TY - JOUR
T1 - Reaction Mechanism of Vapor-Phase Formic Acid Decomposition over Platinum Catalysts
T2 - DFT, Reaction Kinetics Experiments, and Microkinetic Modeling
AU - Bhandari, Saurabh
AU - Rangarajan, Srinivas
AU - Maravelias, Christos T.
AU - Dumesic, James A.
AU - Mavrikakis, Manos
N1 - Publisher Copyright:
© 2020 American Chemical Society.
PY - 2020/4/3
Y1 - 2020/4/3
N2 - A combination of periodic density functional theory (DFT, PW91-GGA) calculations, reaction kinetics experiments, and mean-field microkinetic modeling is used to derive insights on the reaction mechanism and determine the nature of the active site under reaction conditions for the vapor-phase decomposition of formic acid (FA, HCOOH) over Pt/C catalysts. Microkinetic models formulated using DFT energetics derived on the clean Pt(100) and Pt(111) required large parameter adjustments to reproduce the experimentally measured apparent activation energies and reaction orders. Further, these models predicted high surface coverage of adsorbed carbon monoxide (CO∗), inconsistent with the environment of the active site in the DFT calculations on the clean surfaces. Consequently, we reperformed DFT calculations for the entire reaction network on partially CO∗-covered (4/9 monolayer, ML) Pt(111) and Pt(100). The resultant microkinetic models, with thermochemistry and kinetics explicitly dependent on CO∗ coverage, were able to reproduce the experimentally determined activation energies and reaction orders, in addition to being self-consistent in CO∗ coverage. Our results suggest that Pt(100) is likely poisoned by CO∗ under typical reaction conditions and does not contribute significantly to the experimentally observed reactivity. Instead, we find that Pt(111) better represents the active site for FA decomposition reaction on Pt/C catalysts. The optimized model on 4/9 ML CO∗-covered Pt(111) suggests that the reaction occurs via the carboxyl (COOH∗) intermediate and that the spectator CO∗-assisted pathways play a significant role under reaction conditions. This study underscores the importance of spectator species on the energetics and the mechanism of a catalytic reaction and their key role in developing a model that better addresses the nature of the active site under realistic catalytic reaction conditions.
AB - A combination of periodic density functional theory (DFT, PW91-GGA) calculations, reaction kinetics experiments, and mean-field microkinetic modeling is used to derive insights on the reaction mechanism and determine the nature of the active site under reaction conditions for the vapor-phase decomposition of formic acid (FA, HCOOH) over Pt/C catalysts. Microkinetic models formulated using DFT energetics derived on the clean Pt(100) and Pt(111) required large parameter adjustments to reproduce the experimentally measured apparent activation energies and reaction orders. Further, these models predicted high surface coverage of adsorbed carbon monoxide (CO∗), inconsistent with the environment of the active site in the DFT calculations on the clean surfaces. Consequently, we reperformed DFT calculations for the entire reaction network on partially CO∗-covered (4/9 monolayer, ML) Pt(111) and Pt(100). The resultant microkinetic models, with thermochemistry and kinetics explicitly dependent on CO∗ coverage, were able to reproduce the experimentally determined activation energies and reaction orders, in addition to being self-consistent in CO∗ coverage. Our results suggest that Pt(100) is likely poisoned by CO∗ under typical reaction conditions and does not contribute significantly to the experimentally observed reactivity. Instead, we find that Pt(111) better represents the active site for FA decomposition reaction on Pt/C catalysts. The optimized model on 4/9 ML CO∗-covered Pt(111) suggests that the reaction occurs via the carboxyl (COOH∗) intermediate and that the spectator CO∗-assisted pathways play a significant role under reaction conditions. This study underscores the importance of spectator species on the energetics and the mechanism of a catalytic reaction and their key role in developing a model that better addresses the nature of the active site under realistic catalytic reaction conditions.
KW - coverage effects
KW - coverage self-consistency
KW - density functional theory
KW - formic acid
KW - microkinetic modeling
KW - platinum catalyst
KW - reaction kinetics experiments
KW - renewable hydrogen production
UR - http://www.scopus.com/inward/record.url?scp=85084063049&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=85084063049&partnerID=8YFLogxK
U2 - 10.1021/acscatal.9b05424
DO - 10.1021/acscatal.9b05424
M3 - Article
AN - SCOPUS:85084063049
SN - 2155-5435
VL - 10
SP - 4112
EP - 4126
JO - ACS Catalysis
JF - ACS Catalysis
IS - 7
ER -