2007
DOI: 10.1016/j.cej.2007.03.064
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Production of diesel fuel from renewable feeds: Kinetics of ethyl stearate decarboxylation

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Cited by 166 publications
(85 citation statements)
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“…GC-MS analysis revealed that the AP-Ni-MSN sequestered up to 47 wt % of the FFAs in the microalgal extract and catalyzed the conversion of 66% of them into liquid hydrocarbons. The most abundant fatty acid in the original extract was C 16 , and it was also the most sequestered FFA (68 wt %). n-Pentadecane was the major liquid hydrocarbon obtained, which presumably resulted from the decarbonylation of sequestered C 16 FFAs (Figure 8c,d).…”
Section: Methodsmentioning
confidence: 99%
“…GC-MS analysis revealed that the AP-Ni-MSN sequestered up to 47 wt % of the FFAs in the microalgal extract and catalyzed the conversion of 66% of them into liquid hydrocarbons. The most abundant fatty acid in the original extract was C 16 , and it was also the most sequestered FFA (68 wt %). n-Pentadecane was the major liquid hydrocarbon obtained, which presumably resulted from the decarbonylation of sequestered C 16 FFAs (Figure 8c,d).…”
Section: Methodsmentioning
confidence: 99%
“…Ethyl stearate converted into stearic acid before decarboxylating to n-heptadecane, although selectivity to n-heptadecane decreased from 300 to 3608C when aromatics started to be produced instead, which are unsuitable in diesel fuels. The reaction kinetics for ethyl stearate and stearic acid decarboxylation over palladium/carbon (Pd/C) catalyst have also been studied; a problem when using fatty acids is that the Pd/C catalyst is deactivated at high concentrations (Snare et al 2007). investigated a range of catalysts, Ir, Mo, Ni, Os, Pd, Pt, Rh and Ru (supported on carbon and metal oxides) as well as a Raney nickel catalyst.…”
Section: Deoxygenating Fatty Acids For Green Diesel Productionmentioning
confidence: 99%
“…[5,6] An alternate technology to produce biofuels from microalgal oil is through hydrotreating with Ni, Co and Mo sulfides or noble metal catalysts such as Pd and Pt supported on metal oxides. [7][8][9][10][11][12][13][14] While the high price of the noble metals can be avoided by using the sulfided catalysts, slow desulfurization reduces their activity and contaminates the fuel. [7,9,15] Furthermore, these catalysts have shown poor selectivity, favoring cracking and decarbonylation over hydrodeoxygenation to produce broad hydrocarbon distributions.…”
Section: Introductionmentioning
confidence: 99%