conventional manufacturing. [1] Heterogeneous catalytic reactions, which require operating temperatures ranging from 100 to 1000 °C, pose a central challenge to achieving modular chemical processing in the absence of conventional plant-site utility infrastructure as this class of unit operation accounts for upwards of 80% of all chemical conversion processes. [2] Conventional catalytic reactors rely upon combustion for direct or indirect heating, with the latter requiring additional utility infrastructure for steam generation. [3] In addition to limiting the modularity of the resulting overall process, combustionbased heating of catalytic reactors results in significant greenhouse gas emissions. [4] According to a recent study, the chemical and petrochemical industries currently account for ≈10% of global energy consumption and ≈7% of greenhouse gas emissions. [2b] Lastly, external heating of catalytic packed beds introduces radial heat transport limitations, which can compromise catalyst efficiency, reaction selectivity, and opportunities for scale-up. [5] Direct heating of catalytic processes via application of external electrical fields (termed "power-to-chemicals") represents a transformative approach to overcome these limitations to realize modular, intensified processes operable from a variety of renewable electricity sources. The first published study of an electrically heated catalytic reaction was employed for catalytic converters in internal combustion engines to avoid cold-start emissions of NO x ; the converters were comprised of a thin layer of catalysts electrically heated using vehicle's batteries. [6] Labrecque et al. invented a similar electrically-heated reactor for gas phase reforming, which uses steel wool connected to two electrodes for heat generation from electricity. [7] Rieks et al. reported use of direct heating for dry methane reforming using FeCrAl alloy wash-coated with La-Ni-Ru based catalyst inside the reactor, which achieved a conversion of 29.4%. [8] Wismann et al. designed a laboratory scale reactor from FeCrAl alloy coated with nickel-impregnated wash coat on interior for methane reforming achieving 85% conversion of methane. [9] The direct electrical heating of catalytic surface assisted in minimizing thermal gradients, increasing catalyst utilization, and limiting unwanted byproduct formation. However, direct current approach requires electrical contact with reactor internals and thus is limited by safety and manufacturing issues.