Abstract

us to avoid contact of oxides used in classical reference electrodes with the chloride–oxyfluoride melt. The electrolytic processes with accumulation of products electrodeposited on the cathode were per� formed in a sealed electrolyzer in the galvanostatic mode. The cell, as a platinum crucible (30 mm in diameter, 40 mm in height), was placed inside a cylin� der vessel made of stainless steel. The vessel was filled with pure argon. Heating of the vessel was carried out in a shaft furnace; the temperature was maintained with the accuracy of ±2°С. The anode (a tantalum plate 3 mm thick) was placed at the bottom of the plat� inum crucible. Molybdenum rods (5mm in diameter) were used as cathodes. Each portion of an electrolyte (about 40 g) served for a single cathodic deposition cycle only. Cathodic products, after cooling to room temperature in an argon atmosphere, were leached with 10% hydrochloric acid, then washed with dis� tilled water and ethanol, and dried in air at 40°C.

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