In this study, the possibilities of selective sorption of neodymium and praseodymium ions from a mixture of their solution were studied. For this purpose, based on the obtained results on the dynamics of sorption of each ion separately by industrial hydrogels KU-2-8 (Na+): AV-17-8 (Cl-), interpolymer systems with different molar ratios of cation exchanger and anion exchanger, namely 4:2 and 3:3, respectively, were selected. The choice of these ratios was based on the detection of increased sorption of praseodymium ions from a model solution compared to neodymium ions. The sorption (48 h.) and desorption (72 h.) processes were carried out in two modes: dynamic (with active mixing, speed range 80-150 rpm) and static (without mixing the working solution from which REE were extracted), at room temperature (close to 25° С). According to the obtained results, sorption in the dynamic mode in the ratios of 4:2 and 3:3 does not lead to any selectivity (praseodymium ions were sorbed better than neodymium ions by 3.93% and 2.96% for each ratio). However, a high degree of extraction was noted for both ions: Pr3+ = 99.36%, Nd3+ = 95.67% for the 4:2 system and Pr3+ = 81.33%, Nd3+ =79% for the 3:3 system. In the static mode, the degree of extraction of both metals was significantly lower: for the 4:2 system Pr3+ = 19.33%, Nd3+ = 24%.But, despite this, in the static mode, greater selectivity was observed with respect to one of the metals, namely neodymium. Thus, with a ratio of 4:2, neodymium was sorbed better than praseodymium by 24.16%, and in the 3:3 system by 39.83%. When desorption was carried out from the cationite, a similar picture was also preserved. From here it becomes clear the relevance and necessity of further study of the issue of choosing a technological mode for the sorption of REE from industrial solutions, as well as the creation and selection of similar interpolymer systems that can provide sufficient selectivity in relation to one of the target ions in several extraction cycles.