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

dc.contributor.authorShirasangi, R.
dc.contributor.authorPrasad Dasari, H.P.
dc.contributor.authorSaidutta, M.B.
dc.date.accessioned2026-02-04T12:24:48Z
dc.date.issued2024
dc.description.abstractHigh-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.
dc.identifier.citationJournal of Solid State Electrochemistry, 2024, 28, 6, pp. 1773-1784
dc.identifier.issn14328488
dc.identifier.urihttps://doi.org/10.1007/s10008-024-05853-2
dc.identifier.urihttps://idr.nitk.ac.in/handle/123456789/21109
dc.publisherSpringer Science and Business Media Deutschland GmbH
dc.subjectCarbon dioxide
dc.subjectCerium oxide
dc.subjectCharge transfer
dc.subjectChemical shift
dc.subjectDiffusion in gases
dc.subjectElectrodes
dc.subjectElectrolysis
dc.subjectElectrolytic cells
dc.subjectNickel oxide
dc.subjectOpen circuit voltage
dc.subjectPolarization
dc.subjectRegenerative fuel cells
dc.subjectRelaxation time
dc.subjectSolid electrolytes
dc.subjectSolid oxide fuel cells (SOFC)
dc.subjectWater gas shift
dc.subjectYttria stabilized zirconia
dc.subjectYttrium oxide
dc.subjectApplied voltages
dc.subjectCo-electrolysis
dc.subjectDistribution of relaxation time
dc.subjectDoped ceria
dc.subjectElectrochemical impedance spectroscopy
dc.subjectElectrochemical-impedance spectroscopies
dc.subjectOpen-circuit voltages
dc.subjectReverse water-gas shift reaction
dc.subjectSolid oxide electrolyse cell
dc.subjectWater-vapor content
dc.titleElectrochemical characterization of electrolyte supported solid oxide electrolysis cell during CO2/H2O co-electrolysis

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