Abstract
The solvent extraction of Ti(IV) from sulfate medium by the commercial extractant Cyanex 301 (HA) has been studied in order to examine this novel system. Heptan-1-ol (5% (v/v) in the organic phase) is used as a de-emulsifier. The equilibration time is 45 min. The experimental results suggest that the extracted species is always TiOA2 (o), though the composition of the reacting aqueous Ti(IV) species may vary depending on the concentration levels of Ti(IV), pH, HA and . The equilibrium constant (Kex) at 303 K is measured to be 101.117 and 10−1.243 for the reaction of monomeric, non-sulfated, mono, and non-hydrolyzed TiO2+, respectively. The effects of heptan-1-ol, temperature, loading, and diluent type have been reported. Stripping can be done effectively by a solution of 1 mol/dm3 H2SO4 containing 5%(v/v) of “100 volume” H2O2. The possibilities of separation of Ti(IV) from Cu(II), Zn(II), Fe(III), Co(II), and Ni(II) have been predicted. It is proved to be an effective extractant for Ti(IV)/Fe(III) separation from sulphate medium at pH ∼ 1.
ACKNOWLEDGEMENTS
The authors are grateful to Cytec Canada Inc. for supplying Cyanex 301 as a gift. One of the authors (A. K. Karmakar) acknowledges the National Science Information and Communication Technology (NSICT) Division of the Ministry of Science and Technology, Government of the People's Republic of Bangladesh (Secretariat, Dhaka) for awarding a fellowship to complete this work.
Notes
*NE: non-extractable, CE: complete extraction, *: aqueous solution becomes cloudy before extraction but becomes clear after extraction.
*N.B.: T.W˭This work. Data in italics are extrapolated. *Literature is not available.