Methods of obtaining granular sorbents for catching and purifying volatile inorganic fluorides are examined. The results of optimizing the technology of granular lithium fluoride and approaches to obtaining pelleted barium and calcium fluorides are presented. The granules obtained gave capacity to 0.6 g HF/g sorbent while maintaining the initial structure. The initial destruction was negligible, the number of destroyed granules was the same after three sorption-desorption cycles.Absorption processes are finding wide applications for obtaining and purifying volatile inorganic fluorides in the technologies of the nuclear-fuel cycle [1]. The best known sorbent is one that is based on powdered or granular sodium fluoride -a universal absorber of many volatile inorganic fluorides. Thus, positive experience has been gained in using powered and granular lithium fluoride for deep removal of hydrogen fluoride from uranium hexafluoride. Calcium, strontium, and barium fluoride possess high selectivity to technetium and boron fluorides. Barium fluoride has a substantial (to 5 molecules) theoretical capacity for hydrogen fluoride [2]. The main physicochemical and sorption properties of these fluorides have been well studied but the absence of technologies for obtaining in a granular form and regenerating after use is impeding their industrial applications. In this connection, the search for new methods of obtaining sorbents based on fluorides of alkali and alkali-earth methods, meeting modern technological and economic production requirements, is a pressing problem.This article presents the results of production of pelleted sorbents based on lithium, calcium, and barium fluorides and their compositions, suitable for sorbtion removal of hydrogen fluoride from volatile uranium fluorides and refractory metals [3,4].The production of pelleted sorbents is based on the formation of moistened powders with the formation of a "brittle gel," formed during the hydration of NaHF 2 or NH 4 F type salts. Correspondingly, the method of obtaining sorbents includes the following operations: preparation of a mix using ammonium fluoride as the binder and pore-generator, formation on a granulator, drying of sorbent pellets in a hot air stream at 100°C, development at 150-200°C and fixing of a porous structure (sintering) at 350-400°C.The drawbacks of using ammonium fluoride as the pore-generator were revealed in the course of practical tests. Thus, the decomposition of ammonium fluoride gives rise to intense corrosion of the construction materials used for the pro-