JP2002326080A - Method for purifying material contaminated by chemical substance - Google Patents

Method for purifying material contaminated by chemical substance

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Publication number
JP2002326080A
JP2002326080A JP2001134237A JP2001134237A JP2002326080A JP 2002326080 A JP2002326080 A JP 2002326080A JP 2001134237 A JP2001134237 A JP 2001134237A JP 2001134237 A JP2001134237 A JP 2001134237A JP 2002326080 A JP2002326080 A JP 2002326080A
Authority
JP
Japan
Prior art keywords
contaminated
purifying
machine
soil
contaminants
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
JP2001134237A
Other languages
Japanese (ja)
Inventor
Masahiro Eguchi
正浩 江口
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.)
Organo Corp
Original Assignee
Organo Corp
Japan Organo Co 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 Organo Corp, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP2001134237A priority Critical patent/JP2002326080A/en
Publication of JP2002326080A publication Critical patent/JP2002326080A/en
Pending legal-status Critical Current

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  • Fire-Extinguishing Compositions (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently and reliably purify material contaminated by a chemical substance, in particular, soil, bottom material and sludge, etc., contaminated by an organic chlorine compound in a short period. SOLUTION: The contaminated soil 2 is dug and is transferred to a two-shaft mixer 4. Subsequently, iron powder 6 is added to the contaminated soil in the two-shaft mixer and the contaminated soil and the iron powder are uniformly stirred and mixed by the two-shaft mixer. Further, a mixed solution 8 of hydrogen peroxide water and sulfuric acid is added to the contaminated soil which is added with the iron powder and the contaminated soil and the mixed solution are uniformly stirred and mixed by the double shaft mixer. Then, after performing the stirring for a fixed period, the contaminated soil is purified.

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、化学物質により汚
染された汚染物(化学物質汚染物)を物理化学的に浄化
する方法に関する。本発明に係る化学物質汚染物の浄化
方法は、例えば有機塩素化合物に汚染された土壌、底
質、汚泥等の浄化に好適に使用される。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for physicochemically purifying contaminants contaminated by a chemical substance (chemical substance contaminants). The method for purifying chemical contaminants according to the present invention is suitably used, for example, for purifying soil, sediment, sludge and the like contaminated with organic chlorine compounds.

【0002】[0002]

【従来の技術】トリクロロエチレン(TCE)、シス−
1,2−ジクロロエチレン(c−DCE)等の有機塩素
化合物は、発癌性物質である疑いがあるため、近年、上
記有機塩素化合物による土壌、地下水等の汚染が大きな
社会問題となっている。
2. Description of the Related Art Trichlorethylene (TCE), cis-
Organochlorine compounds such as 1,2-dichloroethylene (c-DCE) are suspected to be carcinogens, and in recent years, contamination of soil, groundwater, and the like by the organochlorine compounds has become a major social problem.

【0003】従来、有機塩素化合物で汚染された土壌の
処理法としては、汚染土壌の封じ込め処理、汚染土壌の
掘削・封じ込め処理などが主に行われている。また、有
機塩素化合物で汚染された地下水の処理法としては、揚
水曝気と活性炭処理とを組み合わせたポンプ・アンド・
トリート法などが主に行われている。
[0003] Conventionally, as a method for treating soil contaminated with an organic chlorine compound, a process for containing the contaminated soil, a process for excavating and containing the contaminated soil, and the like are mainly performed. In addition, as a method of treating groundwater contaminated with organochlorine compounds, a pump and a pump that combines pumping aeration and activated carbon treatment is used.
The treatment method is mainly used.

【0004】また、近年では、鉄粉を用いた汚染化学物
質の還元的分解処理法、鉄粉および嫌気性微生物を用い
た汚染化学物質の還元的分解処理法が研究されている。
[0004] In recent years, a method for reductive decomposition of pollutant chemicals using iron powder and a method for reductive decomposition of pollutant chemicals using iron powder and anaerobic microorganisms have been studied.

【0005】[0005]

【発明が解決しようとする課題】しかし、前述した汚染
土壌の封じ込め処理法、汚染土壌の掘削・封じ込め処理
法、汚染地下水のポンプ・アンド・トリート処理法は、
汚染化学物質を積極的に分解して無害化する技術ではな
いこと、莫大なコスト、エネルギー、手間を要するこ
と、浄化期間が10〜20年と長いことなどが問題とな
っていた。
However, the above-described methods for contaminating contaminated soil, excavating and contaminating contaminated soil, and pumping and treating contaminated groundwater are described above.
There have been problems in that it is not a technology for actively decomposing polluting chemical substances to make it harmless, that it requires enormous cost, energy and labor, and that the purification period is as long as 10 to 20 years.

【0006】また、近年、汚染土壌を掘削した後、汚染
土壌に鉄粉、酸化剤等の浄化剤を添加して攪拌すること
により、汚染化学物質を分解処理する技術の開発が行わ
れている。しかし、上記技術を実際の汚染土壌に適用し
た場合、特に粘性土、シルト質土、有機性土といった粘
性土壌に適用した場合、従来攪拌に使用されている1軸
混練機やバックホー(ショベルカー)では、汚染土壌と
浄化剤とを均一に混合することができないため、汚染土
壌の浄化効率が実験室での結果に比較して非常に悪いこ
とが問題となっていた。すなわち、上記従来技術では、
フルスケールの処理(現場処理)における浄化効率が、
ラボスケールの処理(実験処理)における浄化効率に比
べて非常に悪かった。
In recent years, a technique for decomposing contaminated chemical substances by excavating contaminated soil, adding a purifying agent such as iron powder and oxidizing agent to the contaminated soil and stirring the contaminated soil has been developed. . However, when the above technology is applied to actual contaminated soil, particularly when applied to cohesive soil such as cohesive soil, silty soil, and organic soil, a single-shaft kneader or backhoe (shovel car) conventionally used for stirring is used. In this method, since the contaminated soil and the purifying agent cannot be uniformly mixed, there has been a problem that the purification efficiency of the contaminated soil is extremely poor as compared with the results obtained in the laboratory. That is, in the above prior art,
Purification efficiency in full-scale processing (on-site processing)
The purification efficiency was very poor compared with the purification efficiency in the laboratory-scale processing (experimental processing).

【0007】本発明は、前述した事情に鑑みてなされた
もので、フルスケールの処理において、化学物質により
汚染された汚染物、特に有機塩素化合物で汚染された土
壌、底質、汚泥等を、短期間で効率よく、かつ確実に浄
化することができる方法を提供することを目的とする。
The present invention has been made in view of the above-mentioned circumstances, and in full-scale treatment, contaminants contaminated by chemical substances, in particular, soil, sediment, and sludge contaminated by organic chlorine compounds are removed. It is an object of the present invention to provide a method that can efficiently and reliably purify in a short period of time.

【0008】[0008]

【課題を解決するための手段】本発明者は、前記目的を
達成するために、トリクロロエチレン、シス−1,2−
ジクロロエチレンなどの有機塩素化合物に汚染された土
壌を浄化する処理方法について検討した。その結果、汚
染土壌に鉄粉、酸化剤等の浄化剤を添加して攪拌するこ
とにより有機塩素化合物を分解処理する場合において、
汚染物および浄化剤を2軸以上の混練ミキサを用いて攪
拌したとき、あるいは汚染物の原位置で汚染物および浄
化剤を地盤改良機を用いて攪拌ときには、汚染土壌が粘
性土、シルト質土、有機性土等の粘性土壌であっても、
汚染土壌と浄化剤とが均一に混合され、フルスケールの
処理において汚染土壌を短期間で効率よく、かつ確実に
浄化できることを見出した。
Means for Solving the Problems To achieve the above object, the present inventors have proposed trichloroethylene, cis-1,2-bis.
A treatment method to purify soil contaminated with organic chlorine compounds such as dichloroethylene was studied. As a result, when decomposing organic chlorine compounds by adding iron powder, a purifying agent such as an oxidizing agent and the like to the contaminated soil and stirring the contaminated soil,
When the contaminants and the purifying agent are agitated using a kneading mixer having two or more axes, or when the contaminants and the purifying agent are agitated at the original position of the contaminants using a ground improvement machine, the contaminated soil may be viscous or silty soil , Even on clayey soils such as organic soils,
The present inventors have found that contaminated soil and a purifying agent are uniformly mixed, and that contaminated soil can be efficiently and reliably purified in a short period of time in a full-scale treatment.

【0009】また、本発明者は、汚染物に金属系触媒を
添加して2軸以上の混練ミキサあるいは地盤改良機で均
一に攪拌混合した後、金属系触媒を添加した汚染物に過
酸化水素水を添加して2軸以上の混練ミキサあるいは地
盤改良機で均一に攪拌混合した場合、金属系触媒と過酸
化水素との接触により発生するヒドロキシルラジカルに
よって、例えば数日程度という短期間で有機塩素化合物
を分解することができることを見出した。
Further, the inventor of the present invention added a metal catalyst to the contaminated material and uniformly stirred and mixed the mixture with a kneading mixer or a ground improvement machine having two or more shafts, and then added hydrogen peroxide to the contaminated material to which the metal catalyst was added. When water is added and uniformly stirred and mixed with a kneading mixer or a ground improvement machine having two or more axes, hydroxyl radicals generated by contact of the metal-based catalyst with hydrogen peroxide cause, for example, a short period of about several days to reduce organic chlorine. It has been found that the compound can be decomposed.

【0010】本発明は、上述した知見に基づいてなされ
たもので、下記に示す第1発明〜第4発明を提供する。 (第1発明)化学物質により汚染された汚染物を浄化す
るに当たり、汚染物および浄化剤を2軸以上の混練ミキ
サを用いて攪拌することを特徴とする化学物質汚染物の
浄化方法。 (第2発明)化学物質により汚染され地中に存在する汚
染物を浄化するに当たり、汚染物の原位置で汚染物およ
び浄化剤を地盤改良機を用いて攪拌することを特徴とす
る化学物質汚染物の浄化方法。 (第3発明)化学物質により汚染された汚染物を浄化す
るに当たり、汚染物に金属系触媒を添加して2軸以上の
混練ミキサを用いて攪拌した後、前記汚染物に過酸化水
素水を添加して2軸以上の混練ミキサを用いて攪拌する
ことを特徴とする化学物質汚染物の浄化方法。 (第4発明)化学物質により汚染され地中に存在する汚
染物を浄化するに当たり、汚染物に原位置で金属系触媒
を添加して地盤改良機を用いて攪拌した後、前記汚染物
に原位置で過酸化水素水を添加して地盤改良機を用いて
攪拌することを特徴とする化学物質汚染物の浄化方法。
[0010] The present invention has been made based on the above findings, and provides the following first to fourth inventions. (1st invention) A method for purifying chemical contaminants, wherein the contaminants and the purifying agent are agitated using a kneading mixer having two or more axes in purifying the contaminants contaminated by the chemical substance. (Second invention) In purifying contaminants contaminated by chemical substances and existing in the ground, the contaminants and the purifying agent are agitated in situ of the contaminants using a ground improvement machine. How to purify things. (Third invention) In purifying contaminants contaminated by a chemical substance, a metal-based catalyst is added to the contaminants, and the mixture is stirred using a kneading mixer having two or more axes. A method for purifying chemical contaminants, comprising adding and stirring using a kneading mixer having two or more axes. (4th invention) In purifying contaminants present in the ground contaminated by chemical substances, a metal-based catalyst is added to the contaminants in situ, and the mixture is stirred using a ground improvement machine. A method for purifying chemical contaminants, comprising adding a hydrogen peroxide solution at a position and stirring the mixture using a ground improvement machine.

【0011】以下、本発明につきさらに詳しく説明す
る。第1および第3発明で用いる2軸以上の混練ミキサ
は、攪拌槽の内部に2本以上の回転軸が並列配置されて
いるとともに、各回転軸に径方向外方に延びる攪拌翼が
複数本設けられ、一方の回転軸に設けられた攪拌翼の回
転範囲が他方の回転軸近傍に及ぶように、2本以上の回
転軸を互いに逆回転させるようにした混練ミキサであ
る。この2軸以上の混練ミキサは、ミキサ内部にデッド
スペースが生じないこと、攪拌力が強く粘性土壌と浄化
剤とを十分均一に混合できることから、第1および第3
発明ではラボスケールの処理と同等の浄化効率を得るこ
とができる。
Hereinafter, the present invention will be described in more detail. The kneading mixer having two or more shafts used in the first and third inventions has two or more rotating shafts arranged in parallel inside a stirring tank and a plurality of stirring blades extending radially outward on each rotating shaft. This is a kneading mixer in which two or more rotating shafts are rotated in opposite directions so that the rotating range of the stirring blade provided on one rotating shaft extends near the other rotating shaft. The kneading mixer having two or more axes has no dead space inside the mixer, and has strong stirring power and can sufficiently mix the viscous soil and the purifying agent.
According to the present invention, it is possible to obtain purification efficiency equivalent to that of a laboratory-scale treatment.

【0012】第2および第4発明で用いる地盤改良機
は、軟弱な地盤にセメント系土質改良材(固化剤)等の
改質剤を添加して攪拌することにより、軟弱な地盤を強
固な地盤に改良する機械である。第2および第4発明で
は、上記地盤改良機によって汚染物の原位置で汚染物お
よび浄化剤を攪拌することにより、汚染物と浄化剤を十
分均一に混合して、ラボスケールの処理と同等の浄化効
率を得ることができる。地盤改良機としては、例えば、
ベースマシンに粉体噴射攪拌翼を装着した混合機械、ベ
ースマシンにトレンチャー型スタビライザーを装着した
混合機械、または泥上車に1軸もしくは2軸垂直式撹拌
処理機を装着した混合機械を好適に用いることができ
る。
[0012] The soil improvement machine used in the second and fourth inventions is to add a modifier such as a cement-based soil conditioner (solidifying agent) to the soft ground and to stir the soft ground to make the solid ground stronger. It is a machine to improve on. In the second and fourth inventions, the contaminant and the purifying agent are agitated at the original position of the contaminant by the ground improvement machine, so that the contaminant and the purifying agent are sufficiently uniformly mixed. Purification efficiency can be obtained. As a ground improvement machine, for example,
A mixing machine in which a powder injection stirrer is installed in a base machine, a mixing machine in which a trencher type stabilizer is installed in a base machine, or a mixing machine in which a single-shaft or two-shaft vertical stirrer is installed in a mud wheel are preferably used. be able to.

【0013】第1および第2発明では、浄化剤として少
なくとも酸化剤(過マンガン酸カリウム、過酸化水素、
過硫酸塩など)または金属系触媒を用いることができ
る。また、第3および第4発明において、金属系触媒と
しては、過酸化水素と接触してヒドロキシルラジカルを
発生させるものを用いる。上記金属系触媒として、具体
的には、鉄粉、硫酸鉄および塩化鉄から選ばれるものを
好適に用いることができる。
In the first and second inventions, at least an oxidizing agent (potassium permanganate, hydrogen peroxide,
Persulfate) or a metal-based catalyst. In the third and fourth aspects of the present invention, a metal-based catalyst that generates hydroxyl radicals by contacting hydrogen peroxide is used. As the metal-based catalyst, specifically, one selected from iron powder, iron sulfate, and iron chloride can be suitably used.

【0014】金属系触媒として鉄粉を使用する場合、鉄
粉の性状に特に限定はないが、粒径が小さく均一な鉄粉
であることが好ましい。また、鉄粉の添加量は化学物質
汚染物の0.01〜1重量%、特に0.05〜0.5重
量%とすることが適当である。
When iron powder is used as the metal-based catalyst, there is no particular limitation on the properties of the iron powder, but it is preferable that the iron powder be small and uniform in particle size. The amount of the iron powder added is suitably 0.01 to 1% by weight, particularly 0.05 to 0.5% by weight of the chemical contaminants.

【0015】金属系触媒として硫酸鉄や塩化鉄を使用す
る場合、これらの溶液を化学物質汚染物に添加すること
が適当である。また、硫酸鉄および塩化鉄の添加量は化
学物質汚染物の0.01〜1重量%、特に0.05〜
0.5重量%とすることが好ましい。
When iron sulfate or iron chloride is used as a metal-based catalyst, it is appropriate to add these solutions to chemical contaminants. Further, the addition amount of iron sulfate and iron chloride is 0.01 to 1% by weight of the chemical contaminants, particularly 0.05 to 1% by weight.
It is preferably 0.5% by weight.

【0016】第3および第4発明において、金属系触媒
を添加した汚染物に過酸化水素水を添加する場合、過酸
化水素水の添加量は100%過酸化水素として、化学物
質汚染物の1.0重量%以下、特に0.1〜0.5重量
%とすることが適当である。過酸化水素水の添加量が1
00%過酸化水素として化学物質汚染物の1.0重量%
を超えても、汚染化学物質の分解効果はそれ以上は改善
されず、浄化費用が高くなることがある。
In the third and fourth aspects of the present invention, when adding aqueous hydrogen peroxide to contaminants to which a metal-based catalyst has been added, the amount of the added hydrogen peroxide water is 100% hydrogen peroxide, and the amount of the chemical contaminants is one. It is suitable that the content is 0.0% by weight or less, particularly 0.1 to 0.5% by weight. The amount of hydrogen peroxide added is 1
1.0% by weight of chemical contaminants as 00% hydrogen peroxide
Beyond this, the effect of decomposing polluting chemicals is not further improved and the cost of purification can be high.

【0017】第3および第4発明では、汚染物に過酸化
水素を添加する前に汚染物に金属系触媒を添加して攪拌
してあるので、過酸化水素が金属系触媒と接触して汚染
化学物質の酸化分解反応が開始される時点で、既に金属
系触媒が汚染物中に均一に存在している。そのため、第
3および第4発明では、過酸化水素が酸素と水に分解し
て無駄に消費されることが抑制され、ヒドロキシルラジ
カルが有効に生成し、汚染化学物質の分解効率が向上し
たものと推測される。また、過酸化水素を添加した後に
さらに汚染物を攪拌することで、汚染化学物質の分解効
率がより向上したものと推測される。
In the third and fourth aspects of the present invention, the metal catalyst is added to the contaminant and stirred before the hydrogen peroxide is added to the contaminant. At the time when the oxidative decomposition reaction of the chemical substance is started, the metal-based catalyst is already uniformly present in the contaminant. Therefore, in the third and fourth inventions, it is suppressed that hydrogen peroxide is decomposed into oxygen and water and is wasted, and hydroxyl radicals are effectively generated, thereby improving the decomposition efficiency of pollutant chemicals. Guessed. Further, it is presumed that the stirring efficiency of the contaminants after the addition of hydrogen peroxide further improved the decomposition efficiency of the contaminant chemicals.

【0018】また、第3および第4発明においては、汚
染物に過酸化水素水と硫酸の混合液を添加して酸性条件
下、好ましくはpH3〜5の条件下で攪拌することがよ
り適当である。これにより、汚染化学物質をさらに効率
的に酸化分解することができる。この場合、酸性条件と
するためには硫酸を用いることが適当である。塩酸は揮
発性が高く、安全性、作業性の面で好ましくない。硝酸
の使用は窒素成分が増加するため好ましくない。有機酸
の使用は酸化の対象となる有機物を不要に多くし、コス
ト的にも高くなるため好ましくない。
In the third and fourth aspects of the present invention, it is more appropriate to add a mixed solution of aqueous hydrogen peroxide and sulfuric acid to the contaminants and stir the mixture under acidic conditions, preferably at pH 3 to 5. is there. This makes it possible to more efficiently oxidatively decompose contaminant chemicals. In this case, it is appropriate to use sulfuric acid in order to obtain acidic conditions. Hydrochloric acid has high volatility and is not preferred in terms of safety and workability. The use of nitric acid is not preferred because the nitrogen component increases. Use of an organic acid is not preferred because it unnecessarily increases the amount of organic substances to be oxidized and increases the cost.

【0019】第1〜第4発明は、有機塩素化合物に汚染
された土壌、底質、汚泥、地下水等の浄化に好適に使用
されるが、これに限定されるものではない。すなわち、
第1〜第4発明は、有機塩素化合物(TCE、PCE、
ダイオキシン類、PCB類など)による汚染物の浄化の
みならず、他の有機物、例えば油、ベンゼン、トルエ
ン、キシレン等による汚染物の浄化にも適用可能であ
る。特に、第3および第4発明は、金属系触媒と過酸化
水素水との接触により発生する酸化力の強いヒドロキシ
ルラジカルによって有機物を酸化分解するため、様々な
有機物を効率的に分解することができる。
The first to fourth inventions are suitably used for purifying soil, sediment, sludge, groundwater, etc., which are contaminated with an organic chlorine compound, but are not limited thereto. That is,
The first to fourth inventions relate to organic chlorine compounds (TCE, PCE,
The present invention is applicable not only to purification of contaminants by dioxins and PCBs, but also to purification of contaminants by other organic substances such as oil, benzene, toluene, xylene and the like. In particular, in the third and fourth inventions, various organic substances can be decomposed efficiently because organic substances are oxidatively decomposed by hydroxyl radicals having strong oxidizing power generated by contact between the metal-based catalyst and aqueous hydrogen peroxide. .

【0020】[0020]

【発明の実施の形態】次に、添付図面を参照して本発明
の実施の形態を説明する。図1は第1および第3発明の
一実施形態を示す図である。本実施形態では、まず、
(a)図に示すように汚染土壌2を掘削し、これを2軸
混練ミキサ4に移す。次に、(b)図に示すように2軸
混練ミキサ4内の汚染土壌2に鉄粉6を添加し、2軸混
練ミキサ4により汚染土壌2と鉄粉6とを均一に攪拌混
合する。さらに、(c)図に示すように鉄粉6を添加し
た汚染土壌2に過酸化水素水と硫酸の混合液8を添加
し、2軸混練ミキサ4により上記汚染土壌2と混合液8
とを均一に攪拌混合する。一定時間(通常2〜60分程
度)攪拌を行うと汚染土壌2が浄化される。ただし、攪
拌終了後も汚染化学物質の酸化分解反応は進行する。そ
の後、(d)図に示すように2軸混練ミキサ4から浄化
土壌10を排出し、(e)図に示すように浄化土壌10
を元の場所に埋め戻す。埋め戻し後、雨水などが混入し
ないように浄化土壌10をビニールシートなどで覆い、
経時的に土をサンプリングして汚染化学物質の浄化状況
をモニタリングする。
Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a diagram showing one embodiment of the first and third inventions. In the present embodiment, first,
(A) As shown in the figure, contaminated soil 2 is excavated and transferred to a biaxial kneading mixer 4. Next, as shown in FIG. 2B, the iron powder 6 is added to the contaminated soil 2 in the twin-screw kneading mixer 4, and the contaminated soil 2 and the iron powder 6 are uniformly stirred and mixed by the twin-screw kneading mixer 4. Further, as shown in FIG. 3C, a mixed solution 8 of a hydrogen peroxide solution and sulfuric acid is added to the contaminated soil 2 to which the iron powder 6 has been added, and the contaminated soil 2 and the mixed solution 8 are mixed by the twin-screw kneading mixer 4.
And stir and mix uniformly. If the stirring is performed for a certain time (usually about 2 to 60 minutes), the contaminated soil 2 is purified. However, the oxidative decomposition reaction of the polluting chemical substance proceeds even after the stirring is completed. Thereafter, the purified soil 10 is discharged from the twin-screw kneading mixer 4 as shown in (d), and the purified soil 10 is discharged as shown in (e).
Back in place. After backfilling, the purified soil 10 is covered with a vinyl sheet or the like so that rainwater etc. will not enter.
Soil is sampled over time to monitor the status of purification of pollutant chemicals.

【0021】本例で用いた2軸混練ミキサ4は、図1
(a)の概略正面図、図2の概略側面図を参照すると、
攪拌槽20の内部に2本の回転軸22a、22bが水平
かつ並列に配置されているとともに、各回転軸22a、
22bに径方向外方に延びる攪拌翼24a、24bが複
数本設けられ、一方の回転軸22aに設けられた攪拌翼
24aの回転範囲が他方の回転軸22b近傍に及ぶよう
に、2本の回転軸22a、22bを互いに逆回転させる
ようにした混練ミキサである。
The biaxial kneading mixer 4 used in the present embodiment is the same as that shown in FIG.
Referring to the schematic front view of (a) and the schematic side view of FIG.
Two rotating shafts 22a, 22b are arranged horizontally and in parallel inside the stirring tank 20, and each rotating shaft 22a, 22b
A plurality of stirring blades 24a and 24b extending radially outward are provided on the rotation shaft 22b, and two rotations are provided so that the rotation range of the stirring blade 24a provided on one rotation shaft 22a extends near the other rotation shaft 22b. This is a kneading mixer in which the shafts 22a and 22b are rotated in opposite directions.

【0022】図3は第2および第4発明の一実施形態を
示す図である。本実施形態では、まず、(a)図に示す
ように汚染土壌30上を適量の鉄粉32で覆った後、ベ
ースマシン34に粉体噴射攪拌翼36を装着した混合機
械(地盤改良機)38を用い、原位置で汚染土壌30と
鉄粉32とを均一に攪拌混合する。次に、(b)図に示
すように鉄粉32を添加した汚染土壌30に過酸化水素
水を添加し、混合機械38により上記汚染土壌30と過
酸化水素水とを均一に攪拌混合する。一定時間(通常2
〜60分程度)攪拌を行うと汚染土壌30が浄化され
る。ただし、攪拌終了後も汚染化学物質の酸化分解反応
は進行する。その後、雨水などが混入しないように浄化
土壌をビニールシートなどで覆い、経時的に土をサンプ
リングして汚染化学物質の浄化状況をモニタリングす
る。
FIG. 3 is a diagram showing one embodiment of the second and fourth inventions. In the present embodiment, first, as shown in FIG. 7A, a mixing machine (ground improvement machine) in which a contaminated soil 30 is covered with an appropriate amount of iron powder 32 and then a powder injection stirring blade 36 is mounted on a base machine 34. 38, the contaminated soil 30 and the iron powder 32 are uniformly stirred and mixed in situ. Next, as shown in FIG. 3 (b), a hydrogen peroxide solution is added to the contaminated soil 30 to which the iron powder 32 has been added, and the mixing machine 38 uniformly mixes the contaminated soil 30 and the hydrogen peroxide solution with stirring. For a certain time (usually 2
When the stirring is performed, the contaminated soil 30 is purified. However, the oxidative decomposition reaction of the polluting chemical substance proceeds even after the stirring is completed. Then, the purified soil is covered with a vinyl sheet or the like so that rainwater or the like is not mixed in, and the soil is sampled over time to monitor the purification status of pollutant chemicals.

【0023】本例で用いた混合機械38は、粉体噴射攪
拌工法による地盤改良機であり、上記粉体噴射攪拌工法
は、軟弱地盤中に粉粒体の改良材を供給し、原位置で強
制的に土と改良材を攪拌混合することにより、土と改良
材を化学的に反応させて、土質性状を安定なものにする
とともに強度を高める工法である。粉体噴射攪拌工法で
は、図4に示した粉体噴射攪拌翼36の概略図を参照す
ると、浄化剤は空気流により搬送され、攪拌翼の付け根
部から翼の回転によって生じる空隙部に吐出される。吐
出された浄化剤は攪拌翼の回転に伴って回転軌跡の全面
に均等に散布され、原位置で土と攪拌混合される。浄化
剤と分離した空気は攪拌軸に沿って軸と土の間隙から地
表に放出される。
The mixing machine 38 used in the present embodiment is a ground improvement machine based on a powder injection stirring method, and the powder injection stirring method supplies an improving material of powder and granular material to soft ground. This method involves forcibly mixing and improving the soil and the improver to chemically react the soil with the improver, thereby stabilizing the soil properties and increasing the strength. In the powder injection stirring method, referring to the schematic view of the powder injection stirring blade 36 shown in FIG. 4, the purifying agent is conveyed by an air flow and discharged from the root of the stirring blade to a gap created by rotation of the blade. You. The discharged purifying agent is evenly spread over the entire rotation trajectory with the rotation of the stirring blade, and is stirred and mixed with the soil at the original position. The air separated from the purifying agent is discharged to the ground surface along the stirring shaft from the gap between the shaft and the soil.

【0024】地盤改良機としては、上述したベースマシ
ンに粉体噴射攪拌翼を装着した混合機械の他に、例えば
図5や図6に示すものを用いることができる。図5の地
盤改良機50は、ベースマシン52にトレンチャー型ス
タビライザー54を装着した混合機械である。図6の地
盤改良機60は、泥上車62に1軸もしくは2軸垂直式
撹拌処理機64を装着した混合機械である。
As the ground improvement machine, for example, the one shown in FIG. 5 or FIG. 6 can be used in addition to the above-described mixing machine in which the powder injection stirring blade is mounted on the base machine. The ground improvement machine 50 of FIG. 5 is a mixing machine in which a trencher-type stabilizer 54 is mounted on a base machine 52. The ground improvement machine 60 of FIG. 6 is a mixing machine in which a one-axis or two-axis vertical stirring processor 64 is mounted on a mud wheel 62.

【0025】[0025]

【実施例】実施例1 200mLのバイアルビンに実汚染粘土150gを入
れ、この土に下記〜に示す条件で鉄粉、過酸化水素
などを添加した後、バイアルビンを密閉して処理実験を
開始した。そして、経時的に各バイアルビンから土を採
取し、溶出トリクロロエチレン(TCE)の濃度をガス
クロマトグラフィーで測定することにより、処理効果に
ついて評価した。下記条件〜の内、およびは汚
染粘土と浄化剤を十分均一に攪拌した例、およびは
汚染粘土と浄化剤を十分均一には攪拌しなかった例であ
る。
Example 1 150 g of real contaminated clay was placed in a 200 mL vial bin, iron powder, hydrogen peroxide, etc. were added to the soil under the following conditions, and the vial bin was sealed to start a processing experiment. did. Then, soil was collected from each vial bin with time, and the concentration of eluted trichloroethylene (TCE) was measured by gas chromatography to evaluate the treatment effect. Among the following conditions 1 and 2, an example in which the contaminated clay and the purifying agent were sufficiently uniformly stirred, and an example in which the contaminated clay and the purifying agent were not sufficiently uniformly stirred.

【0026】(実験条件) ブランク試験 土に水45mLを添加して攪拌した。 鉄粉還元法(5分攪拌) 土に水45mLおよび還元鉄粉5gを添加して5分攪拌
した。 鉄粉還元法(0.5分攪拌) 土に水45mLおよび還元鉄粉5gを添加して0.5分
攪拌した。 鉄粉+過酸化水素水(pH4)(5分攪拌) 土に水45mLおよび鉄粉5gを添加して5分攪拌した
後、過酸化水素水1000mg/kg土および硫酸を添
加して5分攪拌した。 鉄粉+過酸化水素水(pH4)(0.5分攪拌) 土に水45mLおよび鉄粉5gを添加して0.5分攪拌
した後、過酸化水素水1000mg/kg土および硫酸
を添加して0.5分攪拌した。
(Experimental conditions) Blank test 45 mL of water was added to the soil and stirred. Iron powder reduction method (stirring for 5 minutes) 45 mL of water and 5 g of reduced iron powder were added to the soil and stirred for 5 minutes. Iron powder reduction method (0.5 minute stirring) 45 mL of water and 5 g of reduced iron powder were added to the soil and stirred for 0.5 minute. Iron powder + hydrogen peroxide solution (pH 4) (stir for 5 minutes) After adding 45 mL of water and 5 g of iron powder to the soil and stirring for 5 minutes, add 1000 mg / kg of hydrogen peroxide solution and sulfuric acid and stir for 5 minutes. did. Iron powder + aqueous hydrogen peroxide (pH 4) (0.5 minutes stirring) After adding 45 mL of water and 5 g of iron powder to the soil and stirring for 0.5 minutes, 1000 mg / kg of hydrogen peroxide aqueous solution and sulfuric acid were added. And stirred for 0.5 minutes.

【0027】(処理結果)図7に処理結果を示す。と
、およびとの比較から、5分攪拌して汚染粘土と
浄化剤を十分均一に攪拌することで、浄化時間が顕著に
短くなることが明らかとなった。なお、鉄粉および過酸
化水素を用いた酸化処理法は鉄粉還元法に比較して処理
時間が短いこと、鉄粉還元法では中間生成物としてジク
ロロエチレン、ビニルクロライドの蓄積が生じることが
確認された。
(Processing Result) FIG. 7 shows the processing result. From the comparison between and, it was clarified that the stirring time was significantly shortened by stirring the contaminated clay and the cleaning agent sufficiently uniformly by stirring for 5 minutes. In addition, it was confirmed that the oxidation treatment method using iron powder and hydrogen peroxide had a shorter treatment time than the iron powder reduction method, and accumulation of dichloroethylene and vinyl chloride as intermediate products occurred in the iron powder reduction method. Was.

【0028】実施例2 トリクロロエチレンに汚染された1m3の土壌に、鉄粉
20kg、過酸化水素0.5w/v%、および硫酸をp
H4になるように添加し、図1および図2に示した2軸
混練ミキサと、タンクローリー車で各々5分攪拌し処理
を行った。そして、経時的に土を採取し、溶出TCE濃
度をガスクロマトグラフィーで測定することにより、処
理効果について評価した。
Example 2 20 kg of iron powder, 0.5 w / v% of hydrogen peroxide and sulfuric acid were added to 1 m 3 of soil contaminated with trichloroethylene.
H4 was added, and the mixture was stirred for 5 minutes using a two-shaft kneading mixer and a tank truck as shown in FIGS. 1 and 2, respectively. The soil was collected over time, and the eluted TCE concentration was measured by gas chromatography to evaluate the treatment effect.

【0029】(処理結果)図8に処理結果を示す。どち
らの処理でもTCEが分解しているのが確認されたが、
2軸混練ミキサを用いた場合は、タンクローリー車を用
いた場合に較べてより浄化処理性能が高く、ラボテスト
と同等の性能を得られることが明らかとなった。
(Processing Result) FIG. 8 shows the processing result. It was confirmed that TCE was decomposed in both treatments,
It was clarified that when the two-shaft kneading mixer was used, the purification processing performance was higher than when a tank lorry was used, and performance equivalent to a lab test was obtained.

【0030】[0030]

【発明の効果】以上のように、本発明によれば、フルス
ケールの処理において、化学物質により汚染された汚染
物、特に有機塩素化合物で汚染された土壌、底質、汚泥
等を、短期間で効率よく、かつ確実に浄化することがで
きる。また、特に第3および第4発明は、各種の難分解
性化学物質を効率的に分解できるラジカル反応を利用し
ているため、高濃度の複合汚染物の浄化にも有効であ
り、その有用性は極めて大きい。
As described above, according to the present invention, in a full-scale treatment, contaminants contaminated by chemical substances, in particular, soil, sediment, and sludge contaminated by an organic chlorine compound can be removed in a short period of time. Thus, purification can be performed efficiently and reliably. The third and fourth inventions, in particular, utilize a radical reaction that can efficiently decompose various hardly decomposable chemical substances, and are therefore effective for purifying high-concentration complex contaminants. Is extremely large.

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

【図1】第1および第3発明の一実施形態を示す図であ
る。
FIG. 1 is a diagram showing one embodiment of the first and third inventions.

【図2】図1の実施形態で用いた2軸混練ミキサの概略
側面図である。
FIG. 2 is a schematic side view of a twin-screw kneading mixer used in the embodiment of FIG.

【図3】第2および第4発明の一実施形態を示す図であ
る。
FIG. 3 is a diagram showing one embodiment of the second and fourth inventions.

【図4】図3の実施形態で用いた混合機械の粉体噴射攪
拌翼の概略図である。
FIG. 4 is a schematic view of a powder injection stirring blade of the mixing machine used in the embodiment of FIG.

【図5】ベースマシンにトレンチャー型スタビライザー
を装着した混合機械の一例を示す概略図である。
FIG. 5 is a schematic view showing an example of a mixing machine in which a trencher type stabilizer is mounted on a base machine.

【図6】泥上車に1軸もしくは2軸垂直式撹拌処理機を
装着した混合機械の一例を示す概略図である。
FIG. 6 is a schematic view showing an example of a mixing machine in which a one-shaft or two-shaft vertical stirring processor is mounted on a mud carrier.

【図7】実施例1の浄化処理における処理経過日数と溶
出TCE濃度との関係を示すグラフである。
FIG. 7 is a graph showing the relationship between the number of days elapsed in the purification process of Example 1 and the concentration of eluted TCE.

【図8】実施例2の浄化処理における処理経過日数と溶
出TCE濃度との関係を示すグラフである。
FIG. 8 is a graph showing the relationship between the number of days elapsed in the purification process of Example 2 and the concentration of eluted TCE.

【符号の説明】[Explanation of symbols]

2 汚染土壌 4 2軸混練ミキサ 6 鉄粉 8 過酸化水素水と硫酸の混合液 10 浄化土壌 20 攪拌槽 22 回転軸 24 攪拌翼 30 汚染土壌 32 鉄粉 34 ベースマシン 36 粉体噴射攪拌翼 38 地盤改良機 50 地盤改良機 52 ベースマシン 54 トレンチャー型スタビライザー 60 地盤改良機 62 泥上車 64 1軸もしくは2軸垂直式撹拌処理機 2 Contaminated soil 4 Two-axis kneading mixer 6 Iron powder 8 Mixed solution of hydrogen peroxide and sulfuric acid 10 Purified soil 20 Stirrer tank 22 Rotating shaft 24 Stirrer blade 30 Contaminated soil 32 Iron powder 34 Base machine 36 Powder injection stirrer blade 38 Ground Improvement machine 50 Soil improvement machine 52 Base machine 54 Trencher type stabilizer 60 Soil improvement machine 62 Mud car 64 Single-axis or two-axis vertical stirring processor

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 11/06 Fターム(参考) 2E191 BA11 BA12 BA13 BA15 BB01 BC01 BD13 4D004 AA41 AB05 AB06 AB07 AC04 AC07 CA15 CA35 CA36 CB21 CB27 CC09 CC11 CC12 DA20 4D059 AA09 BC02 BF12 BJ07 DA22 DA23 DA24 DA33 DA44 EA05 EB05 4G078 AA02 AB20 BA01 BA07 CA01 CA05 CA12 CA17 DA30 EA20──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 11/06 F term (Reference) 2E191 BA11 BA12 BA13 BA15 BB01 BC01 BD13 4D004 AA41 AB05 AB06 AB07 AC04 AC07 CA15 CA35 CA36 CB21 CB27 CC09 CC11 CC12 DA20 4D059 AA09 BC02 BF12 BJ07 DA22 DA23 DA24 DA33 DA44 EA05 EB05 4G078 AA02 AB20 BA01 BA07 CA01 CA05 CA12 CA17 DA30 EA20

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 化学物質により汚染された汚染物を浄化
するに当たり、汚染物および浄化剤を2軸以上の混練ミ
キサを用いて攪拌することを特徴とする化学物質汚染物
の浄化方法。
1. A method for purifying a chemical contaminant comprising purifying a contaminant contaminated by a chemical substance using a kneading mixer having two or more axes.
【請求項2】 化学物質により汚染され地中に存在する
汚染物を浄化するに当たり、汚染物の原位置で汚染物お
よび浄化剤を地盤改良機を用いて攪拌することを特徴と
する化学物質汚染物の浄化方法。
2. Purification of a contaminant contaminated by a chemical substance and existing in the ground, wherein the contaminant and the purifying agent are agitated in situ of the contaminant using a ground improvement machine. How to purify things.
【請求項3】 地盤改良機として、ベースマシンに粉体
噴射攪拌翼を装着した混合機械、ベースマシンにトレン
チャー型スタビライザーを装着した混合機械、または泥
上車に1軸もしくは2軸垂直式撹拌処理機を装着した混
合機械を用いることを特徴とする請求項2に記載の化学
物質汚染物の浄化方法。
3. As a ground improvement machine, a mixing machine in which a powder injection stirring blade is mounted on a base machine, a mixing machine in which a trencher type stabilizer is mounted on a base machine, or a one-axis or two-axis vertical stirring process on a mud carrier. The method according to claim 2, wherein a mixing machine equipped with a mixing machine is used.
【請求項4】 浄化剤として少なくとも酸化剤または金
属系触媒を用いることを特徴とする請求項1〜3のいず
れか1項に記載の化学物質汚染物の浄化方法。
4. The method for purifying a chemical contaminant according to claim 1, wherein at least an oxidizing agent or a metal catalyst is used as the purifying agent.
【請求項5】 化学物質により汚染された汚染物を浄化
するに当たり、汚染物に金属系触媒を添加して2軸以上
の混練ミキサを用いて攪拌した後、前記汚染物に過酸化
水素水を添加して2軸以上の混練ミキサを用いて攪拌す
ることを特徴とする化学物質汚染物の浄化方法。
5. In purifying contaminants contaminated by a chemical substance, a metal-based catalyst is added to the contaminants and the mixture is stirred using a kneading mixer having two or more axes. A method for purifying chemical contaminants, comprising adding and stirring using a kneading mixer having two or more axes.
【請求項6】 化学物質により汚染され地中に存在する
汚染物を浄化するに当たり、汚染物に原位置で金属系触
媒を添加して地盤改良機を用いて攪拌した後、前記汚染
物に原位置で過酸化水素水を添加して地盤改良機を用い
て攪拌することを特徴とする化学物質汚染物の浄化方
法。
6. In purifying contaminants present in the ground contaminated by a chemical substance, a metal-based catalyst is added to the contaminants in situ, and the mixture is stirred using a ground improvement machine. A method for purifying chemical contaminants, comprising adding a hydrogen peroxide solution at a position and stirring the mixture using a ground improvement machine.
【請求項7】 地盤改良機として、ベースマシンに粉体
噴射攪拌翼を装着した混合機械、ベースマシンにトレン
チャー型スタビライザーを装着した混合機械、または泥
上車に1軸もしくは2軸垂直式撹拌処理機を装着した混
合機械を用いることを特徴とする請求項6に記載の化学
物質汚染物の浄化方法。
7. As a ground improvement machine, a mixing machine in which a powder injection stirring blade is mounted on a base machine, a mixing machine in which a trencher type stabilizer is mounted on a base machine, or a one-axis or two-axis vertical stirring process on a mud carrier. 7. The method according to claim 6, wherein a mixing machine equipped with a mixing machine is used.
【請求項8】 金属系触媒として鉄粉、硫酸鉄および塩
化鉄から選ばれるものを用いることを特徴とする請求項
5〜7のいずれか1項に記載の化学物質汚染物の浄化方
法。
8. The method according to claim 5, wherein a metal catalyst selected from iron powder, iron sulfate and iron chloride is used.
JP2001134237A 2001-05-01 2001-05-01 Method for purifying material contaminated by chemical substance Pending JP2002326080A (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
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Family

ID=18981962

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Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003071425A (en) * 2001-09-05 2003-03-11 Japan Organo Co Ltd Treating method for chemical contaminant
JP2003080223A (en) * 2001-09-13 2003-03-18 Japan Organo Co Ltd Method of treating chemical contaminant
JP2005034696A (en) * 2003-07-16 2005-02-10 Tosoh Corp Treatment method for making object to be treated contaminated by organic halogen compound harmless
JP2006341195A (en) * 2005-06-09 2006-12-21 Japan Organo Co Ltd Method of clarifying organic contaminant
JP2014171955A (en) * 2013-03-08 2014-09-22 Jfe Mineral Co Ltd Purification method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003071425A (en) * 2001-09-05 2003-03-11 Japan Organo Co Ltd Treating method for chemical contaminant
JP2003080223A (en) * 2001-09-13 2003-03-18 Japan Organo Co Ltd Method of treating chemical contaminant
JP2005034696A (en) * 2003-07-16 2005-02-10 Tosoh Corp Treatment method for making object to be treated contaminated by organic halogen compound harmless
JP4701588B2 (en) * 2003-07-16 2011-06-15 東ソー株式会社 A treatment method for detoxifying a workpiece contaminated with an organic halogen compound
JP2006341195A (en) * 2005-06-09 2006-12-21 Japan Organo Co Ltd Method of clarifying organic contaminant
JP4548782B2 (en) * 2005-06-09 2010-09-22 オルガノ株式会社 Purification method for organic pollutants
JP2014171955A (en) * 2013-03-08 2014-09-22 Jfe Mineral Co Ltd Purification method

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