2011
DOI: 10.1016/j.apcatb.2010.10.031
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Hydrodeoxygenation of guaiacol

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Cited by 364 publications
(167 citation statements)
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“…3c), the first two peaks located at 161.4 and 162.5 eV were due to the spin−orbit coupling in metal sulfide, 53, 54 while S 2p peak at 163.5 eV suggested the existence of covalent S-C bonds in the as-synthesized composites 55,56 indicating that S has been covalently inserted in N-doped porous carbon. 43 No peaks at around 164.5 eV corresponds to polysulfides (S n 2-) can be found in all samples, [57][58][59] and the peaks at 168.5 and 169.5 eV in S 2p spectrum indicate that inconsequential amount of Co x S y compounds were also formed during the thermal treatment process. 60,61 Moreover, the main peaks for N 1s spectra (shown in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…3c), the first two peaks located at 161.4 and 162.5 eV were due to the spin−orbit coupling in metal sulfide, 53, 54 while S 2p peak at 163.5 eV suggested the existence of covalent S-C bonds in the as-synthesized composites 55,56 indicating that S has been covalently inserted in N-doped porous carbon. 43 No peaks at around 164.5 eV corresponds to polysulfides (S n 2-) can be found in all samples, [57][58][59] and the peaks at 168.5 and 169.5 eV in S 2p spectrum indicate that inconsequential amount of Co x S y compounds were also formed during the thermal treatment process. 60,61 Moreover, the main peaks for N 1s spectra (shown in Fig.…”
Section: Resultsmentioning
confidence: 99%
“…Ni-MoS2/ZrO2 was chosen as catalyst, as promotion by nickel previously has been shown to be slightly superior to cobalt promotion for HDO purposes [9,25] and ZrO2 was previously found as a suitable support for HDO [31][32][33][34][35] and does apparently not suffer from the instability in high concentration of water, as reported for the conventionally used -Al2O3 support for hydrotreating catalysts [9,36,37].…”
Section: Introductionmentioning
confidence: 99%
“…In addition to reactant structures, catalyst properties such as acidity play an important role in coke formation. In the study for HDO of guaiacol over CoMoS catalysts, Bui et al reported the conventional alumina support obviously induced the formation of heavier products resulting in catalyst deactivation, while supports with less acidity (ZrO 2 and TiO 2 ) formed less heavy by-products [116]. Meanwhile, it is proposed that Lewis acid sites bind reactant species adsorb to catalyst surface, and Brønsted acid sites supply protons to form carbocations as coke precursors [114].…”
Section: Catalyst Deactivationmentioning
confidence: 99%