The Zn, Mn and C extraction processes from spent primary batteries and the synthesis of recycled Zn film, MnO 2 and MnO 2 /C for Zn-ion battery application were developed in the project. The Zn, Mn and C extraction process involved the acid leaching of Zn and Mn ions from the spent alkaline and Zn-C battery electrodes in the lab-scale was initially investigated using various leaching conditions. The acid leaching using 0.5-2 M HCl and H 2 SO 4 at ambient temperature providing Zn extraction efficiencies in a range of 72.3-95.3%. By introducing an inexpensive reducing agent namely sodium sulfide (Na 2 S), sodium metabisulfite (Na 2 S 2 O 5 ) or hydrogen peroxide (H 2 O 2 ) in 2M H 2 SO 4 , the Mn extraction efficiency for Mn was increased from 21.9% (with no reducing agent) up to 48.4%, 82.8% and 98.9%, respectively. The upscale leaching study was subsequently performed in a 100-L pilot scale reactor demonstrated the Zn and Mn extraction efficiencies of 71% and 65%, respectively. Using the leaching solutions from the upscale hydrometallurgical route, Zn-film fabrication via electrodeposition process, and the MnO 2 and MnO 2 /C synthesis via hydrothermal techniques were performed. Additionally, the one-step synthesis of MnO 2 /C via one-step hydrothermal method with no acid leaching was also explored in this study. The recycled Zn, MnO 2 , MnO 2 /C and C residual were subsequently used as the anode and cathode main components in the CR2032 and pouch-cell rechargeable Zn-ion batteries. The recycled MnO 2 and MnO 2 /C provided similar performance as the commercial products, which indicating the recycled MnO 2 , MnO 2 /C could be effectively utilized in the Zn-ion battery, while the utilization of recycled Zn-film provided slightly lower performance compared to that of the commercial Zn foil.
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Pornprasertsuk et al. (2024) studied this question.
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