In order to reduce the environmental impact due to land disposal of LD (Linz-Donawitz) converter slag from steelmaking plant and to valorise this waste material, an acid leaching study was carried out to assess the effect of several parameters on the kinetics of vanadium dissolution. The characterisation and morphology of the feed investigated using XRD, XRF. The factors influencing leaching vanadium such as particle size, temperature, slurry density and the concentration of sulfuric acid were investigated and optimised._x000D_
The maximum vanadium recovery about 95 per cent achieved at 70C, S/L: 1/15, acid concentration: 3M and for 150 minutes of leaching time. The dissolution of vanadium in sulfuric acid shows that there are two stages in the kinetics of leaching. At the first 15minutes, there is a sharp increase in the amount of vanadium extracted and at longer leaching time, the extraction increase slightly. In the present work, the shrinking core model (SCM) was used to describe the acid leaching of vanadium compounds. A summary of the controlling regimes in the SCM are examined below for short time (less than 12 min.) and long time (more than 30 min.) stages. So, it was found that the kinetics of leaching in both stages is controlled by solid product diffusion regime._x000D_
CITATION:Aarabi, M, Rashchi, F, Vahidi, E and Mostoufi, N, 2010. Kinetic study on the leaching of vanadium from LD converter slag using sulfuric acid, in Proceedings XXV International Mineral Processing Congress (IMPC) 2010, pp 233-242 (The Australasian Institute of Mining and Metallurgy: Melbourne).