JPH1144417A - Treatment method of refuse incineration ash - Google Patents

Treatment method of refuse incineration ash

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Publication number
JPH1144417A
JPH1144417A JP20040697A JP20040697A JPH1144417A JP H1144417 A JPH1144417 A JP H1144417A JP 20040697 A JP20040697 A JP 20040697A JP 20040697 A JP20040697 A JP 20040697A JP H1144417 A JPH1144417 A JP H1144417A
Authority
JP
Japan
Prior art keywords
container
incineration ash
ash
incinerator
sealed
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.)
Pending
Application number
JP20040697A
Other languages
Japanese (ja)
Inventor
Koichi Shimoyama
孝市 下山
Ten Shimoyama
天 下山
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP20040697A priority Critical patent/JPH1144417A/en
Publication of JPH1144417A publication Critical patent/JPH1144417A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To completely pyrolyze dioxin at a low cost by placing the incineration ash in a heat resistant container in a sealed condition, and heating and melting it in an incinerator. SOLUTION: The incineration ash 3 which is the municipal refuse 1 incinerated in a refuse incinerator 2, is placed in a container 4, and sealed by a lid 4a, and heated and melted in an incinerator 5. The container 4 is a ceramic heat resistant container capable of withstanding high temperature of >=1,700 deg.C, and an aluminum powder is applied to an inner surface of the container. The incineration ash 3 of approximately 0.5 ton is filled in the container 4, and the container is sealed by the lid 4a which is similarly heat resistant to the container body. The incinerator 5 employs a ceramic oven which is fired with LPG, and the container 4 is taken in/out using a charging truck 5a attached to the ceramic oven. The incinerator 5 is heated in advance until the in-furnace temperature reaches approximately 1,300 deg.C. Then, the container 4 filled with the incineration ash 3 and sealed is loaded on the charging truck 5a, and charged in the furnace, and the incineration ash 3 is melted through the heating for approximately 18 hours.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ごみ焼却設備から
排出される焼却灰の処理方法に関する。
The present invention relates to a method for treating incinerated ash discharged from a refuse incineration plant.

【0002】[0002]

【従来の技術】近年、市町村のごみ焼却設備でのごみ焼
却に際して発生するダイオキシンが問題になっており、
焼却設備から排出される焼却灰についてもダイオキシン
を含有していることから、焼却灰中のダイオキシンを無
害化する方法が種々提案されている。
2. Description of the Related Art In recent years, dioxin generated during incineration of municipal incineration facilities has become a problem.
Since incineration ash discharged from incineration equipment also contains dioxin, various methods for detoxifying dioxin in incineration ash have been proposed.

【0003】このなかで、焼却灰を溶融してダイオキシ
ンを熱分解する処理方法として、特開昭64−3341
6号公報および特開平3−232579号公報に、ダイ
オキシン含有灰分を溶融炉で溶融してダイオキシンを熱
分解する方法が、特開平7−214032号公報および
特開平8−145330号公報に、ごみ焼却灰を燃料と
純酸素を利用した燃焼バーナーによって高温で溶解して
ダイオキシンを熱分解する方法が記載されている。
[0003] Among them, as a treatment method for melting incineration ash and thermally decomposing dioxin, Japanese Patent Application Laid-Open No. 64-3341 discloses a method.
No. 6 and JP-A-3-232579 disclose a method of melting dioxin-containing ash in a melting furnace to thermally decompose dioxin. JP-A-7-214032 and JP-A-8-145330 disclose waste incineration. A method is described in which ash is dissolved at a high temperature by a combustion burner using fuel and pure oxygen to thermally decompose dioxin.

【0004】ダイオキシンは600℃以上の温度で分解
し始め、900℃以上の高温下ではほとんどが分解する
といわれており、上記の各公開公報の記載によれば、い
ずれの処理方法の場合もダイオキシンをほぼ完全に無害
化できるとされている。
[0004] It is said that dioxin starts to decompose at a temperature of 600 ° C or higher and almost decomposes at a high temperature of 900 ° C or higher. According to the descriptions of the above publications, dioxin is decomposed in any treatment method. It is said that it can be almost completely detoxified.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、前記特
開昭64−33416号公報および特開平3−2325
79号公報には、溶融炉の形式や燃焼法、溶融温度など
の焼却灰の溶融についての具体的な実施態様が記載され
ておらず、実施による効果も明らかでない。
However, Japanese Patent Application Laid-Open No. 64-33416 and Japanese Patent Application Laid-Open No. 3-2525 are not disclosed.
No. 79 does not describe a specific embodiment of melting of incineration ash such as a type of a melting furnace, a combustion method, and a melting temperature, and the effect of the implementation is not clear.

【0006】また、特開平7−214032号公報およ
び特開平8−145330号公報に記載の処理方法は、
燃料とともに純酸素を使用することによって1600℃
程度の高温を得ることが特徴であり、さらに、珪素土や
ソーダ灰をごみ焼却灰と一緒に溶解炉に投入して溶解さ
れるごみ焼却灰をガラス状にするものであるが、このよ
うな方法を実施するためには相当に大きな溶融炉や燃焼
装置を必要とし、処理量がさほど多くない場合には処理
コストが高くなるという問題がある。
Further, the processing methods described in JP-A-7-214032 and JP-A-8-145330 are
1600 ° C by using pure oxygen with fuel
It is characterized by obtaining a high temperature of about the same level, and furthermore, silicon incineration ash and soda ash are put into a melting furnace together with refuse incineration ash and the refuse incineration ash that is melted is made into a glass. In order to carry out the method, a considerably large melting furnace or a combustion apparatus is required, and if the throughput is not so large, there is a problem that the processing cost increases.

【0007】本発明が解決すべき課題は、ごみ焼却灰を
溶融してダイオキシンを熱分解するにあたり、低コスト
でかつダイオキシンを完全に熱分解する手段を得ること
にある。
An object of the present invention is to provide a low-cost means for completely decomposing dioxin when melting incineration ash to thermally decompose dioxin.

【0008】[0008]

【課題を解決するための手段】本発明のごみ焼却灰の処
理方法は、ごみ焼却設備から排出される焼却灰を溶融処
理する方法であって、前記焼却灰を耐熱容器に入れ密閉
した状態で燃焼炉内で加熱し、前記耐熱容器内で焼却灰
を溶融させることを特徴とする。
The method for treating incinerated ash of the present invention is a method for melting incinerated ash discharged from refuse incineration equipment, wherein the incinerated ash is placed in a heat-resistant container and sealed. It is characterized by heating in a combustion furnace and melting incineration ash in the heat-resistant container.

【0009】本発明において対象とするごみ焼却灰は、
一般の都市ごみを焼却炉で焼却した後の焼却灰である。
このごみ焼却灰にはダイオキシンが含まれており、本発
明においてはごみ焼却灰を溶融することによりダイオキ
シンを熱分解して無害化するものである。
The waste incineration ash targeted in the present invention is:
Incinerated ash after incineration of general municipal waste.
This incineration ash contains dioxin. In the present invention, dioxin is thermally decomposed and made harmless by melting the incineration ash.

【0010】本発明においては、ごみ焼却灰を溶融する
のに、耐熱容器に入れ密閉した状態で燃焼炉内で加熱す
る。この耐熱容器としては、1500℃程度以上の耐熱
性を有する容器、好ましくはセラミックス製の容器を用
いる。焼却灰を入れた耐熱容器を密閉するのは、焼却灰
中に含まれるダイオキシンが容器外に漏出しないよう
に、また、容器内の焼却灰が飛散しないように、さら
に、焼却灰中に含まれる重金属類が容器外に揮散しない
ようにするためである。
In the present invention, the incineration ash is melted by heating in a combustion furnace in a heat-resistant container in a sealed state. As this heat-resistant container, a container having a heat resistance of about 1500 ° C. or more, preferably a ceramic container is used. The heat-resistant container containing the incinerated ash is sealed so that the dioxin contained in the incinerated ash does not leak out of the container, and the incinerated ash in the container is not scattered. This is to prevent heavy metals from volatilizing outside the container.

【0011】燃焼炉としては、重油、LPG、LNGそ
の他の燃料を用いる燃焼炉を用いる。小規模な炉設備と
しては、たとえばLPGを燃料とする陶磁器製造用の窯
を用いることができる。この燃焼炉のなかに前記のごみ
焼却灰を入れ密閉した耐熱容器を装入して、炉内温度1
300℃程度で長時間加熱すると、容器内のごみ焼却灰
は溶融し、この過程で、ごみ焼却灰に含まれるダイオキ
シンは熱分解して無害化される。
As the combustion furnace, a combustion furnace using heavy oil, LPG, LNG or other fuel is used. As the small-scale furnace equipment, for example, a kiln for producing ceramics using LPG as a fuel can be used. Into the combustion furnace, a sealed heat-resistant container containing the refuse incineration ash was placed, and the temperature in the furnace was set to 1
When heated at about 300 ° C. for a long time, the refuse incineration ash in the container melts, and in this process, dioxin contained in the refuse incineration ash is thermally decomposed and made harmless.

【0012】本発明の方法によりごみ焼却灰を溶融処理
することによって、ダイオキシンは完全に熱分解して無
害化され、同時に焼却灰中の重金属粒は溶融物の中に閉
じ込められる。焼却灰は密閉容器に入れられて加熱溶融
されるので、加熱時に焼却灰中に含まれるダイオキシン
が容器外に漏出したり、焼却灰が飛散したりするこがな
く、また、焼却灰中に含まれる重金属類が容器外に揮散
して燃焼炉が損傷を受けることがない。また、燃焼炉か
らの容器の出し入れも容易である。燃焼炉は陶器窯など
の既存の小型炉を利用することができるので、設備コス
トを低減することができる。溶融物は、冷却した後粉砕
してコンクリートやアスファルト原料に利用することが
できる。
[0012] By melting and treating the refuse incineration ash according to the method of the present invention, dioxin is completely decomposed by thermal decomposition and rendered harmless, and at the same time, heavy metal particles in the incineration ash are confined in the melt. Since the incinerated ash is placed in a closed container and heated and melted, the dioxin contained in the incinerated ash does not leak out of the container and the incinerated ash does not scatter during heating, nor is it contained in the incinerated ash. The burning furnace will not be damaged by the heavy metals that are volatilized outside the container. In addition, it is easy to put the container in and out of the combustion furnace. As the combustion furnace can use an existing small furnace such as a pottery kiln, it is possible to reduce equipment costs. The melt can be cooled and then pulverized and used as a raw material for concrete or asphalt.

【0013】[0013]

【発明の実施の形態】図1は本発明の実施の形態におけ
るごみ焼却灰の処理手順を示す図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a view showing a procedure for treating incinerated ash in an embodiment of the present invention.

【0014】本実施形態において用いたごみ焼却灰は、
都市ごみ1をごみ焼却炉2で焼却した後の焼却灰3であ
る。この焼却灰3を、容器4に入れ、蓋4aをして密閉
し、燃焼炉5で加熱溶融させる。
The refuse incineration ash used in this embodiment is:
This is incineration ash 3 after incineration of municipal waste 1 in a refuse incinerator 2. The incinerated ash 3 is put in a container 4, sealed with a lid 4 a, and heated and melted in a combustion furnace 5.

【0015】容器4は、1700℃以上の高温に耐える
セラミックス製の耐熱容器であり、容器内面にアルミナ
粉を塗布しておく。この容器4に0.5トンの焼却灰3
を充填し、容器本体と同様な耐熱性のある蓋4aにより
密閉する。
The container 4 is a heat-resistant container made of ceramics which can withstand a high temperature of 1700 ° C. or more, and alumina powder is applied to the inner surface of the container. This container 4 contains 0.5 tons of incinerated ash 3
And sealed with a lid 4a having the same heat resistance as the container body.

【0016】燃焼炉5は、LPGを燃料とする陶器窯を
使用し、陶器窯に付設されている装入台車5aを利用し
て容器4の出し入れを行う。この燃焼炉5を、炉内温度
が約1300℃になるまで予め加熱し、その後、焼却灰
3を充填し密閉した容器4を装入台車5aに載置して炉
内に装入し、約18時間加熱を続ける。
The combustion furnace 5 uses a pottery kiln using LPG as a fuel, and puts the container 4 in and out using a loading cart 5a attached to the pottery kiln. The combustion furnace 5 is preheated until the temperature in the furnace reaches about 1300 ° C., and thereafter, the container 4 filled with the incineration ash 3 and sealed is placed on a loading cart 5a and charged into the furnace. Continue heating for 18 hours.

【0017】この加熱により、焼却灰3は溶融する。加
熱終了後、装入台車5aを炉外に引き出し、容器4内の
溶融物6が固化する前に冷却台上に排出する。容器4の
内面にはアルミナ粉が塗布されているので、溶融物6は
容器内面に付着残留することなく、全量が排出される。
溶融物6を排出した後の容器4は約100℃になるまで
空冷した後、さらに常温程度に水冷する。排出した溶融
物6は、冷却固化した後、小塊に破砕して、コンクリー
トやアスファルトなどへの再生使用のための中間製品7
とする。
By this heating, the incineration ash 3 is melted. After the heating, the loading cart 5a is pulled out of the furnace, and is discharged onto the cooling table before the molten material 6 in the container 4 is solidified. Since the alumina powder is applied to the inner surface of the container 4, the entire amount of the melt 6 is discharged without adhering and remaining on the inner surface of the container.
After discharging the molten material 6, the container 4 is air-cooled to about 100 ° C., and then water-cooled to about room temperature. The discharged molten material 6 is cooled and solidified, then crushed into small lumps, and an intermediate product 7 for recycling to concrete or asphalt.
And

【0018】上記の加熱溶融過程において、焼却灰3に
含まれたダイオキシンは完全に熱分解して無害化され、
同時に焼却灰3中の重金属粒は固化物7の中に閉じ込め
られる。焼却灰3は密閉された容器4に入れられて加熱
溶融されるので、加熱時に焼却灰3中に含まれるダイオ
キシンが容器外に漏出したり、焼却灰3が飛散したり、
焼却灰3中に含まれる重金属類が容器4外に揮散したり
することはなく、燃焼炉5が損傷を受けることもない。
また、装入台車5aを利用して燃焼炉5からの容器4の
出し入れを迅速に行うことができるので、燃焼炉5を効
率よく稼働させることができる。溶融物6を排出した後
の容器4は、繰り返し使用することができる。
In the above-mentioned heating and melting process, dioxin contained in the incineration ash 3 is completely decomposed by heat and detoxified.
At the same time, the heavy metal particles in the incineration ash 3 are confined in the solidified material 7. Since the incineration ash 3 is put into the closed container 4 and melted by heating, the dioxin contained in the incineration ash 3 leaks out of the container at the time of heating, the incineration ash 3 scatters,
The heavy metals contained in the incineration ash 3 do not volatilize out of the container 4 and the combustion furnace 5 is not damaged.
Further, since the container 4 can be quickly taken in and out of the combustion furnace 5 by using the loading cart 5a, the combustion furnace 5 can be operated efficiently. After discharging the melt 6, the container 4 can be used repeatedly.

【0019】[0019]

【発明の効果】本発明により以下の効果を奏することが
できる。
According to the present invention, the following effects can be obtained.

【0020】(1)ごみ焼却灰を耐熱容器に入れ密閉し
た状態で燃焼炉内で加熱溶融させることにより、加熱時
に焼却灰中に含まれるダイオキシンが容器外に漏出した
り、焼却灰が飛散したり、また、焼却灰中に含まれる重
金属類が容器外に揮散したりすることがない。
(1) The waste incineration ash is placed in a heat-resistant container and heated and melted in a combustion furnace in a sealed state, so that the dioxin contained in the incineration ash leaks out of the container during heating and the incineration ash is scattered. Also, heavy metals contained in the incineration ash do not volatilize outside the container.

【0021】(2)耐熱容器としてセラミックス製の容
器を用いることにより、溶融物を排出した後の容器を繰
り返し使用することができる。
(2) By using a ceramic container as the heat-resistant container, the container after discharging the melt can be used repeatedly.

【0022】(3)燃焼炉は陶器窯などの既存の小型炉
を利用することができるので、設備コストを低減するこ
とができる。
(3) Since an existing small furnace such as a pottery kiln can be used as the combustion furnace, equipment costs can be reduced.

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

【図1】 本発明の実施の形態におけるごみ焼却灰の処
理手順を示す図である。
FIG. 1 is a diagram showing a procedure for treating incineration ash in an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 都市ごみ 2 焼却炉 3 焼却灰 4 容器 4a 蓋 5 燃焼炉 5a 装入台車 6 溶融物 7 中間製品 Reference Signs List 1 municipal solid waste 2 incinerator 3 incineration ash 4 container 4a lid 5 combustion furnace 5a loading cart 6 molten material 7 intermediate product

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ごみ焼却設備から排出される焼却灰を溶
融処理する方法において、前記焼却灰を耐熱容器に入れ
密閉した状態で燃焼炉内で加熱し、前記耐熱容器内で焼
却灰を溶融させることを特徴とするごみ焼却灰の処理方
法。
1. A method for melting incinerated ash discharged from a refuse incineration plant, wherein the incinerated ash is placed in a heat-resistant container, heated in a combustion furnace in a sealed state, and melted in the heat-resistant container. A method for treating waste incineration ash.
【請求項2】 前記耐熱容器がセラミックス製の容器で
あることを特徴とする請求項1記載のごみ焼却灰の処理
方法。
2. The method according to claim 1, wherein the heat-resistant container is a container made of ceramics.
JP20040697A 1997-07-25 1997-07-25 Treatment method of refuse incineration ash Pending JPH1144417A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20040697A JPH1144417A (en) 1997-07-25 1997-07-25 Treatment method of refuse incineration ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20040697A JPH1144417A (en) 1997-07-25 1997-07-25 Treatment method of refuse incineration ash

Publications (1)

Publication Number Publication Date
JPH1144417A true JPH1144417A (en) 1999-02-16

Family

ID=16423797

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20040697A Pending JPH1144417A (en) 1997-07-25 1997-07-25 Treatment method of refuse incineration ash

Country Status (1)

Country Link
JP (1) JPH1144417A (en)

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