% IMPORTANT: The following is UTF-8 encoded. This means that in the presence
% of non-ASCII characters, it will not work with BibTeX 0.99 or older.
% Instead, you should use an up-to-date BibTeX implementation like “bibtex8” or
% “biber”.
@INPROCEEDINGS{Thankappakurup:1054009,
author = {Thankappakurup, Saranya and Vibhu, Vaibhav and Wolf,
Stephanie and Frömling, Till and Eichel, Rüdiger-A.},
title = {{E}lectrochemical impedance analysis and degradation
behavior of a commercial {N}i-{YSZ}/{YSZ}/{GDC}/{LSC} single
cell in direct {CO}2 electrolysis},
reportid = {FZJ-2026-01663},
year = {2025},
abstract = {This study investigated the performance and electrochemical
behavior of a commercial Ni-YSZ/YSZ/GDC/LSC single cell
using AC- and DC- techniques under high temperature CO2
electrolysis conditions. The effects of the operating
temperature, CO2 content in the fuel gas, and the oxygen
partial pressure on the oxygen electrode side were
evaluated. The maximum current density observed was 1.36
A‧cm-2 at 1.5 V and 900 °C. Furthermore, the maximum
current densities of -1.2, -0.99, and -0.77 A·cm-2 were
observed at 850, 800, and 750 °C, respectively, at 1.5 V
under a fuel gas composition of $80\%$ CO2 and $20\%$ CO.
The corresponding observed Area Specific Resistance (ASR)
values are 0.29, 0.33, 0.38, and 0.49 Ω·cm2 at 900, 850,
800, 800, and 750 °C, respectively. A direct correlation
was observed between temperature and ASR values: as the
temperature increases, the current density increases, while
the ASR values decrease. Furthermore, to analyze the ohmic
resistance (RΩ), polarization resistance (Rp), and
electrode processes, electrochemical impedance spectroscopy
(EIS) was used. The recorded impedance spectrum was analyzed
using the Distribution of Relaxation Times (DRT) method and
an equivalent circuit model (ECM). The ECM consisting of
four-time constants (LR–RC1–RC2–RQ–Ws) gives the
best fit of the impedance data compared to other models. The
activation energies for RΩ and Rp were calculated from the
slopes of the Arrhenius plots. The obtained activation
energies were 44 ± 8 kJ mol⁻¹ and 32 ± 3 kJ mol⁻¹
for RΩ and Rp, respectively. The electrode processes were
then compared with the literature and found that the
low-frequency Warburg short element (Ws) was attributed to
gas diffusion at the fuel electrode, while the mid-frequency
processes (R₃ and R₄) were associated with the combined
contributions of the fuel and oxygen electrodes. Activation
energies for the resistances R1, R2, R3, R4 and Ws were
calculated using the Arrhenius plot.Finally, the short-term
stability tests were conducted at 700, 750, and 800 °C for
over 650 hours under a constant current load of -0.5
A‧cm⁻² under $80\%$ CO2 and $20\%$ CO gas composition.
The degradation rates of 38, 36, and 34 mV‧kh-1 were found
at 700, 750, and 800 °C, respectively. These are lower than
the values reported in the literature under CO2 electrolysis
conditions},
month = {Jul},
date = {2025-07-13},
organization = {19th International Symposium on Solid
Oxide Fuel Cells (SOFC-XIX), Stockholm
(Sweden), 13 Jul 2025 - 18 Jul 2025},
subtyp = {After Call},
cin = {IET-1},
cid = {I:(DE-Juel1)IET-1-20110218},
pnm = {1232 - Power-based Fuels and Chemicals (POF4-123)},
pid = {G:(DE-HGF)POF4-1232},
typ = {PUB:(DE-HGF)6},
url = {https://juser.fz-juelich.de/record/1054009},
}