کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
212569 | 462056 | 2012 | 6 صفحه PDF | دانلود رایگان |
![عکس صفحه اول مقاله: Thiocyanate hydrometallurgy for the recovery of goldPart III: Thiocyanate stability Thiocyanate hydrometallurgy for the recovery of goldPart III: Thiocyanate stability](/preview/png/212569.png)
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[Fe2+]dt=−8d[SCN−]dt=k[SCN−]1.36[Fe3+]0[H+]0=k[SCN−]1.36Oxide 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.
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► The rate of Fe2+ generation from the redox reaction of SCN and Fe3+ is significant.
► The rate of ferric oxidation of thiocyanate is controlled by chemical reaction.
► Oxide minerals do not have a profound effect on the oxidation of SCN by ferric ion.
► Sulfide minerals accelerate the redox reaction of SCN and ferric ion.
► Cu2+ results in the oxidation of SCN and formation of insoluble CuSCN.
Journal: Hydrometallurgy - Volumes 113–114, February 2012, Pages 19–24