JP2002086129A - Method for purifying contaminated soil - Google Patents

Method for purifying contaminated soil

Info

Publication number
JP2002086129A
JP2002086129A JP2000283589A JP2000283589A JP2002086129A JP 2002086129 A JP2002086129 A JP 2002086129A JP 2000283589 A JP2000283589 A JP 2000283589A JP 2000283589 A JP2000283589 A JP 2000283589A JP 2002086129 A JP2002086129 A JP 2002086129A
Authority
JP
Japan
Prior art keywords
soil
dioxins
dioxin
contaminated
hot water
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.)
Granted
Application number
JP2000283589A
Other languages
Japanese (ja)
Other versions
JP4315584B2 (en
Inventor
Seiji Otsuka
誠治 大塚
Hiroyuki Hagiwara
弘之 萩原
Hiroyuki Yamamoto
博之 山本
Takeshi Sasakura
剛 笹倉
Michitaka Okamoto
道孝 岡本
Tatsuji Kawai
達司 河合
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.)
Kajima Corp
Original Assignee
Kajima Corp
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Filing date
Publication date
Application filed by Kajima Corp filed Critical Kajima Corp
Priority to JP2000283589A priority Critical patent/JP4315584B2/en
Publication of JP2002086129A publication Critical patent/JP2002086129A/en
Application granted granted Critical
Publication of JP4315584B2 publication Critical patent/JP4315584B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To reform soil a surface layer of which is contaminated with low concentration of dioxins to soil with lower concentration of the dioxins by simple treatment of low cost. SOLUTION: In a method for purifying contaminated soil, the soil with lower concentration of dioxins is obtained via a stage in which the soil contaminated with the dioxins is gathered from an original position and is washed with hot water and a stage in which muddy water accompanied with the dioxins is separated from the soil.

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,ダイオキシン類で
汚染された土壌の浄化方法に関する。
[0001] The present invention relates to a method for purifying soil contaminated with dioxins.

【0002】[0002]

【従来の技術】ごみ焼却場などから発生するダイオキシ
ン類は猛毒物質であるばかりでなく,いわゆる環境ホル
モンとして人体に生理的な害を及ぼす物質であり,その
発生は深刻な社会問題となっている。焼却場からの発生
に関しては国の規制もあり,焼却炉の改善等によって今
後の発生は抑制されるであろうが,すでに環境中に飛散
してしまったダイオキシン類によって汚染された土壌に
ついては,その浄化処理が必要である。
2. Description of the Related Art Dioxins generated from garbage incineration plants are not only highly toxic substances but also so-called environmental hormones that cause physiological harm to the human body, and their generation is a serious social problem. . There is a national regulation on incinerator emissions, and future incineration will be curbed by improvements to incinerators. However, soil contaminated by dioxins that have already scattered into the environment will The purification process is necessary.

【0003】従来よりダイオキシン類に汚染された土壌
の無害化技術には高温熱処理法が多く用いられてきた
が,最近では,汚染土壌に電極を差し込んで高熱を発生
させ,溶岩のように土壌を溶融固化する方法(溶融固化
法)や,汚染土壌に触媒やアルカリを加えて高熱をかけ
てダイオキシンを分解する方法(アルカリ触媒化学分解
法)などが開発され,このような方法を実施すればダイ
オキシン類をほぼ完全に無害化が可能である。
Hitherto, high-temperature heat treatment has been widely used as a detoxification technique for soil contaminated with dioxins. Recently, however, an electrode has been inserted into contaminated soil to generate high heat, and soil has been removed like lava. Melt-solidification method (melt-solidification method) and method of adding catalyst or alkali to contaminated soil to decompose dioxin by applying high heat (alkali-catalyzed chemical decomposition method) have been developed. Classification can be made almost completely harmless.

【0004】[0004]

【発明が解決しようとする課題】前記の溶融固化法やア
ルカリ触媒化学分解法はダイオキシン類をほぼ完全に無
害化できる点では高度な技術であると言える。したがっ
て,ダイオキシン濃度が高く且つ小エリアの土壌に対し
ては効果を奏する。しかし,ダイオキシン濃度が低く且
つ広く浅く分布しているような土壌に対してこの技術を
適用すると,処理費用が非常に高くなるという問題があ
る。また,これらの方法で処理されたものは形態的にも
機能的にも土壌と呼べるものではなくなってしまい,植
物を生育させるのに適さないばかりか,処理土を再利用
できる用途が見いだせなければ,廃棄物として再び処理
が必要となり更にコストがかかってしまう。
The above-mentioned melt-solidification method and alkali-catalyzed chemical decomposition method can be said to be advanced technologies in that dioxins can be almost completely rendered harmless. Therefore, the present invention is effective for soil having a high dioxin concentration and a small area. However, if this technique is applied to a soil where the dioxin concentration is low and is widely and shallowly distributed, there is a problem that the treatment cost becomes extremely high. In addition, those treated by these methods can no longer be called soil in terms of morphology or function, so they are not suitable for growing plants, and if there is no use that can reuse the treated soil. In addition, the waste must be treated again and the cost is further increased.

【0005】また,これまでのダイオキシン汚染土壌の
浄化は,多くのものは熱エネルギーや電気エネルギー,
さらには薬剤を多大に必要とするので,設備的にも大が
かりなものとならざるを得なかった。
[0005] Further, the purification of dioxin-contaminated soil up to now has mainly involved thermal energy, electric energy,
Furthermore, since a large amount of medicine is required, the equipment must be large.

【0006】ところが,ダイオキシンの汚染形態は,焼
却場近辺エリアにおける低濃度の表層汚染である場合が
殆んどであり,広い範囲の表層土に分布する低濃度のダ
イオキシン類をさらに基準値以下の濃度に低下させる処
理としては,従来の技術ではあまりにも大がかりになり
すぎたり,高コストを必要とする点で,必ずしも適する
ものではなかった。
However, the form of dioxin contamination is almost always low-level surface pollution in the area near the incineration plant, and low-level dioxins distributed over a wide range of surface soil are further reduced to below the standard value. The conventional technology for reducing the concentration is not always suitable because it is too large or requires high cost.

【0007】したがって,本発明はこのような従来技術
の問題を解決することを課題とするものであり,低汚染
濃度の土壌に対しても簡易に且つ安価に処理できるダイ
オキシン汚染土壌の浄化法を提供しようとするものであ
る。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to solve such a problem of the prior art, and a method for purifying dioxin-contaminated soil that can easily and inexpensively treat low-contamination concentration soil is provided. It is something to offer.

【0008】[0008]

【課題を解決するための手段】本発明者らは,前記の課
題解決のため種々の試験研究を行ってきたが,(1) ダイ
オキシン類の水に対する溶解度は温度に大きく依存して
温度が高いほど溶解しやすい,(2) 熱水で土壌を洗った
時に水側に同伴する微粒分(微細なサスペンション分)
にはダイオキシン類が付着している確率が高く,したが
って,この微粒分を洗浄水と共に土壌から分離すれば,
大部分のダイオキシン類が土壌から分離可能である,と
の現象を利用すると,具体的には,ダイオキシン類で汚
染された土壌を熱水で洗浄してダイオキシン類同伴の汚
水を分離すれば,前記の目的が有利に達成できることを
知った。
Means for Solving the Problems The present inventors have carried out various tests and studies to solve the above-mentioned problems. (1) The solubility of dioxins in water greatly depends on the temperature and the temperature is high. (2) Fine particles accompanying the water side when the soil is washed with hot water (fine suspension)
It is highly probable that dioxins are attached to the soil, so if this fine fraction is separated from the soil together with the wash water,
Utilizing the phenomenon that most dioxins can be separated from soil, concretely, if the soil contaminated with dioxins is washed with hot water and the dioxin accompanying sewage is separated, I found that the purpose could be achieved advantageously.

【0009】したがって,本発明によれば,ダイオキシ
ン類で汚染された土壌を原位置から採取して熱水で洗う
段階と,ダイオキシン類同伴の泥水を該土壌から分離す
る段階を経てダイオキシン類濃度の低下した土壌を得る
汚染土壌の浄化方法を提供する。
Therefore, according to the present invention, the dioxin-contaminated soil is collected from the original position and washed with hot water, and the dioxin-contaminated mud is separated from the soil through the dioxin-concentration process. Provided is a method for purifying contaminated soil to obtain reduced soil.

【0010】そして,該課題を解決するための一層具体
的な手段として,本発明は,ダイオキシン類で汚染され
た土壌を移送手段(例えばコンベア)で搬送しつつその
上から(例えば25〜100℃の)熱水を撒水し,ダイ
オキシン類同伴の泥水を該土壌から自重で流出させてダ
イオキシン類濃度の低下した土壌を得る汚染土壌の浄化
方法:ダイオキシン類で汚染された土壌を容器に入れて
(例えば25〜100℃の)熱水と接触させたあと,ダ
イオキシン類同伴の泥水を該土壌から分離してダイオキ
シン類濃度の低下した土壌を得る汚染土壌の浄化方法:
ダイオキシン類で汚染された土壌と(例えば25〜10
0℃の)熱水とを入れた容器から移送手段(例えばスク
リューコンベア)で斜め上方に内容物を払い出すことに
よりダイオキシン類同伴の泥水を容器内に残し,ダイオ
キシン類濃度の低下した土壌を容器外に排出する汚染土
壌の浄化方法:を提供する。
As a more specific means for solving the above problems, the present invention provides a method for transporting soil contaminated with dioxins by means of a transfer means (for example, a conveyor) and then transferring the soil (for example, at 25 to 100 ° C.). B) Hot water is sprinkled, and mud accompanying dioxins is discharged from the soil by its own weight to obtain soil with a reduced concentration of dioxins. Purification method of contaminated soil: Put the soil contaminated with dioxins into a container ( After contacting with hot water (for example, at 25 to 100 ° C.), a method for purifying contaminated soil in which dioxin-entrained mud is separated from the soil to obtain a soil with a reduced concentration of dioxins:
Soil contaminated with dioxins (eg, 25-10
By discharging the contents obliquely upward from a container containing hot water (at 0 ° C.) by a transfer means (for example, a screw conveyor), mud water accompanying dioxins is left in the container, and soil having a reduced dioxin concentration is removed from the container. Purification method for contaminated soil discharged to the outside:

【0011】いずれの方法においても,熱水で処理され
たあとの土壌は,土壌中に生息していた細菌類は死滅す
るものも多く,したがって,この土壌にダイオキシン分
解菌を添加すると,この菌が優先種となって生育しやす
くなり,土壌に残留するダイオキシン類の分解効率が高
まることがわかった。したがって,本発明によれば,よ
り有利に該課題を解決する手段として,前記の方法によ
って得られたダイオキシン類濃度の低下した土壌にダイ
オキシン分解菌を添加することを特徴とする汚染土壌の
浄化方法を提供する。
[0011] In any of the methods, the soil treated with hot water often kills the bacteria living in the soil. Therefore, when dioxin-decomposing bacteria are added to the soil, the bacteria are removed. Became the priority species and became easier to grow, increasing the efficiency of decomposing dioxins remaining in the soil. Therefore, according to the present invention, as a means for solving the problem more advantageously, a method for purifying contaminated soil, which comprises adding dioxin-decomposing bacteria to soil having a reduced concentration of dioxins obtained by the above method. I will provide a.

【0012】[0012]

【発明の実施の形態】ダイオキシンは多くの異性体があ
る。とくにダイオキシンの一種である 2,3,7,8−四塩化
ジベンゾ−パラ−ジオキシン (2,3,7,8 -TCDD)は最も毒
性が高い。このため,環境庁告示のダイオキシン基準値
は 2,3,7,8-TCDD の毒性に換算した値を採用している。
本明細書においても「ダイオキシン類」とは環境庁告示
と同様に各種の異性体を含む意味で使用する。なお,2,
3,7,8-TCDD の25℃の水に対する溶解度は非常に小さ
く8〜200ng/L程度であると言われている。
DETAILED DESCRIPTION OF THE INVENTION Dioxin has many isomers. In particular, 2,3,7,8-dibenzo-para-dioxin (2,3,7,8-TCDD), a type of dioxin, is the most toxic. For this reason, the dioxin standard value notified by the Environment Agency uses the value converted to the toxicity of 2,3,7,8-TCDD.
Also in this specification, the term "dioxins" is used to mean various isomers as in the notification of the Environment Agency. Note that 2,
It is said that the solubility of 3,7,8-TCDD in water at 25 ° C. is very small, about 8 to 200 ng / L.

【0013】ダイオキシン類の土壌汚染は,実際には焼
却場付近エリアの表層土に見られることが多い。とくに
深さ10cmまで,場合によっては5cm程度までの極
表層に局在しており,これより深い地盤中ではその濃度
は極端に低下するのが普通である。
[0013] Soil contamination of dioxins is often found in the surface soil near the incineration plant. In particular, it is localized in the extreme surface layer up to a depth of 10 cm, and in some cases up to about 5 cm, and its concentration is usually extremely reduced in deeper ground.

【0014】これは,焼却場から飛散する灰分に同伴し
たダイオキシン類が地表に直接的に舞い落ちたり,各種
植物等に付着したあと時を経て地表に有機物と共に点在
するようになるが,前記のようにダイオキシン類は水に
対する溶解度が極めて低いので,水を媒体として地中に
浸透するようなことも比較的進行し難いのではないかと
考えられる。しかし,降雨時などに水の道が自然にでき
ると,その水に運ばれて高濃度に堆積する部分が発生
し,基準値を超える所が局在するようになることも考え
られる。したがって,ダイオキシン類に汚染された土壌
であると言っても,基準値である1000pg−TEQ
/gを超えるところが点在するようなことが多いのが実
状であり,近辺の土壌,或いはその地下地盤では基準値
以下であるところが多い。
[0014] This is because dioxins accompanied by ash scattered from the incineration plant fall directly to the surface of the ground or adhere to various plants, etc., and then become scattered with organic substances on the surface of the ground over time. Since dioxins have a very low solubility in water, it is considered that the permeation into the ground using water as a medium is relatively difficult to proceed. However, if the water path is formed naturally during rainfall, a portion of the water that is carried by the water and accumulates at a high concentration will occur, and it is conceivable that a portion exceeding the reference value may be localized. Therefore, even though the soil is contaminated with dioxins, the standard value of 1000 pg-TEQ
/ G in many cases is scattered, and in the soil near the ground or its underground ground, it is often lower than the reference value.

【0015】このようなダイオキシン類汚染の分布形態
から見ると,溶融固化法やアルカリ触媒化学分解法を適
用して広いエリアを高深度まで完全浄化するようなこと
は必ずしも合理的な対策ではないと言い得る。
In view of the distribution form of such dioxin contamination, it is not necessarily a rational measure to completely purify a wide area to a high depth by applying a solidification method or an alkali-catalyzed chemical decomposition method. I can say.

【0016】このような観点に立って本発明は,ダイオ
キシン類の汚染土壌に対し,表層部の汚染土壌を剥ぎ取
りながら,好ましくは,汚染地帯における深さ50cm
までの表層土を剥ぎ取りながら,これを熱水で洗浄処理
することを要旨とするものであり,ダイオキシン類の水
に対する溶解度は温度が上昇するほど急激に大きくなる
という現象と,土壌中のダイオキシン類は洗浄水に同伴
するような微粒成分に付着している場合が多いという現
象を有利に利用するものであり,ダイオキシン類で汚染
された土壌を原位置から採取して熱水で洗う段階と,ダ
イオキシン類同伴の泥水を該土壌から分離する段階を経
てダイオキシン類濃度の低下した土壌を得ることを特徴
とする。
In view of the above, according to the present invention, the dioxin-contaminated soil is preferably stripped of the contaminated soil in the surface layer, and preferably has a depth of 50 cm in the contaminated zone.
The purpose of this study is to wash the surface soil with hot water while stripping the soil up to the point where the solubility of dioxins in water increases rapidly with increasing temperature. It is advantageous to take advantage of the phenomenon that the soil is often attached to the fine particles that accompany the washing water. The soil contaminated with dioxins is collected in situ and washed with hot water. And obtaining a soil having a reduced concentration of dioxins through a step of separating mud water accompanying dioxins from the soil.

【0017】ここで,熱水とは常温以上100℃までの
温度(25〜100℃)を有した水であり,この熱水で
土壌を洗う段階は,汚染エリヤや土壌の種類・性質に応
じて以下に説明するような種々の好ましい態様のもとで
実施するが,基本的には,汚染土壌を熱水で洗浄するこ
とにより,熱水中にダイオキシン類を溶解させること
と,土壌中の微粒分(有機物・無機物を問わず,洗浄後
の水に同伴する微細なサスペンション分)を熱水側にサ
スペンド(同伴)させることにある。
Here, the hot water is water having a temperature of from normal temperature to 100 ° C. (25 to 100 ° C.). The step of washing the soil with this hot water depends on the contamination area and the type and properties of the soil. It is carried out in various preferred embodiments as described below, but basically, the dioxins are dissolved in the hot water by washing the contaminated soil with the hot water, The purpose of the present invention is to suspend fine particles (fine suspensions, regardless of organic and inorganic substances, which accompany water after washing) toward the hot water side.

【0018】そのさい,熱水に有機溶媒を添加してお
き,この有機溶媒にダイオキシン類を溶解させることも
できる。例えば, 2,3,7,8-TCDD の各種有機溶媒に対す
る溶解度(リットル当り)は水に対するngオーダに対
しmgオーダで溶解するので,溶媒使用によってもダイ
オキシン類の洗浄水側への移行を促進させることができ
る。有機溶媒の例とその溶解度を例示すると,ベンゼン
(溶解度=570mg/L), クロロホルム(同=370mg/L), ア
セトン(同=110mg/L), n-オクタノール(同=50mg/L),
メタノール(同=10mg/L) などがある。
At this time, an organic solvent can be added to hot water, and the dioxins can be dissolved in the organic solvent. For example, the solubility of 2,3,7,8-TCDD in various organic solvents (per liter) dissolves in the order of mg to the order of ng in water, so the use of solvent promotes the transfer of dioxins to the wash water side. Can be done. Examples of organic solvents and their solubility are as follows: benzene (solubility = 570 mg / L), chloroform (370 mg / L), acetone (110 mg / L), n-octanol (50 mg / L),
Methanol (same as 10 mg / L).

【0019】いずれにしても,熱水で土壌を洗う段階
は,対象とする土壌がダイオキシン類で汚染されている
関係上,その処理によって発生する水蒸気や微粒子・ミ
スト等が周囲に飛散したりすると思わぬ危険を及ぼす可
能性がある。このため,できる限りこの熱水による洗浄
は密閉系で行うか,排気処理を考慮した設備で行うこと
が好ましい。
In any case, in the step of washing the soil with hot water, the target soil is contaminated with dioxins, so that water vapor, fine particles, mist and the like generated by the treatment are scattered around. It may cause unexpected danger. For this reason, it is preferable that the washing with hot water be performed in a closed system as much as possible, or in equipment that takes exhaust treatment into consideration.

【0020】次いで,この洗浄段階に引き続いて「ダイ
オキシン類同伴の泥水」を土壌から分離する段階を実施
するが,これは洗い終えた熱水を土壌から分離すること
である。この分離は,もっとも簡便には, 土壌から洗浄
水を自重を利用して土壌から自然に流出させる方法がよ
い。この場合, 土壌中には間隙水が残留するが,洗浄に
使用する熱水の量が充分であれば,間隙水中に残存する
ダイオキシン類は非常に微量となるので特に問題はな
い。
Next, following the washing step, a step of separating "dioxin-entrained muddy water" from the soil is performed, in which hot water after washing is separated from the soil. The simplest method of this separation is to allow the washing water to flow naturally out of the soil using its own weight. In this case, pore water remains in the soil, but there is no particular problem if the amount of hot water used for washing is sufficient because dioxins remaining in the pore water will be very small.

【0021】洗浄水の分離段階においては,流出する微
粒分の量と粒度は固液分離の程度に応じて異なるが,自
重を利用して土壌から自然に洗浄水 (熱水) を放出させ
る場合には,土壌中の微粒分が洗浄水に同伴して流れ出
る現象が生ずる。本発明においては,この自然に流出す
る程度の微粒分は, どのような固液分離手段を採用しよ
うとも,洗浄水側に移行させるようにする。この微粒分
の洗浄水側への移行によって,微粒分に同伴若しくは付
着しているダイオキシン類を洗浄水側に移行させる点に
本発明の一つの特徴がある。したがって「ダイオキシン
類同伴の泥水」とは,ダイオキシン類が同伴若しくは付
着した微粒分と,ダイオキシン類が溶解した洗浄水 (熱
水) との混合物を意味しており,この混合物は通常は泥
水状である。土壌から分離されるダイオキシン類同伴の
泥水は,好ましくは常温以上(25℃以上)の温度
(熱)を保持したまま土壌から分離する。
In the washing water separation step, the amount and the particle size of the fine particles flowing out differ depending on the degree of solid-liquid separation, but when the washing water (hot water) is naturally released from the soil using its own weight. , A phenomenon occurs in which fine particles in the soil flow out along with the washing water. In the present invention, the fine particles that flow out naturally are transferred to the washing water side regardless of the solid-liquid separation means employed. One feature of the present invention is that dioxins accompanying or adhering to the fine particles are transferred to the washing water side by transferring the fine particles to the washing water side. Therefore, “mud with dioxins” means a mixture of fine particles with or attached dioxins and washing water (hot water) in which dioxins are dissolved, and this mixture is usually muddy. is there. The mud accompanying dioxins separated from the soil is preferably at a temperature above normal temperature (25 ° C or higher).
Separate from soil while retaining (heat).

【0022】土壌から分離されたダイオキシン類同伴の
泥水は,これを沈降槽や場合によって固液分離装置に導
いて泥分を分離し,この泥分はダイオキシン類除去のた
めに二次処理に供すると共に,泥分を分離した水はこれ
を熱水として再び土壌の洗浄に循環使用することができ
る。
The mud accompanying dioxins separated from the soil is guided to a sedimentation tank or a solid-liquid separator if necessary, to separate mud, and the mud is subjected to a secondary treatment for removing dioxins. At the same time, the water from which mud has been separated can be reused as hot water for washing the soil again.

【0023】以下に図面を参照しながら,本発明の好ま
しい態様を説明する。図1の態様は,ダイオキシン類で
汚染された土壌をコンベアで搬送しつつその上から25
〜100℃の熱水を撒水し,ダイオキシン類同伴の泥水
を該土壌から自重で流出させてダイオキシン類濃度の低
下した土壌を得るようにした本発明方法の1形態とし
て,走行式浄化装置によってこれを実施する例を示した
ものである。
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings. In the embodiment shown in FIG. 1, soil contaminated with dioxins is transported on a conveyor while 25
As one form of the method of the present invention in which hot water of -100 ° C is sprinkled and mud accompanying dioxins is allowed to flow out of the soil by its own weight to obtain soil with a reduced concentration of dioxins, this method is carried out by a traveling purification apparatus. Is shown.

【0024】図1において,1は原位置表層部のダイオ
キシン類汚染土壌を示しており,この汚染土壌1をバッ
クホウ2によって表層部から剥ぎ取り,これをキャタピ
ラーの上に設置された走行式浄化装置3のホッパー4に
投入する。走行式浄化装置3は,熱水による汚染土壌の
洗浄と分離を連続して行えるシステムをキャタピラーの
上に設置したものであり,次のように構成されている。
なお,図1のAは走行式浄化装置3を平面的に見た略
図,同Bは洗浄槽の内部を側面的に見た略図である。
In FIG. 1, reference numeral 1 designates a dioxin-contaminated soil at an in-situ surface layer. The contaminated soil 1 is peeled off from the surface layer by a backhoe 2, and the contaminated soil 1 is mounted on a caterpillar. And put into the hopper 4. The traveling purification device 3 is provided with a system capable of continuously cleaning and separating contaminated soil by hot water on a caterpillar, and is configured as follows.
1A is a schematic view of the traveling purifier 3 as viewed in plan, and FIG. 1B is a schematic view of the inside of the cleaning tank as viewed from the side.

【0025】ホッパー4から第1スクリューコンベア6
と第2スクリューコンベア7を経て洗浄槽5に土壌が搬
送される。洗浄槽5内には第3スクリューコンベア8が
吐出端9をリア側に向けて設置されており,また,洗浄
槽5の上部には熱水噴射器10が設置され,この熱水噴射
器10から第3スクリューコンベア8上の土壌に対して熱
水が撒水される。第3スクリューコンベア8は,図1B
に見られるように,樋状ホッパー11の底部に沿って設置
されており,第2スクリューコンベア7から樋状ホッパ
ー11に受入れられた土壌は,第3スクリューコンベア8
によって掻き混ぜられながら,熱水散布を受けて吐出端
9に向けて搬送され,この搬送の間に水切りが自然に行
われ,ダイオキシン類同伴の泥水12となって第3スクリ
ューコンベア8から落下して洗浄槽5の下部に溜まる。
他方の,このダイオキシン類同伴の泥水12が分離される
ことによって,ダイオキシン類濃度の低下した土壌13は
前記の吐出端9から放出され,処理済土壌14となって地
表に戻される。
From the hopper 4 to the first screw conveyor 6
Then, the soil is transported to the washing tank 5 through the second screw conveyor 7. A third screw conveyor 8 is installed in the washing tank 5 with the discharge end 9 facing the rear side, and a hot water injector 10 is installed above the washing tank 5. , Hot water is sprayed on the soil on the third screw conveyor 8. The third screw conveyor 8 is shown in FIG.
As shown in FIG. 3, the soil received along the bottom of the gutter hopper 11 from the second screw conveyor 7 into the gutter hopper 11 is disposed along the third screw conveyor 8.
While being stirred by hot water, it is sprayed with hot water and transported toward the discharge end 9. During this transport, the water is drained naturally and becomes muddy water 12 accompanied by dioxins and falls from the third screw conveyor 8 And accumulates in the lower part of the washing tank 5.
On the other hand, by separating the muddy water 12 accompanying the dioxins, the soil 13 having a reduced concentration of the dioxins is discharged from the discharge end 9 and returned to the surface as treated soil 14.

【0026】他方,加熱槽15が適切な位置(図例では洗
浄槽5の上)に設置されており,この加熱槽15で作られ
た熱水を熱水噴射器10に送り込む。そのさい,添加物タ
ンク16(図A)から有機溶媒を加熱槽15に必要に応じて
添加する。洗浄槽5の底部に溜まったダイオキシン類同
伴の泥水12は,ポンプ17によって固液分離槽18(図A)
に送り込み,ここで分離された水は不可避の泥分と共に
加熱槽15に戻される。固液分離槽18には処理の進行につ
れて泥分が堆積してくるが,これは別途回収してダイオ
キシン類除去のための二次処理用に貯留しておく。
On the other hand, a heating tank 15 is installed at an appropriate position (on the washing tank 5 in the illustrated example), and the hot water produced in the heating tank 15 is sent to the hot water injector 10. At that time, an organic solvent is added from the additive tank 16 (FIG. A) to the heating tank 15 as needed. The muddy water 12 accompanying dioxins accumulated at the bottom of the washing tank 5 is removed by a pump 17 into a solid-liquid separation tank 18 (FIG. A).
The water separated here is returned to the heating tank 15 together with inevitable mud. Mud accumulates in the solid-liquid separation tank 18 as the treatment proceeds, but this is separately collected and stored for secondary treatment for removing dioxins.

【0027】加熱槽15の熱源としては自走装置のエンジ
ン排ガスを利用することができる。また固液分離槽18と
して遠心分離機を適用する場合にはその回転動力として
は自走用エンジンが利用でき,同様にスクリューコンベ
アやポンプ動力も自走用エンジンを利用できる。
As a heat source of the heating tank 15, engine exhaust gas from a self-propelled device can be used. When a centrifugal separator is applied as the solid-liquid separation tank 18, a self-propelled engine can be used as the rotational power, and a self-propelled engine can also be used for the screw conveyor and pump power.

【0028】図1Aの19は運転台を表しており,この運
転台19で浄化装置3の自走操作と共にスクリューコンベ
アの稼働や加熱槽等の制御を行えるようにして,バック
ホー2から受け入れた土壌を連続的に浄化処理すること
ができ,この装置の稼働によって処理済土壌14の埋戻し
も作業性よく行うことができる。
Reference numeral 19 in FIG. 1A denotes a driver's cab. The driver's cab 19 controls the operation of the screw conveyor and the control of the heating tank together with the self-propelled operation of the purification device 3. Can be continuously purified, and by operating this apparatus, backfilling of the treated soil 14 can be performed with good workability.

【0029】なお,吐出端9から「ダイオキシン類濃度
の低下した土壌13」を地表に戻すさいに,ダイオキシン
分解菌を添加しておくと,該土壌13は熱水処理されて各
種の細菌が死滅若しくは菌数が低下しているので,ダイ
オキシン分解菌が優先種として培養される結果,土壌14
に不可避に残留したダイオキシン類が分解しやすくな
り,浄化目的が一層有利に達成される。すなわち,熱水
処理する前の土壌1に該分解菌を接種する場合に比べ
て,本発明で処理した土壌14に接種した場合には,分解
菌による分解効率を格段に向上させることができる。
If dioxin-decomposing bacteria are added before returning the “soil 13 with reduced dioxin concentration” from the discharge end 9 to the ground surface, the soil 13 is treated with hot water to kill various bacteria. Alternatively, dioxin-degrading bacteria are cultivated as a priority species due to a decrease in the number of bacteria.
The dioxins unavoidably remaining in the waste are easily decomposed, and the purification purpose is more advantageously achieved. That is, when inoculated into the soil 14 treated according to the present invention, the decomposition efficiency by the decomposed bacteria can be remarkably improved as compared with the case where the decomposed bacteria are inoculated into the soil 1 before the hot water treatment.

【0030】図2は,本発明の他の態様,すなわち,ダ
イオキシン類で汚染された土壌を容器に入れて25〜1
00℃の熱水と接触させたあと,ダイオキシン類同伴の
泥水を該土壌から分離してダイオキシン類濃度の低下し
た土壌を得る汚染土壌の浄化方法を図解的に示したもの
である。
FIG. 2 shows another embodiment of the present invention, that is, a method in which soil contaminated with dioxins is placed in a container,
1 is a diagram schematically illustrating a method for purifying contaminated soil in which mud accompanying dioxins is separated from the soil after contact with hot water at 00 ° C. to obtain soil with a reduced concentration of dioxins.

【0031】この態様では,図2に示すように,ダイオ
キシン類で汚染された土壌20を,中腹下方にスリット21
をもつ閉鎖容器22内に入れ,この容器内土壌20に対し
て,容器上部に設置した熱水噴射器23から熱水をふりか
けるようにしたものである。熱水はスリット21上の土壌
20と接触しながら土壌中を流下し,その間に,土壌20を
洗浄しながらスリット21から容器底部の泥水溜まり24に
落下する。すなわち, スリット21は固液分離器の役割を
果たし,ダイオキシン類同伴の泥水が土壌20から分離さ
れて泥水溜まり24に捕集される。スリット21の開口の大
きさによって,泥水に同伴する微粒の大きさも異なるこ
とになるが,比較的大きな開口例えば2〜3mm程度を
有するものであっても,泥水の通流の間にスリット21の
目詰まりが自然と発生するので,山盛りした土壌の側面
や下面から過剰の水が自重により自然に放出するのと同
じような具合に, 微粒の同伴物を伴った泥水がスリット
21を通過するようになり,粗粒分の通過は殆んど見られ
なくなる。
In this embodiment, as shown in FIG. 2, a soil 20 contaminated with dioxins is formed by a slit 21
The hot water is sprayed from a hot water sprayer 23 installed on the upper part of the container 20 into the closed container 22 having. Hot water is in the soil on slit 21
It flows down in the soil while being in contact with 20, and in the meantime, falls from the slit 21 into the mud pool 24 at the bottom of the container while washing the soil 20. That is, the slit 21 serves as a solid-liquid separator, and the mud accompanying dioxins is separated from the soil 20 and collected in the mud pool 24. Depending on the size of the opening of the slit 21, the size of the fine particles accompanying the muddy water will also differ. Since the clogging occurs naturally, the muddy water with fine accompanying substances is slit in the same way that excess water is naturally released from the side and underside of the heaped soil by its own weight.
21 and the passage of coarse particles is hardly observed.

【0032】熱水はヒータ25をもつ加熱槽26で作られ,
熱水ポンプ27によって熱水噴射器23に送られる。他方,
容器22の泥水溜まり24に集積した泥水は,泥水ポンプ28
によって固液分離槽29に送り込まれ, ここで泥分を沈降
分離する。槽底部の泥分30は泥分抜出し口のコック31を
開くことにより適宜排出し,ダイオキシン類除去の二次
処理に供すべく溜め置かれる。他方, 槽29の上澄み液は
オーバーフロー口34から加熱槽26に戻され, 再び加熱さ
れて洗浄用熱水に利用される。加熱槽26には必要に応じ
て添加槽32から有機溶媒33が添加される。
Hot water is produced in a heating tank 26 having a heater 25,
The hot water is sent to the hot water injector 23 by the hot water pump 27. On the other hand,
The mud accumulated in the mud pool 24 of the container 22 is supplied to a mud pump 28.
Is fed into the solid-liquid separation tank 29, where the mud is settled and separated. The mud 30 at the bottom of the tank is discharged as appropriate by opening the cock 31 at the mud outlet, and is stored for secondary processing of dioxins removal. On the other hand, the supernatant liquid of the tank 29 is returned from the overflow port 34 to the heating tank 26, heated again, and used as hot water for washing. An organic solvent 33 is added to the heating tank 26 from an addition tank 32 as necessary.

【0033】図3は,本発明のさらに別の態様,すなわ
ち,ダイオキシン類で汚染された土壌と25〜100℃
の熱水とを入れた容器からスクリューコンベアで斜め上
方に内容物を払い出すことによりダイオキシン類同伴の
泥水を容器内に残し,ダイオキシン類濃度の低下した土
壌を容器外に排出する汚染土壌の浄化方法の要部を図解
的に示したものである。
FIG. 3 shows yet another embodiment of the present invention, namely, soil contaminated with dioxins and 25-100 ° C.
Purification of contaminated soil by discharging dirt and dioxin-bearing mud in the container by discharging the contents diagonally upward from the container containing hot water with a screw conveyor, and discharging soil with reduced dioxin concentration out of the container 1 schematically illustrates a main part of the method.

【0034】本例では,容器35に対し, 容器底部に受入
れ端を,容器外部に吐出端をもつようにスクリューコン
ベア37を傾斜させて設置し,容器35内に収容した土壌と
熱水の混合物38から, コンベア37のスクリュウで掻き上
げられる土砂分41を容器外に払い出し, スクリュウで掻
き上げられない泥水分は容器35内に残すようにしてい
る。
In this example, a screw conveyor 37 is installed at an angle to the container 35 so as to have a receiving end at the bottom of the container and a discharge end outside the container, and a mixture of soil and hot water stored in the container 35 is provided. From 38, the sediment 41 that is scraped up by the screw of the conveyor 37 is paid out of the container, and mud water that cannot be scraped up by the screw is left in the container 35.

【0035】容器35には,ホッパー39からダイオキシン
類で汚染された土壌40を投入し,また加熱槽26の熱水を
入れたうえ,容器内に設置した掻き混ぜ用スクリュー機
42の駆動により容器内混合物38を攪拌混合する。スクリ
ューコンベア37の吐出端から容器外に払い出される土砂
分41は熱水で洗われてダイオキシン類濃度の低下した土
壌であり,処理済土壌43として埋め戻しその他に利用さ
れる。他方, 容器35内に残される泥水分は泥水抜き出し
口44から, 図2の場合と同様に,固液分離槽29に抜き出
され, ここで泥分30を沈降分離し,泥分抜出し口のコッ
ク31を開くことにより適宜排出し,ダイオキシン類除去
の二次処理に供すべく溜め置かれる。熱水はヒータ25を
もつ加熱槽26で作られ, 熱水ポンプ27によって容器35に
送られるが,この加熱槽26には,固液分離槽29の上澄み
液がオーバーフロー口34を経て戻され, 再び加熱されて
洗浄用熱水に利用される。加熱槽26には必要に応じて添
加槽32から有機溶媒33が添加される。
A container 35 is charged with soil 40 contaminated with dioxins from a hopper 39, and is filled with hot water from a heating tank 26, and a stirring screw machine installed in the container.
The mixture 38 in the container is stirred and mixed by driving the 42. The earth and sand 41 discharged from the discharge end of the screw conveyor 37 to the outside of the container is soil that has been washed with hot water and has a reduced concentration of dioxins, and is used as a treated soil 43 for backfilling and other purposes. On the other hand, the mud water remaining in the container 35 is drawn out from the muddy water discharge port 44 to the solid-liquid separation tank 29 in the same manner as in FIG. 2, where the mud 30 is settled and separated, and When the cock 31 is opened, it is discharged as appropriate, and is stored for secondary processing of dioxin removal. Hot water is produced in a heating tank 26 having a heater 25 and sent to a vessel 35 by a hot water pump 27. In this heating tank 26, the supernatant liquid of the solid-liquid separation tank 29 is returned through an overflow port 34, It is heated again and used for hot water for cleaning. An organic solvent 33 is added to the heating tank 26 from an addition tank 32 as necessary.

【0036】いずれの態様による場合にも,ダイオキシ
ン類で汚染された土壌は原位置から容器内またはコンベ
ア上に移され, ここで,熱水と接触または攪拌混合され
て熱水洗浄がなされ,この熱水洗浄のあと, 洗浄後液と
して泥分同伴のダイオキシン含有泥水が分離され,この
泥水を分離することによってダイオキシン類濃度の低下
した土壌が回収されるものであるから,熱水洗浄と熱水
分離を簡易且つ効率よく行なうことができる。そして,
回収したダイオキシン類濃度の低下した土壌は水切りが
されていると同時に微粒分が除去されているから,適度
な湿度を有しながら空気がとおりやすい性質を有してい
る。このため,水と酸素の供給が良好であり,微生物の
生息に適した土壌となっている。したがって,この土壌
にダイオキシン類分解菌を接種すると,その分解菌によ
るダイオキシン類分解効率が高くなる。とくに,微粒分
(有機物・無機物)に強固に付着したダイオキシン類は
土中の微生物による分解が困難であるが,このような微
粒分は熱水洗浄で除去されているので,本発明で得られ
た土壌は生物分解に適したものとなっている。
In any of the embodiments, the soil contaminated with dioxins is transferred from the original position into a container or a conveyor, where it is brought into contact with hot water or mixed with stirring to be washed with hot water. After washing with hot water, the dioxin-containing mud accompanying mud is separated as a post-wash liquid, and the soil with a reduced dioxin concentration is recovered by separating the mud. Separation can be performed easily and efficiently. And
Since the collected dioxin-concentrated soil has been drained and fine particles removed at the same time, it has the property of being able to easily pass air while maintaining appropriate humidity. For this reason, the water and oxygen supply are good and the soil is suitable for the inhabitation of microorganisms. Therefore, when this soil is inoculated with dioxin-decomposing bacteria, the decomposition efficiency of dioxins by the decomposing bacteria increases. In particular, dioxins which are firmly attached to fine particles (organic and inorganic substances) are difficult to decompose by microorganisms in the soil, but such fine particles have been removed by hot water washing, and thus can be obtained by the present invention. The soil is suitable for biodegradation.

【0037】なお,以上はダイオキシン類汚染土壌を対
象とした場合の本発明法を説明してきたが,ダイオキシ
ン以外にも,油類や,ベンゼン,トルエン,キシレン等
の有機溶媒類,各種農薬,PCB,水銀,シアン化合物
等で汚染された土壌に対しても,本発明法は同様に適用
可能である。
Although the method of the present invention for dioxin-contaminated soil has been described above, in addition to dioxin, oils, organic solvents such as benzene, toluene, xylene, various agricultural chemicals, PCBs The method of the present invention can be similarly applied to soil contaminated with sulfur, mercury, cyanide, and the like.

【0038】[0038]

【発明の効果】以上説明したように,本発明によると,
熱水洗浄という簡単な処理法により,ダイオキシン類汚
染土壌をダイオキシン類濃度の低下した土壌に改良する
ことができる。そして,この改良土壌は熱水洗浄によっ
て微生物濃度が低下しているか死滅しているものも多
く,且つ適度な湿分と通気性を有しているから,ダイオ
キシン分解菌の生育環境に優れるようにも改質されてい
る。このため,さらにダイオキシン類濃度を微生物分解
によって低下させることができる。
As described above, according to the present invention,
Dioxin-contaminated soil can be improved to a soil with reduced dioxin concentration by a simple treatment method called hot water washing. In addition, many of these improved soils have reduced or died microbial concentrations due to washing with hot water, and have appropriate moisture and air permeability, so that they have an excellent growth environment for dioxin-degrading bacteria. Has also been modified. Therefore, the concentration of dioxins can be further reduced by microbial decomposition.

【0039】さらに,本発明法は熱水洗浄と熱水分離と
いう簡易な処理の組合せからなっているから,ダイオキ
シン類が低濃度に分布した表層汚染土を対象とした広い
エリアの処理に適用したとしても,溶融固化法やアルカ
リ触媒化学分解法等では殆んど不可能なような安価な費
用で処理可能であり,ダイオキシン類の分布状況に則し
た経済的且つ効率的な方法であると言える。
Further, since the method of the present invention comprises a combination of simple treatments of hot water washing and hot water separation, the method is applied to the treatment of a large area for surface contaminated soil in which dioxins are distributed at a low concentration. However, it can be treated at a low cost, which is almost impossible with the melt-solidification method or the alkali-catalyzed chemical decomposition method, and it can be said that it is an economical and efficient method according to the distribution of dioxins. .

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

【図1】本発明法を走行式浄化装置で実施する例を示し
た稼働状態図である。
FIG. 1 is an operation state diagram showing an example in which the method of the present invention is implemented in a traveling purification device.

【図2】本発明法を固定式設備で実施する例を示した機
器配置系統図である。
FIG. 2 is an equipment layout system diagram showing an example in which the method of the present invention is implemented in a fixed facility.

【図3】本発明法を土砂払い出し機で実施する例を示し
た機器配置系統図である。 1 原位置のダイオキシン類汚染土壌 3 自走式洗浄装置 5 洗浄槽 6 第1スクリューコンベア 7 第2スクリューコンベア 8 洗浄槽内の第3スクリューコンベア 10 熱水噴射器 12 ダイオキシン類同伴の泥水 13 ダイオキシン類濃度が低下した土壌 14 処理済土壌 15 加熱槽 16 添加物タンク 18 固液分離槽 19 運転台 21 スリット 22 容器 23 熱水噴射器 24 ダイオキシン類同伴の泥水 29 固液分離槽 26 加熱槽 32 有機溶媒添加槽 35 容器 37 土砂払い出しスクリューコンベア 38 ダイオキシン類汚染土壌と熱水の混合物 40 ダイオキシン類汚染土壌 41 ダイオキシン類濃度の低下した土壌 42 攪拌用スクリュー
FIG. 3 is an equipment arrangement system diagram showing an example in which the method of the present invention is carried out by a sediment discharging machine. 1 In-situ dioxin-contaminated soil 3 Self-propelled cleaning device 5 Cleaning tank 6 First screw conveyor 7 Second screw conveyor 8 Third screw conveyor in cleaning tank 10 Hot water injector 12 Mud water accompanied by dioxins 13 Dioxins Soil with reduced concentration 14 Treated soil 15 Heating tank 16 Additive tank 18 Solid-liquid separation tank 19 Cab 21 Slit 22 Vessel 23 Hot water injector 24 Mud with dioxins 29 Solid-liquid separation tank 26 Heating tank 32 Organic solvent Addition tank 35 Vessel 37 Screw conveyor for dispensing earth and sand 38 Mixture of dioxin-contaminated soil and hot water 40 Dioxin-contaminated soil 41 Dioxin-concentrated soil 42 Stirring screw

───────────────────────────────────────────────────── 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) C12N 1/00 B09B 5/00 S // C07D 319/24 (72)発明者 山本 博之 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 (72)発明者 笹倉 剛 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 (72)発明者 岡本 道孝 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 (72)発明者 河合 達司 東京都港区元赤坂一丁目2番7号 鹿島建 設株式会社内 Fターム(参考) 2E191 BA15 BB01 BC05 BD00 BD20 4B065 AA01X AC20 BB04 BB13 CA56 4D004 AA41 AB07 AC07 CA18 CA22 CA40 CA41 CB04 CB31 CC03 CC04 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) C12N 1/00 B09B 5/00 S // C07D 319/24 (72) Inventor Hiroyuki Yamamoto Minato-ku, Tokyo 1-2-7 Akasaka, Kashima Construction Co., Ltd. (72) Inventor Go Tsuyoshi Sakura 1-2-7, Moto, Akasaka, Minato-ku, Tokyo Inside Kashima Construction Co., Ltd. (72) Inventor Michitaka Okamoto, Minato-ku, Tokyo 1-7-2 Akasaka, Kashima Construction Co., Ltd. (72) Inventor Tatsushi Kawai 1-2-7, Moto Akasaka, Minato-ku, Tokyo Kashima Construction Co., Ltd. F-term (reference) 2E191 BA15 BB01 BC05 BD00 BD20 4B065 AA01X AC20 BB04 BB13 CA56 4D004 AA41 AB07 AC07 CA18 CA22 CA40 CA41 CB04 CB31 CC03 CC04

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 ダイオキシン類で汚染された土壌を原位
置から採取して熱水で洗う段階と,ダイオキシン類同伴
の泥水を該土壌から分離する段階を経てダイオキシン類
濃度の低下した土壌を得る汚染土壌の浄化方法。
1. A method for obtaining soil having a reduced concentration of dioxins through a step of collecting dioxin-contaminated soil from an in-situ site and washing it with hot water, and a step of separating dioxin-entrained mud from the soil. How to clean the soil.
【請求項2】 ダイオキシン類で汚染された土壌を移送
手段で搬送しつつその上から熱水を撒水し,ダイオキシ
ン類同伴の泥水を該土壌から自重で流出させてダイオキ
シン類濃度の低下した土壌を得る汚染土壌の浄化方法。
2. Soil contaminated with dioxins is conveyed by a transfer means while hot water is sprinkled thereon, and mud accompanying dioxins is allowed to flow out of the soil by its own weight to remove the soil having a reduced concentration of dioxins. How to purify the contaminated soil you get.
【請求項3】 ダイオキシン類で汚染された土壌を容器
に入れて熱水と接触させたあと,ダイオキシン類同伴の
泥水を該土壌から分離してダイオキシン類濃度の低下し
た土壌を得る汚染土壌の浄化方法。
3. A method for purifying contaminated soil in which dioxin-contaminated soil is put into a container and brought into contact with hot water, and then mud water accompanying dioxins is separated from the soil to obtain soil with a reduced dioxin concentration. Method.
【請求項4】 ダイオキシン類で汚染された土壌と熱水
とを入れた容器から移送手段で斜め上方に内容物を払い
出すことによりダイオキシン類同伴の泥水を容器内に残
し,ダイオキシン類濃度の低下した土壌を容器外に排出
する汚染土壌の浄化方法。
4. A dioxin-contaminated muddy water is discharged obliquely upward from a container containing dioxin-contaminated soil and hot water by a transfer means, so that dioxin-enriched muddy water is left in the container to lower the dioxin concentration. Of contaminated soil by discharging polluted soil outside the container.
【請求項5】 ダイオキシン類で汚染された土壌は,汚
染地帯における表層土である請求項1ないし4のいずれ
かに記載の汚染土壌の浄化方法。
5. The method according to claim 1, wherein the soil contaminated with dioxins is a surface soil in a contaminated area.
【請求項6】 熱水には有機溶媒が添加される請求項1
ないし5のいずれかに記載の汚染土壌の浄化方法。
6. An organic solvent is added to the hot water.
6. The method for purifying contaminated soil according to any one of claims 5 to 5.
【請求項7】 ダイオキシン類濃度の低下した土壌を得
たあと,これにダイオキシン分解菌を添加する請求項1
ないし6のいずれかに記載の汚染土壌の浄化方法。
7. The method according to claim 1, wherein a soil having a reduced dioxin concentration is obtained, and a dioxin-degrading bacterium is added to the soil.
7. The method for purifying contaminated soil according to any one of claims 6 to 6.
【請求項8】 ダイオキシン類同伴の泥水は,熱を保有
した状態で土壌から分離される請求項1ないし7のいず
れかに記載の汚染土壌の浄化方法。
8. The method for purifying contaminated soil according to claim 1, wherein the mud accompanying dioxins is separated from the soil while retaining heat.
JP2000283589A 2000-09-19 2000-09-19 Traveling purification device Expired - Fee Related JP4315584B2 (en)

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JP4315584B2 JP4315584B2 (en) 2009-08-19

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009108581A (en) * 2007-10-30 2009-05-21 Penta Ocean Construction Co Ltd Earth and sand impurity separating bucket and separating method
JP2015211956A (en) * 2014-04-19 2015-11-26 加藤 行平 Radioactive polluted soil cleaning device and system

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104759462B (en) * 2015-04-15 2017-06-13 上田环境修复股份有限公司 A kind of Soil leaching upgrading prosthetic device with tail gas treating function

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009108581A (en) * 2007-10-30 2009-05-21 Penta Ocean Construction Co Ltd Earth and sand impurity separating bucket and separating method
JP2015211956A (en) * 2014-04-19 2015-11-26 加藤 行平 Radioactive polluted soil cleaning device and system

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