JP2001276771A - Treatment method for making incineration residue and/or molten fly ash harmless - Google Patents

Treatment method for making incineration residue and/or molten fly ash harmless

Info

Publication number
JP2001276771A
JP2001276771A JP2000093457A JP2000093457A JP2001276771A JP 2001276771 A JP2001276771 A JP 2001276771A JP 2000093457 A JP2000093457 A JP 2000093457A JP 2000093457 A JP2000093457 A JP 2000093457A JP 2001276771 A JP2001276771 A JP 2001276771A
Authority
JP
Japan
Prior art keywords
fly ash
molten fly
titanium dioxide
dioxins
raw material
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
JP2000093457A
Other languages
Japanese (ja)
Inventor
Mitsuru Takada
満 高田
Masanori Shimizu
正紀 清水
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.)
Sintokogio Ltd
Original Assignee
Sintokogio 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 Sintokogio Ltd filed Critical Sintokogio Ltd
Priority to JP2000093457A priority Critical patent/JP2001276771A/en
Publication of JP2001276771A publication Critical patent/JP2001276771A/en
Pending legal-status Critical Current

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Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Catalysts (AREA)
  • Fire-Extinguishing Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a treatment method for making an incineration residue and molten fly ash harmless, capable of conducting a perfect decomposition treatment of dioxins and the like, and low in both initial and running costs. SOLUTION: This treatment method for making an incineration residue and molten fly ash harmless is characterized by adding inexpensive titanium dioxide as a catalyst to the raw materials to be treated composed of an incineration residue and molten fly ash, heating and agitating the dioxins and the like at a predetermined temperature for a predetermined time to decompose it with oxidation catalytic action by titanium dioxide followed by conducting an elution prevention treatment of heavy metals.

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、都市ゴミ等の焼却
設備から排出される焼却残渣及び/又は溶融設備から排
出される溶融飛灰を無害化処理する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for detoxifying incineration residues discharged from an incineration facility for municipal waste and / or molten fly ash discharged from a melting facility.

【0002】[0002]

【従来の技術】従来、都市ゴミ等の焼却設備から排出さ
れる焼却残渣(主灰・飛灰)及び/又は溶融設備から排
出される溶融飛灰はキレ−ト薬剤処理により重金属溶出
防止処理を施して最終処分場に廃棄されている。また最
近になって焼却残渣及び/又は溶融飛灰中のダイオキシ
ン類の分解(脱塩素)装置及びダイオキシン類の分解
(脱塩素)薬剤が開発されつつある。
2. Description of the Related Art Conventionally, incineration residues (main ash and fly ash) discharged from incineration facilities for municipal garbage and the like and / or molten fly ash discharged from melting facilities are subjected to a treatment for preventing heavy metal elution by a chelating chemical treatment. And disposed at the final disposal site. Recently, a device for decomposing (dechlorinating) dioxins in incineration residues and / or molten fly ash and a chemical for decomposing (dechlorinating) dioxins have been developed.

【0003】[0003]

【発明が解決しようとする課題】しかしダイオキシン類
の分解(脱塩素)装置は、処理原料を低酸素状態で加熱
攪拌する必要があり、装置(主にロ−タリ−キルン)の
シ−ル構造が複雑になると共にダイオキシン再合成を防
止するための急冷装置が必要であり、イニシャルコスト
が高いという問題がある。またダイオキシン類を分解
(脱塩素)する薬剤を使用する場合は、通常酸素状態で
の運転が可能になり、装置のシ−ル構造を簡略化できる
が薬剤のコストが高く長期ランニングコストの面で問題
がある。本発明は上記の問題に鑑みて成されたもので、
ダイオキシン類をイニシャルコスト及びランニングコス
トとも低コストで完全に分解処理できる焼却残渣及び/
又は溶融飛灰の無害化処理方法を提供することを目的と
する。
However, in the apparatus for decomposing (dechlorinating) dioxins, it is necessary to heat and agitate the processing raw materials in a low oxygen state, and the sealing structure of the apparatus (mainly a rotary kiln) is required. However, there is a problem that a rapid cooling device for preventing re-synthesis of dioxin is required, and the initial cost is high. When a chemical that decomposes (dechlorinates) dioxins is used, it is possible to operate in a normal oxygen state and the sealing structure of the apparatus can be simplified, but the cost of the chemical is high and the long-term running cost is low. There's a problem. The present invention has been made in view of the above problems,
Incineration residue that can completely decompose dioxins at low initial and running costs and / or
Another object of the present invention is to provide a method for detoxifying molten fly ash.

【0004】[0004]

【課題を解決するための手段】上記の目的を達成するた
めに本発明における焼却残渣及び/又は溶融飛灰の無害
化処理方法は、焼却残渣及び/又は溶融飛灰から成る処
理原料に対し二酸化チタンを触媒として添加する工程
と、該二酸化チタンを添加した処理原料をロ−タリ−キ
ルンにより100〜500℃の温度で5〜60分間加熱
攪拌し、もって処理原料中に含まれるダイオキシン類を
二酸化チタンの持つ酸化触媒作用により分解させる工程
と、該ダイオキシン類を分解させた処理物に薬剤及び水
を添加混合させて重金属溶出防止処理する工程と、を具
備することを特徴とするものである。
Means for Solving the Problems In order to achieve the above object, the method for detoxifying incineration residues and / or molten fly ash according to the present invention provides a method for treating a raw material comprising incinerated residues and / or molten fly ash with a carbon dioxide. A step of adding titanium as a catalyst, and heating and stirring the processing raw material to which the titanium dioxide is added by a rotary kiln at a temperature of 100 to 500 ° C. for 5 to 60 minutes to thereby dioxins contained in the processing raw material It is characterized by comprising a step of decomposing by the oxidation catalytic action of titanium, and a step of adding and mixing a chemical and water to the processed product obtained by decomposing the dioxins to prevent elution of heavy metals.

【0005】[0005]

【発明の実施の形態】以下本発明の実施の形態を図面に
基づいて詳しく説明する。図1に示すように焼却残渣及
び/又は溶融飛灰から成る処理原料を原料定量供給装置
1から定量切り出しすると共に切り出しをされた処理原
料に対し二酸化チタンを触媒定量供給装置2から定量供
給する。この際触媒としての二酸化チタンの添加量は
0.5〜10重量%の範囲の量がダイオキシン類(ここ
でダイオキシン類とは、ポリ塩化ジベンゾパラジオキシ
ン類(PCDDs)、ポリ塩化ジベンゾフラン及びコプ
ラナ−PCB(ポリ塩化ビフェニル)のことをいう)完
全分解と共に経済的にも有利である。
Embodiments of the present invention will be described below in detail with reference to the drawings. As shown in FIG. 1, a processing raw material composed of incineration residues and / or molten fly ash is quantitatively cut out from a raw material quantitative supply device 1, and titanium dioxide is quantitatively supplied to the cut out processing raw material from a catalyst quantitative supply device 2. At this time, the amount of titanium dioxide added as a catalyst is in the range of 0.5 to 10% by weight of dioxins (here, dioxins are polychlorinated dibenzoparadioxins (PCDDs), polychlorinated dibenzofurans and coplanar-PCB). It is economically advantageous together with the complete decomposition (refers to polychlorinated biphenyl).

【0006】次に二酸化チタンを添加された処理原料
は、温度を100〜500℃に設定されたロ−タリ−キ
ルンで成る分解装置3に投入されて加熱攪拌される。こ
の際処理原料は、分解装置(ロ−タリ−キルン)3内を
5〜60分間滞留して二酸化チタンの酸化触媒作用によ
り処理原料中に含まれるダイオキシン類が分解され、ダ
イオキシン類の含有量が基準値以下となった処理物とし
て分解装置3から排出される。また分解装置3から発生
した少量の煤塵を含む排ガスは集塵機4で煤塵除去し、
排ガスは図示されない焼却炉内または2次燃焼炉へ戻さ
れ、捕集された煤塵は排出された処理物の中に戻され
る。
Next, the processing raw material to which titanium dioxide has been added is put into a decomposition apparatus 3 composed of a rotary kiln whose temperature is set at 100 to 500 ° C., and is heated and stirred. At this time, the processing raw material stays in the decomposition device (rotary kiln) 3 for 5 to 60 minutes, and the dioxins contained in the processing raw material are decomposed by the oxidation catalytic action of titanium dioxide, and the content of dioxins is reduced. It is discharged from the decomposer 3 as a processed product that has become below the reference value. Exhaust gas containing a small amount of dust generated from the decomposition device 3 is removed by the dust collector 4 so that the dust is removed.
The exhaust gas is returned to an incinerator (not shown) or a secondary combustion furnace, and the collected dust is returned to the discharged processed material.

【0007】次に排出された処理物及び煤塵は、搬送装
置5により重金属溶出防止設備6に搬入され、薬剤及び
水を添加混合して重金属溶出防止処理が施され無害化処
理される。このようにしてダイオキシン類の分解及び重
金属溶出防止等の無害化処理を施された処理物は順次最
終処分場に搬送されて廃棄される。
[0007] The discharged material and dust thus discharged are carried into the heavy metal elution prevention equipment 6 by the transport device 5, where a chemical and water are added and mixed, the heavy metal elution prevention treatment is performed, and the detoxification treatment is performed. The detoxified substances such as the decomposition of dioxins and the prevention of elution of heavy metals are sequentially conveyed to a final disposal site and discarded.

【0008】[0008]

【発明の効果】本発明は上記の説明から明らかなよう
に、焼却残渣及び/又は溶融飛灰から成る処理原料に対
し、安価な二酸化チタンを触媒として添加し、これを所
定温度で所定時間加熱攪拌してダイオキシン類を二酸化
チタンの酸化触媒作用により分解させた後重金属溶出防
止処理を施すものであるから、イニシャルコスト及びラ
ンニングコスト共に低コストでダイオキシン類を分解で
き、焼却残渣及び/又は溶融飛灰の無害化処理を安価に
成し得る効果がある。
As is clear from the above description, according to the present invention, inexpensive titanium dioxide is added as a catalyst to a processing raw material comprising incineration residues and / or molten fly ash, and this is heated at a predetermined temperature for a predetermined time. Since dioxins are agitated to decompose by the catalytic action of oxidation of titanium dioxide and then subjected to a treatment for preventing elution of heavy metals, dioxins can be decomposed at low initial costs and low running costs, resulting in incineration residues and / or melting and flying. There is an effect that the ash can be detoxified at low cost.

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

【図1】本発明を実施する設備の構成図である。FIG. 1 is a configuration diagram of equipment for implementing the present invention.

【符号の説明】[Explanation of symbols]

1 原料定量供給装置 2 触媒定量供給装置 3 分解装置 4 集塵機 5 搬送装置 6 重金属溶出防止設備 Reference Signs List 1 raw material fixed supply device 2 catalyst fixed supply device 3 decomposition device 4 dust collector 5 transfer device 6 heavy metal elution prevention equipment

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2E191 BA02 BA12 BB00 BC01 BD13 3K061 NA01 NA07 4D004 AA36 AA46 AB03 AB07 CA15 CA22 CB09 CB34 CC03 CC09 CC11 DA02 DA03 DA06 DA10 4G069 AA02 BA04A BA04B BB04A BB04B CA04 CA07 CA19 DA05  ────────────────────────────────────────────────── ─── Continued on the front page F-term (reference) 2E191 BA02 BA12 BB00 BC01 BD13 3K061 NA01 NA07 4D004 AA36 AA46 AB03 AB07 CA15 CA22 CB09 CB34 CC03 CC09 CC11 DA02 DA03 DA06 DA10 4G069 AA02 BA04A BA04B BB04A BB0419 CA05 CA07

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 焼却残渣及び/又は溶融飛灰から成る処
理原料に対し二酸化チタンを触媒として添加する工程
と、該二酸化チタンを添加した処理原料をロ−タリ−キ
ルンにより100〜500℃の温度で5〜60分間加熱
攪拌し、もって処理原料中に含まれるダイオキシン類を
二酸化チタンの持つ酸化触媒作用により分解させる工程
と、該ダイオキシン類を分解させた処理物に薬剤及び水
を添加混合させて重金属溶出防止処理する工程と、を具
備することを特徴とする焼却残渣及び/又は溶融飛灰の
無害化処理方法。
1. A process in which titanium dioxide is added as a catalyst to a processing raw material comprising incineration residues and / or molten fly ash, and the processing raw material to which the titanium dioxide is added is heated to 100 to 500 ° C. by a rotary kiln. Heating and stirring for 5 to 60 minutes, thereby decomposing the dioxins contained in the processing raw material by the oxidation catalytic action of titanium dioxide, and adding and mixing a drug and water to the processed product obtained by decomposing the dioxins. A method for detoxifying incineration residues and / or molten fly ash, comprising:
【請求項2】 前記二酸化チタンの添加量を処理原料に
対し、0.5〜10重量%の範囲にすることを特徴とす
る請求項1記載の焼却残渣及び/又は溶融飛灰の無害化
処理方法。
2. The detoxification treatment of incineration residues and / or molten fly ash according to claim 1, wherein the added amount of said titanium dioxide is in the range of 0.5 to 10% by weight based on the raw material to be processed. Method.
JP2000093457A 2000-03-30 2000-03-30 Treatment method for making incineration residue and/or molten fly ash harmless Pending JP2001276771A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000093457A JP2001276771A (en) 2000-03-30 2000-03-30 Treatment method for making incineration residue and/or molten fly ash harmless

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000093457A JP2001276771A (en) 2000-03-30 2000-03-30 Treatment method for making incineration residue and/or molten fly ash harmless

Publications (1)

Publication Number Publication Date
JP2001276771A true JP2001276771A (en) 2001-10-09

Family

ID=18608638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000093457A Pending JP2001276771A (en) 2000-03-30 2000-03-30 Treatment method for making incineration residue and/or molten fly ash harmless

Country Status (1)

Country Link
JP (1) JP2001276771A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010248331A (en) * 2009-04-14 2010-11-04 Vip Corporation:Kk Soil-improving material from burned ash and method for producing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010248331A (en) * 2009-04-14 2010-11-04 Vip Corporation:Kk Soil-improving material from burned ash and method for producing the same

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