JPS6237290B2 - - Google Patents
Info
- Publication number
- JPS6237290B2 JPS6237290B2 JP52134419A JP13441977A JPS6237290B2 JP S6237290 B2 JPS6237290 B2 JP S6237290B2 JP 52134419 A JP52134419 A JP 52134419A JP 13441977 A JP13441977 A JP 13441977A JP S6237290 B2 JPS6237290 B2 JP S6237290B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- waste sludge
- melting point
- waste
- sludge
- 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
Landscapes
- Gasification And Melting Of Waste (AREA)
Description
〔産業上の利用分野〕
本発明は、炉への投入前に、被処理物である廃
汚泥に融点降下材をミキサーで混入し、そのミキ
サーからの混合物を前記炉内で加熱溶融する廃汚
泥処理方法に関する。
さらに説明すると、廃汚泥を、加熱溶融により
嵩が低くて有害物質の流出の無いものにし、埋立
て材料、骨材、路床材等として後利用できるもの
にし、その上、炉への投入前に廃汚泥に融点降下
材をミキサーで混入して、一般に廃汚泥の融点が
高いにもかかわらず、廃汚泥の加熱溶融に際し、
大量の燃料を必要とすると共に炉の熱損傷が激し
く、さらに窒素酸化物の発生が多くなる等の欠点
が伴わないようにする廃汚泥処理方法に関する。
〔従来の技術〕
従来、融点降下材として川砂を廃汚泥に混入し
て、廃汚泥の融点を降下させていた。
〔発明が解決しようとする問題点〕
ところが、川砂はかなり高価でありかつ入手し
にくい資源であるために、経費の増大をまねくの
みならず、本来溶融処理不要な川砂をも溶融させ
るために溶融物の量が必要以上に多くなり、溶融
処理の利点である残留物量減少を損なう欠点があ
つた。
本発明の目的は、極めて合理的な手段でもつて
廃汚泥の融点降下を行い、経済的に有利にすると
共に、省資源を図り、かつ、溶融物の不要な増量
を防止できるようにする点にある。
〔問題点を解決するための手段〕
本発明の特徴手段は、炉への投入前にミキサー
で廃汚泥に混入する融点降下材として都市ゴミ焼
却灰を使用することにあり、その作用効果は次の
通りである。
〔作 用〕
すなわち、都市ゴミ焼却灰中には、シリカ分等
が豊富に含まれており、適量の都市ゴミ焼却灰を
予めミキサーで十分に混入すると、十分に廃汚泥
の融点を降下させる事ができ、このように、むし
ろ処分に困つている都市ごみ焼却灰を有効利用す
る事により、廃汚泥の加熱溶融処理を、極めて経
済的にかつ有効資源を必要とせずに、かつ不要に
溶融物量を増やさずに行える。
〔発明の効果〕
その結果、廃汚泥を融点降下させて加熱溶融処
理するに、融点降下のための材料経費を不要にで
き、省資源面で有利にでき、溶融物の不必要な増
量を無くせ、全体として廃汚泥の加熱溶融処理に
極めて好適な融点降下技術を確立できた。
〔実施例〕
次に実施例を示す。
第1図に示すごとく、竪型炉1の上部にコーク
ス供給用ホツパ2を設け、流体圧シリンダー3
a,3bによるゲート4及びベル5の開閉で炉1
内に適量のコークスを供給し、炉内下部に燃焼コ
ークスから成る高温炉床6を形成する。
炉床6はバーナ7で点火され、着火後は、バー
ナ7を停止して、ブロワー8から熱交換器9を経
て供給される予熱空気により炉床6の燃焼を継続
させる。
予熱空気は、炉床6の中間部に対する下部供給
経路10a、炉床6の上面に対する中間供給経路
10b、及び、炉上部空間に対する上部供給経路
10cから供給され、炉床6を廃棄物溶融に足る
高温に維持すると共に、炉1上部における後燃焼
で完全燃焼を行わせ、そして、燃焼ガスは排ガス
路11を通つて灰分離機12及び前記熱交換器9
に送られる。
高温炉床6の直上方において炉内周壁面1aを
上拡がりテーパ面に構成して、炉床6からの上昇
ガス流速を低下させ、燃焼ガスによる灰飛散を抑
制する。
第2図に示すごとく、廃汚泥をホツパ28から
かつ都市ゴミ焼却灰をホツパ29から夫々ミキサ
ー30に供給し、都市ゴミ焼却灰を混入した廃汚
泥を、ミキサー30から供給ホツパ13に送り、
供給ホツパ13からロータリーフイーダー14に
送り、ブロワ15からの加圧空気により焼却灰混
入廃汚泥を炉床6の上面に吹付け、燃焼ガス及び
燃焼用空気の流動にかかわらず、供給後直ちに廃
汚泥及び焼却灰が高温炉床6に接触して溶融さ
れ、かつ、灰飛散が防止されるようにする。
この廃棄物供給系には、流体圧シリンダー3c
で操作される供給量調節用シヤツタ16、安全口
17、付着防止板18、及び、流量調整弁19等
を設けてあり、溶融処理に適した廃棄物供給を維
持できる。
溶融物は、せき20a,20bを備えた排出路
を経て比重選別部21に送られ、溶融物が二層に
分かれた場合、比重の軽い溶融物は第1取出口2
2から、かつ比重の重い溶融物は第2取出口23
から夫々排出され、また、選別部21のガスは排
ガス管11aを経て炉1上部からの排ガスに合流
される。
図中、24は炉保護用水冷ジヤケツトであり、
25は後燃焼用空気取入口であり、26は排ガス
量調整用ダンパーであり、27は予熱空気量調整
用ダンパーである。
すなわち、上記炉1を使用して廃汚泥を溶融す
れば、都市ゴミ焼却灰中のシリカ分等が有効に作
用して、炉温を比較的低くした状態で廃汚泥の溶
融処理を行えるのである。ちなみに下水汚泥を単
独で溶融すると融点が1580℃であつたのが、下水
汚泥に都市ゴミ焼却灰を重量比で1:0.5の割合
で混合して溶融すると、融点が1320℃に降下し
た。
実験に使用した下水汚泥は予め焼却処理したも
ので、下水汚泥灰分の組成は下記表に示す通りで
ある。
[Industrial Application Field] The present invention relates to waste sludge, in which a melting point depressing material is mixed into waste sludge, which is a material to be treated, in a mixer before being input into a furnace, and the mixture from the mixer is heated and melted in the furnace. Regarding processing method. To explain further, the waste sludge is heated and melted to make it low in bulk and free of harmful substances, which can be used later as landfill material, aggregate, roadbed material, etc. However, when waste sludge is heated and melted, a melting point depressing material is mixed into the waste sludge using a mixer.
The present invention relates to a waste sludge treatment method that does not require a large amount of fuel, severely damage the furnace, and generate more nitrogen oxides. [Prior Art] Conventionally, river sand was mixed into waste sludge as a melting point lowering material to lower the melting point of the waste sludge. [Problems to be solved by the invention] However, since river sand is a resource that is quite expensive and difficult to obtain, it not only increases costs, but also requires melting to melt river sand that does not originally require melting. The amount of material was larger than necessary, which was a disadvantage of reducing the amount of residue, which is an advantage of melt processing. The purpose of the present invention is to lower the melting point of waste sludge by extremely rational means, to make it economically advantageous, to save resources, and to prevent unnecessary increases in the amount of molten material. be. [Means for Solving the Problems] The characteristic means of the present invention is to use municipal waste incineration ash as a melting point depressing material that is mixed into the waste sludge in a mixer before being introduced into the furnace, and its effects are as follows. It is as follows. [Function] In other words, municipal waste incineration ash contains abundant silica, etc., and if an appropriate amount of municipal waste incineration ash is mixed in with a mixer in advance, the melting point of waste sludge can be sufficiently lowered. In this way, by making effective use of municipal waste incineration ash, which is rather difficult to dispose of, heating and melting treatment of waste sludge can be carried out extremely economically, without requiring effective resources, and by reducing the amount of molten material unnecessarily. This can be done without increasing. [Effects of the invention] As a result, when waste sludge is heated and melted to lower its melting point, the cost of materials for lowering the melting point can be eliminated, making it advantageous in terms of resource conservation, and eliminating unnecessary increases in the amount of molten material. As a whole, we were able to establish a melting point lowering technology that is extremely suitable for heating and melting treatment of waste sludge. [Example] Next, an example will be shown. As shown in FIG. 1, a hopper 2 for supplying coke is provided at the top of a vertical furnace 1,
Furnace 1 is opened and closed by gate 4 and bell 5 by a and 3b.
An appropriate amount of coke is supplied into the furnace to form a high-temperature hearth 6 made of burnt coke in the lower part of the furnace. The hearth 6 is ignited by a burner 7, and after ignition, the burner 7 is stopped and the combustion of the hearth 6 is continued by preheated air supplied from a blower 8 via a heat exchanger 9. Preheating air is supplied from a lower supply route 10a to the middle part of the hearth 6, an intermediate supply route 10b to the upper surface of the hearth 6, and an upper supply route 10c to the upper space of the hearth, and the preheated air is supplied from the lower supply route 10a to the middle part of the hearth 6, and the upper supply route 10c to the upper space of the hearth. While maintaining the high temperature, complete combustion is performed by after-combustion in the upper part of the furnace 1, and the combustion gas passes through the exhaust gas passage 11 to the ash separator 12 and the heat exchanger 9.
sent to. Directly above the high-temperature hearth 6, the inner peripheral wall surface 1a of the furnace is formed into an upwardly expanding tapered surface to reduce the flow rate of rising gas from the hearth 6 and suppress the scattering of ash caused by the combustion gas. As shown in FIG. 2, waste sludge is supplied from the hopper 28 and municipal waste incineration ash is supplied from the hopper 29 to the mixer 30, and waste sludge mixed with the municipal waste incineration ash is sent from the mixer 30 to the supply hopper 13.
The waste sludge mixed with incineration ash is sent from the supply hopper 13 to the rotary feeder 14, and the waste sludge mixed with incineration ash is blown onto the upper surface of the hearth 6 by pressurized air from the blower 15, and is disposed of immediately after being supplied, regardless of the flow of combustion gas and combustion air. Sludge and incineration ash are brought into contact with a high-temperature hearth 6 and melted, and ash scattering is prevented. This waste supply system includes a fluid pressure cylinder 3c.
A supply amount adjustment shutter 16, a safety port 17, an adhesion prevention plate 18, a flow rate adjustment valve 19, etc., which are operated by a shutter 16, a safety port 17, an adhesion prevention plate 18, a flow rate adjustment valve 19, etc. are provided, and the waste supply suitable for the melting process can be maintained. The molten material is sent to the specific gravity sorting section 21 through a discharge path equipped with weirs 20a and 20b, and when the molten material is separated into two layers, the molten material with a lighter specific gravity is sent to the first outlet 2.
2, and the molten material with heavy specific gravity is taken out from the second outlet 23.
Further, the gas in the sorting section 21 is combined with the exhaust gas from the upper part of the furnace 1 through the exhaust gas pipe 11a. In the figure, 24 is a water cooling jacket for protecting the furnace.
25 is an air intake port for after-combustion, 26 is a damper for adjusting the amount of exhaust gas, and 27 is a damper for adjusting the amount of preheating air. In other words, if the waste sludge is melted using the furnace 1, the silica in the municipal waste incineration ash acts effectively, and the waste sludge can be melted at a relatively low furnace temperature. . By the way, when sewage sludge was melted alone, the melting point was 1,580°C, but when sewage sludge was mixed with municipal waste incineration ash at a weight ratio of 1:0.5 and melted, the melting point dropped to 1,320°C. The sewage sludge used in the experiment was previously incinerated, and the composition of the sewage sludge ash is shown in the table below.
【表】
また、実験に使用した都市ゴミ焼却灰の組成は
下記表に示す通りである。[Table] The composition of the municipal waste incineration ash used in the experiment is shown in the table below.
次に別実施例を説明する。
廃汚泥の炉1への供給手段は、前記ホツパ2か
ら炭素系可燃物質と混合状態であるいは交互に供
給する等の変更が可能である。
溶融に利用する炉は、上述キユポラタイプ以外
に、バーナータイプの竪型炉、ロータリーキルン
等の横型炉等、各種公知のものがある。
Next, another embodiment will be described. The means for supplying waste sludge to the furnace 1 can be changed such that it is supplied from the hopper 2 in a mixed state with carbon-based combustible material or alternately. In addition to the above-mentioned cupola type, there are various known furnaces used for melting, such as a burner type vertical furnace and a horizontal furnace such as a rotary kiln.
図面は本発明に使用する設備例を示し、第1図
は一部省略縦断面図、第2図は第1図の―線
断面図である。
1…炉、30…ミキサー。
The drawings show an example of equipment used in the present invention, with FIG. 1 being a partially omitted vertical sectional view, and FIG. 2 being a sectional view taken along the line -- in FIG. 1...Furnace, 30...Mixer.
Claims (1)
融点降下材をミキサー30で混入し、そのミキサ
ー30からの混合物を前記炉1内で加熱溶融する
廃汚泥処理方法であつて、前記融点降下材として
都市ゴミ焼却灰を使用する廃汚泥処理方法。1. A waste sludge treatment method in which a melting point depressing material is mixed into waste sludge, which is a material to be treated, in a mixer 30 before being input into the furnace 1, and the mixture from the mixer 30 is heated and melted in the furnace 1, A waste sludge treatment method using municipal waste incineration ash as the melting point lowering material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13441977A JPS5468078A (en) | 1977-11-08 | 1977-11-08 | Method of disposiong waste sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13441977A JPS5468078A (en) | 1977-11-08 | 1977-11-08 | Method of disposiong waste sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5468078A JPS5468078A (en) | 1979-05-31 |
| JPS6237290B2 true JPS6237290B2 (en) | 1987-08-12 |
Family
ID=15127938
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13441977A Granted JPS5468078A (en) | 1977-11-08 | 1977-11-08 | Method of disposiong waste sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5468078A (en) |
-
1977
- 1977-11-08 JP JP13441977A patent/JPS5468078A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5468078A (en) | 1979-05-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204648253U (en) | A kind of dangerous waste incineration device | |
| EP0884545B1 (en) | Electric ARC melting furnace | |
| WO2002014743A1 (en) | Method for incineration disposal of waste | |
| US5605104A (en) | Method and device for melting down solid combustion residues | |
| JPH10103635A (en) | Direct connected type incineration ash melting and processing facility and its processing method | |
| CN108168320A (en) | A kind of symmetrical double furnace chambers scrap steel preheating melting appartus and steel scrap melt method | |
| CN112460603A (en) | Hazardous waste incineration system and hazardous waste incineration method | |
| GB1243489A (en) | Incinerator for refuse | |
| CN1511797A (en) | A kind of production process of mineral wool granular cotton and its hot air system | |
| JPS5838693B2 (en) | Industrial waste processing furnace | |
| JP2515039B2 (en) | Coal fired boiler equipment | |
| JPS6237290B2 (en) | ||
| EP0747492A1 (en) | Method for melting ferrous metals by means of an electric arc furnace charged with ferrous materials containing energy-releasing substances | |
| CN110805911A (en) | Self-discharging type incineration waste ash melting treatment device | |
| JPS6150894B2 (en) | ||
| JPH035611A (en) | Waste melting furnace | |
| CN209013209U (en) | Danger wastes incineration residue melting plant | |
| EP0846919A4 (en) | BURNING / FUSION PROCESS FOR WASTE FUSION OVEN | |
| JPH0331966B2 (en) | ||
| KR100559796B1 (en) | Brown gas high temperature pyrolysis melting incinerator | |
| JPS5838694B2 (en) | Industrial waste treatment furnace | |
| CN221763527U (en) | Vertical cyclone oxygen-enriched combustion melting furnace | |
| CA1148411A (en) | Furnace for treating industrial wastes | |
| JP3278780B2 (en) | Incinerator | |
| JPH02303585A (en) | Method for melting asbestos |