Commercial catalysts, including zeolites (HZSM-5), fluid catalytic cracking
(FGC) catalysts, transition metal catalysts (Fe/Cr), and aluminas, were su
ccessfully evaluated in a fixed bed catalytic reactor using a mixture of mo
del compounds to simulate biomass flash pyrolysis vapors. Successful criter
ia including the stability index (SI), the water generation (WG), and the l
oss of organics (LO) were introduced to monitor the effect of catalysts and
ascertain major changes in the obtained liquid product composition. SI bei
ng a measure of the effective carbonyls reduction after catalytic cracking
reached 100% in the case of HZSM-5 catalysts, leading to the selective prod
uction of aromatic hydrocarbons. Transition metal catalysts (Fe/Cr) lead to
the selective production of phenol and light phenolics. Comparable trends
were obtained using solid biomass in the catalytic fixed bed reactor.