Abstract

From aqueous to non-aqueous redox flow batteries, the general membrane properties are unchanged: electronically isolating anolyte and catholyte and allowing conductance through the membrane to keep charge balance. However, on top of the high cost(1), existing membranes for non-aqueous flow battery inherit the natural disadvantage of non-hydrogen-bonding transport compared to all-vanadium redox system while leaving the door wide open for redox species to pass through. Crossover-induced capacity fade remains one of the most challenging problems for non-aqueous flow battery(2). Efforts have been made to address the issue. For example, composite membranes(3), crosslinking(4) and size exclusion approaches (5) have all been used. Herein, we use Perfluorsulfonate Ion Exchange Membrane (PFSA) as a benchmark to study the crossover behavior in non-aqueous system. For membranes swollen with non-aqueous solvents, tetraalkylammonium cations in the membrane have outperform lithium ion in terms of ionic conductivity(6). However, a large volume of swelling is observed in our study and also in literature(3). In fact, our previous vibrational data suggested that only a small portion of the organic solvent in the membrane participates in solvation of cations, leaving a substantial portion of the solvent molecules as potential carriers to dissolve and transport redox species across the membrane(7). The solvent mediated process, crossover of redox species through PFSA will be presented from a fundamental, interaction-oriented perspective. In-depth understanding of interactions among redox species, solvent and membrane are obtained by combining various spectroscopic measurements with transport measurements. This understanding is crucially necessary to shed light on future membrane design exclusive for non-aqueous flow batteries. Acknowledgement We gratefully acknowledge the support of this work by the U.S. Department of Energy, Office of Electricity Delivery and Energy Reliability (Dr. Imre Gyuk). We also thank 3M for providing membranes. References Darling RM, Gallagher KG, Kowalski JA, Ha S, Brushett FR. Pathways to low-cost electrochemical energy storage: a comparison of aqueous and nonaqueous flow batteries. Energy Environ Sci. 2014;7(11):3459–77.Su L, Darling RM, Gallagher KG, Xie W, Thelen JL, Badel AF, et al. An Investigation of the Ionic Conductivity and Species Crossover of Lithiated Nafion 117 in Nonaqueous Electrolytes. J Electrochem Soc. 2016;163(1):A5253–62.Bamgbopa MO, Almheiri S. Influence of solvents on species crossover and capacity decay in non-aqueous vanadium redox flow batteries: Characterization of acetonitrile and 1, 3 dioxolane solvent mixture. J Power Sources. 2017 Feb 28;342:371–81.Li Y, Sniekers J, Malaquias JC, Van Goethem C, Binnemans K, Fransaer J, et al. Crosslinked anion exchange membranes prepared from poly(phenylene oxide) (PPO) for non-aqueous redox flow batteries. J Power Sources. 2018;378:338–44.Hendriks KH, Robinson SG, Braten MN, Sevov CS, Helms BA, Sigman MS, et al. High-Performance Oligomeric Catholytes for Effective Macromolecular Separation in Nonaqueous Redox Flow Batteries. ACS Cent Sci. 2018;4(2):189–96.Escalante-García IL, Wainright JS, Thompson LT, Savinell RF. Performance of a Non-Aqueous Vanadium Acetylacetonate Prototype Redox Flow Battery: Examination of Separators and Capacity Decay. J Electrochem Soc. 2015;162(3):A363–72.Lou K, Peng J, Tang Z, Zawodzinski TA. Solvation of Perfluorsulfonate Ion Exchange Membrane in Non-Aqueous Solvents. Meet Abstr. 2018;MA2018-01(30):1760–1760.

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