Local ionic transport enables selective PGM-free bipolar membrane electrode assembly
Mengran Li (TU Delft - ChemE/Materials for Energy Conversion and Storage, University of Melbourne)
Eric W. Lees (University of British Columbia, Lawrence Berkeley National Laboratory)
Wen Ju (Technical University of Berlin, Leibniz Institute for Catalysis)
Siddhartha Subramanian (TU Delft - ChemE/Materials for Energy Conversion and Storage)
K. Yang (TU Delft - ChemE/Materials for Energy Conversion and Storage)
Hugo Pieter Iglesias van Montfort (TU Delft - ChemE/Materials for Energy Conversion and Storage)
Maryam Abdinejad (TU Delft - ChemE/Materials for Energy Conversion and Storage, Massachusetts Institute of Technology)
Joost Middelkoop (TU Delft - ChemE/O&O groep)
Thomas Burdyny (TU Delft - ChemE/Materials for Energy Conversion and Storage)
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Abstract
Bipolar membranes in electrochemical CO2 conversion cells enable different reaction environments in the CO2-reduction and O2-evolution compartments. Under ideal conditions, water-splitting in the bipolar membrane allows for platinum-group-metal-free anode materials and high CO2 utilizations. In practice, however, even minor unwanted ion crossover limits stability to short time periods. Here we report the vital role of managing ionic species to improve CO2 conversion efficiency while preventing acidification of the anodic compartment. Through transport modelling, we identify that an anion-exchange ionomer in the catalyst layer improves local bicarbonate availability and increasing the proton transference number in the bipolar membranes increases CO2 regeneration and limits K+ concentration in the cathode region. Through experiments, we show that a uniform local distribution of bicarbonate ions increases the accessibility of reverted CO2 to the catalyst surface, improving Faradaic efficiency and limiting current densities by twofold. Using these insights, we demonstrate a fully platinum-group-metal-free bipolar membrane electrode assembly CO2 conversion system exhibiting <1% CO2/cation crossover rates and 80-90% CO2-to-CO utilization efficiency over 150 h operation at 100 mA cm−2 without anolyte replenishment.