Title of article
Thiocyanate hydrometallurgy for the recovery of goldPart III: Thiocyanate stability
Author/Authors
Li، نويسنده , , Jinshan and Safarzadeh، نويسنده , , M. Sadegh and Moats، نويسنده , , Michael S. and Miller، نويسنده , , Jan D. and LeVier، نويسنده , , K. Marc and Dietrich، نويسنده , , Meg and Wan، نويسنده , , Rong Yu، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2012
Pages
6
From page
19
To page
24
Abstract
The effects of metal ions, minerals, temperature, thiocyanate concentration, activated carbon, and pH on the rate of thiocyanate oxidation were determined. The rate of ferrous ion generation from the redox reaction between thiocyanate and ferric ion was found to be significant at 50 °C. The reaction constant (k) at 25 °C was found to be 1.43 × 10− 5 L0.4 mol− 0.4 min− 1. Ferric oxidation of thiocyanate was sensitive to temperature with an activation energy of 76.4 kJ/mol, typical of homogenous chemical reactions. Based on the kinetic data, the empirical rate equation for thiocyanate consumption and/or ferrous ion generation was found to have the following form: d [ F e 2 + ] d t = − 8 d [ S C N − ] d t = k [ S C N − ] 1.36 [ F e 3 + ] 0 [ H + ] 0 = k [ S C N − ] 1.36
minerals did not have a profound effect on the oxidation of thiocyanate by ferric ion. Sulfide minerals, especially pyrite and galena catalyzed the redox reaction. The addition of cupric ion resulted in the oxidation of thiocyanate and formation of an insoluble cuprous thiocyanate compound.
Keywords
Oxidation , sulfide minerals , Activation energy , Activated carbon , Thiocyanate
Journal title
HYDROMETALLURGY
Serial Year
2012
Journal title
HYDROMETALLURGY
Record number
2372812
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