Studies on mathematical modeling of the leaching process in order to efficiently recover lead from the sulfate/oxide lead paste

Copyright © 2016 Elsevier Ltd. All rights reserved.

Bibliographische Detailangaben
Veröffentlicht in:Waste management (New York, N.Y.). - 1999. - 60(2017) vom: 19. Feb., Seite 723-733
1. Verfasser: Buzatu, Traian (VerfasserIn)
Weitere Verfasser: Ghica, Gabriel Valeriu, Petrescu, Ionuţ Mircea, Iacob, Gheorghe, Buzatu, Mihai, Niculescu, Florentina
Format: Online-Aufsatz
Sprache:English
Veröffentlicht: 2017
Zugriff auf das übergeordnete Werk:Waste management (New York, N.Y.)
Schlagworte:Journal Article Leaching extraction efficiency Mathematical modeling NaOH solubilisation Sulfate/oxide lead paste Oxides Lead 2P299V784P lead oxide 4IN6FN8492 mehr... Sodium Hydroxide 55X04QC32I lead sulfate C516H654O8
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245 1 0 |a Studies on mathematical modeling of the leaching process in order to efficiently recover lead from the sulfate/oxide lead paste 
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520 |a Copyright © 2016 Elsevier Ltd. All rights reserved. 
520 |a Increasing global lead consumption has been mainly supported by the acid battery manufacturing industry. As the lead demand will continue to grow, to provide the necessary lead will require an efficient approach to recycling lead acid batteries. In this paper was performed a mathematical modeling of the process parameters for lead recovery from spent lead-acid batteries. The results of the mathematical modeling compare well with the experimental data. The experimental method applied consists in the solubilisation of the sulfate/oxide paste with sodium hydroxide solutions followed by electrolytic processing for lead recovery. The parameters taken into considerations were NaOH molarity (4M, 6M and 8M), solid/liquid ratio - S/L (1/10, 1/30 and 1/50) and temperature (40°C, 60°C and 80°C). The optimal conditions resulted by mathematical modeling of the electrolytic process of lead deposition from alkaline solutions have been established by using a second-order orthogonal program, in order to obtain a maximum efficiency of current without exceeding an imposed energy specific consumption. The optimum value for the leaching recovery efficiency, obtained through mathematical modeling, was 89.647%, with an error of δy=3.623 which leads to a maximum recovery efficiency of 86.024%. The optimum values for each variable that ensure the lead extraction efficiency equal to 89.647% are the following: 3M - NaOH, 1/35 - S/L, 70°C - temperature 
650 4 |a Journal Article 
650 4 |a Leaching extraction efficiency 
650 4 |a Mathematical modeling 
650 4 |a NaOH solubilisation 
650 4 |a Sulfate/oxide lead paste 
650 7 |a Oxides  |2 NLM 
650 7 |a Lead  |2 NLM 
650 7 |a 2P299V784P  |2 NLM 
650 7 |a lead oxide  |2 NLM 
650 7 |a 4IN6FN8492  |2 NLM 
650 7 |a Sodium Hydroxide  |2 NLM 
650 7 |a 55X04QC32I  |2 NLM 
650 7 |a lead sulfate  |2 NLM 
650 7 |a C516H654O8  |2 NLM 
700 1 |a Ghica, Gabriel Valeriu  |e verfasserin  |4 aut 
700 1 |a Petrescu, Ionuţ Mircea  |e verfasserin  |4 aut 
700 1 |a Iacob, Gheorghe  |e verfasserin  |4 aut 
700 1 |a Buzatu, Mihai  |e verfasserin  |4 aut 
700 1 |a Niculescu, Florentina  |e verfasserin  |4 aut 
773 0 8 |i Enthalten in  |t Waste management (New York, N.Y.)  |d 1999  |g 60(2017) vom: 19. Feb., Seite 723-733  |w (DE-627)NLM098197061  |x 1879-2456  |7 nnns 
773 1 8 |g volume:60  |g year:2017  |g day:19  |g month:02  |g pages:723-733 
856 4 0 |u http://dx.doi.org/10.1016/j.wasman.2016.08.005  |3 Volltext 
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