ABSTRACT Acidic wastewater from steel works was selected to reduce pyrolusite. The effects of leaching parameters such as the ratio of FeCl2 to MnO2, leaching temperature, liquid–solid ratio and initial HCl concentration in acidic wastewater on the leaching rate of manganese were investigated. The results show that under the conditions including the molar ratio of FeCl2 and MnO2 ( m FeC l 2 / m Mn O 2 ) at 2.2, the leaching temperature of 363 K, a leaching time of 180 min, an L/S ratio of 11:1, and an initial HCl concentration in acidic wastewater of 2.5 mol/L, the leaching rate of manganese in pyrolusite was 97.14%. An unreacted shrinking core model was employed to explore the kinetics of manganese in pyrolusite arising from the reduction leaching of acidic wastewater from steel plants. The results imply that the rate-determining step changed in the leaching process; among which, the first stage (0–100 min) of leaching was subject to the control of interfacial chemical reactions; the second stage (100–180 min) was controlled by internal diffusion. The apparent activation energy of the two stages was 15.57 and 125.48 kJ/mol respectively, and the apparent rate equations were respectively: 1 – ( 1 – r ) 1 / 3 = 0.39 ( m FeC l 2 / m Mn O 2 ) 1.18 [ HCl ] 0.21 ( V L / M S ) 0.62 exp ( − 15.57 / RT ) t 1 – 3 [ ( 1 – r ) / ( 1 – r 1 ) ] 2 / 3 + 2 [ 1 – ( 1 – r 1 ) ( r – r 1 ) 1 / 3 ] = 2.22 × 10 16 ( m FeC l 2 / m Mn O 2 ) 5.81 [ HCl ] exp ( − 125.48 RT ) t
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