“…Still, the upkeep of cost and energy consumption effectiveness remains challenging. For HM, corrosive chemicals are required to induce metal leaching. , Highly toxic acidic and alkali leaching reagents, such as H 3 NO 3 S-NaCl-H 2 O 2 , NH 3 -(NH 4 ) 2 SO 4 , cyanide, halide, thiourea, and thiosulfate, are most frequently utilized for common metal extractions or precipitation, such as Sn, Pb, Fe, Cu, and Zn. , HM’s metal leaching selectivity and efficiency could be controlled and tailored with solvent selection, making it generally more suitable to handle more valuable metals than PM. However, the non-pH-neutral solvent and the generation of toxic fume release from metal dissolution are the common criticisms for employing HM as a metal leaching strategy, and it requires a stoichiometric amount of acid or alkaline reagents that induces substantial chemical and post-treatment processing cost.…”