Sorption Of Rare Metal Ions by Ionite Based on Diglycidyl Thiourea and Various Amines

F. B. Eshkurbonov, E.R. Safarova, B.Y. Ismoilov
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Abstract

The article studies the process of sorption of molybdenum and vanadium ions on anion exchangers obtained on the basis of thiourea, epichlorohydrin and various amines. Various amines (urea, guanidine, melamine, polyethylene polyamine, ethylenediamine, etc.) are used as substances containing ionic groups. The regularities of ion exchange and the main properties of the tested anionites are given, the influence of the pH of the medium and interfering ions in the process of sorption of molybdenum and vanadium ions are studied. For vanadium, the use of empirical partition relations and of an extended Freundlich equation were tested, with promising results. The objective of this paper is to investigate the use of the pH dependent Freundlich model of Gustafsson et al., for describing vanadate(V) sorption to 26 mineral soils (all having less than 12% organic C), and to discuss the possible use of the model for risk assessments. The kinetic curves of the sorption process, the values of the diffusion coefficients for the initial periods of molybdenum sorption are given. In particular, the distribution coefficient of the radiotracers of 99Mo and 131I as homologs of Sg and Ts using the surface modification of chabazite was investigated as liquid-solid system in the present study. The kinetics of molybdenum sorption was carried out under static conditions from an ammonium molybdate solution with a concentration of 1 g/L for molybdenum ions and at pH 4.5–5.  Under the same conditions, molybdenum ions are sorbed much faster by the DGT + M anion exchanger in comparison with AN-2F anion exchangers, in which the diffusion coefficient is much lower. The static exchange capacity (SEC) was determined in industrial solutions in the presence of mineral acids (hydrochloric, sulfuric and nitric), usually contained in them. The obtained kinetic equilibrium parameters of the tested anion exchangers were compared with those of industrial polycondensation anion exchangers, such as AN-2F and AN-1.
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基于二缩水硫脲和各种胺的离子石对稀有金属离子的吸附作用
文章研究了钼和钒离子在以硫脲、环氧氯丙烷和各种胺为基础的阴离子交换剂上的吸附过程。各种胺(尿素、胍、三聚氰胺、聚乙烯多胺、乙二胺等)被用作含有离子基团的物质。研究了钼和钒离子吸附过程中介质 pH 值和干扰离子的影响。对于钒,使用经验分配关系和扩展的 Freundlich 方程进行了测试,结果令人鼓舞。本文的目的是研究如何使用 Gustafsson 等人提出的与 pH 值有关的 Freundlich 模型来描述 26 种矿物土壤(有机碳含量均低于 12%)中的钒酸盐(V)吸附情况,并讨论在风险评估中使用该模型的可能性。文中给出了吸附过程的动力学曲线、钼吸附初期的扩散系数值。特别是,在本研究中,将 99Mo 和 131I 作为 Sg 和 Ts 的同系物,利用表面改性的夏巴锡岩作为液固系统,对其放射性痕量物质的分布系数进行了研究。钼离子浓度为 1 g/L、pH 值为 4.5-5 的钼酸铵溶液在静态条件下进行了钼吸附动力学研究。 在相同条件下,与扩散系数低得多的 AN-2F 阴离子交换器相比,DGT + M 阴离子交换器吸附钼离子的速度要快得多。在通常含有矿物酸(盐酸、硫酸和硝酸)的工业溶液中测定了静态交换容量(SEC)。将测试得出的阴离子交换器动力学平衡参数与 AN-2F 和 AN-1 等工业缩聚阴离子交换器的动力学平衡参数进行了比较。
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