posted on 2021-09-17, 10:44authored byYucheng He, Chao Wu
Subsurface
carbon in Pd-based catalysts plays a key role in the
selectivity of hydrogenation reactions. The existing model for subsurface
carbon distribution (uniform Pd6C) in Pd inadequately interprets
the structure of all as-prepared PdCx catalysts.
Additionally, compared with neighboring element boron and nitrogen
forming PdA0.5 (A = B or N) alloys, the carbon concentration
in Pd is fairly low (usually PdC0.13). Utilizing density
functional theory calculations combined with Canonical Monte Carlo
(CMC) simulations, our present work investigates the carbon diffusion
into Pd(111) and Pd(100) and equilibrium distribution of carbon with
various concentrations in Pd(111). A zigzag trajectory of C atom diffusion
into Pd(111) and a spiral trajectory of C atom diffusion into Pd(100)
from the most stable adsorption site of the surface are verified.
Then, CMC simulations suggest a nonuniform distribution of dissolved
C atoms in the Pd(111) slab and provide the equilibrium distribution
configurations of dissolved C atoms at different ratios of C/Pd (0.04,
0.13, and 0.18) and the maximum of C atom coverage (0.33 ML) in odd
number sublayers (Suby, y = 1, 3, 5...). Finally, low carbon concentration and distribution
patterns of dissolved C atoms in Pd(111) are ascribed to strong in-plane
first nearest neighboring (1NN) C–C repulsion and isotropic
character of repulsion in Pd(111). Our results have provided a clear
microscopic description for carbon in Pd-based catalysts and been
instructive for understanding the role of C in hydrogenation reactions.