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A mathematical model of a three-compartment electro-reactor process with ion-exchange membranes for recycling and resource recovery of desulfurization residuals was developed. This model describes the electrochemical separation process in the bulk solution and the diffusion boundary layer close to themembrane surfaces with a multiphysics-based approach. This approach considered the following mechanisms: diffusion and migration in different control volumes, the effect of bubbles, the effect of the geometry of the reactor, and the electrochemical reactions of the gases. The analytical solution to the developed model was obtained using a Laplace transformation, and the numerical solution was solved inWolfram Mathematica and COMSOL Multiphysics. All analytical solutions exhibit a good agreement with the numerical solutions. The analysis of the model revealed that the following parameters may have a positive effect on the performance of the electro-reactor: (1) a high concentration gradient across themembrane enhances mass transport; (2) the current density is the key controlling parameter for both mass transport and bubble formation; (3) a small gap in the cell spacermay improve the performance of the reactor; (4) appropriate effective areas of the membrane for mass transfer guarantees high performance.
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