Studies of Selective Recovery of Zinc and Manganese from Alkaline Batteries Scrap by Leaching and Precipitation.

Recovery of zinc and manganese from scrapped alkaline batteries were carried out in the following way: leaching in H 2 SO 4 and selective precipitation of zinc and manganese by alkalization/neutralization. As a result of non-selective leaching, 95.6-99.7% Zn was leached and 83.7-99.3% Mn was leached. A critical technological parameter is the liquid/solid treatment (l/s) ratio, which should be at least 20 mL∙g -1 . Selective leaching, which allows the leaching of zinc only, takes place with a leaching yield of 84.8-98.5% Zn, with minimal manganese co-leaching, 0.7-12.3%. The optimal H 2 SO 4 concentration is 0.25 mol∙L -1 . Precipitation of zinc and manganese from the solution after non-selective leaching, with the use of NaOH at pH = 13, and then with H 2 SO 4 to pH = 9, turned out to be ineffective: the manganese concentrate contained 19.9 wt.% Zn and zinc concentrate, and 21.46 wt.% Mn. Better selectivity results were obtained if zinc was precipitated from the solution after selective leaching: at pH = 6.5, 90% of Zn precipitated, and only 2% manganese. Moreover, the obtained concentrate contained over 90% of ZnO. The precipitation of zinc with sodium phosphate and sodium carbonate is non-selective, despite its relatively high efficiency: up to 93.70% of Zn and 4.48-93.18% of Mn and up to 95.22% of Zn and 19.55-99.71% Mn, respectively for Na 3 PO 4 and Na 2 CO 3 . Recovered zinc and manganese compounds could have commercial values with suitable refining processes.