Purolite S950 Research Articles

An Integrated Process for the Removal of Cd and U from Wet Phosphoric Acid

In this work, an integrated process based on the application of two membrane technologies for the selective recovery of the U and the Cd contained in wet phosphoric acid is presented. The process is based on the removal of U by ion exchange using the Purolite S940 resin as ion-exchange resin followed by the selective removal of Cd by means of membrane-assisted solvent extraction with Aliquat 336 as the selective extractant. After sorption of U, the elution step was carried out with a 1 M solution of Na{sub 2}CO{sub 3} whereas the back extraction of Cd was efficiently achieved by simply using water in the back-extraction phase. Because of working with acidic solutions containing initially 200 mg/l of U and 50 mg/l of Cd, the viability of the process for reduction of the U and Cd concentration below 2 mg/l has been checked, obtaining the kinetic models and parameters of the removal steps, thus, establishing the basis for the process design and optimization.

Recovery of Uranium from Phosphoric Acid Solutions Using Chelating Ion-Exchange Resins

Experimental measurements have been made on the batch extraction of uranium from phosphoric acid solutions using various chelating ion-exchange resins (RSPO, Diaion-CRP200, Diphonix, Purolite S940, Duolite ES467, and Lewatit OC 1060) and a solvent containing ion-exchange resins (Actinide-CU). The kinetic performance of ion-exchange resins was compared, and the effect of Fe(II) and Ca(II) ions on the sorption and elution performance has also been examined. The results showed that the resin Actinide-CU containing a diphosphonate extractant was very effective for removing uranium from phosphoric acid solution. However, the elution performance of this resin with both acid and carbonate eluants was poor. It is concluded that the chelating resins Diphonix, Duolite ES467, Lewatit OC 1060, and Purolite S940 give reasonable sorption of uranium in the presence of Fe(II) ions in batch sorption trials. The desorption of uranium has been performed quantitatively using carbonate eluants. Purolite S940 was used in small...

Distribution coefficients and ion exchange behaviour of some elements with Purolite S-950 in hydrochloric acid.

Equilibrium distribution coefficients, K(d), are presented for some elements in hydrochloric acid using the phosphonated polystyrene ion exchange resin Purolite S-950. A few possible separations using this resin are demonstrated by elution curves and separations of synthetic mixtures of some elements (Ru, Rh, Mo, I, Li, Te, Si, Y).

Mechanistic studies of chelating resins using two-phase potentiometry

The elucidation of metal ion binding mechanisms with chelating resins by treating the resin as a collection of monomeric units is an established approach. In this paper, this approach is used to treat data obtained from two-phase potentiometric titrations by the programme ESTA. Apparent protonation and formation constants could be calculated. From these, species distribution plots could be obtained. These, in turn, allowed the calculation of the more familiar distribution ratios. The method was tested on Fe(III) and Nd(III) bonding with the iminodiacetate functionalized resin, Chelex 100; and Ca(II) bonding to the aminomethylphosphonate functionalized resin, Purolite S940. Good results were obtained indicating the applicability of this method. Comparisons with the literature are made.