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JPH0474073B2 - - Google Patents
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JPH0474073B2 - - Google Patents

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Publication number
JPH0474073B2
JPH0474073B2 JP63220555A JP22055588A JPH0474073B2 JP H0474073 B2 JPH0474073 B2 JP H0474073B2 JP 63220555 A JP63220555 A JP 63220555A JP 22055588 A JP22055588 A JP 22055588A JP H0474073 B2 JPH0474073 B2 JP H0474073B2
Authority
JP
Japan
Prior art keywords
amount
humic acid
waste
heavy metals
metals
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.)
Expired - Lifetime
Application number
JP63220555A
Other languages
Japanese (ja)
Other versions
JPH0268192A (en
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 filed Critical
Priority to JP63220555A priority Critical patent/JPH0268192A/en
Publication of JPH0268192A publication Critical patent/JPH0268192A/en
Publication of JPH0474073B2 publication Critical patent/JPH0474073B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/286Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/22Chromium or chromium compounds, e.g. chromates

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Removal Of Specific Substances (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) この発明は有害重金属類を含む産業廃棄物に対
し、無害化処理剤として 一般式 (但しRはアルキル基、MはNaまたはNH4
示す)で表されるジアルキルジチオカルバミン酸
塩に安定剤としてフミン酸を含有せしめたことを
特徴とする廃水または産業廃棄物中の有害重金属
捕集剤に関するものである。有害重金属類を含む
産業廃棄物、例えば重金属を含む工場廃水、また
は重金属を含む汚染土などに添加して、重金属類
と反応して不溶解性の物質を生成せしめ、該産業
廃棄物を無害化するような公害分野で利用され
る。 (従来の技術) 従来、この種の産業廃棄物を処理する方法とし
てアルカリ剤による中和、凝集、沈澱などの方
法、電解法、イオン交換法、セメントによる固給
法などの方法が用いられてきた。 (解決しようとする問題点) 従来のアルカリ剤による中和、凝集、沈澱など
の方法に於ては処理効果が完全でなく、特に銅ア
ンモニア錯塩を含む錯体化合物などについて、こ
の方法では処理出来なかつた。 イオン交換法は再生の際に再び別の処理装置が
必要になり、金属の再利用方式を除いては設備費
が増大する欠点があつた。 セメントによる固結法は非常に濃厚な有害廃棄
物であれば費用的に有効であるが、一般の廃棄物
をコンクリート固化するとセメントを多量に必要
とし、さらに固結した後の処理物量が増加し、投
棄する費用、場所がさらに問題化されてくるなど
の欠点があつた。 (問題を解決する為の具体的な手段) 本発明は有害重金属類を含む廃水または産業廃
棄物に対し、無害化処理剤として 一般式 (但しRはアルキル基、MはNaまたはNH4
示す)で表されるジアルキルジチオカルバミン酸
塩に安定剤としてフミン酸を含有せしめたことを
特徴とする廃水または産業廃棄物中の有害重金属
捕集剤に係る。 従来のジアルキルジチオカルバミン酸塩単独で
は、この処理剤自身が空気自然酸化により2分子
が結合してチユーラム系の化合物となり、重金属
イオンとの結合力がなくなつてしまう。 本発明ではジアルキルジチオカルバミン酸塩に
フミン酸を混合して、2モルのシアルキルジチオ
カルバミン酸塩がチユーラム系の化合物となら
ず、自然状態の中でも安定して自己の化学組成を
保有し、廃水または産業廃棄物の中の有害重金属
類と結合して不溶解性物質を生成し、完全に無害
化処理出来ることに特徴がある。 更に、このフミン酸自身も重金属と反応し、結
合力の強いキレート化物を生成し、またジアルキ
ルジチオカルバミン酸塩との併用は互いにその効
果を増大させ、処理剤としての性能を向上する特
徴がある。 廃棄物が汚染水の場合、本発明品を添加するこ
とにより、有害金属類が反応して不溶解性物質に
変化させると共にこれを分離除去し、完全なる無
害化を行う。廃棄物が汚染土の場合、本発明品を
混練した後、セメント等の適当な固結剤を利用し
て固結せしめ有害金属類の再溶出を防止し、完全
なる無害化が可能となる。 本発明に於て処理剤の必要量は汚染水の場合、
廃棄物中の有害金属含有量により異なるが、一般
に無害化に必要な最低限度量はジアルキルジチオ
カルバミン酸塩量として含まれる有害金属類の2
倍モル数量以上を添加することが必要である。こ
れ以下の量では有害金属類がイオンの形で水中に
残存することがあり、特に亜鉛イオンについては
3倍モル数量が最適であつた。汚染土の場合、有
害金属類の2倍モル数量以上の本発明と汚染土重
量に対して12%以上のセメントを添加することに
より、廃棄物中の含有有害金属イオンを完全に封
鎖することが出来た。 本発明品が有効な反応機構はジアルキルジチオ
カルバミン酸塩中のMイオンがフミン酸の存在下
で安定的に有害重金属イオンと置換するものと思
われる。この反応はPH領域によつても異なつた状
態を示し、PHが6以上に於て効果的に反応し、残
留金属イオンを完全に除去することが出来た。 ジアルキルジチオカルバミン酸塩の代表的な物
質として、ジメチルジチオカルバミン酸ナトリウ
ム、ジエチルジチオカルバミン酸ナトリウム、ジ
プロピルジチオカルバミン酸ナトリウム、ジブチ
ルジチオカルバミン酸ナトリウム等がある。 フミン酸には土壌フミン酸と石炭質フミン酸が
あり、いづれも使用し得る。これらはイオン交換
性を有し、コロイド的諸性質を示すが、この性質
が重金属類の捕集に効果をもたらしているものと
推定され、また多価フエノール基及びカルボキシ
ル基を所有するところからジアルキルジチオカル
バミン酸系化合物の空気自然酸化による重金属類
との結合力劣化を防止しているものと推定され
る。 本発明品は還元力もあり、硫酸第一鉄等に比べ
て約10倍以上の還元力を有している。従つて、六
価クロム等を含む廃棄物については非常に効果的
な働きをもたらすものである。即ち、有害な六価
クロムを三価のクロムに還元する力があり、この
ことは廃棄物が汚染水の場合は水溶液中で、一旦
六価クロムイオンが三価クロムイオンになり、そ
れから本発明品と結合し、不溶解性の物質を作る
ものと思われる。廃棄物が汚染土の場合は汚染土
中の六価クロムが三価クロムに還元された後にセ
メントにより固結され六価クロムを含まない無害
な処理物とすることが出来る。 (実施例 1) 実験材料としてフミン酸は腐植質中の付随物を
有機溶媒で除き、希アルカルで抽出したものを使
用し、有害金属類を含む廃棄物として1000mg/
濃度の銅、亜鉛、鉛、カドミウム、六価クロムの
各廃液を調整したものを使用した。PHは7.5に統
一した。 実験の方法としては、一定量の廃液に比較とし
て、ジメチルジチオカルバミン酸ナトリウムを添
加する場合とこれにフミン酸を混合した本発明品
を添加する場合の二通りを行つた。添加して生成
した反応生成物を定性用ろ紙No.2で除き、そのろ
液についてPHを7.5に調整し、原子吸光分析装置
にて残存金属イオン量(mg/)を測定した。 (1) 比較例:ジメチルジチオカルバミン酸ナトリ
ウムを単独処理した場合の結果を第1表に示
す。但し、イオン量はmg/の単位である。
(Industrial Application Field) This invention is a detoxifying treatment agent for industrial waste containing hazardous heavy metals. Collection of hazardous heavy metals in wastewater or industrial waste characterized by containing humic acid as a stabilizer in a dialkyldithiocarbamate represented by (R is an alkyl group and M is Na or NH 4 ) This is related to drugs. When added to industrial waste containing hazardous heavy metals, such as factory wastewater containing heavy metals or contaminated soil containing heavy metals, it reacts with the heavy metals to produce insoluble substances, rendering the industrial waste harmless. It is used in such pollution fields. (Prior art) Conventionally, methods such as neutralization with alkaline agents, coagulation, and precipitation, electrolytic methods, ion exchange methods, and cement fixation methods have been used to treat this type of industrial waste. Ta. (Problem to be solved) Conventional methods such as neutralization, coagulation, and precipitation using alkaline agents do not have a perfect treatment effect, and in particular complex compounds containing copper ammonium complex salts cannot be treated with this method. Ta. The ion exchange method requires another processing device for regeneration, and has the drawback of increasing equipment costs except for metal reuse methods. Consolidation with cement is cost-effective for highly concentrated hazardous wastes, but consolidating general waste with concrete requires a large amount of cement, and the amount of material to be treated after consolidation increases. However, there were disadvantages such as the cost and location of dumping. (Specific means for solving the problem) The present invention is a detoxifying treatment agent for wastewater or industrial waste containing harmful heavy metals. Collection of hazardous heavy metals in wastewater or industrial waste characterized by containing humic acid as a stabilizer in a dialkyldithiocarbamate represented by (R is an alkyl group and M is Na or NH 4 ) Related to drugs. When a conventional dialkyldithiocarbamate is used alone, two molecules of the treatment agent itself combine with each other due to natural air oxidation to form a thulum-based compound, which loses its binding strength with heavy metal ions. In the present invention, by mixing humic acid with dialkyldithiocarbamate, 2 moles of sialkyldithiocarbamate does not become a thulum-based compound, stably retains its own chemical composition even in natural conditions, and can be used in wastewater or industrial applications. It is unique in that it combines with hazardous heavy metals in waste to produce insoluble substances, making it completely harmless. Furthermore, this humic acid itself reacts with heavy metals to produce a chelate with strong binding strength, and when used in combination with a dialkyldithiocarbamate, the effects are mutually enhanced and the performance as a processing agent is improved. When the waste is contaminated water, by adding the product of the present invention, toxic metals react and change into insoluble substances, which are separated and removed, thereby completely rendering the water harmless. When the waste is contaminated soil, after kneading the product of the present invention, it is solidified using a suitable solidifying agent such as cement to prevent harmful metals from re-eluting, making it possible to completely render it harmless. In the present invention, in the case of contaminated water, the required amount of treatment agent is
Although it varies depending on the content of hazardous metals in the waste, the minimum amount necessary for detoxification is generally 2 of the hazardous metals contained in the amount of dialkyldithiocarbamate.
It is necessary to add more than twice the molar amount. If the amount is less than this, harmful metals may remain in the water in the form of ions, and especially for zinc ions, 3 times the molar amount was optimal. In the case of contaminated soil, it is possible to completely sequester the toxic metal ions contained in the waste by adding the present invention in a molar amount more than twice that of the toxic metals and cement in an amount of 12% or more based on the weight of the contaminated soil. done. The reaction mechanism by which the product of the present invention is effective is thought to be that M ions in the dialkyldithiocarbamate stably replace harmful heavy metal ions in the presence of humic acid. This reaction showed different conditions depending on the pH range, and the reaction was effective at a pH of 6 or higher, and residual metal ions could be completely removed. Representative substances of dialkyldithiocarbamates include sodium dimethyldithiocarbamate, sodium diethyldithiocarbamate, sodium dipropyldithiocarbamate, and sodium dibutyldithiocarbamate. Humic acids include soil humic acid and coal humic acid, both of which can be used. These have ion-exchange properties and exhibit colloidal properties, and this property is presumed to be effective in collecting heavy metals, and because they have polyvalent phenol groups and carboxyl groups, It is presumed that this prevents deterioration of the bonding strength of dithiocarbamic acid compounds with heavy metals due to natural oxidation in the air. The product of the present invention also has reducing power, which is about 10 times or more compared to ferrous sulfate and the like. Therefore, it has a very effective effect on waste containing hexavalent chromium and the like. In other words, it has the power to reduce harmful hexavalent chromium to trivalent chromium, and this means that when the waste is contaminated water, the hexavalent chromium ions first turn into trivalent chromium ions in an aqueous solution, and then the present invention It is thought to combine with other substances to form an insoluble substance. If the waste is contaminated soil, the hexavalent chromium in the contaminated soil is reduced to trivalent chromium and then consolidated with cement, making it a harmless treated product that does not contain hexavalent chromium. (Example 1) Humic acid used as an experimental material was obtained by removing accompanying substances in humic substances with an organic solvent and extracting with dilute alkali.
Adjusted concentrations of copper, zinc, lead, cadmium, and hexavalent chromium were used. The pH was unified to 7.5. Two experimental methods were used for comparison: adding sodium dimethyldithiocarbamate to a certain amount of waste liquid, and adding the product of the present invention mixed with humic acid. The reaction product produced by the addition was removed using qualitative filter paper No. 2, the pH of the filtrate was adjusted to 7.5, and the amount of residual metal ions (mg/) was measured using an atomic absorption spectrometer. (1) Comparative Example: Table 1 shows the results when sodium dimethyldithiocarbamate was treated alone. However, the ion amount is in units of mg/.

【表】【table】

【表】 (2) 比較例:フミン酸による単独処理の場合、処
理結果を第2表に示す。フミン酸の添加量は廃
水1に対するg数である。
[Table] (2) Comparative example: In the case of single treatment with humic acid, the treatment results are shown in Table 2. The amount of humic acid added is the number of grams per 1 part of waste water.

【表】 (3) 本発明例:ジメチルジチオカルバミン酸ナト
リウム(DDTC)2モルにフミン酸を0〜10
%添加した場合の処理結果を第3表に示す。但
し、フミン酸の添加量が0の場合は比較例であ
る。
[Table] (3) Example of the present invention: 0 to 10 humic acid added to 2 moles of sodium dimethyldithiocarbamate (DDTC)
% addition is shown in Table 3. However, the case where the amount of humic acid added is 0 is a comparative example.

【表】【table】

【表】 (実施例 2) 実験材料は実施例1と同じであるが、廃棄物中
の含有有害金属イオン量1モル/にジメチルジ
チオオルバミン酸ナトリウム3モル/とこの3
モル/に対してフミン酸を10%混合したものと
処理剤として加えた。比較例としてPH値を2〜
5、本発明例としてPH値が6〜11に変化した結果
を第4表に示す。
[Table] (Example 2) The experimental materials were the same as in Example 1, except that sodium dimethyldithioorbamate was added 3 moles per mole of harmful metal ions contained in the waste, and 3 moles of sodium dimethyldithioorbamate were added.
A 10% mixture of humic acid was added as a treatment agent based on mole/mol. As a comparative example, the PH value is 2~
5. Table 4 shows the results when the pH value changed from 6 to 11 as an example of the present invention.

【表】 但しイオン量の単位はppmである。 (実施例 3) 有害金属として銅、亜鉛、鉛、カドミウム、六
価クロムを各3000ppm含有する汚染土1Kgをと
り、本発明品の処理剤としてジメチルジチオカル
バミン酸ナトリウムとフミン酸の混合物を各有害
金属量の2〜3倍モル数量を添加し、セメントを
汚染土重量に対して5〜16%添加してよく混練し
た。比較例がセメント添加量が少ない範囲のもの
で、本発明例は12〜14%以上の添加量のところで
ある。 実験方法として固結した処理物を24時間放置後
「産業廃棄物に含まれる有害物質の検定方法」環
境庁告示第13号を用いて再溶出してくる有害金属
イオン量を測定した。その結果を第5,6表に示
す。
[Table] However, the unit of ion amount is ppm. (Example 3) 1 kg of contaminated soil containing 3000 ppm each of copper, zinc, lead, cadmium, and hexavalent chromium as toxic metals was taken, and a mixture of sodium dimethyldithiocarbamate and humic acid was used as a treatment agent for each toxic metal. Cement was added in an amount of 2 to 3 times the molar amount, and 5 to 16% of cement was added to the weight of the contaminated soil, and the mixture was thoroughly kneaded. The comparative example has a small amount of cement added, and the example of the present invention has an added amount of 12 to 14% or more. As an experimental method, the solidified processed material was left to stand for 24 hours, and the amount of toxic metal ions re-eluted was measured using the Environment Agency Notification No. 13, ``Method for Assaying Hazardous Substances Contained in Industrial Waste.'' The results are shown in Tables 5 and 6.

【表】【table】

【表】【table】

【表】 (発明の効果) 実施例1のように有害重金属の捕集剤としてジ
アルキルカルバミン酸塩及びフミン酸のそれぞれ
単独で使用した比較例では第1表、第2表のよう
に捕集効果はあまり上がつていない。これに対
し、本発明例の第3表に示すように本発明品のジ
アルキルジチオカルバミン酸塩にフミン酸を混合
したものを使用した場合、処理液中の残存重金属
イオンが不検出まで処理することが可能となり、
従来重金属残存イオンを完全に処理出来なかつた
ことに対し、画期的なことである。またジメチル
ジチオカルバミン酸ナトリウム(約2倍モル数量
以上の溶液)に対しフミン酸を約8%以上混合す
ることが効果的である。 本発明品が有効に働くにはPH値が6以上の条件
が良く、これは実験例2で示されている。 対象が汚染土の場合は実施例3のように有害金
属類の2倍モル数量以上のジアルキルジチオカル
バミン酸塩を含む本発明品に加えてセメント添加
量が汚染土重量に対して約14%以上添加すると効
果がある。
[Table] (Effects of the invention) In a comparative example in which dialkyl carbamate and humic acid were used alone as a scavenger for harmful heavy metals as in Example 1, the scavenging effects were as shown in Tables 1 and 2. has not improved much. On the other hand, as shown in Table 3 of the invention examples, when the dialkyldithiocarbamate of the invention mixed with humic acid is used, it is possible to treat the treatment solution until residual heavy metal ions are not detected. It becomes possible,
This is an epoch-making achievement as it has not been possible to completely treat residual heavy metal ions in the past. It is also effective to mix about 8% or more of humic acid with sodium dimethyldithiocarbamate (a solution of about twice the molar amount or more). For the product of the present invention to work effectively, the PH value is preferably 6 or more, and this is shown in Experimental Example 2. If the target is contaminated soil, as in Example 3, in addition to the product of the present invention containing dialkyldithiocarbamate in a molar amount or more twice that of toxic metals, add cement in an amount of approximately 14% or more based on the weight of the contaminated soil. Then it works.

Claims (1)

【特許請求の範囲】 1 有害重金属類を含む廃水または産業廃棄物に
対し、無害化処理剤として 一般式 (但しRはアルキル基、MはNaまたはNH4
示す)で表わされるジアルキルジチオカルバミン
酸塩に安定剤としてフミン酸を含有せしめたこと
を特徴とする廃水または産業廃棄物中の有害重金
属捕集剤。
[Claims] 1. As a detoxification treatment agent for wastewater or industrial waste containing hazardous heavy metals. (wherein R is an alkyl group and M is Na or NH 4 ) A hazardous heavy metal collector in wastewater or industrial waste characterized by containing humic acid as a stabilizer in a dialkyldithiocarbamate. .
JP63220555A 1988-09-05 1988-09-05 Harmful heavy metal trapping agent for waste water or industrial waste Granted JPH0268192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63220555A JPH0268192A (en) 1988-09-05 1988-09-05 Harmful heavy metal trapping agent for waste water or industrial waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63220555A JPH0268192A (en) 1988-09-05 1988-09-05 Harmful heavy metal trapping agent for waste water or industrial waste

Publications (2)

Publication Number Publication Date
JPH0268192A JPH0268192A (en) 1990-03-07
JPH0474073B2 true JPH0474073B2 (en) 1992-11-25

Family

ID=16752830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63220555A Granted JPH0268192A (en) 1988-09-05 1988-09-05 Harmful heavy metal trapping agent for waste water or industrial waste

Country Status (1)

Country Link
JP (1) JPH0268192A (en)

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WO2014030622A1 (en) 2012-08-21 2014-02-27 住友ゴム工業株式会社 Puncture sealing agent

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2508903B2 (en) * 1990-08-31 1996-06-19 日揮株式会社 Method for treating heavy metal contaminated soil
JP2002320955A (en) * 2001-04-27 2002-11-05 Okumura Corp Heavy metal insolubilizer in soil and method for insolubilizing heavy metal in soil
GB0207876D0 (en) * 2002-04-05 2002-05-15 British Nuclear Fuels Plc Removal of blockages from pipework

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2269812A2 (en) 2009-06-30 2011-01-05 Sumitomo Rubber Industries, Ltd. Puncture sealant
US8242196B2 (en) 2009-06-30 2012-08-14 Sumitomo Rubber Industries, Ltd. Puncture sealant
US8318839B2 (en) 2009-06-30 2012-11-27 Sumitomo Rubber Industries, Ltd. Puncture sealant
WO2014030622A1 (en) 2012-08-21 2014-02-27 住友ゴム工業株式会社 Puncture sealing agent

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