2020
DOI: 10.1016/j.jiec.2020.08.030
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Kinetics for the biodiesel production from lauric acid over Keggin heteropolyacid loaded in silica framework

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Cited by 24 publications
(17 citation statements)
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“…In the transesterification reaction, a rate limiting step is, indeed, the substitution between both functional groups. The increase in contact time between alcohol and lipid having two different functional groups is a key factor to enhance the reaction kinetics of transesterification reaction 55 . In conventional transesterification reaction, known as base‐catalyzed transesterification works around 65°C because the boiling temperature of methanol is low (65°C).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…In the transesterification reaction, a rate limiting step is, indeed, the substitution between both functional groups. The increase in contact time between alcohol and lipid having two different functional groups is a key factor to enhance the reaction kinetics of transesterification reaction 55 . In conventional transesterification reaction, known as base‐catalyzed transesterification works around 65°C because the boiling temperature of methanol is low (65°C).…”
Section: Resultsmentioning
confidence: 99%
“…The increase in contact time between alcohol and lipid having two different functional groups is a key factor to enhance the reaction kinetics of transesterification reaction. 55 In conventional transesterification reaction, known as basecatalyzed transesterification works around 65 C because the boiling temperature of methanol is low (65 C). As an effort to significantly enhance contact frequency between two reactants (methanol and lipid), heterogeneous reactions between methanol (MeOH) and lipid were developed using porous materials in our previous study.…”
Section: Valorization Of Pwb As a Catalyst For Bd Productionmentioning
confidence: 99%
“…The reaction was performed with a 10% catalyst and methanol/oil ratio of 17:1 at 200 °C for 10 h. The optimal conversion reached 94.9%, while reaction conversion decreased to 90.3% after the second run. 41 Gaurav et al kinetically modeled one-step biodiesel manufacture using a solid HSiW/Al 2 O 3 heteroatom catalyst loaded on alumina in the presence of high concentrations of free fatty acids in the used oils. Esterification rate constants and activation parameters were modeled for the essential fatty acid components of oleic, yellow grease, palmitic, and linoleic lipids.…”
Section: Heteropolyacid (Hpa)-based Catalystsmentioning
confidence: 99%
“…Kurhade et al reported biodiesel production using an aluminum oxide catalyst saturated with 12-tungstophosphoric acid. The reaction was performed with a 10% catalyst and methanol/oil ratio of 17:1 at 200 °C for 10 h. The optimal conversion reached 94.9%, while reaction conversion decreased to 90.3% after the second run . Gaurav et al kinetically modeled one-step biodiesel manufacture using a solid HSiW/Al 2 O 3 heteroatom catalyst loaded on alumina in the presence of high concentrations of free fatty acids in the used oils.…”
Section: Heteropolyacid (Hpa)-based Catalystsmentioning
confidence: 99%
“…Multiple catalysts, including solid super acid [ 16 ], heteropoly acid [ 17 ], high-acidic cation exchange resin [ 18 ] and zeolite molecular sieve [ 19 ], have been employed with wide and intensive study in catalysis, yet the mechanism of these catalysts were heterogeneous catalysis with low catalytic activity, together with problems in complexity of synthetic process and high capital cost [ 20 ]. Application of ILs in esterification could effectively avoid excess of side reaction and increase productivity [ 21 , 22 ], compared with a conventional inorganic acid catalyst.…”
Section: Introductionmentioning
confidence: 99%