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• W2056536943 abstract "Catalytic cracking of soybean oil using hierarchical zeolite-containing mesoporous silica-aluminas was successfully estimated using a Curie point pyrolyzer. Most of the prepared catalysts exhibited higher catalytic activity and selectivity for gasoline than did a simple zeolite. The catalysts prepared using a larger amount of malic acid developed mesoporous structures and showed higher olefin/paraffin ratios and research octane numbers (RONs) than the simple zeolite and a catalyst with a microporous structure. When β zeolite-containing catalysts were used, the ratio of multi/single branched products in the gasoline fraction reached more than 0.40, which was considerably larger than that obtained using a simple zeolite. When the yields of gasoline, single-branched products and multi-branched products were plotted against the conversion of soybean oil, approximately linear relationships were observed for every plot. When the yields of gasoline and single-branched products were compared at the same conversion, the yields from the HY zeolite-containing catalysts were higher than those from the β zeolite-containing catalysts. These results were consistent with those for the catalytic cracking of VGO previously reported. However, the yields of multi-branched products from β zeolite-containing catalysts were higher than those from HY zeolite-containing catalysts. This result was different for VGO cracking, where the yield of multi-branched products from HY zeolite was higher. Furthermore, the RON of gasoline and the yield of aromatic compounds were higher than those for the catalytic cracking of VGO." @default.
• W2056536943 created "2016-06-24" @default.
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• W2056536943 date "2015-01-01" @default.
• W2056536943 modified "2023-10-14" @default.
• W2056536943 title "Catalytic cracking of soybean oil by hierarchical zeolite containing mesoporous silica-aluminas using a Curie point pyrolyzer" @default.
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• W2056536943 doi "https://doi.org/10.1016/j.molcata.2014.10.010" @default.
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