Abstract
The research established patterns of the separation of phenylalanine aqueous salt solutions by electrodialysis. It also determined the conditions for the effective and selective separation of the target component by selecting a membrane with the desired properties. The composition of the model solution simulating industrial water in the technology of microbiological synthesis included an aromatic amino acid, phenylalanine (0.05 M), and sodium chloride (0.01 M). Experimental membranes with different mass fractions of sulfonated cation-exchange resin were used. The experiments were carried out in galvanostatic mode using a seven-section electrodialyzer. It was established that the content of the ion-exchanger in the membrane influences the features of the transport of mineral salt and amino acid ions, the value of the separation factor, and the degree of solution demineralization. It was shown that the change in the content of the sulfonated cation-exchanger in the membranes from 45 to 70 wt % makes it possible to increase the rate of mass transfer of a mineral ion by 1.5 times during the electrodialysis of a mixed solution of an amino acid and a mineral salt. For all experimental membranes, the separation factor dependencies on the current density are characterized by the point of extremum corresponding to the interval exceeding the limiting diffusion current ilim by 2–3 times. The maximum separation efficiency was found for a membrane with a cation-exchanger content of 70 wt %. When the value of the limiting diffusion current was exceeded by 2 times, with an increase in the resin content in the membrane, the separation factor increased by 1.5 times. Additionally, the degree of demineralization of the mixed solution in the case of the membrane with the maximum content of the ion-exchanger was 40–60%. The possibility of almost complete demineralization of the solution in the case of the membrane with a resin content of 70 wt % was established when the limiting current density was exceeded by 6 times. The study revealed the role of electroconvection in increasing the loss of an amino acid (the target product) at overlimiting current modes of electrodialysis. It was shown that the main reason for the increase in the amino acid transport through the sulfonated cation-exchange membrane in intense current modes is electroconvection. The occurrence of electroconvection negatively affects the process of water splitting. The electroconvective mixing of the solution at the membrane/solution interface destroys the barrier effect of the depleted diffusion layer with a high pH value. The possibility of deep demineralization of phenylalanine mineral salt solution with a minimal loss of the target product using a membrane with 70 wt % fraction of a sulfonated cation-exchange resin in intense current modes of electrodialysis was established.
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The study was supported by a grant from the Russian Science Foundation no. 21-19-00397, https://rscf.ru/en/ project/21-19-00397/.
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Vasil’eva, V.I., Saud, A.M. & Akberova, E.M. Separation of Phenylalanine Aqueous Salt Solutions by Electrodialysis Using Membranes with Different Mass Fractions of Sulfonated Cation-Exchange Resin. Russ J Electrochem 59, 988–997 (2023). https://doi.org/10.1134/S1023193523110149
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DOI: https://doi.org/10.1134/S1023193523110149