Efforts to elucidate the conductivity behavior of AEMs have been mostly experimental, but some theoretical models have also been developed using various approximations [5, 10-13]. Some past models assume chemical equilibrium among ionic species, however in an operating AEM this may not be the case. Furthermore, most of the theoretical models describe the behavior of isolated AEMs, that is, in the absence of polarization and electrochemical reactions that supply and consume ions and influences the ion exchange process. This work will incorporate these effects in order to predict the conductivity of an operating AEM in the presence of CO2 and under various operational current densities and temperatures. The model itself is a direct extension of [7], in that it adapts the same reaction mechanism for CO2 conversion to carbonate/bicarbonate ions in the AEM. Additional fundamental insight into the self-purging mechanism and potential scenarios for the recovery of membrane conductivity will be discussed.
Acknowledgements
Financial support from the Army Research Office (award number W911NF-14-1-0298) is gratefully acknowledged.
References
[1] G. Merle, M. Wessling, and K. Nijmeijer, “Anion exchange membranes for alkaline fuel cells: A review,” J. Memb. Sci., vol. 377, no. 1–2, pp. 1–35, 2011.
[2] J. R. Varcoe and R. C. T. Slade, “Prospects for alkaline anion-exchange membranes in low temperature fuel cells,” Fuel Cells, vol. 5, no. 2, pp. 187–200, 2005.
[3] M. A. Hickner, A. M. Herring, and E. B. Coughlin, “Anion exchange membranes: Current status and moving forward,” J. Polym. Sci. Part B Polym. Phys., vol. 51, no. 24, pp. 1727–1735, 2013.
[4] W. A. Rigdon et al., “Carbonate dynamics and opportunities with low temperature, AEM-based electrochemical CO2 separators,” J. Electrochem. Energy Convers. Storage, no. c, pp. 1–29, 2016.
[5] M. Eisaman et al., “Energy-efficient electrochemical CO2 capture from the atmosphere,” Tech. Proc. 2009 Clean Technol. Conf. Trade Show, pp. 5–8, 2009.
[6] S. Suzuki, H. Muroyama, T. Matsui, and K. Eguchi, “Influence of CO2 dissolution into anion exchange membrane on fuel cell performance,” Electrochim. Acta, vol. 88, pp. 552–558, 2013.
[7] T. D. Myles, K. N. Grew, A. A. Peracchio, and W. K. S. Chiu, “Transient ion exchange of anion exchange membranes exposed to carbon dioxide,” J. Power Sources, vol. 296, pp. 225–236, 2015.
[8] K. N. Grew, X. Ren, and D. Chu, “Effects of temperature and carbon dioxide on anion exchange membrane conductivity,” Electrochem. Solid-State Lett., vol. 14, no. 12, pp. B127–B131, 2011.
[9] M. I. Matsui Yu, Morihiro Saito, Akimasa Tasaka, “Influence of Carbon Dioxide on the Performance of Anion-Exchange Membrane Fuel Cells,” ECS Trans., vol. 25, no. 13, pp. 105–110, 2010.
[10] Z. Siroma, S. Watanabe, K. Yasuda, K. Fukuta, and H. Yanagi, “Mathematical Modeling of the Concentration Profile of Carbonate Ions in an Anion Exchange Membrane Fuel Cell,” J. Electrochem. Soc., vol. 158, no. 6, pp. B682–B689, 2011.
[11] K. N. Grew and W. K. S. Chiu, “A Dusty Fluid Model for Predicting Hydroxyl Anion Conductivity in Alkaline Anion Exchange Membranes,” J. Electrochem. Soc., vol. 157, pp. B327-B337, 2010.
[12] M. B. DeGostin, A. A. Peracchio, T. D. Myles, B. N. Cassenti, and W. K. S. Chiu, “Charge transport in the electrospun nanofiber composite membrane’s three-dimensional fibrous structure,” J. Power Sources, vol. 307, pp. 538–551, 2016.
[13] V. Nikonenko, K. Lebedev, J. A. Manzanares, and G. Pourcelly, “Modelling the transport of carbonic acid anions through anion-exchange membranes,” Electrochim. Acta, vol. 48, no. 24, pp. 3639–3650, 2003.