The general stages of application of modeling of mass transfer of substances through a membrane in solution separation process for designing industrial apparatuses are presented. Numerical values of empirical coefficients are obtained to calculate friction coefficients of solvent–membrane, solute–membrane, and solute–solvent systems for anode-adjacent and cathode-adjacent membranes for separation of model aqueous CuSO4, Fe(NO3)3, and Ni(NO3)2 solutions of engineering industries.
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Translated from Khimicheskoe i Neftegazovoe Mashinostroenie. Vol. 56. No. 3, pp. 7–10, March, 2020.
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Shestakov, K.V., Lazarev, S.I. & Khokhlov, P.A. Application of Modeling of Mass Transfer of Substances through Membrane for Designing Industrial Electromembrane Apparatuses. Chem Petrol Eng 56, 176–181 (2020). https://doi.org/10.1007/s10556-020-00756-1
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DOI: https://doi.org/10.1007/s10556-020-00756-1