Abstract
AbstractA series of alumina supported Pd‐ZnO catalysts were synthesized and studied for methanol steam reforming. Pd loading and Pd/Zn ratio were optimized to improve catalyst activities. Among all the catalysts studied, the catalyst with a Pd loading of 8.9 wt % and a Pd/Zn molar ratio of 0.38 exhibited the highest methanol conversion and the lowest CO selectivity. The significantly improved Pd‐ZnO/Al2O3 catalyst activity was one of the main factors improving the efficiency of a microscale fuel processor from 9 % to 15 %.
References
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Dates
Type | When |
---|---|
Created | 20 years, 4 months ago (March 30, 2005, 6:20 a.m.) |
Deposited | 1 year, 11 months ago (Sept. 10, 2023, 10:20 p.m.) |
Indexed | 2 months, 2 weeks ago (June 10, 2025, 9:14 p.m.) |
Issued | 20 years, 4 months ago (March 30, 2005) |
Published | 20 years, 4 months ago (March 30, 2005) |
Published Online | 20 years, 4 months ago (March 30, 2005) |
Published Print | 20 years, 4 months ago (April 1, 2005) |
@article{Xia_2005, title={Development of Highly Active Pd‐ZnO/Al2O3 Catalysts for Microscale Fuel Processor Applications}, volume={28}, ISSN={1521-4125}, url={http://dx.doi.org/10.1002/ceat.200407174}, DOI={10.1002/ceat.200407174}, number={4}, journal={Chemical Engineering & Technology}, publisher={Wiley}, author={Xia, G. and Holladay, J. D. and Dagle, R A.. and Jones, E. O. and Wang, Y.}, year={2005}, month=mar, pages={515–519} }