Direct electrocatalytic CO2 reduction in a pressurized tubular protonic membrane reactor

Handle

https://riunet.upv.es/handle/10251/200989

Cita bibliográfica

Quina-García, I.; Almar-Liante, L.; Catalán-Martínez, D.; Dayaghi, AM.; Martinez Feliu, A.; Norby, T.; Escolástico Rozalén, S.... (2023). Direct electrocatalytic CO2 reduction in a pressurized tubular protonic membrane reactor. Chem Catalysis (Online). 3(10):1-17. https://doi.org/10.1016/j.checat.2023.100766

Titulación

Resumen

[EN] Power-to-methane technology enables storage of renewable elec-tricity in chemical energy, which can be transported and converted us-ing existing infrastructure. The moderate energy efficiency of this pro-cess is associated with high reactor exothermicity and complex thermal integration. Proton-ceramic electrochemical cells (PCECs) enable ther-mal combination of methanation and electrochemically driven H2 steps via endothermic reactions, boosting energy efficiency and heat man-agement. Here, we report single-step methane production from CO2 in a tubular PCEC at 450 degrees C and less than 30 bar. The H2 reactant is sup-plied by electrochemical pumping of protons from H2 in the external chamber. The electrochemical cell consists of an -25-mm-thick electro-lyte (BaZr0.8Ce0.1Y0.1O3-8) supported on a BaZr0.8Ce0.1Y0.1O3-8/Ni com-posite acting as a methanation catalyst. The reaction was studied as a function of total pressure, H2/CO2 ratio, and current density, reaching CH4 yields greater than 99% above 20 bar. High pressure and a CO2- rich atmosphere ameliorated the electrochemical behavior because of higher electrolyte hydration and boosted electrode kinetics.

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Fuente

Chem Catalysis (Online)

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