JP2004337695A - Purification method for heavy-metal-contaminated soil - Google Patents

Purification method for heavy-metal-contaminated soil Download PDF

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Publication number
JP2004337695A
JP2004337695A JP2003135568A JP2003135568A JP2004337695A JP 2004337695 A JP2004337695 A JP 2004337695A JP 2003135568 A JP2003135568 A JP 2003135568A JP 2003135568 A JP2003135568 A JP 2003135568A JP 2004337695 A JP2004337695 A JP 2004337695A
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Japan
Prior art keywords
soil
liquid
separating
heavy metals
contaminated soil
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JP2003135568A
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JP4097562B2 (en
Inventor
Noboru Nakada
暢 中田
Hiroshi Horiuchi
裕志 堀内
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Teijin Frontier Co Ltd
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Teijin Fibers Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for efficiently removing heavy metals from a heavy-metal-containing soil to separate and recover the heavy metals. <P>SOLUTION: The purification method for heavy-metal-containing soil comprises separating and removing heavy metals from a contaminated soil containing the heavy metals. The method comprises (a) a cleaning step for extracting metal components from the contaminated soil with a cleaning solution, (b) a separation step for separating a liquid obtained by the cleaning step and containing soil dispersed therein into the soil and a liquid containing a fine particle component, (c) an agglomeration step for agglomerating the liquid containing the fine particle component and obtained at the separation step, (d) a reseparation step for subjecting a liquid containing agglomerated particles dispersed therein and obtained at the agglomeration step to solid-liquid separation, and (e) a step for separating and recovering heavy metals from a liquid obtained at the reseparation step. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、重金属類を含んだ土壌の浄化処理方法に関するものである。さらに詳しくは、重金属類を含んだ土壌から重金属類を効率的に除去し、重金属類を分離回収する、土壌の浄化方法に関するものである。
【0002】
【従来の技術】
昨今、市街地再開発による調査の増加に伴い、工場跡地等の重金属汚染が判明する事例が増加している。平成14年の土壌汚染対策法の成立により、かかる土壌汚染に対する法制度が整備され、汚染の除去等の処置の事例が今後大幅に増加することが予測される。
【0003】
土壌の重金属汚染に対して、現在国内で行われている汚染対策は、不溶化処理、覆土工事、遮水工事など、周辺環境を汚染源から遮断する方法が一般的である。しかし、これらの方法は重金属類を現場に残したままであることから、環境の変化により再溶出して汚染を引き起こす危険性が残るために土地の資産価値が損なわれる可能性があるうえ、希少資源である重金属類の節約の観点からも好ましい方法とはいえない。
【0004】
上記の方法とは別の方法として、汚染土壌を掘削して清浄な土壌と入れ替え、該汚染土壌を産業廃棄物として処分する方法もある。しかし、近年最終処分場の逼迫が社会問題となっており、この方法も好ましいとはいえない。
【0005】
このような問題を解消するため、汚染土壌から汚染物を分離・除去して清浄な土壌へ戻す、土壌の浄化法の導入が検討されている。例えば、▲1▼汚染土壌の分級洗浄、▲2▼泡沫浮上法による土壌洗浄、▲3▼重金属汚染土壌の加熱処理技術、▲4▼水蒸気加熱法による汚染土壌浄化、▲5▼塩化揮発法、▲6▼電気泳動土壌修復技術、▲7▼電気泳動法による重金属汚染土壌の浄化、▲8▼電気浸透土壌修復技術などが知られている。(非特許文献1参照)
【0006】
これらの浄化法のうち、汚染土壌の分級洗浄法は、土壌を分級しながら水に溶けやすい汚染物質を溶解して取り除くとともに、金属が主として吸着されやすい微小粒子も同時に取り除くことによって、汚染金属が分離された土壌を取り出す方法である。しかし、この方法には、汚染重金属が吸着された微小粒子分の廃棄物処理が必要という問題点がある。
【0007】
泡沫浮上法による土壌洗浄法は、浮遊選鉱法ともいわれる技術で、疎水性表面を有する粒子をバブリングによって生じた泡沫に付着させて浮上分離する方法である。この方法は、疎水性表面を有する重金属の硫化物には効果的であるが、一般の土壌中に含まれる重金属含有粒子が疎水性表面を必ずしも有していないため、通常の浮遊選鉱では分離できない場合があるという問題点がある。硫化剤を併用して重金属を硫化物に変換させて分離する方法も考えられるが、硫化剤が高価であったり、土壌中に硫化剤が残留する可能性があるという問題がある。
【0008】
重金属汚染土壌の加熱処理技術は、重金属含有土壌に空気を通じながら1000℃程度に加熱して揮発しやすい金属を土壌から除去する方法である。この方法は、有機物との複合汚染土壌の土壌処理技術としては有効であるが、揮発する前に溶融しやすい重金属は処理できないこと、重金属を含んだ排ガスを処理する必要があること、加熱した土壌は元の土壌とはかなり性質が変化するため埋め戻しが困難であるなどの問題がある。
【0009】
水蒸気加熱法による汚染土壌浄化法は、土壌を加熱しながら加熱蒸気を吹き込んで金属を揮散させることにより土壌から金属を分離する技術である。この方法は、金属の分離効率に優れており、土壌を埋め戻しできる可能性も高い利点を有するが、加熱蒸気を供給する熱源が必要なこと、排ガスおよび凝縮水の処理が必要となること、揮発しにくい金属は分離できないなどの問題がある。
【0010】
塩化揮発法は、塩化カルシウム水溶液を土壌に添加し、重金属を塩化物にして沸点を低下させたのち、土壌を800〜1000℃に加熱して重金属を揮発分離する方法である。この方法も、重金属汚染処理の加熱処理技術や水蒸気加熱法による汚染土壌浄化の方法と同様に、排ガスの処理が必要であり、排ガスの処理に用いられる水の処理が必要となることや、加熱によって非意図的に有害物質が生成する恐れがあるなどの問題がある。
【0011】
電気泳動土壌修復技術は、土壌中の間隙に水を満たして直流電流を加えることにより、陰イオンの金属を陽極に移動させ、陽極部に濃縮された金属を回収する方法である。この方法によれば、原位置で抽出できるが、除去速度が速くないために時間がかかるという問題がある。また、土壌中に塩素イオンが大量に含まれる場合には、塩素ガスの発生が予想されるという問題もある。
【0012】
電気泳動法による重金属汚染土壌の浄化は、水を含んだ土壌に直流電流を流すことで、陰イオンは陽極に、陽イオンは陰極に移動するので、土壌中に挿入した電極付近に重金属を集めて除去する技術であり、電極を半透性膜で覆い、膜内に注入したEDTA溶液を循環することにより重金属を捕集する方法が報告されている。この方法も、電気泳動土壌修復技術の方法と同様に、処理に時間がかかる傾向があり、また、塩素イオンが大量に含まれる場合には塩素ガスの発生に留意しなければならないといった問題もある。
【0013】
電気浸透土壌修復技術は、地中に直流電流を流して電磁場を作り、土壌水を陽極から陰極へ移動させて、この流れとともに水溶性の金属を陽極から陰極に移動させて回収する方法である。この方法も、電気泳動土壌修復技術や電気泳動法による重金属汚染土壌の浄化方法と同様に処理時間が長くかかり、塩素イオンが土壌中に含まれる場合には塩素ガスの発生に留意する必要があること、水を供給する必要がある場合にはこの水の後処理も必要になるなどの問題がある。
【0014】
【非特許文献1】
「土壌・地下水に係る調査・対策指針運用基準」環境庁水質保全局編,1999年,p.51−53
【0015】
【発明が解決しようとする課題】
本発明は、上記のような従来技術の課題を背景になされたもので、その目的は、土壌中の有害な重金属を、副生廃棄物を出すことなく効率的に分離・除去して、汚染土壌を修復する浄化方法を提供することにある。
【0016】
【課題を解決するための手段】
本発明者らは、上記課題を達成するために鋭意検討を重ねた結果、
重金属類を含有する汚染土壌を浄化する方法において、該方法には下記(a)〜(e)の工程が存在することを特徴とする汚染土壌の浄化方法により達成できることが見いだされた。
(a)洗浄液を用いて汚染土壌中の金属成分を抽出する洗浄工程
(b)洗浄工程で得られた土壌が分散している液を土壌と細粒分を含有する液とに分離する分離工程
(c)分離工程で得られた細粒分を含有する分離液を凝集処理する凝集工程
(d)凝集工程で得られた凝集粒子が分散している液を固液分離する再分離工程
(e)再分離工程で得られた分離液から重金属類を分離回収する工程
【0017】
【発明の実施の形態】
以下、本発明の実施の形態について詳細に説明する。
本発明が浄化の対象する汚染土壌に含有される重金属類としては、例えば、カドミウム、銅、鉛、砒素、カルシウム、鉄、アルミニウムなどを挙げることができる。これらの重金属類の土壌中における存在形態は特に限定されないが、通常イオン、酸化物、水酸化物などの状態で含有されている場合が多い。
【0018】
本発明においては、先ず洗浄液を用いて上記の汚染土壌中の重金属成分を洗浄液中に抽出する。その際、該汚染土壌は、予め粉砕機等で粉砕して微粒子としてもよいし、そのまま用いてもよい。粉砕機は既存の粉砕機を用いればよく、例えば、高速回転式衝撃粉砕機、自生粉砕機、ボールミル等を挙げることができる。一方、洗浄液としては、重金属成分を溶解抽出できるものであれば特に限定されず、例えば酸水溶液、アルカリ水溶液、キレート剤溶液等、任意の洗浄液を用いることができる。中でも酸水溶液が好ましく、特に塩酸水溶液が好ましい。
【0019】
上記の洗浄工程で、汚染土壌中の重金属成分は洗浄液中に抽出されるが、この工程により得られた土壌が分散している液を、土壌と細粒分を含有する液とに分離する。ここで用いられる分離装置としては、通常の遠心濾過機、ドラムフィルター、ヤングフィルター、フィルタープレス、ベルトプレス、液体サイクロンなど、任意の分離装置を用いることができる。分離された固形分は、該固形分中に残る洗浄液中の重金属イオン等の重金属成分をさらに回収するため、例えば新たな洗浄液での再洗浄及び固液分離を繰り返し実施してもよい。このようにして重金属類の含有量が低減された土壌は、浄化土壌として排出することができる。
【0020】
なお、上記の分離工程では、該工程の処理能力を増加させるため、土壌の細粒分、好ましくは粒径が100μm以下の細粒分を液側に同伴させる必要がある。ここで細粒分を液側に同伴させる方式は任意であるが、例えば分離装置の濾布の目開きを大きくするなどの手段を例示することができる。
【0021】
次に、上記分離工程で分離された、重金属及び土壌細粒分を含有する分離液に、例えば凝集剤(PAC等)を添加して該細粒分を凝集させる。得られた凝集粒子が分散する分散液を、例えば沈降装置に送って所定時間静置することにより再分離する。ここで分離された凝集細粒分は、例えば前記(b)の分離工程に返送することにより、該工程の分離装置で固形分として分離され、浄化土壌として排出される。
【0022】
一方、再分離工程で凝集細粒分から分離された重金属を含む分離液は、公知の処理装置を用いて該分離液から重金属成分を分離除去して処分施設へ送り、回収された洗浄液は、例えば洗浄工程の洗浄液や、分離された固形分の再洗浄用の洗浄液として循環使用することができる。
【0023】
以下、本発明の一態様を模式的に表した図1を用いて具体的に説明するが、本発明はこれにより何ら限定を受けるものではない。本発明においては、先ず重金属類を含有する土壌を、そのまま、あるいは粉砕機などを用いて微細な粒子となして、抽出装置(図中1)に送る。該抽出装置では、汚染土壌に洗浄液を添加した後に撹拌または振盪により、土壌粒子から重金属成分を抽出する。
【0024】
次いで、固液分離装置(図中2)にて固形分を分離する。その際、例えばフィルターの目開きを調整して、細粒分を液側に同伴させる。
【0025】
分離された固形分は、該固形分に残る残液中の重金属類イオンをさらに回収するため、固液分離装置(図中3)にて再洗浄および固液分離を繰り返し実施することが好ましい。該固液分離装置(図中3)からの洗浄液は、排液処理装置(図中6)に送られ、重金属が除去され、循環洗浄液として再使用される。再洗浄された、重金属が所望の含有量まで低減された土壌は、浄化土壌として排出される。
【0026】
固液分離装置(図中2)で分離された、重金属および細粒分を含む洗浄液は凝集装置(図中4)に送られる。該凝集装置では、凝集剤(PAC等)を添加して細粒分を凝集させ、沈降装置(図中5)に送られる。そこで所定時間静置し、沈降した凝集細粒分は固液分離装置(図中2)へ返送される。
【0027】
一方、沈降装置(図中5)で分離された重金属を含む洗浄液は、排液処理装置(図中6)で重金属成分が分離除去され、回収された洗浄液は、固液分離装置(図中3)の洗浄液として循環使用される。
【0028】
【発明の効果】
以上に説明した本発明によれば、土壌中の有害な重金属を効率よく、しかも、副生廃棄物を出すことなく分離・除去できるので、汚染土壌を浄化土壌に修復する方法として極めて有用である。
【図面の簡単な説明】
【図1】本発明実施の一態様を示したプロセスの概略図である。
【符号の説明】
1 抽出装置
2 固液分離装置
3 固液分離装置
4 凝集装置
5 沈降装置
6 排液処理装置
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for purifying soil containing heavy metals. More specifically, the present invention relates to a soil purification method for efficiently removing heavy metals from soil containing heavy metals and separating and recovering the heavy metals.
[0002]
[Prior art]
In recent years, with the increase in investigations due to redevelopment of urban areas, cases in which heavy metal contamination at factory sites and the like are found are increasing. With the enactment of the Soil Contamination Countermeasures Law of 2002, a legal system for such soil contamination is established, and it is expected that the number of cases of measures such as removal of contamination will increase significantly in the future.
[0003]
The current countermeasures against heavy metal contamination in the soil in Japan are generally methods of isolating the surrounding environment from the source of pollution, such as insolubilization, earth covering, and water shielding. However, these methods leave heavy metals in the field, which may lead to pollution due to re-elution due to changes in the environment, which may damage the property value of the land. It is not a preferable method from the viewpoint of saving heavy metals.
[0004]
As another method different from the above method, there is a method of excavating contaminated soil and replacing it with clean soil, and disposing the contaminated soil as industrial waste. However, the tightness of the final disposal site has become a social problem in recent years, and this method is not preferable.
[0005]
In order to solve such a problem, introduction of a soil purification method for separating and removing contaminants from contaminated soil and returning the soil to clean soil is being studied. For example, (1) classification cleaning of contaminated soil, (2) soil cleaning by foam floating method, (3) heat treatment technology for heavy metal contaminated soil, (4) purification of contaminated soil by steam heating method, (5) chloride volatilization method, (6) Electrophoretic soil repair technology, (7) Purification of heavy metal contaminated soil by electrophoresis, (8) Electroosmotic soil repair technology, and the like are known. (See Non-Patent Document 1)
[0006]
Among these purification methods, the classification and cleaning method for contaminated soil involves dissolving and removing contaminants that are easily soluble in water while classifying the soil, and simultaneously removing microparticles that are mainly adsorbed by metals. It is a method to take out the separated soil. However, this method has a problem that it is necessary to treat the waste of the fine particles having the contaminated heavy metal adsorbed thereon.
[0007]
The soil washing method based on the foam flotation method is a technique also referred to as flotation ore separation method, in which particles having a hydrophobic surface are attached to foam generated by bubbling and floated and separated. This method is effective for heavy metal sulfides having a hydrophobic surface, but cannot be separated by ordinary flotation because heavy metal-containing particles contained in general soil do not necessarily have a hydrophobic surface There is a problem that there are cases. Although a method of converting heavy metals into sulfides and separating them by using a sulphide in combination is also conceivable, there is a problem that the sulphide is expensive or the sulphide may remain in the soil.
[0008]
The heat treatment technique for heavy metal contaminated soil is a method of removing volatile metals from the soil by heating to about 1000 ° C. while passing air through the heavy metal-containing soil. This method is effective as a soil treatment technology for complex contaminated soil with organic matter, but cannot treat heavy metals that are easily melted before volatilizing, it is necessary to treat exhaust gas containing heavy metals, There are problems such as difficulty in backfilling because the properties change considerably from the original soil.
[0009]
The contaminated soil purification method by the steam heating method is a technique for separating a metal from soil by blowing heated steam while heating the soil to volatilize the metal. This method is excellent in metal separation efficiency and has a high possibility that soil can be backfilled.However, it requires a heat source for supplying heated steam, requires treatment of exhaust gas and condensed water, There is a problem that metals that are difficult to volatilize cannot be separated.
[0010]
The chloride volatilization method is a method in which a calcium chloride aqueous solution is added to soil to convert heavy metals into chlorides to lower the boiling point, and then the soil is heated to 800 to 1000 ° C. to volatilize and separate heavy metals. This method also requires the treatment of exhaust gas, as well as the heat treatment technology for heavy metal contamination treatment and the method of contaminated soil purification by steam heating, and requires the treatment of water used for exhaust gas treatment, Harmful substances may be generated unintentionally.
[0011]
The electrophoretic soil restoration technique is a method in which a gap in the soil is filled with water and a direct current is applied to move an anion metal to the anode and collect the metal concentrated in the anode. According to this method, extraction can be performed at the original position, but there is a problem that it takes time because the removal speed is not high. In addition, when the soil contains a large amount of chloride ions, there is a problem that generation of chlorine gas is expected.
[0012]
Purification of heavy metal-contaminated soil by electrophoresis is performed by passing a direct current through water-containing soil, where anions move to the anode and cations move to the cathode, so heavy metals are collected near the electrode inserted into the soil. A method of collecting heavy metals by covering an electrode with a semipermeable membrane and circulating an EDTA solution injected into the membrane has been reported. This method, like the method of the electrophoretic soil remediation technique, tends to take a long time for the treatment, and also has a problem that when a large amount of chloride ions is contained, attention must be paid to the generation of chlorine gas. .
[0013]
Electro-osmosis soil restoration technology is a method in which a direct current is passed through the ground to create an electromagnetic field, soil water is moved from the anode to the cathode, and with this flow, water-soluble metals are moved from the anode to the cathode to collect them. . This method also requires a long treatment time, similar to the method for remediation of heavy metal contaminated soil by electrophoretic soil remediation technology or electrophoresis, and it is necessary to pay attention to the generation of chlorine gas when chlorine ions are contained in the soil. In addition, when water needs to be supplied, there is a problem that post-treatment of the water is also required.
[0014]
[Non-patent document 1]
"Operation Standards for Surveys and Countermeasures for Soil and Groundwater," edited by Water Quality Bureau, Environment Agency, 1999, p. 51-53
[0015]
[Problems to be solved by the invention]
The present invention has been made in the background of the above-mentioned problems of the prior art, and its object is to efficiently separate and remove harmful heavy metals in soil without producing by-product waste, thereby contaminating the soil. It is to provide a purification method for repairing soil.
[0016]
[Means for Solving the Problems]
The present inventors have conducted intensive studies in order to achieve the above object,
It has been found that a method for purifying contaminated soil containing heavy metals can be achieved by a method for purifying contaminated soil characterized by including the following steps (a) to (e).
(A) a washing step of extracting metal components in contaminated soil using a washing liquid; and (b) a separating step of separating a liquid in which the soil obtained in the washing step is dispersed into a soil and a liquid containing fine particles. (C) an aggregating step of aggregating the separated liquid containing fine particles obtained in the separating step; (d) a re-separating step of solid-liquid separating the liquid in which the agglomerated particles obtained in the aggregating step are dispersed (e) A) separating and recovering heavy metals from the separated liquid obtained in the re-separation step;
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail.
The heavy metals contained in the contaminated soil to be purified by the present invention include, for example, cadmium, copper, lead, arsenic, calcium, iron, aluminum and the like. The form in which these heavy metals are present in the soil is not particularly limited, but is usually contained in the form of ions, oxides, hydroxides, and the like.
[0018]
In the present invention, first, heavy metal components in the above-mentioned contaminated soil are extracted into the washing liquid using the washing liquid. At this time, the contaminated soil may be pulverized by a pulverizer or the like in advance to obtain fine particles, or may be used as it is. An existing pulverizer may be used as the pulverizer, and examples thereof include a high-speed rotary impact pulverizer, an autogenous pulverizer, and a ball mill. On the other hand, the washing liquid is not particularly limited as long as it can dissolve and extract heavy metal components. For example, an arbitrary washing liquid such as an aqueous acid solution, an aqueous alkali solution, and a chelating agent solution can be used. Among them, an aqueous acid solution is preferable, and an aqueous hydrochloric acid solution is particularly preferable.
[0019]
In the above-mentioned washing step, heavy metal components in the contaminated soil are extracted into the washing liquid. The liquid in which the soil obtained in this step is dispersed is separated into a soil and a liquid containing fine particles. As the separation device used here, any separation device such as a usual centrifugal filter, a drum filter, a young filter, a filter press, a belt press, and a liquid cyclone can be used. In order to further recover heavy metal components such as heavy metal ions in the washing liquid remaining in the separated solid matter, for example, re-washing with a new washing liquid and solid-liquid separation may be repeatedly performed. The soil in which the content of heavy metals has been reduced in this way can be discharged as purified soil.
[0020]
In the above-mentioned separation step, in order to increase the treatment capacity of the step, it is necessary to bring fine particles of soil, preferably fine particles having a particle size of 100 μm or less, into the liquid side. Here, the method of entraining the fine particles into the liquid side is arbitrary, and examples thereof include means for increasing the aperture of the filter cloth of the separation device.
[0021]
Next, for example, an aggregating agent (PAC or the like) is added to the separated liquid containing the heavy metal and the soil fine particles separated in the above separation step to aggregate the fine particles. The dispersion liquid in which the obtained aggregated particles are dispersed is sent again to, for example, a sedimentation device and left for a predetermined time to be separated again. The separated aggregated fine particles are returned to the separation step (b), for example, to be separated as solids by the separation device in this step, and are discharged as purified soil.
[0022]
On the other hand, the separation liquid containing the heavy metal separated from the aggregated fine particles in the re-separation step is separated and removed from the separation liquid using a known processing apparatus and sent to a disposal facility, and the collected cleaning liquid is, for example, It can be circulated and used as a washing solution in the washing step or a washing solution for rewashing the separated solids.
[0023]
Hereinafter, one embodiment of the present invention will be specifically described with reference to FIG. 1 schematically illustrating the present invention, but the present invention is not limited thereto. In the present invention, first, soil containing heavy metals is sent to an extraction device (1 in the figure) as it is or as fine particles using a crusher or the like. The extractor extracts a heavy metal component from soil particles by stirring or shaking after adding a washing liquid to contaminated soil.
[0024]
Next, the solid content is separated by a solid-liquid separation device (2 in the figure). At this time, for example, the aperture of the filter is adjusted so that the fine particles are entrained on the liquid side.
[0025]
The separated solid is preferably subjected to repeated washing and solid-liquid separation in a solid-liquid separator (3 in the figure) in order to further recover heavy metal ions in the residual liquid remaining in the solid. The cleaning liquid from the solid-liquid separator (3 in the figure) is sent to a drainage treatment apparatus (6 in the figure) to remove heavy metals and reused as a circulating cleaning liquid. The rewashed soil with the reduced heavy metal content is discharged as purified soil.
[0026]
The washing liquid containing heavy metals and fine particles separated by the solid-liquid separator (2 in the figure) is sent to the aggregating apparatus (4 in the figure). In the aggregating device, a coagulant (PAC or the like) is added to agglomerate the fine particles, and sent to a sedimentation device (5 in the figure). Then, the aggregated fine particles settled for a predetermined time are returned to the solid-liquid separator (2 in the figure).
[0027]
On the other hand, the cleaning liquid containing heavy metals separated by the sedimentation apparatus (5 in the figure) is separated and removed in a wastewater treatment apparatus (6 in the figure), and the recovered cleaning liquid is separated into a solid-liquid separation apparatus (3 in the figure). It is circulated and used as a cleaning solution.
[0028]
【The invention's effect】
According to the present invention described above, harmful heavy metals in soil can be efficiently separated and removed without producing by-product waste, so that they are extremely useful as a method for restoring contaminated soil to purified soil. .
[Brief description of the drawings]
FIG. 1 is a schematic diagram of a process illustrating one embodiment of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Extraction apparatus 2 Solid-liquid separation apparatus 3 Solid-liquid separation apparatus 4 Agglomeration apparatus 5 Sedimentation apparatus 6 Drainage treatment apparatus

Claims (4)

重金属類を含有する汚染土壌を浄化する方法において、該方法には下記(a)〜(e)の工程が存在することを特徴とする汚染土壌の浄化方法。
(a)洗浄液を用いて汚染土壌中の金属成分を抽出する洗浄工程
(b)洗浄工程で得られた土壌が分散している液を土壌と細粒分を含有する液とに分離する分離工程
(c)分離工程で得られた細粒分を含有する分離液を凝集処理する凝集工程
(d)凝集工程で得られた凝集粒子が分散している液を固液分離する再分離工程
(e)再分離工程で得られた分離液から重金属類を分離回収する工程
A method for purifying contaminated soil containing heavy metals, the method comprising the following steps (a) to (e):
(A) a washing step of extracting metal components in contaminated soil using a washing liquid; and (b) a separating step of separating a liquid in which the soil obtained in the washing step is dispersed into a soil and a liquid containing fine particles. (C) an aggregating step of aggregating the separated liquid containing fine particles obtained in the separating step; (d) a re-separating step of solid-liquid separating the liquid in which the agglomerated particles obtained in the aggregating step are dispersed (e) ) Step of separating and recovering heavy metals from the separated liquid obtained in the re-separation step
(a)の工程に用いる洗浄液が、塩酸水溶液である請求項1記載の汚染土壌の浄化方法。The method for purifying contaminated soil according to claim 1, wherein the washing liquid used in the step (a) is an aqueous hydrochloric acid solution. (b)の工程で得られる液に含有される細粒分の粒径が100μm以下である請求項1記載の汚染土壌の浄化方法。The method for purifying contaminated soil according to claim 1, wherein the particle diameter of the fine particles contained in the liquid obtained in the step (b) is 100 µm or less. (d)の工程で分離された固形分を(b)の工程の分散液に混合して固液分離する請求項1記載の汚染土壌の浄化方法。The method for purifying contaminated soil according to claim 1, wherein the solids separated in the step (d) are mixed with the dispersion liquid in the step (b) to perform solid-liquid separation.
JP2003135568A 2003-05-14 2003-05-14 Purification method for heavy metal contaminated soil Expired - Fee Related JP4097562B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4823387B1 (en) * 2011-03-01 2011-11-24 株式会社山▲崎▼砂利商店 Material recycling system for producing sand products from mineral mixtures
CN104438305A (en) * 2013-09-20 2015-03-25 重庆文理学院 Drum type soil heavy metal elution system
JP2015171709A (en) * 2014-02-24 2015-10-01 清水建設株式会社 Arsenic-contaminated soil washing method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4823387B1 (en) * 2011-03-01 2011-11-24 株式会社山▲崎▼砂利商店 Material recycling system for producing sand products from mineral mixtures
CN104438305A (en) * 2013-09-20 2015-03-25 重庆文理学院 Drum type soil heavy metal elution system
JP2015171709A (en) * 2014-02-24 2015-10-01 清水建設株式会社 Arsenic-contaminated soil washing method

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