Research Papers by Gerald Pourcelly

Two 2D models of non-stationary and non-isothermal transfer of a strong binary electrolyte in a rectangular electrodialysis desalination cell formed by anion- and cation-exchange membranes are developed. Both gravitational and forced convection occurring in underlimiting current mode are taken into

2 ! A modified static method for investigation of CO3 !, HCO3 and OH! ions sorption by anion-exchange membranes KD — — — — V W — — — zi Dw — — Dissociation constant Ion exchange equilibrium coefficient Mass of membrane sample Number of stages j in experiment k Amount of ion i participating in ion ex