Journal
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
Volume 58, Issue 45, Pages 20620-20629Publisher
AMER CHEMICAL SOC
DOI: 10.1021/acs.iecr.9b04604
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Funding
- U.S. Department of Energy, Office of Science [58495899]
- H Quest Vanguard, Inc. [DE-SC0017227]
- U.S. Department of Energy (DOE) [DE-SC0017227] Funding Source: U.S. Department of Energy (DOE)
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Ni/alpha-Al2O3 catalyst and a series of bimetallic catalysts including Pd-Ag, Ni-Pd, Ni-Zn, Ni-Ag, and Ni-Ga were synthesized, characterized, and tested in selective hydrogenation of acetylene to ethylene. The bimetallic catalyst Ni-Ga exhibited almost the same ethylene selectivity compared to Pd-Ag based catalyst. The effect of the Ni/Ga ratio on the catalytic activity and selectivity to ethylene in acetylene hydrogenation was evaluated. Characterization by transmission electron microscopy, X-ray diffraction, hydrogen temperature-programmed reduction, and X-ray photoelectron spectroscopy was carried out to identify active phases on Ni-Ga based catalysts, which was correlated with catalytic performance and the reaction mechanism occurring over the catalyst. The presence of Ga in Ni-Ga lattice structure confined the movement of dissociated H* and reduced the adsorption binding energy of ethylene, which could prevent overhydrogenation of acetylene.
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