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- W2100960048 abstract "Abstract Catalytic steam reforming of bio‐oil is an economically‐feasible route which produces renewable hydrogen. The Ni/MgO‐La 2 O 3 ‐Al 2 O 3 catalyst was prepared with Ni as active agent, Al 2 O 3 as support, and MgO and La 2 O 3 as promoters. The experiments were conducted in fixed bed and fluidized bed reactors, respectively. Temperature, steam‐to‐carbon mole ratio ( S / C ), and liquid hourly space velocity (LHSV) were investigated with hydrogen yield as index. For the fluidized bed reactor, maximum hydrogen yield was obtained under temperatures 700–800 °C, S / C 15–20, LHSV 0.5–1.0 h –1 , and the maximum H 2 yield was 75.88 %. The carbon deposition content obtained from the fluidized bed was lower than that from the fixed bed. The maximum H 2 yield obtained in the fluidized bed was 7 % higher than that of the fixed bed. The carbon deposition contents obtained from the fluidized bed was lower than that of the fixed bed at the same reaction temperature." @default.
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- W2100960048 date "2010-10-29" @default.
- W2100960048 modified "2023-10-11" @default.
- W2100960048 title "Catalytic Steam Reforming of Fast Pyrolysis Bio-Oil in Fixed Bed and Fluidized Bed Reactors" @default.
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- W2100960048 doi "https://doi.org/10.1002/ceat.201000169" @default.
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