UO_2(NO_3)_2-HNO_3-H_2 O/30%(体积)TBP-240号煤油体系萃取过程的数学模型——Ⅱ.萃取过程中相体积的变化
MATHEMATICAL MODELING OF THE SYSTEM OF UO_2(NO_3)_2-HNO_3-H_2O/30%(Vol.)TBP-KEROSENE IN SOLVENT EXTRACTION PROCESS Ⅱ. THE CHANGE OF PHASE VOLUME IN THE EXTRACTION PROCESS
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摘要: 本文提出了硝酸铀酰和硝酸在水相和有机相的偏克分子体积、相体积变化关联为溶质浓度的函数。提出了溶液比重和硝酸铀酰与硝酸浓度的关系式。水相比重的计算值与实验值相比,95.4%的点误差在±0.020以内,有机相比重的计算值与实验值相比,95.4%的点误差在±0.017以内。应用偏克分子体积值可以修正萃取过程中的体积变化。Abstract: In this paper are recommended the values of partical molar volumes of uranyl nitrate and nitric acid in aqueous phase and organic phase, and the change of phase volume was correlated as a function of the solute concentrations. Thus the relations between densities of the solution and concentrations of uranyl nitrate and nitric acid are provided for. The difference between the calculated and experimental values of densities for 95.4% is within±0.020 and±0.017 for the aqueous phase and organic phase respectively. Using the values of partical molar volume changes of volume can be corrected in the course of the extraction process.