TY - JOUR
T1 - Mechanisms and Active Sites for C-O Bond Rupture within 2-Methyltetrahydrofuran over Ni, Ni12P5, and Ni2P Catalysts
AU - Witzke, Megan E.
AU - Almithn, Abdulrahman
AU - Conrad, Christian L.
AU - Hibbitts, David D.
AU - Flaherty, David W.
N1 - Publisher Copyright:
© Copyright 2018 American Chemical Society.
PY - 2018/8/3
Y1 - 2018/8/3
N2 - Nickel phosphide catalysts (Ni12P5 and Ni2P) preferentially cleave sterically hindered 3C-O bonds over unhindered 2C-O bonds, and Ni2P is up to 50 times more selective toward 3C-O bond cleavage than Ni. Here, we combine kinetic measurements, in situ infrared spectroscopy, and density functional theory (DFT) calculations to describe the mechanism for C-O bond rupture over Ni, Ni12P5, and Ni2P catalysts. Steady-state rate measurements and DFT calculations of C-O bond rupture within 2-methyltetrahydrofuran (MTHF) show that quasi-equilibrated MTHF adsorption and dehydrogenation steps precede kinetically relevant C-O bond rupture at these conditions (1-50 kPa MTHF; 0.1-6 MPa H2; 543 K). Rates for 3C-O and 2C-O bond rupture are inhibited by H2, and the ratio of these rates increases with [H2]1/2, suggesting that the composition of the reactive intermediates for 3C-O and 2C-O rupture differs by one H atom. Site-blocking CO∗, NH3∗, and H∗ inhibit rates without altering the ratio of 3C-O to 2C-O bond rupture, indicating that these C-O bond rupture precursors and transition states bind to identical active sites. DFT-based predictions suggest that these sites are exposed ensembles of 3 Ni atoms on Ni(111) and Ni2P(001) and 4 Ni atoms on Ni12P5(001) and that the incorporation of P disrupts extended Ni ensembles and alters the reactivity of the Ni. Increasing the phosphorus to nickel ratio (P:Ni) decreases measured and DFT-predicted activation enthalpies (ΔH‡, 473-583 K) for 3C-O bond rupture relative to that of 2C-O bond rupture. Selectivity differences between specific C-O bonds within MTHF reflect differences in the H content of reactive intermediates, activation enthalpy barriers, and P:Ni of Ni, Ni12P5, and Ni2P nanoparticles.
AB - Nickel phosphide catalysts (Ni12P5 and Ni2P) preferentially cleave sterically hindered 3C-O bonds over unhindered 2C-O bonds, and Ni2P is up to 50 times more selective toward 3C-O bond cleavage than Ni. Here, we combine kinetic measurements, in situ infrared spectroscopy, and density functional theory (DFT) calculations to describe the mechanism for C-O bond rupture over Ni, Ni12P5, and Ni2P catalysts. Steady-state rate measurements and DFT calculations of C-O bond rupture within 2-methyltetrahydrofuran (MTHF) show that quasi-equilibrated MTHF adsorption and dehydrogenation steps precede kinetically relevant C-O bond rupture at these conditions (1-50 kPa MTHF; 0.1-6 MPa H2; 543 K). Rates for 3C-O and 2C-O bond rupture are inhibited by H2, and the ratio of these rates increases with [H2]1/2, suggesting that the composition of the reactive intermediates for 3C-O and 2C-O rupture differs by one H atom. Site-blocking CO∗, NH3∗, and H∗ inhibit rates without altering the ratio of 3C-O to 2C-O bond rupture, indicating that these C-O bond rupture precursors and transition states bind to identical active sites. DFT-based predictions suggest that these sites are exposed ensembles of 3 Ni atoms on Ni(111) and Ni2P(001) and 4 Ni atoms on Ni12P5(001) and that the incorporation of P disrupts extended Ni ensembles and alters the reactivity of the Ni. Increasing the phosphorus to nickel ratio (P:Ni) decreases measured and DFT-predicted activation enthalpies (ΔH‡, 473-583 K) for 3C-O bond rupture relative to that of 2C-O bond rupture. Selectivity differences between specific C-O bonds within MTHF reflect differences in the H content of reactive intermediates, activation enthalpy barriers, and P:Ni of Ni, Ni12P5, and Ni2P nanoparticles.
KW - 2-methyltetrahydrofuran
KW - DFT
KW - active site
KW - hydrogenolysis
KW - kinetics
KW - nickel phosphide
KW - reaction mechanism
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U2 - 10.1021/acscatal.7b04403
DO - 10.1021/acscatal.7b04403
M3 - Article
AN - SCOPUS:85049227949
SN - 2155-5435
VL - 8
SP - 7141
EP - 7157
JO - ACS Catalysis
JF - ACS Catalysis
IS - 8
ER -