JP2000197867A - Decomposition of dioxins in solid - Google Patents
Decomposition of dioxins in solidInfo
- Publication number
- JP2000197867A JP2000197867A JP11002406A JP240699A JP2000197867A JP 2000197867 A JP2000197867 A JP 2000197867A JP 11002406 A JP11002406 A JP 11002406A JP 240699 A JP240699 A JP 240699A JP 2000197867 A JP2000197867 A JP 2000197867A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- dioxins
- added
- ash
- terms
- 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
Links
Landscapes
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、固体中のダイオキ
シン類の分解方法に係り、特に、焼却飛灰、焼却灰、土
壌などの個体中に含まれるダイオキシン類を酸化分解す
る固体中のダイオキシン類の分解方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing dioxins in solids, and more particularly to dioxins in solids which oxidatively decompose dioxins contained in solids such as incinerated fly ash, incinerated ash and soil. And a method for disassembling.
【0002】[0002]
【従来の技術】従来、固体中のダイオキシン類を分解す
る方法は、溶融固化法のように、燃料の燃焼熱や電気か
ら得られた熱エネルギー等により、概ね1200℃以上
の高温条件下で加熱して、被溶融物中の有機物は熱分
解、ガス化、燃焼させ、無機物は溶融状態とし、冷却固
化後スラグとするか、加熱脱塩素化法のように、酸素不
足の条件下で被処理物を概ね400℃に加熱後、再合成
を抑えるため、200℃以下に急冷する方法であり、い
ずれも高温加熱による方法である。これらの方法は、装
置のイニシャルコストも高く、また、加熱に必要とする
熱エネルギーが、多く必要であるという問題点があっ
た。2. Description of the Related Art Conventionally, a method for decomposing dioxins in a solid is a method of heating under a high temperature condition of about 1200 ° C. or more by the heat of combustion of fuel or heat energy obtained from electricity, as in a melt solidification method. The organic matter in the material to be melted is thermally decomposed, gasified, and burned, and the inorganic matter is made into a molten state, and then cooled and solidified into slag, or treated under heat-deficient oxygen conditions, as in the heat dechlorination method. After heating the product to about 400 ° C., it is quenched to 200 ° C. or less in order to suppress resynthesis. These methods have the problems that the initial cost of the apparatus is high and that a large amount of heat energy is required for heating.
【0003】[0003]
【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解決し、固体中(焼却飛灰、焼却灰、土壌
など)に含まれるダイオキシン類を簡便な方法で、しか
も、多大なエネルギーを消費することなく分解すること
ができる固体中のダイオキシン類の分解方法を提供する
ことを課題とする。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art and reduces dioxins contained in solids (incinerated fly ash, incinerated ash, soil, etc.) by a simple method and greatly. It is an object of the present invention to provide a method for decomposing dioxins in a solid, which can be decomposed without consuming much energy.
【0004】[0004]
【課題を解決するための手段】上記課題を解決するため
に、本発明では、ダイオキシン類を含む固体に水を加
え、湿潤状態又はスラリー状態で混練又は撹拌しなが
ら、硫酸第1鉄を前記固体当たりFe換算で0.1wt
%以上添加し、次いで過酸化水素水を前記固体当たりH
2O2換算で1〜10wt%添加して、ダイオキシン類を
分解することを特徴とする固体中のダイオキシン類の分
解方法としたものである。前記分解方法において、ダイ
オキシン類の分解は、常温〜100℃の温度で行うこと
ができる。上記の様に触媒としての硫酸第1鉄は、固体
当たりFe換算で0.1wt%以上で効果があり、酸化
剤としてのH2O2は、固体当たりH2O2換算で1wt%
の添加で効果があった。H2O2はの添加量は、多い程効
果があるが、コスト的な観点から10%以下が適当であ
る。In order to solve the above-mentioned problems, in the present invention, water is added to a solid containing dioxins, and ferrous sulfate is added to the solid while kneading or stirring in a wet state or a slurry state. 0.1wt per Fe conversion
% Or more, and then aqueous hydrogen peroxide is added to the solids based on H
A method for decomposing dioxins in a solid, characterized in that dioxins are decomposed by adding 1 to 10 wt% in terms of 2 O 2 . In the decomposition method, the decomposition of the dioxins can be performed at a temperature of from room temperature to 100 ° C. As described above, ferrous sulfate as a catalyst is effective at 0.1 wt% or more in terms of Fe per solid, and H 2 O 2 as an oxidizing agent is 1 wt% in terms of H 2 O 2 per solid.
Was effective. The more H 2 O 2 is added, the more effective it is, but from the viewpoint of cost, 10% or less is appropriate.
【0005】[0005]
【発明の実施の形態】本発明は、固体中(焼却飛灰、焼
却灰、土壌など)に含まれるダイオキシン類を分解する
ため、触媒として硫酸第1鉄を被処理物当たりFe換算
で0.1%以上添加し、次いで、酸化剤として過酸化水
素水を添加し、固体中に含まれるダイオキシン類を酸化
分解するものである。上記反応は、水を加えて湿潤状態
又はスラリー状態で混練又は撹拌状態で行うが、混練方
法、撹拌方法は限定されず、公知の方法がいずれも使用
できる。本発明によって、固体中(焼却飛灰、焼却灰、
土壌など)に含まれるダイオキシン類が分解する機構は
不明であるが、過酸化水素による酸化の場合、硫酸第1
鉄の添加により、反応が促進されることが1899年H.J.H.
Fentonにより見いだされ(フェントン試薬と呼ばれる)
ていたが、本発明は実験により、常温では分解しにくい
ダイオキシン類も分解できることを見出した。BEST MODE FOR CARRYING OUT THE INVENTION The present invention decomposes dioxins contained in solids (incineration fly ash, incineration ash, soil, etc.), so that ferrous sulfate is used as a catalyst in an amount of 0.1% in terms of Fe per object. At least 1% is added, and then hydrogen peroxide solution is added as an oxidizing agent to oxidatively decompose dioxins contained in the solid. The above reaction is carried out in a wet or slurry state by adding water and kneading or stirring, but the kneading method and stirring method are not limited, and any known method can be used. According to the present invention, in solid (incineration fly ash, incineration ash,
The mechanism by which dioxins contained in soil and the like are decomposed is unknown, but in the case of oxidation with hydrogen peroxide,
The reaction was promoted by the addition of iron in 1899 HJH
Found by Fenton (called Fenton's reagent)
However, experiments have shown that the present invention can also decompose dioxins that are difficult to decompose at room temperature.
【0006】[0006]
【実施例】以下、本発明を実施例により具体的に説明す
るが、本発明はこれらに限定されるものではない。 実施例1 図1に、本発明のダイオキシン類の分解方法を実施する
ための処理フロー図を示す。図1のように、本発明で
は、混練機に、被処理物(固体)2と水3、硫酸第1鉄
・7水塩4及び過酸化水素5を投入し、撹拌しながら混
練するだけで、加熱等の他の手段を必要とせず、ダイオ
キシン類が分解された処理物6が得られる。図1に従っ
て、被処理物(固体)として、シュレッダーダスト(車
を裁断したときに発生する可燃屑)をガス化溶融炉プラ
ントで高温燃焼させ、溶融固化した際に発生したバグフ
ィルタ捕集灰を用いて実施した。捕集灰の組成を表1に
示す。EXAMPLES Hereinafter, the present invention will be described specifically with reference to Examples, but the present invention is not limited thereto. Example 1 FIG. 1 shows a processing flow chart for implementing the method for decomposing dioxins of the present invention. As shown in FIG. 1, in the present invention, an object to be treated (solid) 2, water 3, ferrous sulfate heptahydrate 4, and hydrogen peroxide 5 are put into a kneader and kneaded while stirring. Thus, the processed product 6 in which the dioxins are decomposed can be obtained without requiring other means such as heating and the like. According to FIG. 1, shredder dust (combustible debris generated when a car is cut) is burned at a high temperature in a gasification and melting furnace plant as an object to be processed (solid), and a bag filter ash generated when melted and solidified is removed. Was carried out. Table 1 shows the composition of the collected ash.
【0007】[0007]
【表1】 表1の組成のバグフィルタ捕集灰に、消石灰を20%/
灰添加し、混練しながら、これに硫酸第1鉄・7水塩を
水3倍重量を加えて溶解したものを、Fe換算で2%/
灰添加し、次いで30%H2O2をH2O2100%当たり
3%/灰添加し、1時間加熱なしで反応させた。処理後
のダイオキシン類濃度は、乾燥乾物換算で0.011n
g−TEQ/gに減少していた。[Table 1] 20% slaked lime was added to the bag filter collected ash having the composition shown in Table 1.
While adding ash and kneading, ferrous sulfate heptahydrate dissolved by adding 3 times the weight of water to this was dissolved at 2% / Fe.
Ash was added, then 30% H 2 O 2 was added at 3% / ash per 100% H 2 O 2 and reacted for 1 hour without heating. The dioxin concentration after the treatment was 0.011 n in terms of dry matter.
g-TEQ / g.
【0008】実施例2 実施例1のバグフィルタ捕集灰に、消石灰を20%/灰
添加し混練しながら、これに硫酸第1鉄・7水塩を水2
倍重量を加えて溶解したものを、Fe換算で2%/灰添
加し、次いで、15%H2O2をH2O2100%当たり3
%/灰添加し、1時間、70℃の加熱状態で反応させ
た。処理後のダイオキシン類濃度は、乾燥乾物換算で
0.008ng−TEQ/gに減少していた。Example 2 Slaked lime was added to the ash collected in the bag filter of Example 1 in an amount of 20% / ash and kneaded, and ferrous sulfate / 7 hydrate was added to water 2
The solution dissolved by adding twice the weight was added at 2% / ash in terms of Fe, and then 15% H 2 O 2 was added at 3% per 100% H 2 O 2.
% / Ash was added and reacted for 1 hour in a heating state at 70 ° C. The dioxin concentration after the treatment was reduced to 0.008 ng-TEQ / g in terms of dry matter.
【0009】実施例3 次に、被処理物(固体)として、流動床式都市ごみ焼却
炉バグフィルタ捕集灰を用いて実施した。捕集灰の組成
を表2に示す。Example 3 Next, a fluid bed type municipal solid waste incinerator bag filter collected ash was used as an object to be treated (solid). Table 2 shows the composition of the collected ash.
【表2】 表2の組成のバグフィルタ捕集灰に、硫酸第1鉄・7水
塩を水2倍重量を加えて溶解したものを、Fe換算で2
%/灰添加し、次いで、15%H2O2をH2O2100%
当たり3%/灰添加し、1時間常温状態で反応させた。
処理後のダイオキシン類濃度は、乾燥乾物換算で0.1
7ng−TEQ/gに減少していた。[Table 2] The fermented sulfate heptahydrate added to twice the weight of water and dissolved in the bag filter collected ash having the composition shown in Table 2 was converted to Fe by 2%.
% / Ash added, then 15% H 2 O 2 is replaced with 100% H 2 O 2
3% / ash was added, and the reaction was carried out at room temperature for 1 hour.
The dioxin concentration after the treatment is 0.1% in terms of dry matter.
It was reduced to 7 ng-TEQ / g.
【0010】実施例4 ダイオキシン類を0.22ng−TEQ/g含む土壌
に、硫酸第1鉄・7水塩を水2倍重量を加えて溶解した
ものを、Fe換算で2%/灰添加し、次いで、15%H
2O2をH2O2100%当たり3%/灰添加し、1時間常
温状態で反応させた。処理後のダイオキシン類濃度は、
乾燥乾物換算で0.056ng−TEQ/gに減少して
いた。Example 4 Ferrous sulfate heptahydrate dissolved in a soil containing dioxins in an amount of 0.22 ng-TEQ / g was added twice as much as water, and 2% ash was added in terms of Fe. , Then 15% H
2 O 2 was added in an amount of 3% / ash per 100% of H 2 O 2 and reacted for 1 hour at room temperature. The dioxin concentration after treatment is
It was reduced to 0.056 ng-TEQ / g in terms of dry matter.
【0011】[0011]
【発明の効果】上記の様に、従来の方法では、固体中
(焼却飛灰、焼却灰)に含まれるダイオキシン類の分解
は、溶融固化法及び加熱脱塩素法といった高温状態で分
解させる方法であったものが、本発明では、固体中(焼
却飛灰、焼却灰、土壌など)に含まれるダイオキシン類
を、常温〜100℃の低温で分解することができ、イニ
シャルコストが安価であるとともに、ハンドリングも容
易であり、熱エネルギーも従来方法と比較すれば非常に
少なくてすむ効果が得られた。As described above, in the conventional method, the decomposition of dioxins contained in a solid (incineration fly ash, incineration ash) is performed by a method of decomposing at a high temperature such as a melt solidification method and a heat dechlorination method. However, in the present invention, dioxins contained in solids (incineration fly ash, incineration ash, soil, etc.) can be decomposed at a low temperature of room temperature to 100 ° C., and the initial cost is low, The handling was easy, and the heat energy was very small compared with the conventional method.
【図1】本発明の分解方法を実施するための処理フロー
図。FIG. 1 is a processing flowchart for implementing a decomposition method of the present invention.
1:混練機、2:被処理物(固体)、3:水、4:Fe
SO4・7H2O、5:H2O2、6:処理物1: kneader, 2: processed object (solid), 3: water, 4: Fe
SO 4 · 7H 2 O, 5 : H 2 O 2, 6: treated
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2E191 BA12 BB00 BB01 BC01 BD11 4D004 AA28 AA36 AA37 AA41 AA46 AB07 AC04 CA15 CA36 CB28 CC11 DA03 DA06 ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 2E191 BA12 BB00 BB01 BC01 BD11 4D004 AA28 AA36 AA37 AA41 AA46 AB07 AC04 CA15 CA36 CB28 CC11 DA03 DA06
Claims (2)
湿潤状態又はスラリー状態で混練又は撹拌しながら、硫
酸第1鉄を前記固体当たりFe換算で0.1wt%以上
添加し、次いで過酸化水素水を前記固体当たりH2O2換
算で1〜10wt%添加して、ダイオキシン類を分解す
ることを特徴とする固体中のダイオキシン類の分解方
法。Claims 1. Water is added to a solid containing dioxins,
Kneading or stirring in a wet state or a slurry state, was added over 0.1 wt% of ferrous sulfate in the solid per terms of Fe, then 110 wt.% Aqueous hydrogen peroxide in the solid per H 2 O 2 conversion A method for decomposing dioxins in a solid, the method comprising decomposing dioxins by addition.
00℃の温度で行うことを特徴とする請求項1記載の固
体中のダイオキシン類の分解方法。2. The decomposition of dioxins is carried out at room temperature to 1
The method for decomposing dioxins in a solid according to claim 1, wherein the method is carried out at a temperature of 00 ° C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11002406A JP2000197867A (en) | 1999-01-08 | 1999-01-08 | Decomposition of dioxins in solid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11002406A JP2000197867A (en) | 1999-01-08 | 1999-01-08 | Decomposition of dioxins in solid |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000197867A true JP2000197867A (en) | 2000-07-18 |
Family
ID=11528373
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11002406A Pending JP2000197867A (en) | 1999-01-08 | 1999-01-08 | Decomposition of dioxins in solid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000197867A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006015287A (en) * | 2004-07-02 | 2006-01-19 | Kankyo Eng Co Ltd | Purification treatment method of soil and purification treatment apparatus of soil |
CN102921717A (en) * | 2012-10-19 | 2013-02-13 | 西安建筑科技大学 | In-situ remediation method aiming at dispersible petroleum-contaminated soil |
CN110394351A (en) * | 2019-07-26 | 2019-11-01 | 昆明理工大学 | The Short flow method and its system of dioxin in a kind of degradation flying dust |
-
1999
- 1999-01-08 JP JP11002406A patent/JP2000197867A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006015287A (en) * | 2004-07-02 | 2006-01-19 | Kankyo Eng Co Ltd | Purification treatment method of soil and purification treatment apparatus of soil |
CN102921717A (en) * | 2012-10-19 | 2013-02-13 | 西安建筑科技大学 | In-situ remediation method aiming at dispersible petroleum-contaminated soil |
CN110394351A (en) * | 2019-07-26 | 2019-11-01 | 昆明理工大学 | The Short flow method and its system of dioxin in a kind of degradation flying dust |
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