کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
212168 | 462035 | 2014 | 6 صفحه PDF | دانلود رایگان |

• A Th(IV) extraction mechanism is determined as [ThF]3 ++ 2(HA)2 = ThFA3(HA) + 3H+.
• Rate equation for extracting Th(IV) is formulated as R = k[ThF3 +]1.28[H2A2]1.07[H+]− 0.95.
• A mass transfer model with a rate-controlling step is proposed and evaluated.
Solvent extraction of Th(IV) using 2-ethylhexyl phosphoric acid mono 2-ethylhexyl ester (HEH(EHP)) in kerosene from sulfuric acid medium was studied by investigating the dependence of thorium extraction on aqueous acidity and HEH(EHP) concentration. The extraction mechanism was also determined by slope analysis. Th(IV) extraction kinetics was investigated using a constant interfacial cell with a laminar flow, and the data were analyzed based on the principle of pseudo first-order reaction. Some parameters' effect on the mass transfer, including the effect of temperature, Th(IV) concentration, HEH(EHP) concentration and pH was studied, and the rate equation for thorium extraction was obtained through slope analysis. Based on the high activation energy (Ea = 45.8 kJ mol− 1), the extraction regime was defined to be an interfacial chemical reaction control. In addition, a mass transfer model with a rate-control step was proposed and it was consistent with the experimental results.
The schematic description of mass-transfer process of a metal ion.Figure optionsDownload as PowerPoint slide
Journal: Hydrometallurgy - Volume 150, December 2014, Pages 167–172