2010
DOI: 10.1016/j.apcata.2010.06.003
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Influence of support acidity of NiMoS catalysts in the activity for hydrogenation and hydrocracking of tetralin

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Cited by 67 publications
(48 citation statements)
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“…Figure 3c-f. The distances between the fringes were calculated to be 0.63 nm in the case of molybdenum catalysts, and 0.65 nm in the case of tungsten catalysts, which is consistent with the interplanar spacing for bulk MoS 2 and WS 2 reported in the literature [4,12,23].…”
Section: Synthesis Of Precursors and Characterization Of Catalystssupporting
confidence: 73%
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“…Figure 3c-f. The distances between the fringes were calculated to be 0.63 nm in the case of molybdenum catalysts, and 0.65 nm in the case of tungsten catalysts, which is consistent with the interplanar spacing for bulk MoS 2 and WS 2 reported in the literature [4,12,23].…”
Section: Synthesis Of Precursors and Characterization Of Catalystssupporting
confidence: 73%
“…al. for NiMoS catalysts supported by alumina [4]. Furthermore, modifying benzene rings with even low-acidic OH-groups increases the yields of cracking products [23].…”
Section: Catalytic Experimentsmentioning
confidence: 99%
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“…This difference probably affects the 2 International Journal of Chemical Engineering hydrogenation activity of catalyst and leads to the decrease of aromatics conversion. Generally, model compounds are composed of aromatics and inert hydrocarbons; for example, naphthalene dissolves in -hexadecane [16][17][18][19], -tridecane [20,21], -decane [22], -heptane [5,[10][11][12][13][14]23], and benzene [4] or tetralin dissolves in -dodecane [24], -decane [22,25,26], -heptane [6-9, 12, 15, 27, 28], -hexane [29], and cyclohexane [30,31]. The model compounds using light components as solvents are easier to vaporize and have lower dew point.…”
Section: Introductionmentioning
confidence: 99%