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• W2016202152 abstract "Abstract The catalytic cracking of ginger oil in a fixed-bed tubular reactor with a weight hourly space velocity 1.0 h −1 at temperatures ranging from 300 °C to 450 °C has been accomplished over zeolites MFI, BEA, and FAU having different SiO 2 /Al 2 O 3 ratios. Gasoline fraction yields have been observed along with liquid, gas, and coke yields. Trends in the various yields have been correlated to zeolite structure, SiO 2 /Al 2 O 3 ratio, and reaction conditions where possible." @default.
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• W2016202152 date "2012-06-01" @default.
• W2016202152 modified "2023-09-26" @default.
• W2016202152 title "Comparison of ginger oil conversion over MFI, BEA, and FAU" @default.
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• W2016202152 doi "https://doi.org/10.1016/j.fuel.2012.01.033" @default.
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