2024 AIChE Annual Meeting

(449g) Unsupported Mo2C Catalysts for Low Temperature CO2 Hydrogenation to Methanol

Authors

Ruddy, D., National Renewable Energy Laboratory
Baddour, F., National Renewable Energy Laboratory
To, A., National Renewable Energy Laboratory
Bhan, A., University of Minnesota
CO2 conversion to higher-value products is a key component of technologies aimed at decarbonizing the fuel and chemical industries. The conversion of CO2 to methanol over conventional Cu-based catalysts (473–573 K) is challenged by lower than desired yields, a consequence of the concurrent formation of CO through reverse water gas shift (RWGS) and equilibrium limitations on methanol conversion at these temperatures (X < 8–30%). Achieving higher methanol yields from CO2 hydrogenation requires directing kinetics, and thereby selectivity, towards methanol and operating at low temperatures (< 423 K) where methanol conversion is not significantly equilibrium limited. Herein we report continuous CO2 hydrogenation at low temperatures (373–408 K, H2/CO2 = 0.1–50, 5–35 bar) with high selectivity to methanol (~ 80%) over unsupported Mo2C catalysts.

Methanation and RWGS occur concurrently with methanol synthesis during CO2 hydrogenation over Mo2C. Reaction pathway analysis in conjunction with co-feeding products indicates all products form through primary reaction pathways. Identical dependences of rates on CO2 pressure for methanol synthesis and RWGS rates suggest a common CO2-derived intermediate and shared active site, while methanation occurs through a distinct intermediate. Methanol selectivity increases with increasing hydrogen pressure and decreasing water pressure at fixed conversion, reflecting forward kinetic rates of methanol synthesis that are positive order in hydrogen and negative order in water. Such dependencies are rationalized by kinetically relevant hydrogenation of a CO2-derived intermediate and high surface coverages of H* intermediates. Active site quantification via titration with trifluoroacetic acid at reaction temperatures enables rate normalization without exposing Mo2C samples to ambient conditions. Together, these findings demonstrate the ability of unsupported Mo2C to catalyze CO2 hydrogenation to methanol at low temperatures and provide insight into the reaction network and mechanisms involved in its formation.