The paper is focused on the recovery of zinc and manganese from alkaline and zinc-carbon spent batteries. Metals are extracted by sulphuric acid leaching in the presence of citric acid as reducing agent. Leaching tests are carried out according to a full factorial design, and empirical equations for Mn and Zn extraction yields are determined from experimental data as a function of pulp density, sulphuric acid concentration, temperature, and citric acid concentration. The highest values experimentally observed for extraction yields were 97% of manganese and 100% of zinc, under the following operating conditions: temperature , pulp density 20%, sulphuric acid concentration 1.8?M, and citric acid 40?g . A second series of leaching tests is also performed to derive other empirical models to predict zinc and manganese extraction. Precipitation tests, aimed both at investigating precipitation of zinc during leaching and at evaluating recovery options of zinc and manganese, show that a quantitative precipitation of zinc can be reached but a coprecipitation of nearly 30% of manganese also takes place. The achieved results allow to propose a battery recycling process based on a countercurrent reducing leaching by citric acid in sulphuric solution. 1. Introduction The battery market is steadily increasing worldwide: this behaviour requires a new approach in the management of these devices once they are exhausted [1]. In many countries alkaline and zinc-carbon spent batteries were still landfilled or incinerated up to the end of 2008, instead of being recycled, recovering valuable secondary raw materials and avoiding dispersion of heavy metals in the environment. Several European Countries have autonomously developed national collection systems and infrastructures to collect and recycle all kinds of portable batteries, despite the old Directive 91/157/EEC EEC (and subsequent amending acts of Directives 93/86/EEC and 98/101/EC) that covered only batteries and accumulators containing more than 0.0005% mercury, more than 0.025% cadmium, and more than 0.4% lead (percentages by weight) [2]. These Countries have arranged a financing system that is able to cover all costs related to the recycling activities by applying a surcharge on battery selling price [1]. In 2007 members of the European Battery Recycling Association (EBRA) recycled about 31,079 tonnes of portable batteries and accumulators: compared to the previous year there was a little improvement (30,865 tonnes in 2006) [3]. In more detail, quantities of batteries recycled by EBRA’s members were 26,941 tonnes
References
[1]
European Portable Battery Association, 2008, http://www.epbaeurope.net.
[2]
European Union, 2008, http://europa.eu.int.
[3]
European Battery Recycling Association, 2008, http://www.ebra-recycling.org.
[4]
P. Marini and M. C. Zanetti, “Pre-treatment tests for the recovery of exhaust portable accumulators,” in Proceedings of the 23rd International Mineral Processing Congress, pp. 2158–2162, Istanbul, Turkey, 2006.
[5]
D. C. R. Espinosa, A. M. Bernardes, and J. A. S. Tenório, “An overview on the current processes for the recycling of batteries,” Journal of Power Sources, vol. 135, no. 1-2, pp. 311–319, 2004.
[6]
W. Lindermann, Process for the recovery of raw materials from presorted collected waste, especially scrap electrochemical batteries and accumulators (1996), Patent Application US 5 575 907.
[7]
F. Tedjar, Recycling used electric cells by hydrometallurgical treatment (2003), Patent application WO 03/021 708.
[8]
A. Serstevens, Process for the recycling of salt and alkaline batteries (2001), Patent application EP 1 148 571.
[9]
Batrec Process, 2006, http://www.batrec.ch.
[10]
L. Toro, F. Vegliò, F. Beolchini, F. Pagnanelli, M. Zanetti, and G. Furlani, Process and plant for the treatment of run-down batteries (2006), Patent application EP 1 684 369.
[11]
I. De Michelis, F. Ferella, E. Karakaya, F. Beolchini, and F. Vegliò, “Recovery of zinc and manganese from alkaline and zinc-carbon spent batteries,” Journal of Power Sources, vol. 172, no. 2, pp. 975–983, 2007.
[12]
C. C. B. M. De Souza and J. A. S. Tenório, “Simultaneous recovery of zinc and manganese dioxide from household alkaline batteries through hydrometallurgical processing,” Journal of Power Sources, vol. 136, no. 2, pp. 191–196, 2004.
[13]
C. C. B. M De Souza, D. C. De Oliveira, and J. A. S. Tenório, “Characterization of used alkaline batteries powder and analysis of zinc recovery by acid leaching,” Journal of Power Sources, vol. 103, no. 1, pp. 120–126, 2001.
[14]
S. M. Xará, J. N. Delgado, M. F. Almeida, and C. A. Costa, “Laboratory study on the leaching potential of spent alkaline batteries,” Waste Management, vol. 29, no. 7, pp. 2121–2131, 2009.
[15]
L. R. S. Veloso, L. E. O. C. Rodrigues, D. A. Ferreira, F. S. Magalh?es, and M. B. Mansur, “Development of a hydrometallurgical route for the recovery of zinc and manganese from spent alkaline batteries,” Journal of Power Sources, vol. 152, no. 1-2, pp. 295–302, 2005.
[16]
A. L. Salgado, A. M. O. Veloso, D. D. Pereira, G. S. Gontijo, A. Salum, and M. B. Mansur, “Recovery of zinc and manganese from spent alkaline batteries by liquid-liquid extraction with Cyanex 272,” Journal of Power Sources, vol. 115, no. 2, pp. 367–373, 2003.
[17]
N. B. Devi, K. C. Nathsarma, and V. Chakravortty, “Extraction and separation of Mn(II) and Zn(II) from sulphate solutions by sodium salt of Cyanex 272,” Hydrometallurgy, vol. 45, no. 1-2, pp. 169–179, 1997.
[18]
N. Vatistas, M. Bartolozzi, and S. Arras, “The dismantling of the spent alkaline zinc manganese dioxide batteries and the recovery of the zinc from the anodic material,” Journal of Power Sources, vol. 101, no. 2, pp. 182–187, 2001.
[19]
F. Ferella, I. De Michelis, and F. Vegliò, “Process for the recycling of alkaline and zinc-carbon spent batteries,” Journal of Power Sources, vol. 183, no. 2, pp. 805–811, 2008.
[20]
E. Sayilgan, T. Kukrer, F. Ferella, A. Akcil, F. Veglio, and M. Kitis, “Reductive leaching of manganese and zinc from spent alkaline and zinc-carbon batteries in acidic media,” Hydrometallurgy, vol. 97, no. 1-2, pp. 73–79, 2009.
[21]
G. Xi, Y. Li, and Y. Liu, “Study on preparation of manganese-zinc ferrites using spent Zn-Mn batteries,” Materials Letters, vol. 58, no. 7-8, pp. 1164–1167, 2004.
[22]
J. Nan, D. Han, M. Cui, M. Yang, and L. Pan, “Recycling spent zinc manganese dioxide batteries through synthesizing Zn-Mn ferrite magnetic materials,” Journal of Hazardous Materials, vol. 133, no. 1-3, pp. 257–261, 2006.
[23]
E. Sayilgan, T. Kukrer, G. Civelekoglu et al., “A review of technologies for the recovery of metals from spent alkaline and zinc-carbon batteries,” Hydrometallurgy, vol. 97, no. 3-4, pp. 158–166, 2009.
[24]
J.-W. Kim, S. Barrington, J. Sheppard, and B. Lee, “Nutrient optimization for the production of citric acid by Aspergillus niger NRRL 567 grown on peat moss enriched with glucose,” Process Biochemistry, vol. 41, no. 6, pp. 1253–1260, 2006.
[25]
D.C. Montgomery, Design and Analysis of Experiments, John Wiley & Sons, New York, NY, USA, 3rd edition, 1991.
[26]
D. M. Himmelblau, Process Analysis by Statistical Methods, John Wiley & Sons, New York, NY, USA, 3rd edition, 1978.
[27]
N. S. Gajbhiye, U. Bhattacharya, and V. S. Darshane, “Thermal decomposition of zinc-iron citrate precursor,” Thermochimica Acta, vol. 264, pp. 219–230, 1995.
[28]
Hydra/Medusa software, Chemical Equilibrium Diagrams, http://www.kemi.kth.se/medusa.
[29]
B. S. Boyanov, V. V. Konareva, and N. K. Kolev, “Purification of zinc sulfate solutions from cobalt and nickel through activated cementation,” Hydrometallurgy, vol. 73, no. 1-2, pp. 163–168, 2004.
[30]
F. Ferella, G. Furlani, M. Navarra, et al., “Hydrometallurgical plant to recycle alkaline and Zn-C spent batteries: process and economic analysis,” in Proceedings of the 2nd International Conference on Engineering for Waste Valorization, Patras, Greece, 2008.