JP2000051835A - Method for cleaning soil by using iron powder - Google Patents

Method for cleaning soil by using iron powder

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Publication number
JP2000051835A
JP2000051835A JP10228431A JP22843198A JP2000051835A JP 2000051835 A JP2000051835 A JP 2000051835A JP 10228431 A JP10228431 A JP 10228431A JP 22843198 A JP22843198 A JP 22843198A JP 2000051835 A JP2000051835 A JP 2000051835A
Authority
JP
Japan
Prior art keywords
soil
iron powder
heavy metals
acid
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.)
Pending
Application number
JP10228431A
Other languages
Japanese (ja)
Inventor
Tatsuya Kikuchi
達也 菊地
Satoshi Kawakami
智 川上
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.)
Dowa Holdings Co Ltd
Original Assignee
Dowa Mining Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Dowa Mining Co Ltd filed Critical Dowa Mining Co Ltd
Priority to JP10228431A priority Critical patent/JP2000051835A/en
Publication of JP2000051835A publication Critical patent/JP2000051835A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a method for leaning soil which removes pollutants effectively from the soil polluted with heavy metals and reduces the pollution load on process drainage. SOLUTION: Soil polluted with heavy metal is added with water, iron powder, and a chemical agent which promotes the movement of the heavy metals, the mixture is agitated, the heavy metals in the soil are adsorbed on the iron powder, the iron powder is separated from the soil by using a wet magnetic separator, so that the pollutants are removed efficiently, and a pollutant load on drainage can bed reduced.

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、鉛、ヒ素、カドミ
ウム、六価クロム、セレン、水銀、アンチモン、銅、亜
鉛などの重金属で汚染された土壌の浄化方法に関する。
The present invention relates to a method for purifying soil contaminated with heavy metals such as lead, arsenic, cadmium, hexavalent chromium, selenium, mercury, antimony, copper and zinc.

【0002】[0002]

【従来の技術】重金属で汚染された土壌から重金属を除
去して浄化土を得るための一般的な方法として、分級に
よる方法、化学抽出による方法がある。前者分級による
方法、例えば特開平6−343948号によれば、重金
属、放射性物質、有機物のうち少なくとも1種に汚染さ
れた粒状物質を汚染物質流動化溶液で洗浄し、まず大粒
子を機械的に分離水洗する。汚染物質とともに微粒子を
流動化溶液で中程度粒子から分離し、さらに中程度粒子
をアトリッション研磨して付着微粒子を脱落させ、得ら
れた微粒子を中程度粒子から分離する。後者化学抽出に
よる方法、例えばHerry M. Freeman, Eugene F.Harris
著Hazardous Waste Remediation (1995 Technomic Publ
ishing Company, Inc.) P103〜112「土壌洗浄法」によ
れば、table 10.3に、分級と化学抽出を併用する土壌洗
浄法において、重金属を抽出するために、酸、アルカ
リ、キレート剤などの薬品を用いる方法が開示されてい
る。一方、本出願人は有機塩素系化合物で汚染された土
壌の無害化処理方法として鉄粉を用いた方法の特許出願
を行っている(特願平9-367177)
2. Description of the Related Art As a general method for obtaining purified soil by removing heavy metals from soil contaminated with heavy metals, there are a method by classification and a method by chemical extraction. According to the former classification method, for example, according to JP-A-6-343948, particulate matter contaminated by at least one of heavy metals, radioactive substances, and organic substances is washed with a contaminant fluidizing solution, and large particles are first mechanically removed. Separately wash. The fine particles together with the contaminants are separated from the medium particles by a fluidizing solution, and the medium particles are further subjected to attrition polishing to remove attached fine particles, and the obtained fine particles are separated from the medium particles. Methods by the latter chemical extraction, such as Herry M. Freeman, Eugene F. Harris
By Hazardous Waste Remediation (1995 Technomic Publ
ishing Company, Inc.) According to P103-112 “Soil washing method”, in Table 10.3, in the soil washing method using classification and chemical extraction, chemicals such as acid, alkali, chelating agent, etc. Are disclosed. On the other hand, the present applicant has filed a patent application for a method using iron powder as a method for detoxifying soil contaminated with organochlorine compounds (Japanese Patent Application No. 9-367177).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、分級に
よる方法では、土壌と汚染物質の存在粒度の偏りによっ
て土壌を浄化するため、浄化土と同粒度で存在する汚染
物質が存在する場合に除去の効率が悪い。また化学抽出
による方法では、土壌から汚染物質の除去率は高くなる
ものの、抽出薬剤により浄化土壌からの汚染物質の溶出
量を高める結果となりやすい。そのため、抽出後に不溶
化処置を施すなどの付加工程が必要となり、さらに汚染
物質の大半は抽出液中に移行するため、排水の無害化処
理の負担が大きくなる。したがって本発明の目的は、重
金属で汚染された土壌の浄化にあたり、効果的に汚染物
質を土壌から除去するとともに、工程排水への汚染負荷
を軽減させる浄化方法を提供することにある。
However, in the method based on classification, the soil is purified by the uneven distribution of the particle size of the soil and the contaminants. Therefore, when the contaminants existing at the same particle size as the purified soil are present, the efficiency of removal is reduced. Is bad. In the method using chemical extraction, the removal rate of contaminants from soil is increased, but the amount of contaminants eluted from purified soil is likely to be increased by the extracted chemical. For this reason, an additional step such as performing an insolubilization treatment after the extraction is required, and most of the contaminants move into the extract, so that the burden of the detoxification treatment of the wastewater increases. Therefore, an object of the present invention is to provide a purification method for removing soil contaminated with heavy metals, effectively removing contaminants from the soil, and reducing the pollution load on process wastewater.

【0004】[0004]

【課題を解決するための手段】本発明者らは上記目的を
達成すべく鋭意研究したところ、先願の方法をさらに改
良すれば重金属をも浄化できることを見出した。すなわ
ち、重金属を含む汚染土壌に対して、物質移動媒体とし
ての水と鉄粉と重金属の移動を促す薬剤を加え、汚染物
質を鉄粉に担持すなわち物理的吸着・化学的結合させ、
次いで汚染物質と鉄粉を磁選機を用いて土壌から分離す
るようにすれば、前記分級法よりも効果的に汚染物質を
除去でき、さらに排水への汚染物質負荷も軽減できるこ
とを見出し、本発明に到達した。
Means for Solving the Problems The inventors of the present invention have made intensive studies to achieve the above object, and have found that if the method of the prior application is further improved, heavy metals can be purified. That is, to the contaminated soil containing heavy metals, water and iron powder as a mass transfer medium, an agent that promotes the transfer of heavy metals is added, and the contaminants are carried on the iron powder, that is, physically adsorbed and chemically bonded,
Then, if the contaminants and the iron powder are separated from the soil using a magnetic separator, it has been found that the contaminants can be removed more effectively than the classification method, and that the pollutant load on the wastewater can be reduced. Reached.

【0005】すなわち、本発明は第1に、重金属で汚染
された土壌を浄化する方法であって、重金属で汚染され
た土壌に対し、水と鉄粉と重金属の移動を促す薬剤を加
えて攪拌し、土壌中の重金属を鉄粉に吸着させる第1工
程と、次いで第1工程で重金属を担持した鉄粉を浄化土
壌から分離する第2工程からなることを特徴とする鉄粉
を用いた土壌の浄化方法;第2に、前記鉄粉は土壌に対
して1〜10重量%添加される上記第1記載の浄化方
法;第3に、前記重金属を担持した鉄粉と浄化土壌を分
離する分離機が磁選機である上記第1または第2記載の
浄化方法;第4に、前記重金属の移動を促す薬剤が、塩
酸・硫酸・硝酸・燐酸・酢酸からなる群より選ばれる少
なくとも1種の酸または、水酸化ナトリウム・水酸化カ
リウム・消石灰・炭酸カルシウムからなる群より選ばれ
る少なくとも1種のアルカリ、または各種キレート剤、
またはこれらの組み合わせである上記第1または2記載の
浄化方法を提供するものである。
That is, the present invention firstly provides a method for purifying soil contaminated with heavy metals, in which an agent for promoting the movement of water, iron powder and heavy metals is added to the soil contaminated with heavy metals, followed by stirring. A first step of adsorbing heavy metals in the soil to the iron powder, and a second step of separating the iron powder carrying the heavy metals in the first step from the purified soil. Secondly, the iron powder is added in an amount of 1 to 10% by weight based on the soil; thirdly, a separation method of separating the heavy metal-supporting iron powder from the purified soil. Fourth, the purification method according to the first or second aspect, wherein the agent is a magnetic separator; Fourth, the agent for promoting the movement of the heavy metal is at least one acid selected from the group consisting of hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, and acetic acid. Or sodium hydroxide, potassium hydroxide, slaked lime, carbonic acid At least one alkali selected from the group consisting of calcium or various chelating agents,
Or a purification method according to the first or second aspect, which is a combination thereof.

【0006】[0006]

【発明の実施の形態】本発明法は、鉛、ヒ素、カドミウ
ム、六価クロム、セレン、水銀、アンチモン、銅、亜鉛
などの重金属により汚染された土壌を対象とする。汚染
土壌は、原位置から掘削された後、前処理として夾雑物
(コンクリートがら、鉄筋、木片等)を除き、好ましく
はふるいや破砕機等で整粒しておいて、第1工程として
の以下の方法により土壌中の汚染物質を鉄粉に吸着・結
合させる。
DETAILED DESCRIPTION OF THE INVENTION The method of the present invention is directed to soil contaminated with heavy metals such as lead, arsenic, cadmium, hexavalent chromium, selenium, mercury, antimony, copper, zinc, and the like. After the contaminated soil is excavated from the original position, the contaminants (concrete, rebar, wood chips, etc.) are removed as a pretreatment, and are preferably sized with a sieve or a crusher. Absorb and bind the contaminants in the soil to the iron powder by the method described above.

【0007】まず土壌には汚染物質の移動媒体として水
を添加する。土壌:添加水の比率はおもに土壌の粒度に
より1:0.5〜1:20の範囲で選択するのが適当で
ある。すなわち、土壌粒子が数ミリメートルよりも大き
な砂礫質の場合には、その後の攪拌混合装置としてニー
ダー、ミキサー、ブレンダーなどを用いるのがよい。そ
のために水分を少な目にして土壌:添加水の比率を1:
0.5〜1:2程度とする。また、土壌粒子が数ミリメ
ートルよりも小さな砂質またはそれよりも小さな粘土質
の場合には、攪拌混合装置としてアジデータを用いるの
が効果的なため、土壌:添加水の比率はスラリーとして
扱える1:5〜1:20程度が望ましい。
First, water is added to soil as a transport medium for pollutants. It is appropriate to select the ratio of soil: added water in the range of 1: 0.5 to 1:20 mainly depending on the particle size of the soil. That is, when the soil particles are gravel larger than several millimeters, it is preferable to use a kneader, a mixer, a blender, or the like as the subsequent stirring and mixing device. Therefore, reduce the amount of water and reduce the ratio of soil: added water to 1:
0.5 to about 1: 2. Also, when the soil particles are sandy smaller than several millimeters or clay smaller than a few millimeters, it is effective to use agitator as a stirring and mixing device. : About 5 to 1:20 is desirable.

【0008】鉄粉を混合して汚染物質を吸着・結合させ
るときに、土壌から汚染物質を遊離させる薬剤を併用す
ることで、土壌からの汚染物質の除去率を向上させるこ
とができる。土壌から汚染物質を遊離させる薬剤には、
化学抽出で一般的に用いられる薬剤が利用できる。すな
わち、酸として塩酸・硫酸・硝酸・燐酸・酢酸など、ア
ルカリとして水酸化ナトリウム・水酸化カリウム・消石
灰・炭酸カルシウムなど、その他に金属抽出剤として各
種のキレート剤などを利用して土壌中の汚染物質を移動
媒体である水中に遊離させ、これを鉄粉に吸着・結合さ
せることができる。
When the iron powder is mixed to adsorb and bind the contaminants, the use of an agent for releasing the contaminants from the soil is used together, whereby the contaminant removal rate from the soil can be improved. Drugs that release pollutants from soil include:
Drugs commonly used in chemical extraction are available. That is, soil contamination using hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid, etc. as an acid, sodium hydroxide, potassium hydroxide, slaked lime, calcium carbonate, etc. as an alkali, and various chelating agents as a metal extractant. The substance can be released into water as a transfer medium, and can be adsorbed and bound to iron powder.

【0009】混合する鉄粉には、反応性・吸着性を高く
するために150μm以下の粒径のものが90重量%以
上存在する粉状鉄粉が望ましい。粒度が荒いと反応性・
吸着性が悪くなり、極度に粒子が細かいと磁選における
実収率を低める。土壌に対して添加する割合は、1〜2
0重量%、好ましくは1〜10重量%の間が適当であ
る。これより少量だと汚染物質の除去効果が不足し、多
すぎると経済的に不利となる。鉄粉そのものの持つ物理
吸着能力は、ほとんどすべての汚染物質に対して有効で
ある。汚染物質がクロムや銅などのように酸化還元状態
の影響を受け易い場合、重金属が鉄と反応してフェライ
ト化などにより化学結合する場合には、鉄粉による担持
効果は一層強固となる。
The iron powder to be mixed is desirably a powdery iron powder containing 90% by weight or more of particles having a particle size of 150 μm or less in order to enhance reactivity and adsorptivity. Reactivity when the particle size is coarse
Adsorption is poor, and extremely fine particles reduce the actual yield in magnetic separation. The ratio of addition to soil is 1-2
0% by weight, preferably between 1 and 10% by weight is suitable. If the amount is smaller than this, the effect of removing contaminants is insufficient, and if it is too large, it is economically disadvantageous. The physical adsorption capacity of iron powder itself is effective for almost all pollutants. When the pollutant is susceptible to the oxidation-reduction state, such as chromium or copper, or when the heavy metal reacts with iron and chemically bonds by ferrite formation, the effect of supporting the iron powder is further enhanced.

【0010】第2工程として以下のように土壌と鉄粉を
分離する。すなわち、土壌から鉄粉を分離する方法とし
ては、湿式磁選機を用いるのが効果的である。ドラム型
湿式磁選機を用いる場合には、磁力として1200ガウ
ス以上望ましくは1500ガウス以上であることが、土
壌から鉄粉を効果的に分離するために必要である。磁選
機には希土類磁石や電磁石を利用して磁力をより強くす
べく考案された高価な機種もあるが、土壌から鉄粉を分
離するためには必ずしもそのような高価な磁選機を用い
る必要はない。以上説明したように本発明の方法によれ
ば、各種重金属で汚染された土壌からの重金属除去が可
能である。
As a second step, soil and iron powder are separated as follows. That is, as a method of separating iron powder from soil, it is effective to use a wet magnetic separator. When a drum-type wet magnetic separator is used, a magnetic force of 1200 gauss or more, preferably 1500 gauss or more is necessary for effectively separating iron powder from soil. Although there are expensive models of magnetic separators designed to increase magnetic force using rare earth magnets and electromagnets, it is not always necessary to use such expensive magnetic separators to separate iron powder from soil. Absent. As described above, according to the method of the present invention, heavy metals can be removed from soil contaminated with various heavy metals.

【0011】[0011]

【実施例】鉛、ヒ素、カドミウムで汚染された風乾土壌
1kgに、水5Lを加えてスラリーとした。鉛・ヒ素・カ
ドミウムを水中に遊離させるためpH2となるまで硫酸を
加えた後、鉄粉50gを加えてポリエチレン製ビンに密
封し、往復振とう(200往復/分)で30分間攪拌し
た。その後水酸化ナトリウムを加えてpH8に中和してさ
らに5Lの水を加えて磁選に適当なスラリー濃度とし、
湿式ドラム型磁選機(日本エリーズ社製、ドラム系12
インチ、磁力1500ガウス)で土壌スラリーと鉄粉を
分離した。土壌スラリーは、ブフナーロートを用いてNo
5Cろ紙でろ過して土壌と排水に分離した。上記操作に
より、表1の汚染土壌1kgから、表2の浄化土壌830
gを得ることができた。
EXAMPLE A slurry was prepared by adding 5 L of water to 1 kg of air-dried soil contaminated with lead, arsenic and cadmium. After sulfuric acid was added until pH 2 to release lead, arsenic, and cadmium into water, 50 g of iron powder was added, the mixture was sealed in a polyethylene bottle, and the mixture was stirred with reciprocating shaking (200 reciprocations / minute) for 30 minutes. Thereafter, sodium hydroxide was added to neutralize the solution to pH 8, and 5 L of water was further added to obtain a slurry concentration suitable for magnetic separation.
Wet drum type magnetic separator (Drum 12
Inch, magnetic force 1500 gauss) to separate the soil slurry and iron powder. Soil slurry was prepared using a Buchner funnel
The mixture was separated into soil and drainage by filtration through 5C filter paper. By the above operation, 1 kg of the contaminated soil shown in Table 1 was converted from the purified soil 830 shown in Table 2.
g could be obtained.

【0012】[0012]

【表1】 [Table 1]

【0013】[0013]

【表2】 [Table 2]

【0014】また、排水中の重金属濃度は表3のとおり
であった。
The concentration of heavy metals in the waste water is as shown in Table 3.

【表3】 [Table 3]

【0015】このように、鉛、ヒ素、カドミウムで汚染
された土壌に、担持物質としての鉄粉を加えて鉛・ヒ素
・カドミウムを吸着・結合させた後、磁選によって鉄粉
を除去することで、収率83%で土壌環境基準を満たす
浄化土を得ることができた。さらに、鉛・ヒ素について
は含有量についても環境基準の含有量参考値を下回る結
果となった。また、この方法で排出される排水の水質
は、鉛・ヒ素・カドミウムについて排水基準を十分に満
足するものであった。なお、表2、表3にはいずれも検
液(塩酸でpH5.8〜6.3とした純水への抽出水)中
の濃度で規制される土壌環境基準、および有害物質の公
共水域への排水基準を参考のため併記した。
As described above, iron powder as a support substance is added to soil contaminated with lead, arsenic, and cadmium to adsorb and bind lead, arsenic, and cadmium, and then iron powder is removed by magnetic separation. Purified soil satisfying the soil environmental standards was obtained with a yield of 83%. In addition, the content of lead and arsenic was lower than the reference value of the environmental standard. The water quality of the wastewater discharged by this method sufficiently satisfied the wastewater standards for lead, arsenic, and cadmium. Tables 2 and 3 show soil environmental standards regulated by the concentration in the test solution (extracted water into pure water adjusted to pH 5.8 to 6.3 with hydrochloric acid) and to public water bodies for harmful substances. The effluent standards are also shown for reference.

【0016】[0016]

【比較例1】実施例で用いたものと同じ汚染土壌1kg
を、風乾のまま目開き600μm、300μm、150μ
mの篩で順に分級した。150μmより細かい土壌を10
Lの水でリパルプして38μmの篩を用いて分級した。3
8μmより細かいスラリーは、ブフナーロートを用いてN
o5Cろ紙でろ過して土壌と排水に分離した。これから得
られた各粒群ごとの土壌重量ならびに鉛・ヒ素・カドミ
ウムの含有量は表4の通りとなった。鉛について、表4
中の粒度区分C→B→D→E→Aの順に含有量が増加してい
るため、表5のような浄化土の回収が見込まれる。ま
た、ヒ素については、表4中の粒度区分A→B→C→D→E
の順に含有量が増加しているため、表6のような浄化土
の回収が見込まれる。さらに、カドミウムについては、
表4中の粒土区分A→E→B→C→Dの順に含有量が増加して
いるため、表7のような浄化土の回収が見込まれる。
[Comparative Example 1] 1 kg of contaminated soil same as that used in the example
With air opening 600 μm, 300 μm, 150 μm
Classified in order with a sieve of m. 10 soils finer than 150 μm
It was repulped with L of water and classified using a 38 μm sieve. Three
Slurry finer than 8 μm is treated with a Buchner funnel
o Separated into soil and drainage by filtration through 5C filter paper. Table 4 shows the soil weight and the contents of lead, arsenic, and cadmium for each grain group obtained from this. Table 4 for lead
Since the content increases in the order of C, B, D, E, and A in the particle size categories, recovery of the purified soil as shown in Table 5 is expected. As for arsenic, the particle size classification in Table 4 is A → B → C → D → E
Therefore, the recovery of the purified soil as shown in Table 6 is expected. Furthermore, for cadmium,
Since the content increases in the order of granular soil classification A → E → B → C → D in Table 4, recovery of purified soil as shown in Table 7 is expected.

【0017】[0017]

【表4】 [Table 4]

【0018】[0018]

【表5】 [Table 5]

【0019】[0019]

【表6】 [Table 6]

【0020】[0020]

【表7】 [Table 7]

【0021】実施例で得られた表2の浄化土と、表5、
6、7を比較すると、分級によって実施例と同等に実収
率83%で浄化土を回収した場合には鉛、ヒ素、、カド
ミウムともに浄化土中の重金属含有量が実施例の場合よ
りも高くなる。また、含有量を実施例と同等に鉛430
mg/kg、ヒ素38mg/kg、カドミウム32mg/kgとなるよ
うに浄化土を限定すると、すべての場合において浄化土
の実収率が83%よりも低くなる。また、分級操作で発
生した排水中の重金属は、表8の通りであり、いずれも
実施例の場合より排水への汚染負荷が大きい。
The purified soil shown in Table 2 obtained in the examples and Table 5
Comparing 6 and 7, when the purified soil was collected with the actual yield of 83% as in the example by classification, the heavy metal content in the purified soil was higher for both lead, arsenic, and cadmium than in the example. . Further, the content of lead 430 was the same as in the example.
When the purified soil is limited to mg / kg, arsenic 38 mg / kg, and cadmium 32 mg / kg, the actual yield of the purified soil is lower than 83% in all cases. Further, the heavy metals in the wastewater generated by the classification operation are as shown in Table 8, and in each case, the pollution load on the wastewater is larger than in the case of the embodiment.

【0022】[0022]

【表8】 [Table 8]

【0023】[0023]

【比較例2】実施例で用いたものと同じ風乾土壌1kg
に、水5Lを加えてスラリーとした。鉛・ヒ素・カドミ
ウムを水中に遊離させるためpH2となるまで硫酸を加え
た後、ポリエチレン製ビンに密封し、往復振とう(20
0往復/分)で30分間攪拌した。スラリーを酸性のま
まブフナーロートを用いてNo5Cろ紙でろ過して土壌と
排水に分離した。ろ過した土壌に水5Lを加えてスラリ
ーとし、水酸化ナトリウムを加えてpH8に中和して、ブ
フナーロートを用いてNo5Cろ紙でろ過して土壌と排水
に分離した。これから得られた浄化土壌の分析結果は表
9のとおりであった。また、排水として得られた酸性ろ
液中およびpH8に中和したろ液中の重金属濃度は表10
のとおりであった。
[Comparative Example 2] 1 kg of the same air-dried soil as used in the examples
Was added with 5 L of water to form a slurry. Add sulfuric acid until pH 2 to release lead, arsenic, and cadmium into water, then seal in a polyethylene bottle and shake back and forth (20
(0 reciprocations / min) for 30 minutes. The slurry was filtered through a No. 5C filter paper using a Buchner funnel while being acidic to separate it into soil and drainage. 5 L of water was added to the filtered soil to form a slurry, which was neutralized to pH 8 by adding sodium hydroxide, and filtered through a No. 5C filter paper using a Buchner funnel to separate the soil into drainage. The results of analysis of the purified soil obtained from this are shown in Table 9. The heavy metal concentration in the acidic filtrate obtained as waste water and the filtrate neutralized to pH 8 is shown in Table 10.
It was as follows.

【0024】[0024]

【表9】 [Table 9]

【0025】[0025]

【表10】 実施例と比較すると、排水への重金属負荷が明らかに高
い。また、化学抽出においては浄化土壌の溶出値が抑制
されない結果となり、実施例の優位性が確認された。
[Table 10] Compared to the example, the heavy metal load on the wastewater is clearly higher. Further, in the chemical extraction, the elution value of the purified soil was not suppressed, and the superiority of the example was confirmed.

【0026】[0026]

【発明の効果】以上述べたように、本発明の方法によれ
ば、重金属で汚染された土壌から重金属を担持物質であ
る鉄粉に吸着させ、これを磁選機によって物理的に選別
分離するという簡単な工程で汚染土壌を清浄化できるの
で、土壌の修復に極めて有効である。
As described above, according to the method of the present invention, a heavy metal is adsorbed on iron powder as a supporting substance from soil contaminated with the heavy metal, and this is physically separated and separated by a magnetic separator. Since the contaminated soil can be purified by a simple process, it is extremely effective for soil restoration.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 重金属で汚染された土壌を浄化する方法
であって、重金属で汚染された土壌に対し、水と鉄粉と
重金属の移動を促す薬剤を加えて攪拌し、土壌中の重金
属を鉄粉に担持させる第1工程と、次いで第1工程で重
金属を担持した鉄粉を土壌から分離する第2工程からな
ることを特徴とする土壌の浄化方法。
Claims 1. A method for purifying soil contaminated with heavy metals, comprising adding an agent that promotes movement of water, iron powder, and heavy metals to the soil contaminated with heavy metals, stirring the mixture, and removing heavy metals in the soil. A soil purification method, comprising: a first step of supporting iron powder on iron powder; and a second step of separating the iron powder supporting heavy metal in the first step from soil.
【請求項2】 前記鉄粉は土壌に対して1〜10重量%
添加される請求項1記載の浄化方法。
2. The iron powder is 1 to 10% by weight based on the soil.
The purification method according to claim 1, which is added.
【請求項3】 前記重金属を担持した鉄粉と土壌を分離
する分離機が磁選機である請求項1または2記載の浄化
方法。
3. The purification method according to claim 1, wherein the separator that separates the soil from the iron powder carrying the heavy metal is a magnetic separator.
【請求項4】 前記重金属の移動を促す薬剤が、塩酸・
硫酸・硝酸・燐酸・酢酸からなる群より選ばれる少なく
とも1種の酸、または水酸化ナトリウム・水酸化カリウ
ム・消石灰・炭酸カルシウムからなる群より選ばれる少
なくとも1種のアルカリ、または各種キレート剤、また
はこれらの組み合わせである請求項1または2記載の浄化
方法。
4. The method according to claim 1, wherein the agent for promoting the movement of the heavy metal is hydrochloric acid.
At least one acid selected from the group consisting of sulfuric acid, nitric acid, phosphoric acid, and acetic acid, or at least one alkali selected from the group consisting of sodium hydroxide, potassium hydroxide, slaked lime, calcium carbonate, or various chelating agents, or 3. The purification method according to claim 1, which is a combination thereof.
JP10228431A 1998-08-12 1998-08-12 Method for cleaning soil by using iron powder Pending JP2000051835A (en)

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