dc.contributor.author |
Templis, C |
en |
dc.contributor.author |
Vonortas, A |
en |
dc.contributor.author |
Sebos, I |
en |
dc.contributor.author |
Papayannakos, N |
en |
dc.date.accessioned |
2014-03-01T01:37:31Z |
|
dc.date.available |
2014-03-01T01:37:31Z |
|
dc.date.issued |
2011 |
en |
dc.identifier.issn |
0926-3373 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/21544 |
|
dc.subject |
Co-hydroprocessing |
en |
dc.subject |
Gasoil-vegetable oil mixtures |
en |
dc.subject |
Hydrodeoxygenation |
en |
dc.subject |
Hydrodesulphurization |
en |
dc.subject |
Vegetable oil |
en |
dc.subject.classification |
Chemistry, Physical |
en |
dc.subject.classification |
Engineering, Environmental |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Consumption rates |
en |
dc.subject.other |
Desulphurization |
en |
dc.subject.other |
Formal kinetics |
en |
dc.subject.other |
Hydro desulfurizations |
en |
dc.subject.other |
Hydrodeoxygenation |
en |
dc.subject.other |
Hydrodesulphurization |
en |
dc.subject.other |
Hydroprocessing |
en |
dc.subject.other |
Hydrotreatment |
en |
dc.subject.other |
Palm oil |
en |
dc.subject.other |
Power law |
en |
dc.subject.other |
Three temperature |
en |
dc.subject.other |
Hydrocracking |
en |
dc.subject.other |
Hydrodesulfurization |
en |
dc.subject.other |
Hydrogen |
en |
dc.subject.other |
Lubricating oils |
en |
dc.subject.other |
Mixtures |
en |
dc.subject.other |
Vegetable oils |
en |
dc.title |
Vegetable oil effect on gasoil HDS in their catalytic co-hydroprocessing |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/j.apcatb.2011.03.012 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/j.apcatb.2011.03.012 |
en |
heal.language |
English |
en |
heal.publicationDate |
2011 |
en |
heal.abstract |
The effect of the presence of triglycerides on the catalytic hydrodesulfurization (HDS) of gasoil and the hydrogen consumption reactions have been studied during catalytic hydroprocessing of gasoil-palm oil mixtures at conventional hydrotreatment conditions over a commercial CoMo/gamma-Al2O3 catalyst. The experiments were performed at a pressure of 33 bar, three temperatures (310 degrees C, 330 degrees C and 350 degrees C), and three values of WHSV (0.7 h(-1), 1 h(-1) and 1.4 h(-1)). Desulphurization rates decreased with palm oil content from 0 to 5% but they did not change with a further increase to 10%. Hydrogen consumption rates were not affected by the presence of the vegetable oil molecules. Simple power law formal kinetics has been applied to simulate the desulphurization and hydrogen consumption rates of the gasoil-palm oil mixtures. (C) 2011 Elsevier B.V. All rights reserved. |
en |
heal.publisher |
ELSEVIER SCIENCE BV |
en |
heal.journalName |
Applied Catalysis B: Environmental |
en |
dc.identifier.doi |
10.1016/j.apcatb.2011.03.012 |
en |
dc.identifier.isi |
ISI:000291182100016 |
en |
dc.identifier.volume |
104 |
en |
dc.identifier.issue |
3-4 |
en |
dc.identifier.spage |
324 |
en |
dc.identifier.epage |
329 |
en |