An investigation of copper recovery from acidic solutions in a particulate, cylindrical spouted vessel of conductive particles is presented. The effects of current, initial copper ion concentration, supporting electrolyte concentration, particle loading, liquid flow rate, solution pH, and temperature on copper recovery rate, current efficiency and energy efficiency of the electrolytic deposition process were investigated under galvanostatic conditions. Experiments were also conducted to investigate the effects of backdissolution or 'backstripping' of the deposited metal in the acidic solution. It is hypothesized that the latter occurs via both chemical and electrochemical anodic oxidation in the bed of conductive particles. It was found that sparging of the electrolyte solution with selected gases to remove dissolved oxygen increased the current efficiency by as much as 30% under certain conditions. Finally, a numerical kinetic model of electrochemical deposition and backstripping, coupled with mass transfer in the particulate cathode bed, is presented that describes the behaviour of the net copper recovery curves reasonably well.
List of symbolsa electrode area per unit volume (m )1 ) C j concentration of species j (mol m )3 ) C js concentration of species j at electrode surface (mol m )3 ) C metal cation concentration in solution, initial (ppm or mol m )3 ) C O initial metal cation concentration in solution, initial (ppm or mol m )3 )backstripping rate constant pre-exponential factor (ppm min )1 )/(mol kg )1 bar )1 ) K B backdissolution rate (mol m )3 s )1 ) K H Henry's law constant for oxygen in water (mol oxygen (kg water) -1 (bar )1 ) n apparent reaction order n j number of electrons in rate j r b backstripping rate (ppm min )1 ) r j rate of reaction or mass transport (mol m )3 s )1 ) R gas constant (J K )1 mol )1 ) Re p particle Reynolds number (= u d p /m) ScSchmidt number (= m/D) Sh particle Sherwood number (= k L d p /D) t time (s) T temperature (K) DH Ã 0 heat of activation at equilibrium potential (kJ mol )1 ) a transfer coefficient (Equation 10) m kinematic viscosity (m 2 s )1 )