首页> 外文会议>International mineral processing congress;IMPC 2010 >SELECTIVE REMOVAL OF ARSENIC FROM ACID MINE DRAINAGE CONTAINING FERROUS ION USING SULFIDE PRECIPITATION METHOD
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SELECTIVE REMOVAL OF ARSENIC FROM ACID MINE DRAINAGE CONTAINING FERROUS ION USING SULFIDE PRECIPITATION METHOD

机译:硫化物沉淀法选择性去除含铁离子酸性矿山中的砷

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摘要

Selective removal of dilute arsenic ions (As(III) or As(V)) from acid mine drainage (AMD) containingrnferrous irons was investigated using a sulfide precipitation method. 10 mg/dm3 of As(III) could bernremoved as As_2S_3 at pH ≥ 2.0 in a NaSH solution, which S/As ratio was higher than6.5 after 0.5 hrrnof reaction time. H_2S gas generation correlated with the residual As(III) concentration in AMD.rnBelow pH 2.5, ferrous ions were not found in the sludge and thus selective removal of As(III) wasrnachieved.rnOn the other hand, at pH 2.5, a NaSH solution of S/As ≥ 40 and a reaction time of 24 hr werernrequired to remove 10 mg/dm~3 of As(V) . However, at pH 3, 10 mg/dm3 of As(V) could be removedrnafter 0.5 hr of reaction time by using a NaSH solution of S/As ≥ 6 . Nevertheless, around 1/3 ofrnferrous ions were oxidized and removed as ferrihydrate together with As(V). EXAFS analysis showedrnthat As(V) was adsorbed on ferrihydrate when S/As ratio was 7, but precipitated as As_2S_3 at pHrn3,when S/As ratio was 20. These results showed that reduction of As(V) to As(III) was very slow andrnneeded enormous amount of sulfurising agent and relatively long reaction time.rnThe average primary diameter of the particles in the sludge was under 900 nm, which was increasedrnwith increasing dosage of NaSH. Particles exhibited a negative zeta potential of small value, whichrnindicates that they could coagulate to each other. Therefore, sedimentation rate of the particles fromrnsulfide precipitation method was better than the one from conventional hydroxide co-precipitationrnmethod using calcite or lime. Sedimentation of As(V) sulfide particles at pH 3 occurred at a very fastrnspeed because a small amount of ferrihydrite co-precipitated with As(V) sulfide, which acted as arncoagulant.
机译:使用硫化物沉淀法研究了从含亚铁的酸性矿井排水(AMD)中选择性去除稀砷离子(As(III)或As(V))。在NaSH溶液中,当pH≥2.0时,可以去除10 mg / dm3的As(III)作为As_2S_3,反应0.5小时后,S / As比大于6.5。 H_2S气体的产生与AMD中残留的As(III)浓度有关。在pH低于2.5时,污泥中没有发现亚铁离子,因此选择性去除了As(III).rn另一方面,在pH 2.5时使用NaSH溶液S / As≥40且反应时间为24小时才能除去10 mg / dm〜3的As(V)。然而,在pH值为3时,反应时间为0.5小时后,使用S /As≥6的NaSH溶液可以去除10 mg / dm3的As(V)。然而,大约有1/3的亚铁离子被氧化并作为三价铁与As(V)一起去除。 EXAFS分析表明,当S / As比为7时,As(V)吸附在亚铁水合物上,而当S / As比为20时,在pHrn3下以As_2S_3的形式沉淀。这些结果表明,As(V)还原为As(III)是污泥中颗粒的平均一次粒径在900 nm以下,随NaSH用量的增加而增加。颗粒表现出较小的负ζ电势,表明它们可以彼此凝结。因此,用硫化物沉淀法得到的颗粒的沉淀速率要好于使用方解石或石灰的常规氢氧化物共沉淀法得到的颗粒的沉淀速率。由于少量的水铁矿与作为硫化物的As(V)硫化物共沉淀,因此pH值为3的As(V)硫化物颗粒的沉淀速度非常快。

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  • 来源
  • 会议地点 Brisbane(AU);Brisbane(AU)
  • 作者单位

    Waseda University, Faculty of Science and Engineering, 3-4-1 Okubo, Shinjuku-ku, Tokyo 169-8555, Japan. Email: tokoro@waseda.jp;

    rnWaseda University, Graduate School of Science and Engineering, 3-4-1 Okubo, Shinjuku-ku, Tokyo 169-8555, Japan. Email: w-kazuya-pe.9@ruri.waseda.jp;

    rnThe University of Tokyo, Graduate School of Engineering, 7-3-1 Hongo, Bunkyo-ku, Tokyo 113-8656, Japan. Email: daidanni@hotmail.co.jp;

    rnThe University of Tokyo, Graduate School of Engineering, 7-3-1 Hongo, Bunkyo-ku, Tokyo 113-8656, Japan. Email: dodbiba@sys.t.u-tokyo.ac.jp;

    rnThe University of Tokyo, Graduate School of Engineering, 7-3-1 Hongo, Bunkyo-ku, Tokyo 113-8656, Japan. Email: tfujita@sys.t.u-tokyo.ac.jp;

    rnAqua Tech Co Ltd, 4-2-7-102 Shimaya, Konohana-ku, Osaka 554-0024, Japan. Email: a_ohnishi@aqua-t.co.jp;

    rnWater Re-Use Promotion Center, Water Re-Use Technology Division, Nihombashi Yokoyama-cho, Chuo-ku 103-0003, Japan. Email: nagasawa@wrpc.jp;

    rnJapan Oil, Gas and Metals National Corporation (JOGMEC), Technical Research and Consulting Dvision, Omiya-cho 1310, Saiwai-ku, Kawasaki-shi, Kanagawa 212-8554,Japan. Email: asano-hideo@jogmec.go.jp;

    rnJapan Oil, Gas and Metals National Corporation (JOGMEC), Mining and Metallurgy Technology Division, Omiya-cho 1310, Saiwai-ku, Kawasaki-shi, Kanagawa 212-8554, Japan. Email: hashimoto-koichi@jogmec.go.jp;

  • 会议组织
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 选矿;
  • 关键词

    wastewater treatment; arsenic; sulfide precipitation; sedimentation rate;

    机译:废水处理砷硫化物沉淀沉降速率;

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