Abstract
A process for the recovery of at least one of uranium and vanadium from an aqueous liquor is claimed. It comprises: (a) treating the liquor with a low molecular weight completely water-miscible solvent selected from the group consisting of methanol, iso-propyl alcohol or acetone to form at least two phases; (b) separating the phases; (c) recovering the solvent from the first phase as the azeotropic solvent/water mixture by simple, non-fractional distillation and recycling the mixture to step (a); and (d) recovering metal values from a second one of the phases.
Citation Formats
Vojkovic, M.
Obtaining uranium and/or vanadium values from solutions.
Australia: N. p.,
1982.
Web.
Vojkovic, M.
Obtaining uranium and/or vanadium values from solutions.
Australia.
Vojkovic, M.
1982.
"Obtaining uranium and/or vanadium values from solutions."
Australia.
@misc{etde_6786961,
title = {Obtaining uranium and/or vanadium values from solutions}
author = {Vojkovic, M}
abstractNote = {A process for the recovery of at least one of uranium and vanadium from an aqueous liquor is claimed. It comprises: (a) treating the liquor with a low molecular weight completely water-miscible solvent selected from the group consisting of methanol, iso-propyl alcohol or acetone to form at least two phases; (b) separating the phases; (c) recovering the solvent from the first phase as the azeotropic solvent/water mixture by simple, non-fractional distillation and recycling the mixture to step (a); and (d) recovering metal values from a second one of the phases.}
place = {Australia}
year = {1982}
month = {Apr}
}
title = {Obtaining uranium and/or vanadium values from solutions}
author = {Vojkovic, M}
abstractNote = {A process for the recovery of at least one of uranium and vanadium from an aqueous liquor is claimed. It comprises: (a) treating the liquor with a low molecular weight completely water-miscible solvent selected from the group consisting of methanol, iso-propyl alcohol or acetone to form at least two phases; (b) separating the phases; (c) recovering the solvent from the first phase as the azeotropic solvent/water mixture by simple, non-fractional distillation and recycling the mixture to step (a); and (d) recovering metal values from a second one of the phases.}
place = {Australia}
year = {1982}
month = {Apr}
}