Recovery of Copper from Acid Mine Drainage by an Integrated Sulphate Reducing Process


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An integrated sulfate reducing process was used to treat Acid Mine Drainage with high concentrations of Cu2+, Fe and SO42-. The water treatment system integrated a sulfidogenic UASB bioreactor with a precipitation reactor which was used to recover copper. Sodium lactate was used as energy source. The effective volume of the UASB reactor was 2 L and the hydraulic retention time was 12.57h. In the sulphate removal reactor, sulphate was removed from 21160 to 195 mg/L with a rate of 4427.8 mg/L/d. Cu2+ and Fe was removed by biologically generated S2- and OH- from 360 and 6520 to 0.049 mg/L and less than 10 mg/L respectively. The average COD, copper and iron removal rate was 2523.2, 15.21 and 274.98 mg/L/d separately. The effluent pH reached 6.0-7.0. The results showed potential usage of this bioreactor in treating Acid Mine Drainage.



Advanced Materials Research (Volumes 71-73)

Edited by:

Edgardo R. Donati, Marisa R. Viera, Eduardo L. Tavani, María A. Giaveno, Teresa L. Lavalle, Patricia A. Chiacchiarini




B. W. Chen et al., "Recovery of Copper from Acid Mine Drainage by an Integrated Sulphate Reducing Process", Advanced Materials Research, Vols. 71-73, pp. 557-560, 2009

Online since:

May 2009




[1] J.P. Maree, H.A. Greben and M. d. Beer: Water SA Vol. 30 (2004), p.183.

[2] S. Foucher, F. Battaglia-Brunet, I. Ignatiadis and D. Morin: Chemical Engineering Science Vol. 56 (2001), p.1639.

[3] A. Luptakovaa, M. Kusnierovaa, M. Bezovskaa and P. Feckob, In: Proceedings of the 15th International Biohydrometallurgy Symposium, Athens, Greece, (2003).

[4] R. Renman, W. Jiankang and C. Jinghe: Hydrometallurgy Vol. 83 (2006), p.77.

[5] J. Hollingsworth, R. Sierra-Alvarez, M. Zhou, K.L. Ogden and J.A. Field: Chemosphere Vol. 59 (2005), p.1219.

[6] H.G. Trüper and H.G. Schlegel: Antonie van Leeuwenhoek Vol. 30 (1964), p.225.

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