dc.contributor.author |
Pasias, S |
en |
dc.contributor.author |
Barakos, N |
en |
dc.contributor.author |
Alexopoulos, C |
en |
dc.contributor.author |
Papayannakos, N |
en |
dc.date.accessioned |
2014-03-01T01:24:29Z |
|
dc.date.available |
2014-03-01T01:24:29Z |
|
dc.date.issued |
2006 |
en |
dc.identifier.issn |
0930-7516 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/17283 |
|
dc.subject |
Biofuels |
en |
dc.subject |
Catalysts |
en |
dc.subject |
Esterification |
en |
dc.subject |
Oils |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Chemical reactors |
en |
dc.subject.other |
Esterification |
en |
dc.subject.other |
Fatty acids |
en |
dc.subject.other |
Feedstocks |
en |
dc.subject.other |
Mathematical models |
en |
dc.subject.other |
Reaction kinetics |
en |
dc.subject.other |
Vegetable oils |
en |
dc.subject.other |
Batch reactor |
en |
dc.subject.other |
Biofuels |
en |
dc.subject.other |
Kinetic model |
en |
dc.subject.other |
Biocatalysts |
en |
dc.subject.other |
Biocatalysts |
en |
dc.subject.other |
Chemical reactors |
en |
dc.subject.other |
Esterification |
en |
dc.subject.other |
Fatty acids |
en |
dc.subject.other |
Feedstocks |
en |
dc.subject.other |
Mathematical models |
en |
dc.subject.other |
Reaction kinetics |
en |
dc.subject.other |
Vegetable oils |
en |
dc.title |
Heterogeneously catalyzed esterification of FFAs in vegetable oils |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1002/ceat.200600109 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1002/ceat.200600109 |
en |
heal.language |
English |
en |
heal.publicationDate |
2006 |
en |
heal.abstract |
The production of methyl esters (biodiesel) from free fatty acids (FFAs) contained in vegetable oils was studied using a heterogeneous acid catalyst. The feedstock was a by-product of a vegetable oil refinery. The experiments were performed in a batch reactor, in a temperature range of 363.15-393.15 K, with an initial molar ratio of methanol to FFAs of 6.6/1, while the catalyst mass was fixed at 2 wt % of the total vegetable oil mass. A technical kinetic model has been developed which accounts for the reversible esterification reaction. Kinetic parameters were determined by fitting experimental data to the model. © 2006 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim. |
en |
heal.publisher |
WILEY-V C H VERLAG GMBH |
en |
heal.journalName |
Chemical Engineering and Technology |
en |
dc.identifier.doi |
10.1002/ceat.200600109 |
en |
dc.identifier.isi |
ISI:000242093700011 |
en |
dc.identifier.volume |
29 |
en |
dc.identifier.issue |
11 |
en |
dc.identifier.spage |
1365 |
en |
dc.identifier.epage |
1371 |
en |