Single-Step Conversion of Ethanol to n-Butene over Ag-ZrO2/SiO2 Catalysts

Journal Article · Fri Sep 18 00:00:00 EDT 2020 · ACS Catalysis

DOI:https://doi.org/10.1021/acscatal.0c02235· OSTI ID:1768016

Dagle, Vanessa ^[1]; Winkelman, Austin D. ^[2]; Jaegers, Nicholas R. ^[1]; Saavedra Lopez, Johnny  ^[1]; Hu, Jian Z.  ^[1]; Engelhard, Mark H.  ^[1]; Habas, Susan ^[3]; Akhade, Sneha A. ^[4]; Kovarik, Libor ^[1]; Glezakou, Vassiliki-Alexandra  ^[1]; Rousseau, Roger J. ^[1]; Wang, Yong ^[5]; Dagle, Robert A.  ^[1]

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1. BATTELLE (PACIFIC NW LAB)
2. WASHINGTON STATE UNIV
3. co-author
4. LAWRENCE LIVERMORE
5. Pacific Northwest National Laboratory

Ethanol is a promising platform molecule for production of a variety of fuels and chemicals. Of particular interest is producing middle distillate fuels (i.e., jet and diesel blendstock) from renewable ethanol feedstock. State-of-the-art alcohol-to-jet technology requires multiple process steps based on catalytic dehydration of ethanol to form ethylene, followed by sometimes a multi-step oligomerization, and then hydrotreatment and distillation. Here we report on a new catalytic route in which ethanol is directly converted to n-butene (1- and 2-butene mixtures) over Ag-ZrO2/SBA-16, thus offering the potential for a reduction in the number of required processing steps versus conventional alcohol-to-jet technology. This catalyst system provides the balanced metal and Lewis acid sites required to selectively facilitate a cascading sequence of reactions that includes dehydrogenation, aldol condensation, Meerwein–Ponndorf–Verley reduction, dehydration, and hydrogenation. High conversion and selectivity toward either n-butene or 1,3-butadiene is achieved by tuning the hydrogen feed partial pressure and other process/catalyst parameters. With sufficient hydrogen partial pressure 1,3-butadiene is completely and selectively hydrogenated to form n-butene. The reaction mechanism was elucidated through operando-nuclear magnetic resonance investigations coupled with reactivity measurements. Combined experimental-computational investigation reveals how changes in silver and zirconium composition and the silver oxidation state affects reactivity under controlled hydrogen partial pressures and after prolonged run times. Finally, catalyst effectiveness also was demonstrated when using wet ethanol feed, thus highlighting process flexibility in terms of feedstock purity requirements. This work was financially supported by the U.S. Department of Energy (DOE), Office of Energy Efficiency and Renewable Energy, Bioenergy Technologies Office, and was performed at the Pacific Northwest National Laboratory (PNNL) under Contract No. DE-AC05-76RL01830 and the National Renewable Energy Laboratory under Contract No. DE-AC36- 08GO28308. Part of the work conducted by S. A. Akhade was performed under the auspices of the U.S. DOE at Lawrence Livermore National Laboratory under Contract No. DE-AC52-07NA27344. This work was partly supported through the PNNL-WSU Distinguished Graduate Research Program for ADW. NMR and XPS experiments were performed using EMSL (grid.436923.9), a DOE Office of Science User Facility sponsored by the Office of Biological and Environmental Research

• Research Organization: Pacific Northwest National Lab. (PNNL), Richland, WA (United States)
• Sponsoring Organization: USDOE
• DOE Contract Number: AC05-76RL01830
• OSTI ID: 1768016
• Report Number(s): PNNL-SA-151691
• Journal Information: ACS Catalysis, Vol. 10, Issue 18
• Country of Publication: United States
• Language: English