Holcomb, R.R., and Higgins, I.R. DEVELOPMENT OF THE EXCER PROCESS V: RECOVERY, PURIFICATION, AND IRON REDUCTION OF URANIUM USING A SULFATE ION EXCHANGE SYSTEM. United States: N. p., 1959.
Web. doi:10.2172/4280508.
Holcomb, R.R., & Higgins, I.R. DEVELOPMENT OF THE EXCER PROCESS V: RECOVERY, PURIFICATION, AND IRON REDUCTION OF URANIUM USING A SULFATE ION EXCHANGE SYSTEM. United States. doi:10.2172/4280508.
Holcomb, R.R., and Higgins, I.R. Tue .
"DEVELOPMENT OF THE EXCER PROCESS V: RECOVERY, PURIFICATION, AND IRON REDUCTION OF URANIUM USING A SULFATE ION EXCHANGE SYSTEM". United States.
doi:10.2172/4280508. https://www.osti.gov/servlets/purl/4280508.
@article{osti_4280508,
title = {DEVELOPMENT OF THE EXCER PROCESS V: RECOVERY, PURIFICATION, AND IRON REDUCTION OF URANIUM USING A SULFATE ION EXCHANGE SYSTEM},
author = {Holcomb, R.R. and Higgins, I.R.},
abstractNote = {A uranium sulfate process flowsheet for the production of UF/sub 4/ from sulfate ore leach liquors is presented. The uraninm is sorbed on an anion- exchange resin from 0.2 M sulfate ore leach and eluted with 2 M H/sub 2/S0/sub 4/. Iron powder reduces UO/sub 2/SO/sub 4/ to U(SO/sub 4/)2 which is then sorbed on anion-exchange resin to separate it from the iron and eluted from the anion- exchange resin with 2 M H/sub 2/SO/sub 4/. The resulting U(SO/sub 4)2 is sorbed on a cationexchange resin from the H/sub 2/SO/sub 4/ solution and eluted from the resin with 5 to 6 M HCl. The UCl/sub 4/ thus produced may be treated with stoichiometric amounts of HF in order to precipitate UF/sub 4/.3/4H/sub 2/O. (auth)},
doi = {10.2172/4280508},
journal = {},
number = ,
volume = ,
place = {United States},
year = {Tue Jan 27 00:00:00 EST 1959},
month = {Tue Jan 27 00:00:00 EST 1959}
}
