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Download fileCo and Mo Co-doped Fe2O3 for Selective Ethylene Production via Chemical Looping Oxidative Dehydrogenation
journal contribution
posted on 2021-06-04, 15:38 authored by Xin Tian, Chaohe Zheng, Fanxing Li, Haibo ZhaoIn this study, we investigate Co
and/or Mo doped Fe2O3 (CoxMo1–x/Fe2O3, x =
0, 0.2, 0.3, 0.4, and 1) as redox catalysts for chemical looping oxidative
dehydrogenation (CL-ODH) of ethane. Under the cyclic redox reaction
mode, the five as-prepared samples behave differently toward ethane
conversion. Among the five redox catalysts, CoFe2O4 (x = 1) is highly reactive and tends to
overoxidize ethane into CO2, while Mo/Fe2O3 (x = 0) exhibits promising ethylene selectivity
but inferior H2 removal capability. By tuning the molar
ratio of Co/(Co + Mo), 87.4% ethylene selectivity at 56.2% ethane
conversion can be achieved by the Co0.3Mo0.7/Fe2O3 (x = 0.3) redox catalyst
at 825 °C and 6000 h–1. C2H6-TPR results show that the selectivity of Co0.3Mo0.7/Fe2O3 alters as the ODH reaction
proceeds due to the dynamic change of surface properties of the redox
catalyst in the reaction. XPS results indicate that a relatively low
Fe content as well as a high Mo content at the near-surface of the
redox catalyst is beneficial for its ethylene selectivity in CL-ODH
of ethane. DFT calculations reveal that Co cations in the Co0.3Mo0.7/Fe2O3 structure are responsible
for the activity and H2 combustion capability of the redox
catalyst, while Mo plays a key role in tuning the ethylene selectivity.
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Keywords
redox catalystsethylene selectivityXPSCL-ODHcyclic redox reaction modeH 2 combustion capabilityCoFe 2 O 4TPR results showethaneC 2 H 6redox catalystChemical Looping Oxidative Dehydrog...H 2 removal capabilityMo Co-doped Fe 2 O 3Selective Ethylene ProductionCODFTchemical looping oxidative dehydrog...Fe 2 O 3ODH reaction proceeds