Coking and Sintering Resistance of ALD Catalyst for Dry Reforming of Methane
Natural Gas Utilization Workshop
2018
2nd Natural Gas Utilization Workshop
General Submissions
Advances in catalyst/process chemistries for natural gas conversion
In this work, the objective is to investigate the effect of ALD on the performance of a commercial 20% Ni/Al2O3 catalyst in dry reforming conditions. Using TMA as precursor, various cycles of alumina are overcoated on the commercial catalyst. This catalyst is tested against the uncoated catalyst at different temperatures. Apart from stability testing, the crystallite size of the nickel nanoparticles is determined after definite time periods. The crystallite size is calculated from the dispersion which is obtained from H2 chemisorption. The ALD coating on the nickel active material is purported to prevent sintering by anchoring the nickel nanoparticles. The amount of coke deposited after each run is also estimated by a Temperature-Programmed-Oxidation (TPO) done at the end of each run. At lower temperatures (~600 °C), coking is supposed to be the dominant deactivation mechanism and at higher temperatures (~800 °C), it is sintering. By studying both these phenomena at different temperatures for ALD with different number of cycles, this work will help better understand the role of the overcoat in the performance of ALD catalysts, and help identify the operating conditions where ALD catalysts have a positive effect on catalytic performance.
REFERENCES
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