Recovery of lithium and cobalt from waste lithium ion batteries of mobile phone

Copyright © 2013 Elsevier Ltd. All rights reserved.

Bibliographische Detailangaben
Veröffentlicht in:Waste management (New York, N.Y.). - 1999. - 33(2013), 9 vom: 17. Sept., Seite 1890-7
1. Verfasser: Jha, Manis Kumar (VerfasserIn)
Weitere Verfasser: Kumari, Anjan, Jha, Amrita Kumari, Kumar, Vinay, Hait, Jhumki, Pandey, Banshi Dhar
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2013
Zugriff auf das übergeordnete Werk:Waste management (New York, N.Y.)
Schlagworte:Journal Article Research Support, Non-U.S. Gov't Cobalt Leaching Lithium Recycling Solutions Sulfuric Acids 3G0H8C9362 9FN79X2M3F mehr... Hydrogen Peroxide BBX060AN9V sulfuric acid O40UQP6WCF
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245 1 0 |a Recovery of lithium and cobalt from waste lithium ion batteries of mobile phone 
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520 |a Copyright © 2013 Elsevier Ltd. All rights reserved. 
520 |a In view of the stringent environmental regulations, availability of limited natural resources and ever increasing need of alternative energy critical elements, an environmental eco-friendly leaching process is reported for the recovery of lithium and cobalt from the cathode active materials of spent lithium-ion batteries of mobile phones. The experiments were carried out to optimize the process parameters for the recovery of lithium and cobalt by varying the concentration of leachant, pulp density, reductant volume and temperature. Leaching with 2M sulfuric acid with the addition of 5% H(2)O(2) (v/v) at a pulp density of 100 g/L and 75°C resulted in the recovery of 99.1% lithium and 70.0% cobalt in 60 min. H(2)O(2) in sulfuric acid solution acts as an effective reducing agent, which enhance the percentage leaching of metals. Leaching kinetics of lithium in sulfuric acid fitted well to the chemical controlled reaction model i.e. 1-(1-X)(1/3)=k(c)t. Leaching kinetics of cobalt fitted well to the model 'ash diffusion control dense constant sizes spherical particles' i.e. 1-3(1-X)(2/3)+2(1-X)=k(c)t. Metals could subsequently be separated selectively from the leach liquor by solvent extraction process to produce their salts by crystallization process from the purified solution 
650 4 |a Journal Article 
650 4 |a Research Support, Non-U.S. Gov't 
650 4 |a Cobalt 
650 4 |a Leaching 
650 4 |a Lithium 
650 4 |a Recycling 
650 7 |a Solutions  |2 NLM 
650 7 |a Sulfuric Acids  |2 NLM 
650 7 |a Cobalt  |2 NLM 
650 7 |a 3G0H8C9362  |2 NLM 
650 7 |a Lithium  |2 NLM 
650 7 |a 9FN79X2M3F  |2 NLM 
650 7 |a Hydrogen Peroxide  |2 NLM 
650 7 |a BBX060AN9V  |2 NLM 
650 7 |a sulfuric acid  |2 NLM 
650 7 |a O40UQP6WCF  |2 NLM 
700 1 |a Kumari, Anjan  |e verfasserin  |4 aut 
700 1 |a Jha, Amrita Kumari  |e verfasserin  |4 aut 
700 1 |a Kumar, Vinay  |e verfasserin  |4 aut 
700 1 |a Hait, Jhumki  |e verfasserin  |4 aut 
700 1 |a Pandey, Banshi Dhar  |e verfasserin  |4 aut 
773 0 8 |i Enthalten in  |t Waste management (New York, N.Y.)  |d 1999  |g 33(2013), 9 vom: 17. Sept., Seite 1890-7  |w (DE-627)NLM098197061  |x 1879-2456  |7 nnns 
773 1 8 |g volume:33  |g year:2013  |g number:9  |g day:17  |g month:09  |g pages:1890-7 
856 4 0 |u http://dx.doi.org/10.1016/j.wasman.2013.05.008  |3 Volltext 
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