Commercial, synthetic zeolites, have been evaluated for the removal of
thorium ions from aqueous solution by ion-exchange. Kinetics of uptak
e of thorium ions from solutions of various initial Th concentrations
by four zeolites of different types viz., 13X, AR-1, ZSM-5 and 4A, was
studied in batch experiments. The Th-Na exchange process is accompani
ed by side reactions such as H-Na exchange and surface precipitation o
f Th-hydroxide, making it difficult to derive any conclusive evidence
about the nature of diffusion of thorium ions. Acidity of the solution
, produced due to the hydrolysis of Th ions, has an adverse effect on
the stability of the zeolites. X-ray diffraction and Infra red spectra
l studies were used for the characterization of the zeolites with resp
ect to crystallinity, surface precipitation of Th-hydroxide etc., befo
re and after exchange. Stirring was observed to dramatically affect th
e establishment of equilibrium requiring about 2 weeks for unstirred a
nd just 4 hours for thoroughly stirred solutions. Adsorption isotherms
obtained for Zeolite-13X, the one performing the best, with isonormal
solutions of Th-nitrate at total ionic concentrations (Th + Na) of 0.
024 N in one case and 0.1 N in the other, displayed unique shapes attr
ibutable to the accompanying side reactions. Distributions coefficient
(K(d)) values varied from above 2000 ml/g at 0.1 mM Th to 15 ml/g at
10 mM Th concentration. In column experiments with 1 mM Th-nitrate sol
ution and Zeolite-13X, percent breakthrough of 10, 50 and 96% were obt
ained on passing 125, 350 and 700 bed volumes respectively. Exchange c
apacity of 1.2 meq/g, corresponding to the passage of 300 bed volumes,
was observed.