(715e) A Combined Theoretical and Kinetic Assessment of C–O Bond Rupture Pathways within 2-Methyltetrahydrofuran over Nickel Phosphide Catalyst
AIChE Annual Meeting
2017
2017 Annual Meeting
Catalysis and Reaction Engineering Division
Fundamentals of Supported Catalysis II: Oxygenate Reactions
Thursday, November 2, 2017 - 1:50pm to 2:10pm
The
conversion of oxygenates in biomass-derived feedstocks into more valuable fuels
and chemicals requires selective CO bond cleavage while leaving other CO and
CC bonds intact. Previous studies have shown that metal phosphides (MPs) are
promising catalysts for selective CO, CS, and CN bond rupture over CC bonds
[1]. MPs also exhibit remarkably higher selectivity towards breaking sterically-hindered
CO (3CO) bonds compared to pure transition metals. Our
measurements indicate that Ni2P cleaves 3CO bonds at a
rate three times faster than 2CO bond cleavage, and has 50 times
higher selectivity for 3CO bond cleavage than pure Ni. The specific
mechanism behind CO bond cleavage on NixPy,
as well as the identity of the reactive intermediate and
active site, are not fully understood despite recent studies. Here, we combine
kinetic studies and density functional theory (DFT) calculations to investigate
the mechanisms of hindered and unhindered CO bond cleavage in 2-methyltetrahydrofuran
(2-MTHF) on NixPy
and Ni surfaces.
Previous
studies showed that CC and CO hydrogenolysis in
alkanes and alkanols occur via unsaturated species formed by sequential quasi-equilibrated
dehydrogenation steps [2,3]; the removal of H atoms
weakens the CC and CO bonds by replacing CH bonds with Cmetal bonds. The
measured ratio of products to reactants pressures during the dehydrogenation of
2-methyltetrahydrofuran (2-MTHF) to 2-methylfuran (2-MF) was constant at low
conversions (< 1%), suggesting that CH activation steps are
quasi-equilibrated and leaving the CO bond rupture as the kinetically relevant
step. The measured ratio of 3CO to 2CO bond cleavage
rates (χ) has a half order dependence on hydrogen pressure [H2]1/2,
indicating that the reactive intermediate for 2CO bond rupture must
lose an additional hydrogen atom compared with the reactive intermediate for 3CO
bond rupture; the identity of those intermediates that undergo CO bond
cleavage can be assessed using DFT calculations.
Periodic
plane-wave DFT calculations were performed using the Vienna ab initio Simulation package (VASP) with
the RPBE exchange correlation functional and PAW potentials. The (001) and
(111) surfaces were chosen to model NixPy
and Ni catalysts, respectively, because they exhibit the lowest surface
formation energies. Vibrational frequency calculations were performed to estimate
enthalpies and free energies of each state at temperatures relevant to the
catalytic reactions. Results show that the effective enthalpy barrier (ΔH҂)
for 3CO bond rupture is 34 kJ mol−1 lower than for
2CO on Ni2P(001) and 21 kJ mol−1
on Ni12P5(001) at 543 K. These DFT-derived enthalpy
barriers are consistent with the measured values on 12 nm Ni2P (23 ±
9 kJ mol−1) and on 19 nm Ni12P5 (25 ± 5
kJ mol−1). 2CO bond rupture on Ni(111),
however, is more favorable by 73 kJ mol−1. Although CO bonds
activations through partially dehydrogenated intermediates (i.e. 2CH2O,
2CHO, and 3CHO) have lower enthalpy barriers, the
removal of H atoms from the carbon atom vicinal to the CO bond being broken
results in an increase in entropy, rendering ΔG҂ barrier the
lowest for the fully dehydrogenated CO bond. The contribution of each transition
states to the measured hydrogenolysis rate depends on
their ΔG҂ values, and thus partially dehydrogenated
intermediates are unlikely to contribute to the measured rate. These findings
confirm the essential role of entropy in addition to enthalpy in determining the
rate constants. DFT-predicted ratio of 3CO to 2CO bond cleavage
rates χ is equal to 2.7 on Ni2P(001) and 0.53 on Ni12P5(001)
at 543 K and 1 MPa H2, in agreement with the measured values (~3 on
12 nm Ni2P and ~0.4 on 19 nm Ni12P5) at low
conversions.
References
[1]
Oyama,
S.; Wang, X.; Lee, Y.; Chun, W., Active phase of Ni2P/SiO2 in hydroprocessing reactions. J. Catal.
2004, 221.2, 263−273.
[2]
Flaherty, D.; Hibbitts, D.; Iglesia, E., Theoretical
and kinetic assessment of the mechanism of ethane hydrogenolysis
on metal surfaces saturated with chemisorbed hydrogen. J. Am. Chem. Soc. 2014,
136, 9664.
[3]
Gürbüz,
E.; Hibbitts, D.; Iglesia,
E., Kinetic and Mechanistic Assessment of Alkanol/Alkanal
Decarbonylation and Deoxygenation Pathways on Metal
Catalysts. J. Am. Chem. Soc. 2015, 137(37), 11984−11995.