Abstract

Abstract This paper presents the direct extraction, which works by means of pressure leaching, of vanadium and tungsten from the spent SCR catalysts using a caustic soda. The experimental parameters were concentration of NaOH (aq), the particle size of the feedstock, the temperature, and the S/L ratio. The results of an assessment of the proposed method found that pressure leaching using a caustic soda can more effectively dissolve vanadium and tungsten from the spent SCR catalysts than atmospheric alkaline leaching. The dissolution efficiency of vanadium and tungsten tended to increase with an increase in the concentration of NaOH (aq), a higher temperature and a decrease in the particle size of the feedstock used. The S/L ratio, which affected the dissolution efficiency of vanadium and tungsten, differed depending on the concentration of NaOH (aq). The optimum conditions for the extraction of vanadium and tungsten by pressure leaching were as follows: concentration of NaOH (aq), 3 mol/L; temperature, 250 °C; particle size distribution;

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