Hydrocarbon production by CO2 electro-catalytic reduction in a pressurized protonic electrochemical membrane reactor
Imanol Quina a, Laura Almar a, David Catalán-Martínez a, Andrea Dos Santos a, Amir Masoud Dayaghi b, Truls Norby b, Agustín Martínez a, Jose Manuel Serra a, Sonia Escolástico a
a Instituto de Tecnología Química (Universitat Politècnica de València—Consejo Superior de Investigaciones Científicas), Valencia, Spain
b Department of Chemistry, Centre for Materials Science and Nanotechnology, University of Oslo, Gaustadalléen 21, NO-0349 Oslo, Norway
Proceedings of 24th International Conference on Solid State Ionics (SSI24)
London, United Kingdom, 2024 July 14th - 19th
Organizers: John Kilner and Stephen Skinner
Oral, Sonia Escolástico, presentation 498
Publication date: 10th April 2024

Electrochemical membrane reactors offer the opportunity to increase the yield of relevant chemical reactions such as the production of synthetic liquid fuels as well as to improve their energy efficiency by coupling exothermic and endothermic processes.

This work, developed in the frame of the EU Horizon 2020 “eCOCO2” project, presents the CO2 electro-catalytic reduction into methane by using tubular protonic membrane reactors. Two different modes of operation were employed to provide the needed H2 for the methanation reaction: H2 pumping and electrolysis. In both operation modes, the protonic membrane was composed of BaZr0.8Ce0.1Y0.1O3 as electrolyte and the cermet Ni+BaZr0.7Ce0.2Y0.1O3 as inner metallic electrode acting as support and as methanation catalyst. In the case of the H2 pumping, the outer electrode was made of Ni+BaZr0.7Ce0.2Y0.1O3 whereas for the electrolysis, an electrode made of PrBa0.5Sr0.5Co1.5Fe0.5O5+δ (PBSCF) was used.

Transport properties of the electrochemical cells were evaluated by impedance spectroscopy, i-V curves and H2 production as a function of the applied current density and the operational conditions, from 600 ºC to 450 ºC and pressures up to 30 bar. Then, methanation reaction performance was also evaluated as a function of the operational parameters, analyzing the CO2 conversion and CO and CH4 yields.

In both operational modes, it was observed that the total system pressure plays a key role in both the electrochemical and catalytic performances of the protonic cells. The improvement in the performance at high pressure is due to two effects occurring simultaneously as it was inferred from DRT analysis: (i) an increased hydration of the electrolyte which enhances the proton conductivity and (ii) the improvement of the surface kinetics and mass transfer of the electrodes. Regarding catalytic performance, CO2 conversion and CH4 selectivity increase significantly with pressure, reaching values of 86% and 94% respectively, for a stoichiometric H2/CO2 ratio of 4 at 450 °C and 30 bar.

In addition, computational fluid dynamics (CFD) simulations were conducted to gain critical insights into the reaction kinetics, transport phenomena, and electrochemical performance of the membrane reactor.

This study has received European Union’s Horizon 2020 Research and Innovation funding under grant agreement No 838077. CoorsTek Membrane Sciences is gratefully acknowledged for their assistance in the manufacture of tubular cells.

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