4.6 Article

Understanding the Deactivation of Ag-ZrO2/SiO2 Catalysts for the Single-step Conversion of Ethanol to Butenes

Journal

CHEMCATCHEM
Volume 13, Issue 3, Pages 999-1008

Publisher

WILEY-V C H VERLAG GMBH
DOI: 10.1002/cctc.202001488

Keywords

ethanol; butene; butadiene; Ag-ZrO2/SiO2; deactivation

Funding

  1. U.S. Department of Energy (DOE), Office of Energy Efficiency and Renewable Energy (EERE), Bioenergy Technologies Office (BETO)
  2. PNNL-WSU Distinguished Graduate Research Program
  3. DOE Office of Biological and Environmental Research

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Ag-ZrO2/SBA-16 has been found to efficiently catalyze the conversion of ethanol to butene, but it deactivates over time due to coke deposition, Ag particle sintering, and Ag oxidation state change.
Ag-ZrO2/SBA-16 has recently been found to be efficient for catalyzing the single-step conversion of ethanol to butene (1- and 2-butene mixtures) in the presence of H-2. The reaction proceeds via a cascading sequence of reactions over mixed metal and Lewis sites, with the catalyst composition tuned to selectively favor butene formation. However, the catalyst slowly deactivates when evaluated over long reaction times. In this work, we evaluated the lifetime of the Ag-ZrO2/SBA-16 catalyst system for ethanol-to-butene conversion at 325 degrees C for up to 800 hours on stream. Several characterization techniques were used to elucidate the mechanism(s) by which catalyst deactivation occurs. Coke deposition, Ag particle sintering, and Ag-0-to-Ag+ oxidation state change were identified to be the major causes of catalyst deactivation. Coke deposits cover primarily Lewis acid sites which are responsible for aldol condensation, Meerwein-Ponndorf-Verley (MPV) reduction, and dehydration reactions. Ag particle sintering and Ag oxidation state change leads to a reduction in the number of metallic Ag sites responsible for the dehydrogenation/hydrogenation steps. The fresh catalyst likely experiences hydrothermal sintering in the early stage of reaction and permanently loses some active Lewis acid sites before reaching a new structural steady state. The deactivation of Lewis acid sites leads to a decrease in overall ethanol conversion, whereas the deactivation of the metallic Ag sites decreases the butene selectivity. For catalyst regeneration, oxidative calcination (at 500 degrees C) followed by reduction (at 325 degrees C) successfully removes all the coke species on the catalyst surface and restores the metallic Ag particles of the 4Ag-4ZrO(2)/SBA-16 catalysts.

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