2008
DOI: 10.1002/cssc.200800018
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Green Gasoline by Catalytic Fast Pyrolysis of Solid Biomass Derived Compounds

Abstract: A fuelling success: High‐quality aromatic fuel additives can be produced directly from solid biomass feedstocks by catalytic fast pyrolysis in a single catalytic reactor at short residence times. High heating rates and catalyst‐to‐feed ratios are needed to ensure that pyrolized biomass compounds enter the pores of the ZSM5 catalyst and that thermal decomposition is avoided. Product selectivity is a function of the active site and pore structure of the catalyst.

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Cited by 489 publications
(342 citation statements)
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“…However, this process converts any C1-C5 oxygenates, representing as much as half of the carbon in bio-oil, to C1-C5 hydrocarbons that are too volatile for liquid fuels (Resasco, 2011). Another straightforward approach is to "crack" the pyrolysis vapors using acidic zeolite catalysts into light olefins and aromatic hydrocarbons (primarily benzene, toluene, and o/m/p-xylene) (Bridgwater, 1994;Carlson et al, 2008Carlson et al, , 2009). This approach is appealing because of the lack of an external H2 requirement and the simplicity of the product streams.…”
Section: <1-3mentioning
confidence: 99%
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“…However, this process converts any C1-C5 oxygenates, representing as much as half of the carbon in bio-oil, to C1-C5 hydrocarbons that are too volatile for liquid fuels (Resasco, 2011). Another straightforward approach is to "crack" the pyrolysis vapors using acidic zeolite catalysts into light olefins and aromatic hydrocarbons (primarily benzene, toluene, and o/m/p-xylene) (Bridgwater, 1994;Carlson et al, 2008Carlson et al, , 2009). This approach is appealing because of the lack of an external H2 requirement and the simplicity of the product streams.…”
Section: <1-3mentioning
confidence: 99%
“…Furthermore, since zeolite cracking is widely used in traditional petroleum refining/valorization (Wan et al, 2015), other advantages are the product compatibility with existing refinery infrastructure and the maturity of the process (Wan et al, 2015). However, zeolite cracking is crippled by poor usable carbon yield due to the high amounts of coke, CO, and CO2 formed during the catalytic process (Carlson et al, 2008) and the concomitant rapid catalyst deactivation. Additionally, further catalytic oligomerization and reforming for olefins and aromatics, respectively, are needed to make these products suitable for addition to refinery fuel product streams, increasing the process costs and further reducing overall carbon yield.…”
Section: <1-3mentioning
confidence: 99%
“…Bio-oils must be catalytically upgraded if they are to be used as a conventional liquid transportation fuel [14][15][16]. As we have previously shown introduction of zeolite catalysts into the pyrolysis process can convert oxygenated compounds generated from pyrolysis into aromatics [17]. The purpose of this paper is to discuss in more detail aromatic production by catalytic fast pyrolysis of biomass-derived feedstocks.…”
Section: Introductionmentioning
confidence: 99%
“…111 Recent progress with catalytic fast pyrolysis is a promising method for maximizing output of aromatics while reducing oxygenated compounds. 112 This process employs a combination of high heating rates to initially pyrolyze lignin followed by catalytic conversion of oxygenated molecules with zeolite catalysts to form aromatics, CO 2 and water. 113 Additionally, the reaction only requires short resonance times ($ 2 min).…”
Section: Figure 11mentioning
confidence: 99%