SORPTION AND DESORPTION OF URANYL IONS BY SILICA-GEL - PH, PARTICLE-SIZE AND POROSITY EFFECTS

Citation
P. Michard et al., SORPTION AND DESORPTION OF URANYL IONS BY SILICA-GEL - PH, PARTICLE-SIZE AND POROSITY EFFECTS, Microporous materials, 5(5), 1996, pp. 309-324
Citations number
46
Categorie Soggetti
Chemistry Physical","Material Science","Chemistry Applied
Journal title
ISSN journal
09276513
Volume
5
Issue
5
Year of publication
1996
Pages
309 - 324
Database
ISI
SICI code
0927-6513(1996)5:5<309:SADOUI>2.0.ZU;2-G
Abstract
Uranium sorption by silica gel was shown to be very sensitive to pH; t he optimum pH range is ca. 5-5.5, which coincides with the appearance of hydrolysed forms of uranyl. A two-phase surface mechanism is propos ed: first the adsorption of hydrolysed forms, which precipitate later on the surface of the oxide, then the removal of residue at the new so rbing surface by adsorption or precipitation. Particle size and pore c haracteristics have a limited effect on equilibrium concentration, but greatly influence sorption kinetics. A two-phase kinetic mechanism is proposed which gives external and intraparticle mass transfer coeffic ients of the order of 10(-7)-10(-5) and 10(-8)-10(-7) m min(-1), respe ctively. Both a mesoporous and a microporous silica gel were examined in order to determine the influence of pore size on sorption kinetics: the ratio between solute size and pore diameter appears to be the maj or factor in governing the uptake rate. The desorption of silica gel w as also studied, particularly concerning the nature and concentration of the elution agent. Acid solutions are most effective at removing ur anium. Using a batch system the number of moles of acid needs to be ei ght times greater than those of uranium in order to obtain a desorptio n efficiency higher than 90%. In dynamic desorption, on the other hand , 0.5 M hydrochloric acid gives both total desorption and optimal meta l recovery. Eluate concentrations as high as 100-200 gl(-1) can be obt ained. Furthermore, when seven sorption-desorption cycles were carried out using the column system, removal performances were maintained and the sorbent could be re-used.