JPH1110131A - Method for recovery of heavy metals from soil - Google Patents

Method for recovery of heavy metals from soil

Info

Publication number
JPH1110131A
JPH1110131A JP9200703A JP20070397A JPH1110131A JP H1110131 A JPH1110131 A JP H1110131A JP 9200703 A JP9200703 A JP 9200703A JP 20070397 A JP20070397 A JP 20070397A JP H1110131 A JPH1110131 A JP H1110131A
Authority
JP
Japan
Prior art keywords
soil
heavy metals
flotation
agent
sent
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
JP9200703A
Other languages
Japanese (ja)
Other versions
JP3682670B2 (en
Inventor
Chiaki Izumikawa
千秋 泉川
Yoshikatsu Matsuda
義勝 松田
Masatoshi Sato
政賢 佐藤
Ikuo Kirikoshi
郁夫 桐越
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 JP20070397A priority Critical patent/JP3682670B2/en
Publication of JPH1110131A publication Critical patent/JPH1110131A/en
Application granted granted Critical
Publication of JP3682670B2 publication Critical patent/JP3682670B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To purify soil economically by recovering heavy metals from soil by a method wherein water is added to the soil contaminated with heavy metals such as lead or the like to make slurry, and after adding one kind or two or more kinds selected from a collector, a foaming agent, and a conditioning agent, the slurry is treated with flotation. SOLUTION: Contaminated soil extracted from a bin 1 is weighed with a load cell, and sent to a rod mill 4 with a belt conveyor 3. The soil ground with the rod mill 4 is sent to a primary cyclone 6 with a pump 5 to be classified, and the classified undersize is sent back to the rod mill 4. Besides, a cyclone oversize is sent to a secondary cyclone 8 with a pump 7 to be classified, and the oversize is sent to a roughing flotation conditioner 10. Then, pulp conditioned with the roughing flotation conditioner 10 is sent to a flotation device 11 to execute flotation, the roughed float is sent to a cleaning flotation device 16 through cleaning conditioners 14, 15 to execute cleaning flotation, and cleaned float is recovered as the concentrate after dewatering with a dewatering tank 19.

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、重金属類に汚染さ
れた土壌から重金属類を分離・回収すると共に、土壌を
浄化する方法に関し、更に詳しくは、浮遊選鉱によって
重金属類を浮鉱として土壌から分離回収してリサイクル
すると共に土壌を浄化する土壌からの重金属類の回収方
法に関するものである。
[0001] The present invention relates to a method for separating and recovering heavy metals from soil contaminated with heavy metals and purifying the soil. More specifically, the present invention relates to a method for flotation to convert heavy metals from soil to flotation. The present invention relates to a method for recovering heavy metals from soil that separates and collects and recycles and purifies the soil.

【0002】[0002]

【従来の技術】近年、産業界における汚染物質の除去、
公害防止活動の活発化等に伴い、新たな化学物質による
環境汚染の懸念や、急増する廃棄物の処理問題に関連し
て、過去に蓄積された有害物質を含む土壌汚染の問題が
クローズアップされ、汚染土は「土壌環境基準」に従っ
て有害物質を除去して浄化する対策が必要となって来
た。
2. Description of the Related Art In recent years, the removal of pollutants in the industry,
With the increase in pollution control activities, concerns about environmental pollution caused by new chemical substances and the problem of soil pollution including harmful substances accumulated in the past have been highlighted in connection with the problem of waste disposal that is increasing rapidly. Therefore, it is necessary to take measures to purify contaminated soil by removing harmful substances in accordance with the “Soil Environmental Standards”.

【0003】重金属類に汚染された土壌を修復する手段
としては、化学処理を行った後に封じ込めする方法やコ
ンクリートで固化する方法、物理的な対策としては表層
土壌をある深さにわたって排土し、排土された表面に汚
染されていない土壌を客土する処理方法等が知られてい
る。
[0003] As a means for repairing soil contaminated with heavy metals, a method of confining after carrying out chemical treatment or a method of solidifying with concrete, and as a physical measure, discharging surface soil to a certain depth, There are known treatment methods for removing soil that is not contaminated on the discharged surface.

【0004】しかしながら、従来の化学処理及び物理的
対策では薬剤費や土壌の運搬コストが高い等の問題があ
った。
[0004] However, the conventional chemical treatment and physical countermeasures have problems such as high chemical costs and soil transportation costs.

【0005】一方、実際に重金属類に汚染された土壌か
ら重金属類を分離するために種々の方法が提案され公知
であるが、公知の重金属分離法、例えば錯塩化による分
離またはイオン交換による分離、あるいは鉱酸で重金属
類を溶解して水酸化物として分離する除去法等はいずれ
も満足すべきものではなく、これらは薬品または装置の
コストが高すぎるか又は分離過程が充分に効果のあるも
のではない等の問題がある。
On the other hand, various methods have been proposed and known for separating heavy metals from soils actually contaminated with heavy metals. Known methods for separating heavy metals, for example, separation by complex chloride or separation by ion exchange, have been proposed. Alternatively, none of the removal methods of dissolving heavy metals with a mineral acid and separating them as hydroxides are satisfactory, and these methods are too expensive for chemicals or equipment or the separation process is not sufficiently effective. There are problems such as not.

【0006】上述のように、重金属に汚染されている土
壌から重金属を回収してリサイクルする技術は確立され
ておらず、従って経済的にも安価で有効な処理法の開発
が望まれていた。
As described above, no technique has been established for recovering and recycling heavy metals from soil contaminated with heavy metals, and therefore there has been a demand for an economically inexpensive and effective treatment method.

【0007】[0007]

【発明が解決しようとする課題】本発明は、上記のよう
な従来技術の諸問題を解決し、重金属類に汚染されてい
る土壌を浄化・修復するに際し、有害物質の重金属類を
濃縮分離し・回収してリサイクルするために、該汚染物
を含む土壌を浮遊選鉱処理して経済的に高効率で重金属
類を分離回収すると共に土壌を浄化する方法を提案する
ものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, and purifies and repairs soil contaminated with heavy metals. -To recover and recycle, the present invention proposes a method for separating and recovering heavy metals and purifying the soil economically and efficiently by flotation treatment of soil containing the contaminants.

【0008】[0008]

【課題を解決するための手段】本発明者はかかる課題を
解決するために鋭意研究した結果、重金属類に汚染され
ている土壌から重金属類を回収してリサイクルし、汚染
土壌を浄化する方法として、安価な物理的処理法を開発
することができた。
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above problems, and as a result, as a method of purifying contaminated soil, recovering and recycling heavy metals from soil contaminated with heavy metals. Inexpensive physical treatment method could be developed.

【0009】即ち、第1の発明は、鉛等の重金属類で汚
染された土壌に水を加えてスラリー化し、捕収剤、起泡
剤、条件剤のうちから選ばれる1種又は2種以上を添加
し条件付与した後、該スラリーを浮遊選鉱することによ
り、重金属類を土壌から分離して重金属類を回収すると
共に土壌を浄化することを特徴とする土壌からの重金属
類の回収方法であり、
That is, the first invention is to add water to a soil contaminated with heavy metals such as lead to form a slurry, and to collect one or more selected from a collecting agent, a foaming agent, and a conditioning agent. Is a method for recovering heavy metals from soil, comprising separating the heavy metals from the soil by flotation of the slurry to purify the soil while purifying the soil. ,

【0010】第2の発明は、鉛等の重金属類で汚染され
た土壌粒子の粒径を100μm以下に粉砕した後に水を
加えてスラリー化し、捕収剤,起泡剤,条件剤のうちか
ら選ばれる1種又は2種以上を添加して条件付与した
後、該スラリーを浮遊選鉱することにより、重金属類を
土壌から分離して重金属類を回収すると共に土壌を浄化
することを特徴とする土壌からの重金属類の回収方法で
あり、
A second aspect of the present invention is to grind the soil particles contaminated with heavy metals such as lead to a particle size of 100 μm or less, and then add water to form a slurry, and select from a collecting agent, a foaming agent, and a conditioning agent. A soil characterized by separating one or more heavy metals from the soil to recover the heavy metals and purifying the soil by flotation of the slurry after adding one or more selected one or two or more conditions. Is a method of recovering heavy metals from

【0011】第3の発明は、鉛等の重金属類で汚染され
た土壌に水を加えてスラリー化し、硫化剤を添加又は吹
き込み、続いて捕収剤,起泡剤,条件剤のうちから選ば
れる1種又は2種以上を添加して条件付与した後、該ス
ラリーを浮遊選鉱することにより、重金属類を土壌から
分離して重金属類を回収すると共に土壌を浄化すること
を特徴とする土壌からの重金属類の回収方法であり、
According to a third aspect of the present invention, a soil contaminated with heavy metals such as lead is slurried by adding water, a sulphating agent is added or blown, and then a collecting agent, a foaming agent and a conditioning agent are selected. After adding one or two or more of the conditions described above, the slurry is subjected to flotation to separate heavy metals from the soil to recover the heavy metals and to purify the soil. Is a method of recovering heavy metals

【0012】第4の発明は、鉛等の重金属類で汚染され
た土壌粒子の粒径を100μm以下に粉砕した後に水を
加えてスラリー化し、硫化剤を添加又は吹き込み、続い
て捕収剤,起泡剤,条件剤のうちから選ばれる1種又は
2種以上を添加して条件付与した後、該スラリーを浮遊
選鉱することにより、重金属類を土壌から分離して重金
属類を回収すると共に土壌を浄化することを特徴とする
土壌からの重金属類の回収方法を提供するものである。
[0012] A fourth aspect of the present invention is to pulverize the soil particles contaminated with heavy metals such as lead to a particle size of 100 µm or less, then add water to make a slurry, and add or blow a sulphidizing agent. After adding one or more kinds selected from a foaming agent and a conditioning agent, conditions are added, and the slurry is subjected to flotation to separate heavy metals from the soil to recover the heavy metals and to remove the soil. It is intended to provide a method for recovering heavy metals from soil, which is characterized by purifying water.

【0013】上記本発明において、前記土壌粒子を10
0μm以下に粉砕する粉砕機はロッドミル及び/又はボ
ールミルであることが好ましく、また使用する捕収剤は
ジアルキルジチオカルバミン酸塩,キサントゲン酸塩,
ジアルキルジチオリン酸塩のいずれかを含有する薬剤で
あること、また前記条件剤が酸あるいはアルカリである
こと、更に前記硫化剤が硫化ソーダ,水硫化ソーダまた
は硫化水素のいずれかであることが好ましいのである。
次に、本発明の実施の形態を図面を参照して説明する。
[0013] In the above invention, the soil particles may be 10
The crusher for crushing to 0 μm or less is preferably a rod mill and / or a ball mill, and the collector used is dialkyldithiocarbamate, xanthate,
It is preferable that the agent is a drug containing any of dialkyldithiophosphates, that the conditioner is an acid or an alkali, and that the sulphidating agent is any of sodium sulfide, sodium hydrosulfide or hydrogen sulfide. is there.
Next, embodiments of the present invention will be described with reference to the drawings.

【0014】[0014]

【発明の実施の形態】重金属類による土壌汚染におい
て、汚染物質は細かい沈殿物等として土壌粒子間隙間中
に存在したり、土壌粒子の一部あるいはカチオン交換能
力の高い粘土分に吸着されたりして存在したり、重金属
類がメタル粉の状態で混在していることもある。従っ
て、本発明では重金属類で汚染されている土壌を浮選機
で処理して、浮鉱に重金属類を濃縮分離する点に特徴が
ある。
BEST MODE FOR CARRYING OUT THE INVENTION In soil contamination by heavy metals, contaminants may be present as fine precipitates in the interstices between soil particles, or may be adsorbed on a part of soil particles or on clay having high cation exchange capacity. Or heavy metals may be mixed in the form of metal powder. Therefore, the present invention is characterized in that soil contaminated with heavy metals is treated with a flotation machine to concentrate and separate heavy metals into flotation.

【0015】本発明では、処理対象とする汚染土壌に
は、好ましくは分級等によって重金属類を濃縮してから
浮選を行うのがよいが、これは浮選処理対象物の減量を
図る点に特徴がある。
In the present invention, flotation is preferably performed on the contaminated soil to be treated, preferably after concentration of heavy metals by classification or the like. There are features.

【0016】以下、実施例によって更に詳細に説明する
が、本発明の技術的範囲はこれらに限定されるのもので
はない。
Hereinafter, the present invention will be described in more detail with reference to Examples, but the technical scope of the present invention is not limited thereto.

【0017】実施例1 A地区の重金属汚染土壌を粉砕機で−35メッシュ
(0.417mm)に粉砕した試料500gをポットミ
ルに入れ、水を750cc入れて40分間磨鉱粉砕し、
土壌粒子の平均粒径を100μm以下とした。このパル
プを京大式浮遊選鉱機(1800cc、12500rp
m)に投入し、捕収剤としてジエチルジチオカルバミン
酸ナトリウム150g/tと起泡剤として日本香料
(株)製「日香#125」(商品名)を200g/t添
加し、10分間条件付けを行った後15分間粗選浮選を
行った。浮鉱は更に5分間精選浮選(pH10.6)を
行って、Pb精鉱を採取した。その分離成績の結果は図
1の如くである。
Example 1 A 500 g sample obtained by crushing heavy metal-contaminated soil in Area A with a crusher into -35 mesh (0.417 mm) was put into a pot mill, 750 cc of water was added, and ground and pulverized for 40 minutes.
The average particle size of the soil particles was set to 100 μm or less. This pulp is transferred to Kyoto University flotation machine (1800cc, 12,500rpm)
m), and 150 g / t of sodium diethyldithiocarbamate as a collecting agent and 200 g / t of "Niska # 125" (trade name) manufactured by Nippon Perfume Co., Ltd. as a foaming agent were added, and conditioning was performed for 10 minutes. After that, rough flotation was performed for 15 minutes. For flotation, Pb concentrate was collected by performing flotation (pH 10.6) for another 5 minutes. The result of the separation result is as shown in FIG.

【0018】実施例2 実施例1と同様の試料を用い、浮選の際に水硫化ナトリ
ウムで硫化した後、添加する捕収剤をアミルザンセート
50g/tに変更した他は実施例1と同様の操作によっ
て分離した。その分離成績の結果は図2の如くである。
Example 2 The same sample as in Example 1 was used except that the collector was added to 50 g / t of amyl xanthate after sulfided with sodium hydrosulfide during flotation using the same sample as in Example 1. Separated by operation. The result of the separation result is as shown in FIG.

【0019】実施例3 図3は、A地区の汚染土壌を選鉱工場で処理したときの
フローシートを示すものであり、図4はこのときのマテ
リアルバランスを示すもので、これらを参照して以下説
明する。
Example 3 FIG. 3 shows a flow sheet when contaminated soil in the area A is treated in a beneficiation plant, and FIG. 4 shows a material balance at this time. explain.

【0020】ビン1から抜き出された汚染土壌はロード
セル2で計量され、9t/hの速度でベルトコンベア3
で運ばれ、ロッドミル(8′×13′)4に送られる。
ロッドミル4で磨鉱粉砕された土壌(粉砕後の土壌の平
均粒子径100μm以下)はポンプ5で1次サイクロン
(MD6×3)6に送られ分級される。
The contaminated soil extracted from the bin 1 is weighed by the load cell 2 and is fed at a speed of 9 t / h to the belt conveyor 3.
And sent to the rod mill (8 ′ × 13 ′) 4.
The soil ground and crushed by the rod mill 4 (the average particle diameter of the crushed soil is 100 μm or less) is sent to the primary cyclone (MD6 × 3) 6 by the pump 5 and classified.

【0021】分級されたアンダーはロッドミル4へ繰り
返される。サイクロンオーバーはポンプ7で2次サイク
ロン8に送られ、ここで分級されたオーバーは粗選浮選
コンディショナー(1,5mφ)10に送られる。2次
サイクロンアンダーはボールミル(5′×10′)9に
繰り返される。粗選浮選コンディショナーには捕収剤と
してジエチルジチオカルバミン酸ナトリウム、起泡剤と
して「日香#125」(商品名)を添加して5分間条件
付けを行った。
The classified under is repeated to the rod mill 4. The cyclone over is sent to a secondary cyclone 8 by a pump 7, and the classified over is sent to a rough-selection flotation conditioner (1,5 mφ) 10. The secondary cyclone under is repeated in the ball mill (5 '× 10') 9. Sodium diethyldithiocarbamate as a collecting agent and "Nisuka # 125" (trade name) as a foaming agent were added to the rough flotation conditioner, and conditioning was performed for 5 minutes.

【0022】本発明において、捕収剤は特に限定される
ものではないが、土壌中に含まれる重金属類はメタルや
酸化物が多く、通常の硫化鉱物浮選は適用できない。従
って、硫化剤で硫化してからキサントゲン酸塩やジチオ
カルバミン酸塩などで処理することが好ましい。
In the present invention, the collecting agent is not particularly limited, but heavy metals contained in the soil are mostly metals and oxides, and ordinary sulfide mineral flotation cannot be applied. Therefore, it is preferable to sulfurate with a sulfurizing agent and then treat with xanthate or dithiocarbamate.

【0023】粗選コンディショナー10で条件付けされ
たパルプは、#24FW浮選機(セル数:8区)に送ら
れて粗選浮選が行われる。粗選沈鉱はポンプ13で廃滓
シックナーに送られる。一方、粗選浮鉱は精選コンディ
ショナー14,15を通って#18FW(4区)16に
送られて精選浮選を行い、精選浮鉱は脱水タンク19に
送られて脱水後精鉱として回収される。一方、精選沈鉱
はポンプ17で粗選コンディショナー10に繰り返され
る。
The pulp conditioned by the coarse-selection conditioner 10 is sent to a # 24FW flotation machine (number of cells: 8 wards) to perform a coarse-selection flotation. The coarse sediment is sent to a waste thickener by a pump 13. On the other hand, the coarse flotation is sent to # 18FW (fourth ward) 16 through the fine conditioners 14 and 15 to perform the fine flotation, and the fine flotation is sent to the dewatering tank 19 to be recovered as a concentrate after dehydration. You. On the other hand, the selective smelting is repeated to the coarse conditioner 10 by the pump 17.

【0024】この結果、図4に示すように本発明法によ
って重金属類に汚染された土壌から15.6%の鉛精鉱
を回収することができた。
As a result, as shown in FIG. 4, 15.6% of lead concentrate could be recovered from the soil contaminated with heavy metals by the method of the present invention.

【0025】なお、前記実施例では、重金属類としてP
bを主として説明したが、Cd、As、Hg等について
も本発明法が適用されることは勿論のことであり、実施
例3における供試土壌、浮選沈鉱、Pb精鉱中の分析値
も図4に例示した。また、重金属類を回収した後の土壌
は表1に示す環境庁水質保全局開示の「重金属に係わる
土壌汚染調査・対策指針」の含有量参考値以下であるこ
とが判明した。
In the above embodiment, P was used as the heavy metal.
b, but the present invention is of course applied to Cd, As, Hg, etc., and the analysis values in the test soil, flotation sediment, and Pb concentrate in Example 3 were used. Is also illustrated in FIG. In addition, it was found that the soil after collecting the heavy metals was below the content reference value in the “Guidelines for Soil Pollution Investigation and Countermeasures Related to Heavy Metals” disclosed in the Water Quality Conservation Bureau of the Environment Agency shown in Table 1.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【発明の効果】上述した通り、本発明法は従来ほとんど
顧みられなかった汚染土壌から高品位の重金属類を回収
すると共に土壌の浄化をも可能ならしめるもので、二次
公害防止ならびに資源再利用上きわめて有用である。
As described above, the method of the present invention recovers high-grade heavy metals from contaminated soil, which has rarely been neglected, and also makes it possible to purify the soil, thereby preventing secondary pollution and reusing resources. Above is very useful.

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

【図1】本発明に係る実施例1の分離成績を示す説明図
である。
FIG. 1 is an explanatory diagram showing separation results of Example 1 according to the present invention.

【図2】本発明に係る実施例2の分離成績を示す説明図
である。
FIG. 2 is an explanatory diagram showing separation results of Example 2 according to the present invention.

【図3】本発明に係る実施例3(Pb中間濃縮物浮選試
験)で実施したフローシートを示す図である。
FIG. 3 is a view showing a flow sheet performed in Example 3 (Pb intermediate concentrate flotation test) according to the present invention.

【図4】本発明に係る実施例3のマテリアルバランスを
示す図である。
FIG. 4 is a diagram illustrating a material balance according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1−ビン 2−ロードセル 3−ベルトコンベア 4−ロッドミル 5−ポンプ(1) 6−1次サイクロン 7−ポンプ(2) 8−2次サイクロン 9−ボールミル 10−粗選コンディショナー 11−粗選浮選機 12−ポンプ(3) 13−ポンプ(4) 14−精選コンディショナー(1) 15−精選コンディショナー(2) 16−精選浮選機 17−ポンプ(5) 18−ポンプ(6) 19−脱水タンク 1-bin 2-load cell 3-belt conveyor 4-rod mill 5-pump (1) 6-primary cyclone 7-pump (2) 8-secondary cyclone 9-ball mill 10-coarse conditioner 11-coarse flotation machine 12-pump (3) 13-pump (4) 14-selection conditioner (1) 15-selection conditioner (2) 16-selection flotation machine 17-pump (5) 18-pump (6) 19-dehydration tank

フロントページの続き (72)発明者 桐越 郁夫 秋田県大館市花岡町字堤沢42番地 花岡鉱 業株式会社内Continued on front page (72) Inventor Ikuo Kirikoshi 42 Hazukazawa, Hanaoka-cho, Odate-shi, Akita Hanaoka Mining Co., Ltd.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 鉛等の重金属類で汚染された土壌に水を
加えてスラリー化し、捕収剤,起泡剤,条件剤のうちか
ら選ばれる1種又は2種以上を添加し条件付与した後、
該スラリーを浮遊選鉱することにより、重金属類を土壌
から分離して重金属類を回収すると共に土壌を浄化する
ことを特徴とする土壌からの重金属類の回収方法。
1. Soil contaminated with heavy metals such as lead is slurried by adding water, and one or more selected from a collecting agent, a foaming agent, and a conditioning agent are added and conditions are provided. rear,
A method for recovering heavy metals from soil, comprising separating heavy metals from soil by flotation of the slurry to recover heavy metals and purifying the soil.
【請求項2】 鉛等の重金属類で汚染された土壌粒子の
粒径を100μm以下に粉砕した後に水を加えてスラリ
ー化し、捕収剤,起泡剤,条件剤のうちから選ばれる1
種又は2種以上を添加し条件付与した後、該スラリーを
浮遊選鉱することにより、重金属類を土壌から分離して
重金属類を回収すると共に土壌を浄化することを特徴と
する土壌からの重金属類の回収方法。
2. A soil particle contaminated with heavy metals such as lead is crushed to a particle size of 100 μm or less, and then water is added to form a slurry, which is selected from a collecting agent, a foaming agent, and a conditioning agent.
After adding seeds or two or more kinds and adding conditions, the slurry is subjected to flotation to separate heavy metals from the soil to recover the heavy metals and to purify the soil. Collection method.
【請求項3】 鉛等の重金属類で汚染された土壌に水を
加えてスラリー化し、硫化剤を添加又は吹き込み、続い
て捕収剤,起泡剤,条件剤のうちから選ばれる1種又は
2種以上を添加して条件付与した後、該スラリーを浮遊
選鉱することにより、重金属類を土壌から分離して重金
属類を回収すると共に土壌を浄化することを特徴とする
土壌からの重金属類の回収方法。
3. Soil contaminated with heavy metals such as lead is slurried by adding water, and a sulphating agent is added or blown, and then one or more selected from a collecting agent, a foaming agent, and a conditioning agent. After adding and adding two or more kinds of conditions, the slurry is subjected to flotation to separate heavy metals from the soil to recover the heavy metals and to purify the soil. Collection method.
【請求項4】 鉛等の重金属類で汚染された土壌粒子の
粒径を100μm以下に粉砕した後に水を加えてスラリ
ー化し、硫化剤を添加又は吹き込み、続いて捕収剤,起
泡剤,条件剤のうちから選ばれる1種又は2種以上を添
加して条件付与した後、該スラリーを浮遊選鉱すること
により、重金属類を土壌から分離して重金属類を回収す
ると共に土壌を浄化することを特徴とする土壌からの重
金属類の回収方法。
4. Soil particles contaminated with heavy metals such as lead are pulverized to a particle size of 100 μm or less, and then slurried by adding water, and a sulphating agent is added or blown in, followed by a collecting agent, a foaming agent, After adding one or two or more selected from the conditioning agents and applying conditions, the slurry is subjected to flotation to separate heavy metals from soil to recover heavy metals and to purify the soil. A method for recovering heavy metals from soil, characterized in that:
【請求項5】 前記土壌粒子を100μm以下に粉砕す
る粉砕機がロッドミル及び又はボールミルである請求項
2又は4記載の土壌からの重金属類の回収方法。
5. The method for recovering heavy metals from soil according to claim 2, wherein the crusher for crushing the soil particles to 100 μm or less is a rod mill and / or a ball mill.
【請求項6】 前記捕収剤がジアルキルジチオカルバミ
ン酸塩、キサンドゲン酸塩、ジアルキルジチオリン酸塩
のうち少なくとも1種を含有する薬剤である請求項1〜
4記載の土壌からの重金属類の回収方法。
6. The collecting agent according to claim 1, wherein the collecting agent contains at least one of dialkyldithiocarbamate, xanthate, and dialkyldithiophosphate.
4. The method for recovering heavy metals from soil according to 4.
【請求項7】 前記条件剤が酸又はアルカリである請求
項1〜4記載の土壌からの重金属類の回収方法。
7. The method for recovering heavy metals from soil according to claim 1, wherein the conditioning agent is an acid or an alkali.
【請求項8】 前記硫化剤が硫化ソーダ、水硫化ソーダ
または硫化水素である請求項3又は4記載の土壌からの
重金属類の回収方法。
8. The method for recovering heavy metals from soil according to claim 3, wherein the sulfurizing agent is sodium sulfide, sodium hydrosulfide or hydrogen sulfide.
JP20070397A 1997-06-20 1997-06-20 Recovery method of heavy metals from soil Expired - Lifetime JP3682670B2 (en)

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Application Number Priority Date Filing Date Title
JP20070397A JP3682670B2 (en) 1997-06-20 1997-06-20 Recovery method of heavy metals from soil

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JPH1110131A true JPH1110131A (en) 1999-01-19
JP3682670B2 JP3682670B2 (en) 2005-08-10

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