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Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis

Electrodialysis (ED) with ion-exchange membranes is a promising method for the extraction of phosphates from municipal and other wastewater in order to obtain cheap mineral fertilizers. Phosphorus is transported through an anion-exchange membrane (AEM) by anions of phosphoric acid. However, which ph...

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Autores principales: Rybalkina, Olesya, Tsygurina, Kseniya, Melnikova, Ekaterina, Mareev, Semyon, Moroz, Ilya, Nikonenko, Victor, Pismenskaya, Natalia
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2019
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6678999/
https://www.ncbi.nlm.nih.gov/pubmed/31340475
http://dx.doi.org/10.3390/ijms20143593
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author Rybalkina, Olesya
Tsygurina, Kseniya
Melnikova, Ekaterina
Mareev, Semyon
Moroz, Ilya
Nikonenko, Victor
Pismenskaya, Natalia
author_facet Rybalkina, Olesya
Tsygurina, Kseniya
Melnikova, Ekaterina
Mareev, Semyon
Moroz, Ilya
Nikonenko, Victor
Pismenskaya, Natalia
author_sort Rybalkina, Olesya
collection PubMed
description Electrodialysis (ED) with ion-exchange membranes is a promising method for the extraction of phosphates from municipal and other wastewater in order to obtain cheap mineral fertilizers. Phosphorus is transported through an anion-exchange membrane (AEM) by anions of phosphoric acid. However, which phosphoric acid anions carry the phosphorus in the membrane and the boundary solution, that is, the mechanism of phosphorus transport, is not yet clear. Some authors report an unexpectedly low current efficiency of this process and high energy consumption. In this paper, we report the partial currents of H(2)PO(4)(−), HPO(4)(2−), and PO(4)(3−) through Neosepta AMX and Fujifilm AEM Type X membranes, as well as the partial currents of H(2)PO(4)(−) and H(+) ions through a depleted diffusion layer of a 0.02 M NaH(2)PO(4) feed solution measured as functions of the applied potential difference across the membrane under study. It was shown that the fraction of the current transported by anions through AEMs depend on the total current density/potential difference. This was due to the fact that the pH of the internal solution in the membrane increases with the growing current due to the increasing concentration polarization (a lower electrolyte concentration at the membrane surface leads to higher pH shift in the membrane). The HPO(4)(2−) ions contributed to the charge transfer even when a low current passed through the membrane; with an increasing current, the contribution of the HPO(4)(2−) ions grew, and when the current was about 2.5 i(lim)(Lev) (i(lim)(Lev) was the theoretical limiting current density), the PO(4)(3−) ions started to carry the charge through the membrane. However, in the feed solution, the pH was 4.6 and only H(2)PO(4)(−) ions were present. When H(2)PO(4)(−) ions entered the membrane, a part of them transformed into doubly and triply charged anions; the H(+) ions were released in this transformation and returned to the depleted diffusion layer. Thus, the phosphorus total flux, j(P) (equal to the sum of the fluxes of all phosphorus-bearing species) was limited by the H(2)PO(4)(−) transport from the bulk of feed solution to the membrane surface. The value of j(P) was close to i(lim)(Lev)/F (F is the Faraday constant). A slight excess of j(P) over i(lim)(Lev)/F was observed, which is due to the electroconvection and exaltation effects. The visualization showed that electroconvection in the studied systems was essentially weaker than in systems with strong electrolytes, such as NaCl.
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spelling pubmed-66789992019-08-19 Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis Rybalkina, Olesya Tsygurina, Kseniya Melnikova, Ekaterina Mareev, Semyon Moroz, Ilya Nikonenko, Victor Pismenskaya, Natalia Int J Mol Sci Article Electrodialysis (ED) with ion-exchange membranes is a promising method for the extraction of phosphates from municipal and other wastewater in order to obtain cheap mineral fertilizers. Phosphorus is transported through an anion-exchange membrane (AEM) by anions of phosphoric acid. However, which phosphoric acid anions carry the phosphorus in the membrane and the boundary solution, that is, the mechanism of phosphorus transport, is not yet clear. Some authors report an unexpectedly low current efficiency of this process and high energy consumption. In this paper, we report the partial currents of H(2)PO(4)(−), HPO(4)(2−), and PO(4)(3−) through Neosepta AMX and Fujifilm AEM Type X membranes, as well as the partial currents of H(2)PO(4)(−) and H(+) ions through a depleted diffusion layer of a 0.02 M NaH(2)PO(4) feed solution measured as functions of the applied potential difference across the membrane under study. It was shown that the fraction of the current transported by anions through AEMs depend on the total current density/potential difference. This was due to the fact that the pH of the internal solution in the membrane increases with the growing current due to the increasing concentration polarization (a lower electrolyte concentration at the membrane surface leads to higher pH shift in the membrane). The HPO(4)(2−) ions contributed to the charge transfer even when a low current passed through the membrane; with an increasing current, the contribution of the HPO(4)(2−) ions grew, and when the current was about 2.5 i(lim)(Lev) (i(lim)(Lev) was the theoretical limiting current density), the PO(4)(3−) ions started to carry the charge through the membrane. However, in the feed solution, the pH was 4.6 and only H(2)PO(4)(−) ions were present. When H(2)PO(4)(−) ions entered the membrane, a part of them transformed into doubly and triply charged anions; the H(+) ions were released in this transformation and returned to the depleted diffusion layer. Thus, the phosphorus total flux, j(P) (equal to the sum of the fluxes of all phosphorus-bearing species) was limited by the H(2)PO(4)(−) transport from the bulk of feed solution to the membrane surface. The value of j(P) was close to i(lim)(Lev)/F (F is the Faraday constant). A slight excess of j(P) over i(lim)(Lev)/F was observed, which is due to the electroconvection and exaltation effects. The visualization showed that electroconvection in the studied systems was essentially weaker than in systems with strong electrolytes, such as NaCl. MDPI 2019-07-23 /pmc/articles/PMC6678999/ /pubmed/31340475 http://dx.doi.org/10.3390/ijms20143593 Text en © 2019 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Rybalkina, Olesya
Tsygurina, Kseniya
Melnikova, Ekaterina
Mareev, Semyon
Moroz, Ilya
Nikonenko, Victor
Pismenskaya, Natalia
Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title_full Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title_fullStr Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title_full_unstemmed Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title_short Partial Fluxes of Phosphoric Acid Anions through Anion-Exchange Membranes in the Course of NaH(2)PO(4) Solution Electrodialysis
title_sort partial fluxes of phosphoric acid anions through anion-exchange membranes in the course of nah(2)po(4) solution electrodialysis
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6678999/
https://www.ncbi.nlm.nih.gov/pubmed/31340475
http://dx.doi.org/10.3390/ijms20143593
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