2016
DOI: 10.1166/apm.2016.1116
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Influences of the Support Property and Pd Loading on Activity of Mesoporous Silica-Supported Pd Catalysts in Partial Hydrogenation of Palm Biodiesel Fuel

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Cited by 11 publications
(3 citation statements)
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“…However, the product selectivity for mono-FAME, cis -mono-FAME, and sat-FAME as a function of reaction time over Cl-containing and Cl-free Pd catalysts remained nearly unchanged, particularly those related to high poly-FAME conversions. This result indicated that the hydrogenation of poly-FAME components over the Cl-containing Pd particles was slightly facilitated, presumably due to the Pd surface being slightly electron-deficient owing to the high electronegativity of the Cl species [ 56 , 59 , 60 , 61 ]. However, the activity and selectivity of Pd/AC catalysts in the partial hydrogenation of a commercial palm-BDF were predominately influenced by the sizes of Pd particles.…”
Section: Resultsmentioning
confidence: 99%
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“…However, the product selectivity for mono-FAME, cis -mono-FAME, and sat-FAME as a function of reaction time over Cl-containing and Cl-free Pd catalysts remained nearly unchanged, particularly those related to high poly-FAME conversions. This result indicated that the hydrogenation of poly-FAME components over the Cl-containing Pd particles was slightly facilitated, presumably due to the Pd surface being slightly electron-deficient owing to the high electronegativity of the Cl species [ 56 , 59 , 60 , 61 ]. However, the activity and selectivity of Pd/AC catalysts in the partial hydrogenation of a commercial palm-BDF were predominately influenced by the sizes of Pd particles.…”
Section: Resultsmentioning
confidence: 99%
“…The results are further compared to those of the H-FAME obtained by carbon-supported Pd catalysts in the literature [ 34 ]. The oxidation stability of the antioxidant-stabilized palm-BDF as a commercial product is 13 h, which is higher than that of the antioxidant-free palm-BDF (<5 h) [ 60 , 61 ]. The oxidation stability of palm-BDF is higher than those specified in the ASTM D6751 international fuel standard (>3 h), EN 14,214 international fuel standard (>8 h), and Thai standard (>10 h) for the formulation of B7 fuels [ 62 , 63 ].…”
Section: Resultsmentioning
confidence: 99%
“…[9] Moreover, the support should be capable of reducing the metal agglomeration by controlling its size without passivation of the active surface. [10] Therefore, various supports such as zeolites, [11] carbon nanotube, [12] activated carbon, [13] silica [14] etc. have been reported.…”
Section: Introductionmentioning
confidence: 99%