Electrochemical characterization of electrolyte supported solid oxide electrolysis cell during CO2/H2O co-electrolysis

No Thumbnail Available

Date

2024

Journal Title

Journal ISSN

Volume Title

Publisher

Springer Science and Business Media Deutschland GmbH

Abstract

High-temperature co-electrolysis is studied on electrolyte-supported NiO-YSZ/NiO-SDC/ScSZ/LSCF-GDC/LSCF (NiO: Nickel Oxide, YSZ: Yttria-stabilized zirconia, SDC: Samarium-doped ceria, ScSZ: Scandia-stabilized zirconia, LSCF: Lanthanum Strontium Cobalt Ferrite, GDC: Gadolinium-doped ceria) button cell. Electrochemical impedance spectroscopy (EIS) was recorded under open-circuit voltage (OCV) and co-electrolysis mode over various operating conditions, including temperature, water vapor content, and applied voltage. Interfacial polarization resistance (R<inf>p</inf>) is obtained from peak arcs located in the three regions: gas conversion resistance (Region I (0.01 to 0.1 Hz)), gas diffusion resistance (Region II (0.1 to 100 Hz)) and air electrode charge transfer resistance (Region III (100 to 10,000 Hz)). As the temperature increased from 700 to 850 oC, R<inf>p</inf> decreased from 18.15 to 3.32 Ω.cm2 at 1.3 V for 10%CO<inf>2</inf>/3%H<inf>2</inf>O. From the Distribution of relaxation times (DRT) studies, one additional peak, P<inf>5</inf> (fuel gas conversion or gas-phase diffusion in the pores of the air electrode), is observed, and Region III (100 to 10,000 Hz) consists of two additional peaks: P<inf>1</inf> (ionic transport coupled with gas diffusion close to triple phase boundaries (TPBs)) and P<inf>2</inf> (fuel electrode charge transfer reaction), which were not clearly distinguished from EIS. Region II dominates in the overall polarization resistance. At 800 oC, for 10%CO<inf>2</inf>/3%H<inf>2</inf>O, the R<inf>p</inf> decreased from 6.78 to 4.82 Ω.cm2, with an increase in the applied voltage from 1.3 to 1.5 V. At 800oC/1.5 V, the R<inf>p</inf> values are 4.41, 8.09, and 6.77 Ω.cm2 for H<inf>2</inf>O, CO<inf>2</inf>, and co-electrolysis. At 800 ºC/1.5 V, with an increase in the water vapor content from 3%H<inf>2</inf>O to 15%H<inf>2</inf>O, there is not much change in the R<inf>p</inf> value; therefore, 10%H<inf>2</inf>O is sufficient. H<inf>2</inf> consumption is between 23 and 36%, depending on the temperature at OCV. At 800 °C for (10%H<inf>2</inf>/10%CO<inf>2</inf>/10%H<inf>2</inf>O), co-electrolysis occurs at applied voltage, along with Reverse water gas shift (RWGS) reaction. Graphical Abstract: (Figure presented.) © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2024.

Description

Keywords

Carbon dioxide, Cerium oxide, Charge transfer, Chemical shift, Diffusion in gases, Electrodes, Electrolysis, Electrolytic cells, Nickel oxide, Open circuit voltage, Polarization, Regenerative fuel cells, Relaxation time, Solid electrolytes, Solid oxide fuel cells (SOFC), Water gas shift, Yttria stabilized zirconia, Yttrium oxide, Applied voltages, Co-electrolysis, Distribution of relaxation time, Doped ceria, Electrochemical impedance spectroscopy, Electrochemical-impedance spectroscopies, Open-circuit voltages, Reverse water-gas shift reaction, Solid oxide electrolyse cell, Water-vapor content

Citation

Journal of Solid State Electrochemistry, 2024, 28, 6, pp. 1773-1784

Collections

Endorsement

Review

Supplemented By

Referenced By