TY - JOUR
T1 - Stable Ce0.8Gd0.2O2-δ oxygen transport membrane reactor for hydrogen production
AU - Liang, Wenyuan
AU - Kaiser, Andreas
AU - Feldhoff, Armin
AU - Baumann, Stefan
AU - Meulenberg, Wilhelm A.
AU - Hu, Tianmiao
AU - Xue, Jian
AU - Jiang, Heqing
AU - Cao, Zhengwen
AU - Caro, Jürgen
N1 - Publisher Copyright:
© 2023 Elsevier B.V.
PY - 2023/1/25
Y1 - 2023/1/25
N2 - Hydrogen production using oxygen transport membrane reactors has attracted widespread attention. However, the structural stability of membrane materials under harsh reducing atmospheres is still a significant challenge. Gadolinium doped cerium oxide (CGO) presents high ionic conductivity and good reducing resistance but is limited by its poor electronic conductivity. Herein, a 2 mol.% cobalt-doped Ce0.8Gd0.2O2-δ (CoCGO) ultrathin membrane was manufactured by thin-film technology and applied to hydrogen production from water splitting (WS) with simultaneous syngas production through partial oxidation of methane (POM). Two catalysts, La0.4Sr0.6CoO3-δ (LSC) and Ni/Al2O3, were utilized for promoting WS and POM, respectively. Hydrogen production rate above 1.8 mL min-1 cm-2 and methane conversion of around 80 % were achieved, and no noticeable degradation was detected during 100 h operation, suggesting its prospective stability advantages as a membrane reactor for hydrogen production from water.
AB - Hydrogen production using oxygen transport membrane reactors has attracted widespread attention. However, the structural stability of membrane materials under harsh reducing atmospheres is still a significant challenge. Gadolinium doped cerium oxide (CGO) presents high ionic conductivity and good reducing resistance but is limited by its poor electronic conductivity. Herein, a 2 mol.% cobalt-doped Ce0.8Gd0.2O2-δ (CoCGO) ultrathin membrane was manufactured by thin-film technology and applied to hydrogen production from water splitting (WS) with simultaneous syngas production through partial oxidation of methane (POM). Two catalysts, La0.4Sr0.6CoO3-δ (LSC) and Ni/Al2O3, were utilized for promoting WS and POM, respectively. Hydrogen production rate above 1.8 mL min-1 cm-2 and methane conversion of around 80 % were achieved, and no noticeable degradation was detected during 100 h operation, suggesting its prospective stability advantages as a membrane reactor for hydrogen production from water.
KW - n/a OA procedure
KW - Oxygen transport membrane
KW - Partial oxidation of methane
KW - Stability
KW - Hydrogen production
UR - http://www.scopus.com/inward/record.url?scp=85149803571&partnerID=8YFLogxK
U2 - 10.1016/j.apcata.2022.118980
DO - 10.1016/j.apcata.2022.118980
M3 - Article
AN - SCOPUS:85149803571
SN - 0926-860X
VL - 650
JO - Applied catalysis A: general
JF - Applied catalysis A: general
M1 - 118980
ER -