Evaluation of arsenic immobilization in red mud by CO2 or waste acid acidification combined ferrous (Fe2+) treatment

被引:12
作者
Li, Yiran [1 ,2 ]
Wang, Jun [1 ]
Peng, Xianjia [1 ]
Ni, Fan [1 ]
Luan, Zhaokun [1 ]
机构
[1] Chinese Acad Sci, Ecoenvironm Sci Res Ctr, State Key Lab Environm Aquat Chem, Beijing 100085, Peoples R China
[2] E China Inst Technol, Dept Civil & Environm Engn, Fuzhou 344000, Jiangxi, Peoples R China
关键词
Arsenic immobilization; Acidification; Ferrous; Red mud; AQUEOUS-SOLUTIONS; REMOVAL; SILICATE; REMEDIATION; ADSORPTION; OXIDATION; CARBONATE; PHOSPHATE; SULFATE; SOILS;
D O I
10.1016/j.jhazmat.2011.10.055
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Arsenic was detected in a red mud (RM) produced during alumina production from bauxite known as the Bayer process. The transporting RM was a mixture of RM solid phase (RMsf) and RM liquid phase (RMlf). The mass content of RMsf in RM is about 30-40%. The alkalinities concentrations in the RMlf were in a range of 37.2 x 10(3) mg/l to 51.5 x 10(3) mg/l. Acidification by CO2 or waste acid (WA) combined with ferrous (Fe2+) treatment was evaluated for arsenic immobilization in the RM. The aqueous arsenic concentration in the RMlf decreased from 6.1 mg/l to 0.5 mg/l and 0.06 mg/l with the addition of CO2 and WA, respectively. Ferrous was then added to decrease the aqueous arsenic concentration to be lower than 0.05 mg/l. The cost-effective dosages of CO2 or WA were 80.1 g/l or 26.7 g/l, and the corresponding dosages of ferrous were both 6g/l. A 2(3) full factorial design was employed to evaluate the importance of chemical components of the RM in the cost of arsenic immobilization. High concentrations of arsenic and alkalinities in the RM will increase the cost while the effects of alumina contents varied during the different acidifications. Dissolvable arsenic in the RMsf was 8.2% and 9.5% after the CO2 and WA combined ferrous treatments, respectively. (C) 2011 Published by Elsevier B.V.
引用
收藏
页码:43 / 50
页数:8
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共 29 条
  • [21] Thermal behaviour of clay mixtures with bauxite residue for the production of heavy-clay ceramics
    Pontikes, Y.
    Nikolopoulos, P.
    Angelopoulos, G. N.
    [J]. JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2007, 27 (2-3) : 1645 - 1649
  • [22] Arsenic removal with iron(II) and iron(III) waters with high silicate and phosphate concentrations
    Roberts, LC
    Hug, SJ
    Ruettimann, T
    Billah, M
    Khan, AW
    Rahman, MT
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2004, 38 (01) : 307 - 315
  • [23] Utilization of activated CO2-neutralized red mud for removal of arsenate from aqueous solutions
    Sahu, Ramesh Chandra
    Patel, Rajkishore
    Ray, Bankim Chandra
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2010, 179 (1-3) : 1007 - 1013
  • [24] Immobilization of arsenic in a tailings material by ferrous iron treatment
    Seidel, H
    Görsch, K
    Amstätter, K
    Mattusch, J
    [J]. WATER RESEARCH, 2005, 39 (17) : 4073 - 4082
  • [25] Disposal of water treatment wastes containing arsenic - A review
    Sullivan, Colin
    Tyrer, Mark
    Cheeseman, Christopher R.
    Graham, Nigel J. D.
    [J]. SCIENCE OF THE TOTAL ENVIRONMENT, 2010, 408 (08) : 1770 - 1778
  • [26] Catalytic applications of red mud, an aluminium industry waste: A review
    Sushil, Snigdha
    Batra, Vidya S.
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2008, 81 (1-2) : 64 - 77
  • [27] Sorption Mechanisms of Arsenate during Coprecipitation with Ferrihydrite in Aqueous Solution
    Tokoro, Chiharu
    Yatsugi, Yohei
    Koga, Hajime
    Owada, Shuji
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2010, 44 (02) : 638 - 643
  • [28] Stabilization of Pb and As in soils by applying combined treatment with phosphates and ferrous iron
    Xenidis, Anthimos
    Stouraiti, Christina
    Papassiopi, Nymphodora
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2010, 177 (1-3) : 929 - 937
  • [29] Preparation of glass-ceramics from red mud in the aluminium industries
    Yang, Jiakuan
    Zhang, Dudu
    Hou, Jian
    He, Baoping
    Xiao, Bo
    [J]. CERAMICS INTERNATIONAL, 2008, 34 (01) : 125 - 130