Bioelectrochemical treatment of acid mine drainage dominated with iron

被引:59
作者
Lefebvre, Olivier [1 ]
Neculita, Carmen M.
Yue, Xiaodi [1 ]
Ng, How Yong [1 ]
机构
[1] Natl Univ Singapore, Dept Civil & Environm Engn, Ctr Water Res, Singapore 117576, Singapore
基金
新加坡国家研究基金会;
关键词
Acid mine drainage; Bioelectrochemical treatment; Iron oxy(hydroxi)des; Microbial fuel cell; pH; MICROBIAL FUEL-CELL; ELECTRICITY-GENERATION; CATHODIC REDUCTION; PASSIVE TREATMENT; PERFORMANCE; MEMBRANE; RECOVERY; SYSTEM; PH; TECHNOLOGIES;
D O I
10.1016/j.jhazmat.2012.09.062
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Treatment of acid mine drainage (AMD) dominated with iron (Fe), the most common metal, is a longterm expensive commitment, the goal of which is to increase the pH and remove Fe. In the present study, a proton exchange membrane microbial fuel cell (MFC) showed promise for the efficient treatment of an AMD dominated with ferric iron (pH 2.4 +/- 0.1; 500 mg L-1 Fe3+). Briefly, Fe3+ was reduced to Fe2+ at the cathode of the MFC, followed by Fe2+ re-oxidation and precipitation as oxy(hydroxi)des. Oxygen reduction and cation transfer to the cathode of the MFC further caused a rise in pH. A linear relationship was observed between the charge transferred in the MFC and the performance of the system up to 880 C. Optimal conditions were found at a charge of 662 C, achieved within 7 d at an acetate concentration of 1.6 g L-1 in a membrane MFC. This caused the pH to rise to 7.9 and resulted in a Fe removal of 99%. Treated effluent met the pH discharge limits of 6.5-9. The maximum power generation achieved under these conditions averaged 8.6 +/- 2.3W m(-3), which could help reduce the costs of full-scale bioelectrochemical treatment of AMD dominated with Fe. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:411 / 417
页数:7
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