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Igosawa, Tatsuki*; Matsumiya, Masahiko*; Sasaki, Yuji
Hydrometallurgy, 208, p.105803_1 - 105803_8, 2022/02
Times Cited Count:3 Percentile:18.82(Metallurgy & Metallurgical Engineering)A novel hydrometallurgical process involving leaching, precipitation, solvent extraction using phosphonium-based ionic liquids (ILs), and crystallization stripping was developed. First, the spent catalyst was leached in distilled water. The leaching percentage of W(VI) was
99.9%. The phosphate ions were separated by precipitation using Fe(NO
)
as the precipitating agent. The separation percentage of phosphate was 90.8%. After the removal of phosphate, Alamine 336 and triethyl-npentylphosphonium bis(trifluoromethylaulfonyl)amide ([P
][NTf
]) were used as the extractant and diluent. The extraction percentage of W(VI) reached 94.6%. The stripping percentage of W(VI) reached 100% at pH8. Finally, crystallization proceeded at pH; 4.5, and the obtained precipitate was identified to be ammonium paratungstate.