| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 41081 | Applied Catalysis A: General | 2011 | 9 Pages |
Samples of MoO3/γ-Al2O3 with different MoO3 loadings (8, 12 and 16 wt%) calcined at different temperatures (800, 950 and 1100 K) have been used in the transesterification of sunflower oil with methanol. Activity was the highest when the samples were calcined at 950 K, the most active catalyst being 16%MoO3–Al2O3. XRD and Raman spectroscopy reveal the presence of many Mo-phases, such as dispersed surface molybdenum specie, bulk MoO3 and Al2(MoO4)3 in the samples. The influence of various parameters, such as Mo-loading, calcination temperature, reaction temperature and mole ratio of reactants (methanol:oil), on the reaction is presented. The reaction studies have been carried out both in a batch reactor and in a fixed-bed flow reactor. The studies reveal that a sound fixed-bed continuous transesterification process for the production of biodiesel can be designed using MoO3–Al2O3.
Graphical abstractFigure optionsDownload full-size imageDownload high-quality image (87 K)Download as PowerPoint slideHighlights► MoO3 supported on γ-Al2O3 is active for the transesterification of sunflower oil. ► Catalyst is most active when calcined at 950 K; 16% MoO3 is preferred loading. ► The catalyst is also active for converting oil containing free fatty acids. ► The catalyst is suitable for use in a fixed-bed reactor with continuous operation.
