In this work, operando lab-based micro X-ray computed tomography (µ-XCT) was applied, for the first time, to track the liquid water distribution in the MEA throughout the lifetime of a fuel cell. This novel methodology is enabled by the non-invasive and non-destructive nature of lab-based XCT , allowing multiple identical-location scans at different points in time without interfering with the fuel cell operation or the degradation process. The technique is demonstrated by monitoring the changes in the liquid water distribution within the gas diffusion and catalyst layers of a LT-PEFC subjected to a voltage cycling accelerated stress test designed to induce carbon corrosion. Changes in water accumulation within the porous transport layers as a result of carbon support corrosion are correlated to changes in CCL morphology (thickness and crack size) and CCL composition (Pt/ionomer/carbon content). Representative three dimensional tomography datasets, recorded at beginning-of-life, are shown in Figure 1. The imaging results are further supplemented by electrochemical characterization such as polarization curves, electrochemical surface area (ECSA) and electrochemical impedance spectroscopy (EIS). Highlights of the presentation include the impact of catalyst layer collapse and thinning on liquid water retention behavior of the CCL as well as the effect of increased heat generation on GDL water saturation.
Funding for this research was provided by the Natural Sciences and Engineering Research Council of Canada, Canada Foundation for Innovation, British Columbia Knowledge Development Fund, and Ballard Power Systems through an Automotive Partnership Canada grant.
 R. Borup, J. Meyers, B. Pivovar, Y.S. Kim, R. Mukundan, N. Garland, D. Myers, M. Wilson, F. Garzon, D. Wood, P. Zelenay, K. More, K. Stroh, T. Zawodzinski, J. Boncella, J.E. McGrath, M. Inaba, K. Miyatake, M. Hori, K. Ota, Z. Ogumi, S. Miyata, A. Nishikata, Z. Siroma, Y. Uchimoto, K. Yasuda, K.I. Kimijima, N. Iwashita, Chem. Rev.,107, 3904 (2007).
 K. H. Kangasniemi, D. A. Condit, and T. D. Jarvi, J. Electrochem. Soc., 151, E125 (2004).
 R. T. White, M. Najm, M. Dutta, F. P. Orfino, and E. Kjeang, J. Electrochem. Soc., 163 F1206-F1208, (2016).
Figure 1. (a) Operando liquid water distribution (blue) and gas diffusion layer structure (light gray) at the cathode. (b) Water (blue), flow field (light gray) and cathode catalyst layer grayscale values in false color including cracks (dark gray). Both images represent a 3D rendering of the segmented phases in perspective projection at BOL (field of view 2.7x2.9 mm2; 750 mA cm-2; 23°C).