Biodiesel is a renewable biofuel that has been studied as a possible successor to conventional diesel. Currently, biodiesel is predominantly produced on a commercial scale by means of methyl transesterification via basic catalysis. This production route provides high conversions, however, the alkaline catalyst in the presence of free fatty acids provides the formation of soaps, making it difficult to separate and purify the products, thus making the process more expensive. In this way, studies have been developed with the purpose of replacing conventional basic catalysis with production routes that reduce the formation of by-products and that are simultaneously economically, technically and environmentally viable. According to studies, one of the possible routes with substitution potential is heterogeneous acid catalysis. The objective of this work was to carry out a preliminary analysis with the purpose of verifying the possibility of producing biodiesel through heterogeneous superacid catalysis using niobium oxide supported in gamma alumina as catalysts. Two methods of preparation of the catalysts were evaluated, impregnated and co-precipitate. The catalyst masses were varied in 1%, 2%, 3%, 4%, 5% and 6% in order to find the optimum concentration. The transesterification reaction was conducted at a temperature of 65 ° C with an oil/methanol molar ratio of 1:12 and a reaction time of 5 hours. The results demonstrate that the occurrence of the transesterification reaction. The optimum concentration for both catalysts was 5% and the catalyst that presented the highest conversion was the catalyst obtained by the co-precipitation method.
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