Improvement of the OPAP Uranium Recovery Process from Phosphoric Acid

The American Institute of Mining, Metallurgical, and Petroleum Engineers
M. S. Tsai H. M. Wu Y. D. Chuang
Organization:
The American Institute of Mining, Metallurgical, and Petroleum Engineers
Pages:
5
File Size:
344 KB
Publication Date:
Jan 1, 1984

Abstract

To contact the commercial OPAP-kerosene solution with CH3OH – H20 solution, we used the appropriate concentration of DOPAP / MOPAP solvent. By using this treated OPAP solvent, uranium can be recovered from wet-process phosphoric acid. Electric DC power is supplied on the dual side of the ion-exchange membrane of a specially designed box-type mixer settler. U(VI) is reduced to U(IV) in the cathode and U(IV) is oxidized to U(VI) in the anode. Uranium is extracted in the cathode by treating it with OPAP solvent. Next the uranium is stripped from the loaded OPAP solvent by concentrated phosphoric acid in the anode. After 300 hours of continuous operation total recovery of uranium is as much as 95%.
Citation

APA: M. S. Tsai H. M. Wu Y. D. Chuang  (1984)  Improvement of the OPAP Uranium Recovery Process from Phosphoric Acid

MLA: M. S. Tsai H. M. Wu Y. D. Chuang Improvement of the OPAP Uranium Recovery Process from Phosphoric Acid. The American Institute of Mining, Metallurgical, and Petroleum Engineers, 1984.

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