Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Kinetics of cadmium ion sorption on ion exchange and chelating resins

Journal Article · · Solvent Extraction and Ion Exchange
Cadmium sorption from aqueous solutions on sulfonic (C-150) and iminodiacetic (S-930) Purolite macroporous resins was investigated. The influence of operating variables such as initial pH, Cd(II) concentration, time and temperature on the equilibrium parameters was measured. The ion preference and sorption ability of resins, i.e., binding constant (b) and saturation capacity (x{sub m}), derived from sorption isotherm, depend on the functional group structure. The Cd(II) uptake is only particle diffusion controlled. The kinetic parameters, i.e., t{sub 1/2} values for 50% attainment of equilibrium sorption, rate constant ({bar K}) and diffusion coefficient ({bar D}) are higher on the sulfonic resin. The moving boundary particle diffusion model fits the entire ion sorption process on chelating resin, but only the initial sorption on the sulfonic resin, confirming the difference in chemistry between chelation and ion exchange.
Research Organization:
Technical Univ. of Iassy (RO)
OSTI ID:
20019006
Journal Information:
Solvent Extraction and Ion Exchange, Journal Name: Solvent Extraction and Ion Exchange Journal Issue: 6 Vol. 17; ISSN 0736-6299; ISSN SEIEDB
Country of Publication:
United States
Language:
English

Similar Records

Chelating resins: Sorption characteristics and radioanalytical applications
Conference · Tue Oct 01 00:00:00 EDT 1996 · OSTI ID:370663

Removal of NO by coordination to iron (II) immobilized chelate resins
Journal Article · Tue May 01 00:00:00 EDT 1990 · Industrial and Engineering Chemistry Research; (United States) · OSTI ID:5747744

Recovery of uranium from phosphoric acid solutions using chelating ion-exchange resins
Journal Article · Fri May 01 00:00:00 EDT 1998 · Industrial and Engineering Chemistry Research · OSTI ID:624349