In this investigation batch, ferric leaching experiments were carried out i
n a 100 ml jacketed vessel maintained at 25 degrees C. The parameters varie
d during the course of the experimental program included the initial redox
potential, the total iron concentration, the solids concentration and the p
H of the leaching solution. The initial redox potential used ranged from 62
5 to 470 mV, the overall iron concentration ranged from 8 to 32 g.l(-1), th
e mineral concentration ranged from 5 to 20 g.l(-1) and the initial pH used
ranged from 1.10 to 1.45. The redox potential of the leach solution was mo
nitored continuously using a redox probe connected to a computer. The leach
rates were calculated from the measured change in the redox potential of t
he leaching solution. The variation in the ferric leaching rate of the arse
nopyrite as a function of the solution redox potential displayed similar tr
ends, irrespective of the conditions employed. The ferric leaching rate of
the arsenopyrite decreased with decreasing redox potential of the leaching
solution and could be accurately described using a modified Butler-Volmer e
quation; -r(Fe2+) = r(0)(e(alpha beta(E-E'))-e((1-alpha(beta(E-E'))). High
concentrations of ferric iron and protons, and a reduction in the solids co
ncentration were found to impede the leach rate. The 'rest potential' (i.e.
, the redox potential at which the dissolution of arsenopyrite stops) of th
e arsenopyrite was found to be higher under these conditions. However, no o
ccluding sulphur layer could be detected on the surface of mineral particle
s, hence the results suggest that the reactivity of the mineral decreases w
ith an increase in the effective concentration of the ferric iron species.
Therefore, although the results suggest the likelihood of an electrochemica
l mechanism being operative, it is necessary to modify the Butler-Volmer-ba
sed model to account for the above observations in order to obtain a model
capable of predicting the ferric leaching rate of arsenopyrite across a bro
ad range of operating conditions. (C) 1999 Elsevier Science B.V. All rights
reserved.