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Vegetable oil tansesterification in supercritical conditions using Co-solvent carbon dioxide over solid catalysts: A screening study
dc.contributor.author | Saez, B |
dc.contributor.author | Santana, A |
dc.contributor.author | Ramírez-Llodra, E. |
dc.contributor.author | Maçaira Nogueira, Jose Miguel Lopes |
dc.contributor.author | Ledesma Rodriguez, Cristian |
dc.contributor.author | Llorca Piqué, Jordi |
dc.contributor.author | Larrayoz Iriarte, María Angeles |
dc.contributor.other | Universitat Politècnica de Catalunya. Institut de Tècniques Energètiques |
dc.date.accessioned | 2014-11-28T10:30:37Z |
dc.date.created | 2014-09-01 |
dc.date.issued | 2014-09-01 |
dc.identifier.citation | Saez, B. [et al.]. Vegetable oil tansesterification in supercritical conditions using Co-solvent carbon dioxide over solid catalysts: A screening study. "Energy and fuels", 01 Setembre 2014, vol. 28, núm. 9, p. 6006-6011. |
dc.identifier.issn | 0887-0624 |
dc.identifier.uri | http://hdl.handle.net/2117/24879 |
dc.description.abstract | The transesterification reaction employing supercritical methanol and carbon dioxide used as a co-solvent in the presence of several heterogeneous solid acid catalysts was investigated. The solid acid catalysts were prepared by impregnation methods, with appropriate precursors over magnesium aluminum silicate (cordierite). The catalysts tested were CeO2, WO3, ZnO, ZrO2, ZrO2-SO42-, mixed oxides (50-5096, w/w) WO3- ZrO2, CeO2-ZrO2, ZnO-La2O3, and Al2O3. Reaction tests were conducted at 200 degrees C and 20 MPa under the condition of 25:1 methanol/oil ratio at a space velocity of 4 mm with a fixed-bed continuous flow reactor containing ca. 5 g of catalyst. The best catalytic performance was obtained over ZrO2-SO42- with a yield toward fatty acid methyl esters (FAMEs) of 98%. This value is better to that obtained over the commercial catalyst Nafion SAC-13 (94%). The direct correlation between the conversion and catalyst total acidity was non-existent, but a positive effect of strong acid sites is evidenced. |
dc.format.extent | 6 p. |
dc.language.iso | eng |
dc.publisher | American Chemical Society (ACS) |
dc.rights | Attribution-NonCommercial-NoDerivs 3.0 Spain |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/3.0/es/ |
dc.subject | Àrees temàtiques de la UPC::Energies::Recursos energètics renovables |
dc.subject.lcsh | Methanol |
dc.subject.lcsh | Catalysts |
dc.subject.other | Biodiesel fuel production |
dc.subject.other | Fixed-bed reactor |
dc.subject.other | Soybean |
dc.subject.other | Methanol |
dc.title | Vegetable oil tansesterification in supercritical conditions using Co-solvent carbon dioxide over solid catalysts: A screening study |
dc.type | Article |
dc.subject.lemac | Metanol |
dc.subject.lemac | Catalitzadors |
dc.contributor.group | Universitat Politècnica de Catalunya. GREENER - Grup de recerca d'estudis energètics i de les radiacions |
dc.contributor.group | Universitat Politècnica de Catalunya. FLUIDS - Enginyeria de Fluids |
dc.identifier.doi | 10.1021/ef5006786 |
dc.rights.access | Restricted access - publisher's policy |
local.identifier.drac | 15251969 |
dc.description.version | Postprint (published version) |
dc.date.lift | 10000-01-01 |
local.citation.author | Saez, B.; Santana, A.; Ramírez-Llodra, E.; Maçaira, J.; Ledesma, C.; Llorca, J.; Larrayoz, M. |
local.citation.publicationName | Energy and fuels |
local.citation.volume | 28 |
local.citation.number | 9 |
local.citation.startingPage | 6006 |
local.citation.endingPage | 6011 |
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