TY - JOUR
T1 - Surface structure sensitivity of hydrodeoxygenation of biomass-derived organic acids over palladium catalysts
T2 - a microkinetic modeling approach
AU - Kundu, Subrata Kumar
AU - Vijay Solomon, Rajadurai
AU - Yang, Wenqiang
AU - Walker, Eric
AU - Mamun, Osman
AU - Bond, Jesse Q.
AU - Heyden, Andreas
N1 - Funding Information:
The National Science Foundation funded this work under Grant No. DMREF-1534260 (most gas-phase calculations and models) and OIA-1632824 (most liquid phase calculations). This work was also partially supported by the South Carolina State Center for Strategic Approaches to the Generation of Electricity (SAGE). Computing resources have been provided by the National Energy Research Scientific Computing Center (NERSC) supported by the Office of Science of the U.S. Department of Energy, Extreme Science and Engineering Discovery Environment (XSEDE) by the Texas Advanced Computing Center (TACC) at the University of Texas at Austin (Grant no. TG-CTS090100), the Environmental Molecular Sciences Laboratory (EMSL) under the Pacific Northwest National Laboratory (PNNL) via the CASCADE clusters, and the University of South Carolina's High Performance Computing (HPC) group.
Publisher Copyright:
© The Royal Society of Chemistry 2021.
PY - 2021/9/21
Y1 - 2021/9/21
N2 - Microkinetic models based on parameters obtained from density functional theory and transition state theory have been developed for the hydrodeoxygenation (HDO) of propanoic acid, a model lignocellulosic biomass-derived organic acid, over the flat Pd(100) and Pd(111) surfaces in both vapor and liquid phase reaction conditions. The more open Pd(100) surface was found to be 3-7 orders of magnitude more active than the Pd(111) surface in all reaction environments, indicating that the (111) surface is not catalytically active for the HDO of propanoic acid. Over Pd(100) and in vapor phase, liquid water, and liquid 1,4-dioxane, propanoic acid hydrodeoxygenation follows a decarbonylation (DCN) mechanism that is facilitated by initial α- and β-carbon dehydrogenation steps, prior to the rate controlling C-OH and (partially rate controlling) C-CO bond dissociations. Only over Pd(111) and aqueous reaction environments is the decarboxylation (DCX) preferred over the DCN with the C-CO2step being rate controlling.
AB - Microkinetic models based on parameters obtained from density functional theory and transition state theory have been developed for the hydrodeoxygenation (HDO) of propanoic acid, a model lignocellulosic biomass-derived organic acid, over the flat Pd(100) and Pd(111) surfaces in both vapor and liquid phase reaction conditions. The more open Pd(100) surface was found to be 3-7 orders of magnitude more active than the Pd(111) surface in all reaction environments, indicating that the (111) surface is not catalytically active for the HDO of propanoic acid. Over Pd(100) and in vapor phase, liquid water, and liquid 1,4-dioxane, propanoic acid hydrodeoxygenation follows a decarbonylation (DCN) mechanism that is facilitated by initial α- and β-carbon dehydrogenation steps, prior to the rate controlling C-OH and (partially rate controlling) C-CO bond dissociations. Only over Pd(111) and aqueous reaction environments is the decarboxylation (DCX) preferred over the DCN with the C-CO2step being rate controlling.
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U2 - 10.1039/d1cy01029h
DO - 10.1039/d1cy01029h
M3 - Article
AN - SCOPUS:85115723378
SN - 2044-4753
VL - 11
SP - 6163
EP - 6181
JO - Catalysis Science and Technology
JF - Catalysis Science and Technology
IS - 18
ER -