4.5 Article

Graphene Oxide/Polyethyleneimine-Modified Cation Exchange Membrane for Efficient Selective Recovery of Ammonia Nitrogen from Wastewater

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MEMBRANES
卷 13, 期 8, 页码 -

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MDPI
DOI: 10.3390/membranes13080726

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cation exchange membrane; graphene oxide; polyethyleneimine; Donnan dialysis; selective NH4+ separation

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A novel CEM with a GO-PEI crosslinked layer was designed to achieve efficient NH4+-selective separation. The GO-PEI (20) membrane exhibited high NH4+ transport rate and low Mg2+ transport rate in single-salt solution tests, and maintained good separation performance and structural stability in mixed salt solution tests. This facile surface charge modulation approach provides a promising avenue for achieving efficient NH4+-selective separation by modified CEMs.
Competition for the migration of interfering cations limits the scale-up and implementation of the Donnan dialysis process for the recovery of ammonia nitrogen (NH4+-N) from wastewater in practice. Highly efficient selective permeation of NH4+ through a cation exchange membrane (CEM) is expected to be modulated via tuning the surface charge and structure of CEM. In this work, a novel CEM was designed to form a graphene oxide (GO)-polyethyleneimine (PEI) crosslinked layer by introducing self-assembling layers of GO and PEI on the surface of a commercial CEM, which rationally regulates the surface charge and structure of the membrane. The resulting positively charged membrane surface exhibits stronger repulsion for divalent cations compared to monovalent cations according to Coulomb's law, while, simultaneously, GO forms pi-metal cation conjugates between metal cations (e.g., Mg2+ and Ca2+), thus limiting metal cation transport across the membrane. During the DD process, higher NH4+ concentrations resulted in a longer time to reach Donnan equilibrium and higher NH4+ flux, while increased Mg-2(+) concentrations resulted in lower NH4+ flux (from 0.414 to 0.213 mol center dot m(-2)center dot h(-1)). Using the synergistic effect of electrostatic interaction and non-covalent cross-linking, the designed membrane, referred to as GO-PEI (20) and prepared by a 20 min impregnation in the GO-PEI mixture, exhibited an NH4+ transport rate of 0.429 mol center dot m(-2)center dot h(-1) and a Mg2+ transport rate of 0.003 mol center dot m(-2)center dot h(-1) in single-salt solution tests and an NH4+/Mg2+ selectivity of 15.46, outperforming those of the unmodified and PEI membranes (1.30 and 5.74, respectively). In mixed salt solution tests, the GO-PEI (20) membrane showed a selectivity of 15.46 (similar to 1.36, the unmodified membrane) for NH4+/Mg2+ and a good structural stability after 72 h of continuous operation. Therefore, this facile surface charge modulation approach provides a promising avenue for achieving efficient NH4+-selective separation by modified CEMs.

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