Abstract
A thin-sheet Ni-CeAlO3-Al2O3/FeCrAl-fiber to be used in the COMR process was fabricated by thermally decomposing the catalyst precursor of NiAl-LDHs/FeCrAl-fiber to form the NiO-Al2O3/FeCrAl-fiber, followed by CeO2-modification and H2-reduction. Pre-mounting a γ-Al2O3 layer onto the FeCrAl-fiber is particularly critical for the hydrothermal growth of LDHs along with the fiber surface. The most promising catalyst, with 5 wt% Al2O3, 5 wt% Ni, and 2 wt% CeO2, exhibits high activity, high selectivity, and particularly prolonged stability. At a gas hourly space velocity of 100 L g−1 h−1 and 700 °C, CH4 conversion and H2/CO selectivity can be stably maintained at ~86% and ~96.1/~91.5% for a feed gas with CH4/O2 molar ratio of 2.0/1.0 during 350 h test, in nature, due to the enhanced Ni-sintering and improved carbon resistance. The existence of “CeAlO3-CeO2” cycle enables the catalyst with high carbon resistance because of the intensified C-elimination to inhibit filaments growth.
| Original language | English |
|---|---|
| Article number | 116102 |
| Journal | Fuel |
| Volume | 258 |
| DOIs | |
| State | Published - 15 Dec 2019 |
Keywords
- Carbon resistance
- Catalytic oxy-methane reforming
- Layered double hydroxides
- Ni-based catalysts
- Structured catalysts
- Synthesis gas
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