Counter-ion mobility in cation-exchange membranes: Single electrolytes versus mixtures

Many electrochemical technologies utilize ion-exchange membranes for water treatment (e.g. electrodialysis), energy conversion applications (e.g. redox flow batteries), and electrochemical synthesis (e.g. bipolar membrane electrodialysis). Ion mobility inside the membrane plays a primary role in determining the energy efficiency and ion selectivity of the process. We investigated the mobility of Na + , K + , Mg 2+ , and Ca 2+ inside commercial cation-exchange membranes based on conductivity measurements in single electrolyte solutions. Moreover, we employed a transport model to simulate two scenarios for the counter-ion mobilities in a binary mixture of Na + and Mg 2+ . In a single electrolyte, the mobility of various counter-ions is reduced to different extents mainly based on the membrane water volume fraction as well as the ion hydration. For example, in membranes with low-to-moderate water volume fractions, the Mg 2+ mobility is 9–17 times more reduced than the mobility of Na + . In a mixture, this difference in mobility reduction is less pronounced since the ions are limited by the surrounding counter-ions inside the membranes. In this regard, the counter-ion mobilities for a single electrolyte do not necessarily reflect the counter-ion selectivity during multi-electrolyte experiments. Furthermore, the counter-ion selectivity in electrodialysis is highly influenced by the ion partitioning within the membrane in addition to ion mobilities in the diffusion boundary layer. • Membrane conductivity in single electrolytes does not reflect the ion flux selectivity during electrodialysis of a mixture. • The cation-exchange membrane resistance depends on the counter-ion type: K + < Na + < Ca 2+ < Mg 2+ . • The ion mobility inside the membranes is limited by the mobility of the surrounding ions.