間に亘
つて停止させねばならない不都合なくクリンカー
除去作業を短時間で行なうことができ、そのう
え、付着クリンカー全体の表面をむらなく加温し
ながら付着クリンカー全体をむらなく十分に除去
できるのである。 In short, the clinker adhering to the inner surface of the ascending channel 7 can be removed by a simple operation of burning the high-temperature hearth 2 as described above, and the clinker can be removed without lowering the furnace temperature. The clinker removal work can be carried out in a short time without the inconvenience of having to stop the waste melting work for a long time during the removal work, and in addition, the entire adhered clinker can be heated evenly while the entire surface of the adhered clinker is evenly heated. It can be completely removed without any problems.
尚、本発明を用いて付着クリンカーを除去する
に、クリンカーの上昇流路7の内面近くに位置す
る部分を残す状態で除去すれば、上昇流路7の形
成部材が熱損されるのを回避できるものとなつて
よい。 In addition, when removing the adhered clinker using the present invention, if the part of the clinker located near the inner surface of the ascending channel 7 is removed, heat loss to the forming member of the ascending channel 7 can be avoided. It's good to be what you can be.
又、燃焼排ガスの温度をクリンカーの溶流点以
上に上昇させるに、上昇させるほど迅速にクリン
カーを除去できるものの、反面、使用する炉の壁
を熱損する虞れがあるものであり、使用する炉の
構成、及び、クリンカーの性状等に応じた温度に
上昇させるとよい。 In addition, although raising the temperature of the flue gas above the melting point of the clinker can remove clinker more quickly, on the other hand, there is a risk of heat loss to the walls of the furnace used. The temperature may be raised depending on the composition of the clinker and the properties of the clinker.
又、本発明は、下水汚泥の外に、例えばタイヤ
屑、都市ゴミ焼却灰、廃触媒など各種の産業廃棄
物あるいはその中間処理物を処理対象にでき、そ
して、使用する溶融炉の具体構成は、水冷ジヤケ
ツト10を備えないもの等、各種変更可能であ
り、更に、高温炉床2を形成する炭素系可燃物質
としては、主としてコークスを用いるとよいが、
無煙炭等の練炭、黒煙電極屑等の各種のものを利
用してもよい。 In addition to sewage sludge, the present invention can treat various industrial wastes such as tire scraps, municipal waste incineration ash, and waste catalysts, as well as intermediate products thereof, and the specific configuration of the melting furnace used is Various modifications are possible, such as one without the water-cooling jacket 10, and furthermore, it is preferable to mainly use coke as the carbon-based combustible material forming the high-temperature hearth 2.
Various materials such as briquettes such as anthracite, black smoke electrode scraps, etc. may be used.
以上要するに本発明は、冒記廃棄物溶融方法に
おいて、産業廃棄物又はその中間処理物の供給を
停止させて又は減少させて、前記上昇流路7の内
面に付着したクリンカーを前記高温炉床2からの
燃焼排ガスによつて溶融流下させることを特徴と
する。 In summary, the present invention, in the above-mentioned waste melting method, stops or reduces the supply of industrial waste or its intermediate processed material, and removes clinker adhering to the inner surface of the ascending channel 7 to the high-temperature hearth 2. It is characterized by causing the melt to flow down by combustion exhaust gas from.
すなわち、産業廃棄物又はその中間処理物の供
給を停止又は減少させた状態で、高温炉床2から
の燃焼排ガスの温度をクリンカーの溶流点以上と
なるように維持させて、上昇流路7の内面に付着
したクリンカーを溶融流下させるようにせんとす
るものであるから、産業廃棄物又はその中間処理
物の供給を停止又は減少させた状態で高温炉床2
をそれからの燃焼排ガスの温度がクリンカーの溶
流点以上となるように燃焼させるだけの簡単な操
作で付着クリンカーを除去でき、しかも、炉温を
低下させずにクリンカー除去を行なえるのでクリ
ンカー除去作業に際して廃棄物溶融作業を長時間
に亘つて停止させねばならない不都合なくクリン
カー除去作業を短時間で行なうことができ、その
うえ、付着クリンカー全体の表面をむらなく加温
しながら付着クリンカー全体をむらなく十分に除
去できるのであり、もつて、極めて良好に付着ク
リンカーを除去できるようになつた。 That is, while the supply of industrial waste or its intermediate treatment product is stopped or reduced, the temperature of the combustion exhaust gas from the high-temperature hearth 2 is maintained at a temperature higher than the melting point of the clinker, and the ascending flow path 7 is Since the purpose is to melt and flow down the clinker adhering to the inner surface of the high-temperature hearth 2, the supply of industrial waste or its intermediate products is stopped or reduced.
The adhering clinker can be removed by simply burning the flue gas so that the temperature of the flue gas is above the melting point of the clinker. Moreover, the clinker can be removed without lowering the furnace temperature, making the clinker removal work easier. The clinker removal work can be carried out in a short time without the inconvenience of having to stop the waste melting work for a long time, and in addition, the entire surface of the adhering clinker can be heated evenly and thoroughly. Eventually, it became possible to remove adhering clinker very effectively.
図面は本発明に係る廃棄物溶融方法の実施の態
様を例示し、使用する炉の概略断面図である。
2……高温炉床、7……上昇流路。
The drawing illustrates an embodiment of the waste melting method according to the present invention and is a schematic cross-sectional view of a furnace used. 2...High temperature hearth, 7...Rising channel.
Claims (1)
系可燃物質によつて形成した高温炉床2に供給し
て、焼却溶融させ、燃焼排ガスを前記高温炉床2
の上方に形成した上昇流路7に排出させる廃棄物
溶融方法であつて、産業廃棄物又はその中間処理
物の供給を停止させて又は減少させて、前記上昇
流路7の内面に付着したクリンカーを前記高温炉
床2からの燃焼排ガスによつて溶融流下させるこ
とを特徴とする廃棄物溶融方法。1. Industrial waste or its intermediate treatment product is supplied to a high-temperature hearth 2 formed of carbon-based combustible material, incinerated and melted, and combustion exhaust gas is transferred to the high-temperature hearth 2.
A waste melting method in which the waste is discharged into an ascending channel 7 formed above, and clinker adhering to the inner surface of the ascending channel 7 is removed by stopping or reducing the supply of industrial waste or its intermediate treatment products. A waste melting method characterized in that the waste is melted and flowed down by combustion exhaust gas from the high temperature hearth 2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56166958A JPS5866711A (en) | 1981-10-19 | 1981-10-19 | Melting method for refuse |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56166958A JPS5866711A (en) | 1981-10-19 | 1981-10-19 | Melting method for refuse |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5866711A JPS5866711A (en) | 1983-04-21 |
| JPH0118323B2 true JPH0118323B2 (en) | 1989-04-05 |
Family
ID=15840767
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56166958A Granted JPS5866711A (en) | 1981-10-19 | 1981-10-19 | Melting method for refuse |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5866711A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3309586B2 (en) * | 1994-09-21 | 2002-07-29 | 日本鋼管株式会社 | Gasification and melting method of waste |
-
1981
- 1981-10-19 JP JP56166958A patent/JPS5866711A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5866711A (en) | 1983-04-21 |
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