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Application of chelating weak base resin Dowex M4195 to the recovery of uranium from mixed sulfate/chloride media. / Ogden, Mark; Moon, Ellen M.; Wilson, Abigail et al.
In: Chemical Engineering Journal, Vol. 317, 01.06.2017, p. 80-89.

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Ogden M, Moon EM, Wilson A, Pepper SE. Application of chelating weak base resin Dowex M4195 to the recovery of uranium from mixed sulfate/chloride media. Chemical Engineering Journal. 2017 Jun 1;317:80-89. Epub 2017 Feb 13. doi: 10.1016/j.cej.2017.02.041

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Ogden, Mark ; Moon, Ellen M. ; Wilson, Abigail et al. / Application of chelating weak base resin Dowex M4195 to the recovery of uranium from mixed sulfate/chloride media. In: Chemical Engineering Journal. 2017 ; Vol. 317. pp. 80-89.

RIS

TY - JOUR

T1 - Application of chelating weak base resin Dowex M4195 to the recovery of uranium from mixed sulfate/chloride media

AU - Ogden, Mark

AU - Moon, Ellen M.

AU - Wilson, Abigail

AU - Pepper, Sarah E.

PY - 2017/6/1

Y1 - 2017/6/1

N2 - The use of untreated seawater or bore water in uranium mineral processing circuits may represent a cheaper and more sustainable water resource for Australia’s mining operations. Using present technologies, the increased salinity from these water sources results in decreased uranium extraction and increased extraction of impurities. There is incentive to overcome these challenges, either through new technologies, or repurposing existing technologies. The ion exchange behaviour of U from sulfate media on the weakly basic chelating resin Dowex M4195 (bis-picolylamine functionality) and the effect of competing chloride and impurity metal ions (Th, Fe, Al, Cu, Ni) has been studied. Experiments to determine acid, and sulfate media behaviour, and extraction thermodynamics including the effect of increasing chloride concentration upon extraction behaviour were carried out. Dowex M4195 was found to have pK1 and pK2 values at 4.13 ± 0.04 and 2.1 ± 0.1 determined at 1.0 M NaCl. Dowex M4195 shows affinity for U(VI) over Fe3+ and Al3+ in sulfuric acid media with a U(VI) pH50 a full pH unit below that of Fe3+ at 0.17 and 1.82 respectively. With increasing chloride concentrations U and Th extraction is suppressed but Fe extraction increases. At the highest chloride concentrations explored Fe is preferentially extracted over U, and Th is not extracted at all. As chloride concentration increases the extraction of U passes through a minimum (40%) before increasing to around 60% for 4.0 M chloride at pH 1.80. Al3+ is not extracted by M4195 under any conditions explored. Dowex M4195 does show high selectivity for Cu and Ni over everything else.

AB - The use of untreated seawater or bore water in uranium mineral processing circuits may represent a cheaper and more sustainable water resource for Australia’s mining operations. Using present technologies, the increased salinity from these water sources results in decreased uranium extraction and increased extraction of impurities. There is incentive to overcome these challenges, either through new technologies, or repurposing existing technologies. The ion exchange behaviour of U from sulfate media on the weakly basic chelating resin Dowex M4195 (bis-picolylamine functionality) and the effect of competing chloride and impurity metal ions (Th, Fe, Al, Cu, Ni) has been studied. Experiments to determine acid, and sulfate media behaviour, and extraction thermodynamics including the effect of increasing chloride concentration upon extraction behaviour were carried out. Dowex M4195 was found to have pK1 and pK2 values at 4.13 ± 0.04 and 2.1 ± 0.1 determined at 1.0 M NaCl. Dowex M4195 shows affinity for U(VI) over Fe3+ and Al3+ in sulfuric acid media with a U(VI) pH50 a full pH unit below that of Fe3+ at 0.17 and 1.82 respectively. With increasing chloride concentrations U and Th extraction is suppressed but Fe extraction increases. At the highest chloride concentrations explored Fe is preferentially extracted over U, and Th is not extracted at all. As chloride concentration increases the extraction of U passes through a minimum (40%) before increasing to around 60% for 4.0 M chloride at pH 1.80. Al3+ is not extracted by M4195 under any conditions explored. Dowex M4195 does show high selectivity for Cu and Ni over everything else.

KW - Anion exchange

KW - Mass transfer

KW - Ion exchange resin

KW - Dowex M4195

KW - Uranium

U2 - 10.1016/j.cej.2017.02.041

DO - 10.1016/j.cej.2017.02.041

M3 - Article

VL - 317

SP - 80

EP - 89

JO - Chemical Engineering Journal

JF - Chemical Engineering Journal

SN - 1385-8947

ER -