JP2003275734A - Apparatus for removing harmful chemical substance - Google Patents

Apparatus for removing harmful chemical substance

Info

Publication number
JP2003275734A
JP2003275734A JP2002082145A JP2002082145A JP2003275734A JP 2003275734 A JP2003275734 A JP 2003275734A JP 2002082145 A JP2002082145 A JP 2002082145A JP 2002082145 A JP2002082145 A JP 2002082145A JP 2003275734 A JP2003275734 A JP 2003275734A
Authority
JP
Japan
Prior art keywords
chemical substance
iron powder
harmful chemical
enzyme
contaminated
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
JP2002082145A
Other languages
Japanese (ja)
Inventor
Hirokazu Tsuji
博和 辻
Ikkan Ide
一貫 井出
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.)
Obayashi Corp
Original Assignee
Obayashi Corp
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 Obayashi Corp filed Critical Obayashi Corp
Priority to JP2002082145A priority Critical patent/JP2003275734A/en
Publication of JP2003275734A publication Critical patent/JP2003275734A/en
Pending legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To provide a harmful chemical substance-removing apparatus which efficiently removes a harmful chemical substance from an object contaminated with the harmful chemical substance. <P>SOLUTION: Soil 101 contaminated with dioxins is blended with iron powder in an agitating blender 102 and the contaminated soil with which the iron powder is blended is carried to an iron powder recovering apparatus 103. In the iron powder recovering apparatus 103, the iron powder is recovered by an energized electromagnet. Treated soil 106 from which the iron powder is removed is charged into an enzyme tank 107 storing an angular dioxygenase which is developed in a coil bacillus and then is extracted to perform enzyme treatment. By a series of these operations, the dioxins are efficiently removed and are detoxicated. <P>COPYRIGHT: (C)2003,JPO

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、汚染土壌などの汚
染対象から有害化学物質を除去する有害化学物質除去装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a harmful chemical substance removing apparatus for removing harmful chemical substances from a polluted object such as polluted soil.

【0002】[0002]

【背景となる技術】近年、重金属や有機塩素系化合物な
どの有害化学物質の環境中への拡散が社会問題になって
いる。これら有害化学物質の由来は、産業廃棄物、農
薬、殺虫剤、電化製品、プラスチックなど多岐にわたる
が、中でも、産業廃棄物などが原因である場合、特に拡
散性が高く、環境に対する悪影響が強く、一旦土壌や河
川などが汚染されると除去されにくい傾向がある。その
ような有害化学物質には、内分泌撹乱作用を持つとさ
れ、いわゆる環境ホルモンと呼ばれている化学物質があ
る。このような有害化学物質に汚染された、土壌、燃焼
灰、排水、浸出水などの汚染物質から、有害化学物質を
取り除く方法として、溶解などの物理的処理、電気分解
や酸化還元などの化学的処理、微生物による分解などの
生物的処理などが用いられてきた。
BACKGROUND ART In recent years, diffusion of harmful chemical substances such as heavy metals and organic chlorine compounds into the environment has become a social problem. The origin of these harmful chemical substances is industrial waste, pesticides, pesticides, electrical appliances, plastics, etc., but when they are caused by industrial waste, etc., they are particularly highly diffusible and have a strong adverse effect on the environment. Once soil and rivers are contaminated, they tend to be difficult to remove. Such harmful chemical substances include chemical substances called endocrine disruptors, which are so-called environmental hormones. As a method of removing harmful chemical substances from pollutants such as soil, combustion ash, wastewater, and leachate contaminated with such harmful chemical substances, physical treatment such as dissolution, chemical treatment such as electrolysis and redox Treatments, biological treatments such as microbial degradation, etc. have been used.

【0003】例えば、ダイオキシンは、化学物質の製造
工程、廃棄物の焼却、製紙工場、金属製錬所等で副産物
として生成される他に、農薬などにも不純物として混入
している。このダイオキシンで汚染された土壌からダイ
オキシンを無害化するために、微生物による環開裂など
が利用されている。
For example, dioxin is produced as a by-product in chemical substance manufacturing processes, waste incineration, paper mills, metal smelters, etc., and is also mixed as an impurity in pesticides and the like. In order to detoxify dioxin from the soil polluted with dioxin, ring opening by microorganisms and the like are used.

【0004】[0004]

【発明が解決しようとしている課題】しかし、微生物に
よる環開裂のみでは、あまりに時間がかかり過ぎ、温度
管理などの管理負担も大きい。また、化学構造によって
環開裂のしやすさが大きく異なり、塩素基が多いほど環
開裂されにくくなる。そのため、ダイオキシンの無害化
の効率が低いという問題点があった。
However, the ring opening by microorganisms alone takes too much time, and the management burden such as temperature control is heavy. In addition, the easiness of ring cleavage varies greatly depending on the chemical structure, and the more chlorine groups, the more difficult it is for ring cleavage. Therefore, there is a problem that the efficiency of detoxifying dioxin is low.

【0005】そこで、本発明は、有害化学物質で汚染し
ている土壌などの汚染対象から、効率良く有害化学物質
を除去・無害化する有害化学物質除去装置を提供するこ
とを目的としてなされた。
Therefore, the present invention has been made for the purpose of providing a toxic chemical substance removing device for efficiently removing and detoxifying a toxic chemical substance from a polluted object such as soil polluted with the toxic chemical substance.

【0006】[0006]

【課題を解決するための手段】本発明の有害化学物質除
去方法は、有害化学物質を吸着する金属を該有害化学物
質で汚染された汚染対象に混合する混合手段と、前記金
属を、前記汚染対象と混合した後に回収する回収手段
と、前記回収手段により前記金属を回収された後の前記
汚染対象を、酵素によって処理する酵素処理手段と、を
備えることを特徴とする。
A method for removing harmful chemical substances according to the present invention comprises a mixing means for mixing a metal adsorbing a harmful chemical substance with an object to be polluted contaminated with the harmful chemical substance, and the metal for the contamination. It is characterized by comprising: a recovery means for recovering after mixing with the target, and an enzyme treatment means for treating the contaminated object after the metal is recovered by the recovery means with an enzyme.

【0007】また、前記酵素が、下記の式1または式2
の化合物を環開裂することを特徴としてもよい。
In addition, the enzyme is the following formula 1 or formula 2
The compound may be ring-opened.

【式1】 [Formula 1]

【式2】 [Formula 2]

【0008】ただし、RはHまたはハロゲンとする。ま
た、前記ハロゲンが、Clであることを特徴としてもよ
い。また、前記酵素が、アンギュラー・ジオキシゲナー
ゼであることを特徴としてもよい。さらに、前記金属が
鉄であることを特徴としてもよい。また、前記金属を磁
石で回収することを特徴としてもよい。さらに、前記有
害化学物質が、有機塩素化合物であることを特徴として
もよい。また、前記有害化学物質が、ダイオキシンであ
ることを特徴としてもよい。
However, R is H or halogen. Further, the halogen may be Cl. Further, the enzyme may be an angular dioxygenase. Further, the metal may be iron. Further, the metal may be recovered by a magnet. Further, the harmful chemical substance may be an organic chlorine compound. Further, the harmful chemical substance may be dioxin.

【発明の実施の形態】以下、図を参照しながら、本発明
を詳細に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below with reference to the drawings.

【0009】<実施例1>図1は、本発明の有害化学物
質除去装置の全体構成例である。ここでは、有害化学物
質に汚染された汚染対象として、ダイオキシンに汚染さ
れた汚染土101を例にとり、この汚染土101からダ
イオキシンを除去するダイオキシン除去装置の一例を説
明する。この装置は、混合手段として撹拌・混合機10
2を、回収手段として鉄粉回収装置103を備えてい
る。この鉄粉回収装置103は、無端状で回転するベル
トを備え、鉄粉回収装置103の一部の下面が、所定距
離にわたって、ベルトコンベア104と対面すると共
に、他の一部の下面が、鉄粉回収箱105の上方に延び
ている。この鉄粉回収装置103は、ベルトの上に鉄粉
を回収するための磁石として電磁石を利用しており、そ
のベルトは、鉄粉回収箱105の上方以外の部分で通電
されていて、通電部では磁石の機能を果たす。さらに、
この装置は、汚染土101が鉄粉で処理された後の処理
土106から、さらにダイオキシンを環開裂する酵素処
理を行う酵素タンク107を備えている。
<Embodiment 1> FIG. 1 shows an example of the overall configuration of the hazardous chemical substance removing apparatus of the present invention. Here, an example of a dioxin removing device that removes dioxin from the contaminated soil 101 will be described by taking the contaminated soil 101 contaminated with dioxin as an example of a contamination target contaminated with harmful chemical substances. This device is a mixer / mixer 10 as a mixing means.
2 is equipped with an iron powder recovery device 103 as recovery means. The iron powder recovery device 103 includes an endlessly rotating belt, and a lower surface of a part of the iron powder recovery device 103 faces the belt conveyor 104 over a predetermined distance and a lower surface of another part of the iron powder recovery device 103 is made of iron. It extends above the powder recovery box 105. This iron powder recovery device 103 uses an electromagnet as a magnet for recovering iron powder on a belt, and the belt is energized in a portion other than the upper part of the iron powder recovery box 105, and the energization unit Then it fulfills the function of a magnet. further,
This apparatus is equipped with an enzyme tank 107 that further performs an enzyme treatment for ring-cleaving dioxin from the treated soil 106 after the contaminated soil 101 is treated with iron powder.

【0010】まず、ダイオキシンで汚染された汚染土1
01を、撹拌・混合機102中に投入する。さらに、例
えば汚染土101に対し5重量%で、100メッシュの
鉄粉を投入する。撹拌・混合機102中で、汚染土10
1と鉄粉とを、4時間、激しく振盪することにより混合
する。この間に、ダイオキシンは鉄粉に吸着する。
First, contaminated soil 1 contaminated with dioxins
01 is put into the agitator / mixer 102. Further, for example, 100 wt. Contaminated soil 10 in the agitator / mixer 102
1 and iron powder are mixed by vigorous shaking for 4 hours. During this time, dioxin is adsorbed on the iron powder.

【0011】その後、ベルトコンベア104で、鉄粉が
混合した汚染土101を鉄粉回収装置103に運ぶ。鉄
粉回収装置103では、通電された電磁石によって、ベ
ルトコンベア104上の汚染土101から鉄粉のみが吸
着される。鉄粉回収装置103のベルトに吸着された鉄
粉は、回収箱に運ばれるが、その上方のベルトには電流
が流れていないため、磁力が無くなり、鉄粉はベルトか
ら離れ、回収箱105内に落下し、回収される。
Thereafter, the belt conveyor 104 conveys the contaminated soil 101 mixed with the iron powder to the iron powder recovery device 103. In the iron powder recovery device 103, only iron powder is adsorbed from the contaminated soil 101 on the belt conveyor 104 by the energized electromagnet. The iron powder adsorbed on the belt of the iron powder recovery device 103 is carried to the recovery box, but since no electric current flows in the belt above it, the magnetic force disappears, and the iron powder separates from the belt, and inside the recovery box 105. It is dropped and collected.

【0012】ダイオキシンを、ある程度除去された処理
土106は、そのままベルトコンベア104で運ばれ、
次に、酵素処理タンク107に投入され、酵素処理を行
われる。酵素処理タンク107は、以下のように準備さ
れる。まず、テラバクター属細菌DBF63株から単離
されたアンギュラー・ジオキシゲナーゼ遺伝子DbfA1A2
を、例えば、pET(商品名)のような大腸菌の発現ベク
ターにクローニングし、pET-DfbA1A2と名付ける。pETベ
クターは、IPTG誘導性のT7lac promoterにより、その下
流に挿入されたDfbA1A2の発現を誘導することができ
る。pETベクターの形質転換には、T7 RNAポリメラーゼ
を供給できる大腸菌株、例えばTuner(DE3)pLacI株
(商品名)等を用いる。
The treated soil 106 from which dioxin has been removed to some extent is conveyed as it is on the belt conveyor 104,
Next, it is put into the enzyme treatment tank 107 and subjected to the enzyme treatment. The enzyme treatment tank 107 is prepared as follows. First, the angular dioxygenase gene DbfA1A2 isolated from the Terrabacter bacterium DBF63 strain
Is cloned into an E. coli expression vector such as pET (trade name), and named pET-DfbA1A2. The pET vector can induce the expression of DfbA1A2 inserted downstream thereof by the IPTG-inducible T7lac promoter. For transformation of the pET vector, an Escherichia coli strain capable of supplying T7 RNA polymerase, for example, Tuner (DE3) pLacI strain (trade name) is used.

【0013】pET-DfbA1A2で形質転換したTuner(DE3)p
LacI株を、Novagen社が推奨するプロトコールに従って
大量培養し、IPTGを添加することによりDbfA1A2を発現
させると、大腸菌内でアンギュラー・ジオキシゲナーゼ
が合成される。ホモゲナイザー(homogenizer、すりつ
ぶし器)やソニケーター(sonicator、超音波処理器)
などで、大腸菌を粉砕し、遠心分離などで、細胞残渣な
どを除去すると、アンギュラー・ジオキシゲナーゼを多
量に含んだ培養液が得られる。
Tuner (DE3) p transformed with pET-DfbA1A2
The LacI strain is mass-cultured according to the protocol recommended by Novagen, and when DbfA1A2 is expressed by adding IPTG, angular dioxygenase is synthesized in Escherichia coli. Homogenizer (homogenizer) and sonicator (sonicator)
Escherichia coli is pulverized with, for example, and cell debris is removed by centrifugation or the like to obtain a culture solution containing a large amount of angular dioxygenase.

【0014】このようにして得られた培養液を酵素処理
タンク107内に入れた後、鉄粉を用いてダイオキシン
がある程度除去された処理土106を投入する。そし
て、酵素処理タンク107内の培養液は、18時間、3
0℃に維持され、穏やかに撹拌されることにより、ダイ
オキシンはアンギュラー・ジオキシゲナーゼによって無
害化される。
After the culture solution thus obtained is placed in the enzyme treatment tank 107, treated soil 106 from which dioxin has been removed to some extent using iron powder is introduced. The culture solution in the enzyme treatment tank 107 is kept for 3 hours for 18 hours.
Dioxins are detoxified by angular dioxygenase by maintaining at 0 ° C. and gently stirring.

【0015】ダイオキシンを無害化する際、酵素を用い
た酵素処理だけでは、ダイオキシン分子が塩素原子を多
くもつほど環開裂されにくい傾向がある。逆に、ダイオ
キシン分子が鉄に吸着する場合、ダイオキシン分子が塩
素原子を多く持つほど吸着しやすい傾向にある。そこ
で、これらの方法を順次行うことにより、あらゆる種類
のダイオキシンが容易に除去・無害化されるようにな
る。
In detoxifying dioxin, ring-opening tends to be less likely to occur as the number of chlorine atoms in the dioxin molecule is increased only by enzymatic treatment with an enzyme. On the contrary, when a dioxin molecule is adsorbed on iron, the more dioxin molecules have chlorine atoms, the easier it is to adsorb. Therefore, by sequentially performing these methods, all kinds of dioxins can be easily removed and rendered harmless.

【0016】<実施例2>図2は、本発明の有害化学物
質除去装置の別の全体構成例である。ここでは、有害化
学物質に汚染された汚染対象として、ダイオキシンに汚
染された汚染水を例にとり、この汚染水からダイオキシ
ンを除去するダイオキシン除去装置の一例を説明する。
この装置は、カラム201の両端に、例えば100メッ
シュの鉄粉の径より小さい孔径をもつフィルター202
が装着されており、中には鉄粉のみが充填されている。
<Embodiment 2> FIG. 2 shows another example of the entire structure of the hazardous chemical substance removing apparatus of the present invention. Here, as an object to be polluted with harmful chemical substances, contaminated water contaminated with dioxin will be taken as an example, and an example of a dioxin removing device for removing dioxin from this contaminated water will be described.
This device has a filter 202 having a pore size smaller than that of iron powder of 100 mesh on both ends of a column 201.
Is installed, and is filled only with iron powder.

【0017】このカラムの中を、ダイオキシンで汚染さ
れた汚染水を通し、汚染水中のダイオキシンを鉄粉に吸
着させることにより、汚染水からダイオキシンをある程
度除去することができる。
Dioxin in the contaminated water can be removed to some extent by passing contaminated water contaminated with dioxin through this column and adsorbing the dioxin in the contaminated water to the iron powder.

【0018】その後、鉄粉で処理された処理水を、実施
例1と同様に、アンギュラー・ジオキシゲナーゼを多量
に含んだ培養液の入った酵素処理タンク107に投入
し、酵素処理を行う。
After that, the treated water treated with iron powder is put into the enzyme treatment tank 107 containing the culture solution containing a large amount of angular dioxygenase in the same manner as in Example 1 to perform the enzyme treatment.

【0019】この実施例においても、鉄による処理後、
酵素処理を順次行うことにより、あらゆる種類のダイオ
キシンが容易に除去・無害化されるようになるのは、実
施例1と同様である。
Also in this example, after the treatment with iron,
As in Example 1, it is possible to easily remove and detoxify all kinds of dioxins by sequentially performing the enzyme treatment.

【0020】<その他の実施例>上記の実施例では、汚
染対象として土と水を例に挙げたが、本発明は、焼却灰
などの灰や、砂などにも適用可能である。
<Other Embodiments> In the above embodiments, soil and water have been taken as examples of the objects to be contaminated, but the present invention is also applicable to ash such as incinerated ash and sand.

【0021】また、ダイオキシンを吸着する金属は鉄粉
を例に挙げたが、金属性磁石、例えば鉄製磁石でも構わ
ず、その場合、磁石を回収するのは、磁石だけでなく、
鉄などの磁石に吸着する金属でも構わない。
Although iron powder is taken as an example of the metal that adsorbs dioxin, a metal magnet, for example, an iron magnet may be used. In that case, not only the magnet but also the magnet is recovered.
A metal such as iron that attracts a magnet may be used.

【0022】ダイオキシンを吸着する鉄粉の粒子の大き
さとして、上記例では100メッシュのものを用いた。
吸着効率と回収効率のバランスを考えると、60〜30
0メッシュのものが好ましいが、特に形や大きさは限定
されない。
The size of iron powder particles that adsorb dioxin was 100 mesh in the above example.
Considering the balance between adsorption efficiency and recovery efficiency, 60-30
It is preferably 0 mesh, but the shape and size are not particularly limited.

【0023】鉄粉の添加率は、5%としたが、吸着効率
から、1から10%が好ましい。
The addition rate of iron powder was set to 5%, but it is preferably 1 to 10% from the viewpoint of adsorption efficiency.

【0024】また、ダイオキシンを吸着した鉄を回収す
るのに、電磁石を用いたが、それに限らず、金属製磁石
でもプラスチック磁石でも構わない。
Although an electromagnet is used to recover the iron that has adsorbed dioxin, the invention is not limited to this, and a metal magnet or a plastic magnet may be used.

【0025】ダイオキシンを環開裂するための酵素は、
テラバクター属細菌DBF63株から単離されたアンギ
ュラー・ジオキシゲナーゼ遺伝子DbfA1A2を用いて生産
したが、シュードモナス属DB10株から単離されたジ
オキシゲナーゼ遺伝子を用いて生産しても構わないし、
有害化学物質を分解できる他の酵素でも構わない。
The enzyme for ring opening of dioxin is
Although it was produced using the angular dioxygenase gene DbfA1A2 isolated from the Terrabactor bacterium DBF63 strain, it may be produced using the dioxygenase gene isolated from the Pseudomonas strain DB10 strain,
Other enzymes that can decompose harmful chemical substances may be used.

【0026】また、ジオキシゲナーゼ遺伝子を大腸菌内
で発現させ、ジオキシゲナーゼを生産する方法は、ここ
で用いた pETベクターの系に限らず、pGEX(商品名)や
pFLAG(商品名)などの大腸菌の発現ベクターを用いて
も良く、宿主菌も、ベクターに適合した菌を用いればよ
い。
The method for producing the dioxygenase by expressing the dioxygenase gene in E. coli is not limited to the pET vector system used here, but pGEX (trade name) and
An E. coli expression vector such as pFLAG (trade name) may be used, and a host bacterium may be a bacterium compatible with the vector.

【0027】ジオキシゲナーゼを生産するのに、ここで
は大腸菌内でジオキシゲナーゼ遺伝子を発現させる方法
を用いたが、ジオキシゲナーゼなどの酵素を発現させる
菌は大腸菌に限らず、また、ジオキシゲナーゼ等の酵素
をコードする遺伝子を固有に有する細菌を増殖させ、酵
素の発現を誘導することによって酵素を生産しても良
い。
Although a method of expressing the dioxygenase gene in Escherichia coli was used to produce dioxygenase, the bacterium expressing the enzyme such as dioxygenase is not limited to Escherichia coli, and the enzyme such as dioxygenase is also used. The enzyme may be produced by proliferating a bacterium having a gene encoding the enzyme and inducing the expression of the enzyme.

【0028】また、ジオキシゲナーゼ等の酵素を微生物
から抽出せず、酵素を発現している微生物をダイオキシ
ンなどの有害化学物質と混合することにより、有害化学
物質を分解しても良い。
It is also possible to decompose the harmful chemical substance by mixing the microorganism expressing the enzyme with a harmful chemical substance such as dioxin without extracting the enzyme such as dioxygenase from the microorganism.

【0029】前記有害化学物質は、ダイオキシンに限ら
ず、トリクロロエチレンなどの塩素基を持つ有機塩素化
合物でも良いし、さらに有機塩素化合物以外の有害化学
物質でもよい。
The toxic chemical substance is not limited to dioxins, and may be an organochlorine compound having a chlorine group such as trichlorethylene, or a toxic chemical substance other than the organochlorine compound.

【0030】以上、本発明にかかる他の実施例について
も述べたが、本発明の目的、特徴、利点及びそのアイデ
アは、本明細書の記載により当業者には明らかである。
従って、以上の発明の実施の形態の項の記載及び具体的
な実施例などの記載は、本発明の好ましい態様を示すも
のであり、説明のためにのみここにおいて示されている
ものであることは理解されるべきであり、本明細書で開
示されている本発明の意図並びに範囲内で、様々な改変
並びに修飾は、それらの記載に基づいて当業者には明ら
かであろう。
Although other embodiments according to the present invention have been described above, the objects, features, advantages and ideas of the present invention will be apparent to those skilled in the art from the description of this specification.
Therefore, the above description of the embodiments of the invention and the description of specific examples and the like show preferred embodiments of the present invention, and are presented here only for the purpose of explanation. It should be understood that, within the spirit and scope of the invention disclosed herein, various alterations and modifications will be apparent to those skilled in the art based on their description.

【0031】[0031]

【発明の効果】本発明は、有害化学物質で汚染している
土壌などの汚染対象から、効率良く有害化学物質を除去
・無害化する有害化学物質除去装置を提供することを目
的としてなされた。
The present invention has been made for the purpose of providing a toxic chemical substance removing device for efficiently removing and detoxifying a toxic chemical substance from a polluted object such as soil polluted with the toxic chemical substance.

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

【図1】本発明の一実施例による、有害化学物質除去装
置の全体構成図である。
FIG. 1 is an overall configuration diagram of a hazardous chemical substance removing device according to an embodiment of the present invention.

【図2】本発明の他の一実施例による、有害化学物質除
去装置の全体構成図である。
FIG. 2 is an overall configuration diagram of a hazardous chemical substance removing device according to another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

101 汚染土 102 撹拌・混合機 103 鉄粉回収装置 104 ベルトコンベア 105 回収箱 106 鉄粉により処理された処理土 107 酵素処理タンク 201 カラム 202 フィルター 101 Contaminated soil 102 Stirrer / Mixer 103 Iron powder recovery device 104 belt conveyor 105 Collection Box 106 Treated soil treated with iron powder 107 enzyme treatment tank 201 column 202 filter

───────────────────────────────────────────────────── 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) B09C 1/08 A62D 3/00 ZAB 4G066 C02F 1/28 C12N 9/02 1/58 B09B 3/00 304K C12N 15/09 5/00 S // A62D 3/00 ZAB C12N 15/00 A C12N 9/02 (71)出願人 502101777 羽部 浩 東京都北区岸町2−9−17 ライオンズマ ンション東十条第3 307号室 (72)発明者 辻 博和 東京都清瀬市下清戸4丁目640番地 株式 会社大林組技術研究所内 (72)発明者 井出 一貫 東京都清瀬市下清戸4丁目640番地 株式 会社大林組技術研究所内 Fターム(参考) 4B024 AA03 AA17 BA08 CA02 DA06 4B050 CC03 DD02 FF01 LL05 4D004 AA16 AA36 AA41 AB07 CA09 CA15 CA20 CA47 CC07 CC11 4D024 AA10 AB11 BA14 BB01 BC01 CA01 DB18 4D038 AA10 AB14 BA04 BB06 4G066 AA02B BA20 CA33 DA08─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) B09C 1/08 A62D 3/00 ZAB 4G066 C02F 1/28 C12N 9/02 1/58 B09B 3/00 304K C12N 15/09 5/00 S // A62D 3/00 ZAB C12N 15/00 A C12N 9/02 (71) Applicant 502101777 Hiroshi Habe 2-9-17 Kishimachi, Kita-ku, Tokyo Lions Mansion Higashijujo 3 Room 307 (72) Hirokazu Tsuji 4-640 Shimo-Seido, Kiyose-shi, Tokyo Inside the Obayashi Technical Research Institute Co., Ltd. (72) Inventor, consistently, 4-640 Shimo-Seido, Kiyose-shi Tokyo Metropolitan Institute F-Term (Obayashi Technical Research Institute) Reference) 4B024 AA03 AA17 BA08 CA02 DA06 4B050 CC03 DD02 FF01 LL05 4D004 AA16 AA36 AA41 AB07 CA09 CA15 CA20 CA47 CC07 CC11 4D024 AA10 AB11 BA14 B B01 BC01 CA01 DB18 4D038 AA10 AB14 BA04 BB06 4G066 AA02B BA20 CA33 DA08

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 有害化学物質を吸着する金属を該有害化
学物質で汚染された汚染対象に混合する混合手段と、 前記金属を、前記汚染対象と混合した後に回収する回収
手段と、 前記回収手段により前記金属を回収された後の前記汚染
対象を、酵素によって処理する酵素処理手段と、 を備えることを特徴とする有害化学物質除去装置。
1. A mixing means for mixing a metal that adsorbs a harmful chemical substance with a contamination target contaminated with the harmful chemical substance, a recovery means for recovering the metal after mixing with the contamination target, and the recovery means. An apparatus for removing a harmful chemical substance, comprising: an enzyme treatment unit that treats the contamination target after the metal is recovered by an enzyme.
【請求項2】 前記酵素が、下記の式1または式2の化
合物を環開裂することを特徴とする請求項1に記載の有
害化学物質除去装置。 【式1】 【式2】 ただし、RはHまたはハロゲンとする。
2. The hazardous chemical substance removing device according to claim 1, wherein the enzyme ring-opens a compound of the following formula 1 or formula 2. [Formula 1] [Formula 2] However, R is H or halogen.
【請求項3】 前記ハロゲンが、Clであることを特徴と
する請求項2に記載の有害化学物質除去装置。
3. The hazardous chemical substance removing device according to claim 2, wherein the halogen is Cl.
【請求項4】 前記酵素が、アンギュラー・ジオキシゲ
ナーゼであることを特徴とする請求項1から3のいずれ
かに記載の有害化学物質除去装置。
4. The hazardous chemical substance removing device according to claim 1, wherein the enzyme is an angular dioxygenase.
【請求項5】 前記金属が鉄であることを特徴とする請
求項1から4のいずれかに記載の有害化学物質除去装
置。
5. The harmful chemical substance removing device according to claim 1, wherein the metal is iron.
【請求項6】 前記金属を磁石で回収することを特徴と
する請求項1から5のいずれかに記載の有害化学物質除
去装置。
6. The hazardous chemical substance removing device according to claim 1, wherein the metal is recovered by a magnet.
【請求項7】 前記有害化学物質が、有機塩素化合物で
あることを特徴とする請求項1〜6のいずれかに記載の
有害化学物質除去装置。
7. The harmful chemical substance removing apparatus according to claim 1, wherein the harmful chemical substance is an organic chlorine compound.
【請求項8】 前記有害化学物質が、ダイオキシンであ
ることを特徴とする請求項1〜7のいずれかに記載の有
害化学物質除去装置。
8. The harmful chemical substance removing apparatus according to claim 1, wherein the harmful chemical substance is dioxin.
JP2002082145A 2002-03-22 2002-03-22 Apparatus for removing harmful chemical substance Pending JP2003275734A (en)

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102872972A (en) * 2012-10-26 2013-01-16 昆山特力伯传动科技有限公司 Conveyer belt metal sundry removing and automatic degaussing device
CN103962371A (en) * 2014-05-12 2014-08-06 福建工程学院 Nondestructive restoration method for polluted soil
JP2018069143A (en) * 2016-10-27 2018-05-10 高崎 三晴 Processing system of heavy metal contaminated soil and processing method of heavy metal contaminated soil

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4985660A (en) * 1972-12-23 1974-08-16
JPH05269402A (en) * 1992-03-25 1993-10-19 Taiyo Yuden Co Ltd Apparatus for fractionating magnetic component
JPH0685044U (en) * 1993-05-26 1994-12-06 住友金属工業株式会社 Iron recovery equipment from incineration ash
JPH0938521A (en) * 1995-07-26 1997-02-10 Murata Mfg Co Ltd Fractionation device and fractionation method
JPH10263522A (en) * 1997-03-27 1998-10-06 Dowa Mining Co Ltd Treatment for making organic halogen compound harmless
JP2000140827A (en) * 1998-11-05 2000-05-23 Kansai Shingijutsu Kenkyusho:Kk Method for recovering material in water or soil with high water content and adsorptive composition used in aforementioned method
JP2001079352A (en) * 1999-07-09 2001-03-27 Toda Kogyo Corp Treatment of exhaust gas containing dioxin and combined catalyst for controlling dioxin
JP2001149775A (en) * 1999-11-25 2001-06-05 Ishihara Sangyo Kaisha Ltd Removing method of harmful material
JP2001232346A (en) * 2000-02-24 2001-08-28 Idemitsu Kosan Co Ltd Cleaning method for soil or water contaminated with chlorinated dioxin
JP2001252646A (en) * 2000-03-14 2001-09-18 Idemitsu Kosan Co Ltd Method for decomposing dioxins
JP2001300507A (en) * 2000-04-21 2001-10-30 Taisei Corp Method for recovering toxic chemicals in soil or the like
JP2002028480A (en) * 2000-07-13 2002-01-29 Nippon Steel Corp Adsorbing removing method and decomposing method of organic chlorine compound
JP2002066531A (en) * 2000-08-25 2002-03-05 Taisei Corp Method for cleaning contaminated soil
JP2002065268A (en) * 2000-08-30 2002-03-05 Ohbayashi Corp Oxygenase gene derived from microorganism, and method for degrading dioxin using enzyme encoded by the gene

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4985660A (en) * 1972-12-23 1974-08-16
JPH05269402A (en) * 1992-03-25 1993-10-19 Taiyo Yuden Co Ltd Apparatus for fractionating magnetic component
JPH0685044U (en) * 1993-05-26 1994-12-06 住友金属工業株式会社 Iron recovery equipment from incineration ash
JPH0938521A (en) * 1995-07-26 1997-02-10 Murata Mfg Co Ltd Fractionation device and fractionation method
JPH10263522A (en) * 1997-03-27 1998-10-06 Dowa Mining Co Ltd Treatment for making organic halogen compound harmless
JP2000140827A (en) * 1998-11-05 2000-05-23 Kansai Shingijutsu Kenkyusho:Kk Method for recovering material in water or soil with high water content and adsorptive composition used in aforementioned method
JP2001079352A (en) * 1999-07-09 2001-03-27 Toda Kogyo Corp Treatment of exhaust gas containing dioxin and combined catalyst for controlling dioxin
JP2001149775A (en) * 1999-11-25 2001-06-05 Ishihara Sangyo Kaisha Ltd Removing method of harmful material
JP2001232346A (en) * 2000-02-24 2001-08-28 Idemitsu Kosan Co Ltd Cleaning method for soil or water contaminated with chlorinated dioxin
JP2001252646A (en) * 2000-03-14 2001-09-18 Idemitsu Kosan Co Ltd Method for decomposing dioxins
JP2001300507A (en) * 2000-04-21 2001-10-30 Taisei Corp Method for recovering toxic chemicals in soil or the like
JP2002028480A (en) * 2000-07-13 2002-01-29 Nippon Steel Corp Adsorbing removing method and decomposing method of organic chlorine compound
JP2002066531A (en) * 2000-08-25 2002-03-05 Taisei Corp Method for cleaning contaminated soil
JP2002065268A (en) * 2000-08-30 2002-03-05 Ohbayashi Corp Oxygenase gene derived from microorganism, and method for degrading dioxin using enzyme encoded by the gene

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
G. SCHREINER ET AL, CHEMOSPHERE, vol. Vol34, Nos5-7, JPN6009027141, 1997, pages 1315 - 1331, ISSN: 0001336538 *
H HABE ET AL, APPLIED AND ENVIROMENTAL MICROBIOLOGY, vol. 67, no. 8, JPN6009026970, 2001, pages 3610 - 3617, ISSN: 0001336539 *
R M WITTICH: "Degradation of dioxin-like compounds by microorganisms", APPL MICROBIOL BIOTECHNOL, vol. 49, JPN6009026966, 1998, pages 489 - 499, ISSN: 0001336537 *
羽部浩他: "鉄粉と微生物を併用したダイオキシン汚染土壌の処理", 2002年度日本農芸化学会大会講演要旨集, JPN6007004904, 5 March 2002 (2002-03-05), JP, pages 234, ISSN: 0000917836 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102872972A (en) * 2012-10-26 2013-01-16 昆山特力伯传动科技有限公司 Conveyer belt metal sundry removing and automatic degaussing device
CN103962371A (en) * 2014-05-12 2014-08-06 福建工程学院 Nondestructive restoration method for polluted soil
JP2018069143A (en) * 2016-10-27 2018-05-10 高崎 三晴 Processing system of heavy metal contaminated soil and processing method of heavy metal contaminated soil

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