Abstract
Exchange equilibria between a cation exchange membrane and an aqueous solution were studied experimentally and theoretically. By using thermodynamic components in terms of the Gibbs phase rule, and a suitable reference state, a convenient method for data treatment was obtained. Thermodynamic mixture properties were derived for one membrane with four pairs of monovalent cations. The results show that when the difference in cation size is small, the cation exchange membrane behaves nearly ideal. For larger differences, the membrane may be described as a regular mixture. Activity coefficients for membrane mixtures can be obtained easily for regular mixtures.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
