4.8 Article

Catalytic Conversion Furfuryl Alcohol to Tetrahydrofurfuryl Alcohol and 2-Methylfuran at Terrace, Step, and Corner Sites on Ni

Journal

ACS CATALYSIS
Volume 10, Issue 13, Pages 7240-7249

Publisher

AMER CHEMICAL SOC
DOI: 10.1021/acscatal.0c01441

Keywords

barrier heights; biomass; catalysis; furfural; hydrodeoxygenation; hydrogenation; microkinetic modeling; selectivity

Funding

  1. National Natural Science Foundation of China [NSFC: 91741104, 21871021, 21521005]
  2. National Key Research and Development Program of China [2017YFA0206804]
  3. National Science Foundation [CHE14645360]
  4. Inorganometallic Catalysis Design Center, an Energy Frontier Research Center - U.S. Department of Energy, Office of Science, Basic Energy Sciences [DE-SC0012702]
  5. [buctylkxj01]
  6. [XK1802-6]
  7. [12060093063]

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The surface structures at catalytic sites are critical factors for determining catalytic selectivity. Here, we use periodic density functional theory and microkinetic modeling to systematically investigate the effect of surface structures on the conversion of furfuryl alcohol (FA). We consider nine surface terminations of Ni with various coordination numbers representing terrace, step, and corner sites. We study three reaction paths for FA conversion on various surfaces and find that the surface structure impacts the adsorption configuration and causes significant differences in selectivity. Barrier height analysis shows that terrace sites favor hydrogenation to tetrahydrofurfuryl alcohol (THFA), whereas corner sites favor C-OH bond scission to produce 2-methylfuran (2-MF); step sites show similar barriers for the two reactions. We explain this by identifying three characteristics of the reactant adsorption structures that have a significant effect on selectivity, namely, that a shorter distance between the adsorbed hydrogen atom and the C3 carbon of FA favors hydrogenation to produce THFA, and more negative charge transfer to O-al(co)hol and a longer C-O-al(co)hol bond length favor C-O-al(co)hol bond scission to produce 2-MF. Since the reactions have similar barriers at a step site, microkinetic calculations are employed to calculate the product selectivity on a step site under experimental conditions. At lower temperatures and hiller generalized coordination number ((CN) over bar), THFA is the most favorable product, while the selectivity to 2-MF is higher at lower (CN) over bar and at higher temperature. This work provides guidance for the rational design catalysts to control the product distribution of FA conversion.

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