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Zeolitic Upgrading of Cellulosic Feedstocks

and water [26], A large amount of coke forms during the upgrading of glucose and starch. The coke formation is attributed to the decomposition of glucose monomers at the reaction temperature and pressure (510°C, 1 atm). However, the addition of methanol during the reaction increases hydrocarbon yields and decreases coke formation by promoting decarboxylation reactions [26], [Pg.197]

Catalytic pyrolysis is the conversion of biomass via pyrolysis in the presence of a catalyst [27]. In this process, the catalyst can react in a secondary reactor directly with the vapors produced by pyrolysis, or the catalyst can be mixed with the biomass in a fluidized bed pyrolysis reactor [28], In either system, catalysts with high selectivity to diesel and gasoline range hydrocarbons are often preferred [29-31], Because the pyrolysis products are upgraded by additional deoxygenation reactions on the catalyst, the resulting catalyticaUy produced bio-oil is generally more stable than noncatalytic pyrolysis bio-oil. [Pg.197]

Based on results with HZSM-5, researchers have investigated the use of metal additives on HZSM-5 to improve aromatics production or tune selectivity. The Huber group has shown marked improvement with the use of gallium exchanged HZSM-5 for the catalytic fast pyrolysis of furans. In this report, the gallium should be incorporated by exchange rather than incipient wetness or framework substitution to [Pg.197]

FIGURE 9.4 Thermochemical catalytic conversion of cellulose to biofuels [35]. [Pg.197]

FIGURE 9.5 Metal additives of HZSM-5 to alter selectivity and activity. [Pg.198]


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