“…Several methods have been used to increase reaction rates and break or avoid this passivation layer in leaching systems, including (i) leaching with powerful oxidizing agents such as O 3 [ 30 , 31 , 32 ], H 2 O 2 [ 6 , 33 , 34 , 35 ], potassium permanganate, and potassium dichromate [ 36 , 37 , 38 ], (ii) leaching with high pressure and temperature [ 34 , 39 , 40 , 41 ], and (iii) bacterial leaching [ 11 , 14 , 42 , 43 ], but these improvements are accompanied by limitations, mainly due to the high cost of oxidizers, the corrosive environments they provide and even low copper recoveries [ 39 , 44 ]. These kinds of considerations result in the hydrometallurgical route not being widely used in the dissolution of copper from primary sulfide ore, mainly because of slow leaching kinetics caused by the crystal structure of chalcopyrite (face-centered tetragonal lattice), which makes its lattice energy too high to break S-Cu-Fe bonds [ 23 , 45 ].…”