|کد مقاله||کد نشریه||سال انتشار||مقاله انگلیسی||ترجمه فارسی||نسخه تمام متن|
|215265||1426233||2015||9 صفحه PDF||سفارش دهید||دانلود رایگان|
• LLE data for vanadium extraction by primary amine N1923 were obtained.
• Three extraction reactions were determined with the slope method.
• Thermodynamic equilibrium constants and new Pitzer parameters were regressed.
• The prediction performance of this new model was discussed and verified.
In this work, the solvent extraction of vanadium by using the primary amine N1923 as extractant was studied. Within different vanadium concentration ranges, the extraction reactions were determined using the slope method at T = 298.15 K based on the vanadium phase diagram. The slopes (the stoichiometric ratio) were determined as 5/3, 1 and 11/3 for (RNH2)5/3H3VO4,(RNH2)H3V3O9 and (RNH2)11/3H6V10O28(RNH2)11/3H6V10O28, respectively. The thermodynamic model was established through regression of the experimental results with the Pitzer equation for both aqueous and organic phases by the General Algebraic Modelling System (GAMS). Three different sets of parameters and chemical equilibrium constants K were determined, which corresponded to the three extraction reactions. The orders of the lnK values are V10>V3>V1V10>V3>V1 (organic V species), and the distribution coefficients (DV)DV) are DV1>DV3>DV10DV1>DV3>DV10. The new model was applied to predict the regularities of extraction yield along with different initial conditions, and the results agree well with the experimental values.
Journal: The Journal of Chemical Thermodynamics - Volume 80, January 2015, Pages 13–21