2014
DOI: 10.1021/ef402529k
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Hydrodeoxygenation of Guaiacol over MoO3-NiO/Mesoporous Silicates: Effect of Incorporated Heteroatom

Abstract: Ordered mesoporous silicate SBA-15 and Ti-SBA-15 (Si/Ti = 10) and mesoporous aluminosilicate MAS (Si/Al = 20) supports were prepared by a hydrothermal method. Peptization of γ-alumina with these supports was carried out with 2% acetic acid, and the resulting composite materials were loaded with 3 wt % NiO and 10 wt % MoO 3 by a simple impregnation method. The physicochemical properties of these catalysts were examined with the following techniques, such as XRD, N 2 sorption, diffuse reflectance UV−vis spectra,… Show more

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Cited by 53 publications
(29 citation statements)
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References 52 publications
(65 reference statements)
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“…Metallic oxide also been investigated as catalyst for bio-oil upgrading. Selvaraj et al considered HDO of guaiacol over MoO 3 -NiO/mesoporous silicates at atmospheric pressure, observing the following order of HDO activities: MoO 3 -NiO/MAS (mesoporous aluminosilicate) > MoO 3 -NiO/Ti-SBA-15 > MoO 3 -NiO/SBA-15 [97]. However, naphthenic hydrocarbon was the major product over MoO 3 -NiO/MAS compared to other catalysts, where and aromatic hydrocarbon was the major product.…”
Section: Non-noble Metal Catalystsmentioning
confidence: 99%
“…Metallic oxide also been investigated as catalyst for bio-oil upgrading. Selvaraj et al considered HDO of guaiacol over MoO 3 -NiO/mesoporous silicates at atmospheric pressure, observing the following order of HDO activities: MoO 3 -NiO/MAS (mesoporous aluminosilicate) > MoO 3 -NiO/Ti-SBA-15 > MoO 3 -NiO/SBA-15 [97]. However, naphthenic hydrocarbon was the major product over MoO 3 -NiO/MAS compared to other catalysts, where and aromatic hydrocarbon was the major product.…”
Section: Non-noble Metal Catalystsmentioning
confidence: 99%
“…However, lignin-derived phenolic compounds are highly persistent in hydrodeoxygenation reaction. Therefore, transformation of phenolic compounds to high-value and stable components is a research field of great interest, and several researches have been conducted for study of catalytic hydrogenation of phenols [20][21][22][23][24][25][26] . High-pressure hydrogen gas is commonly used for catalytic hydrogenation of bio-oil/bio-oil model compounds.…”
Section: Introductionmentioning
confidence: 99%
“…It is considered that the CNTs-supported Ni catalyst reveals a model of "support The typical N 2 adsorption-desorption isotherm and BJH (Barrett-Joyner-Halenda) pore size distribution plot of 5% Ni/CNTs are displayed in Figure 2. A representative-type IV curve was exhibited in the nitrogen adsorption-desorption isotherm with sharp capillary condensation steps at relative pressures of 0.8-0.98 (Figure 2a) [41]. The H1-type hysteresis loop demonstrates the typical mesoporous material property [42].…”
Section: Characterization Of Catalystmentioning
confidence: 99%