Rice husks were pyrolysed in a fluidised bed reactor at 400, 450, 500, 550
and 600 degrees C. The rice husks were then pyrolysed at 550 degrees C with
zeolite ZSM-5 catalyst upgrading of the pyrolysis vapours at catalyst temp
eratures of 400, 450, 500, 550, and 600 degrees C. The pyrolysis oils were
collected in a series of condensers and cold traps and analysed to determin
e their yield and composition in relation to process conditions. The gases
were analysed off-line by packed column gas chromatography. The pyrolysis o
ils before catalysis were homogeneous, of low viscosity and highly oxygenat
ed. Polycyclic aromatic hydrocarbons (PAH) were present in the oils at low
concentration and increased in concentration with increasing temperature of
pyrolysis. Oxygenated compounds in the oils consisted mainly of phenols; c
resols, benzenediols and guaiacol and their alkylated derivatives. In the p
resence of the catalyst the yield of oil was markedly reduced, although the
oxygen content of the oil was reduced with the formation of coke on the ca
talyst. The influence of the catalyst was to convert the oxygen in the pyro
lysis oil to largely H2O at the lower catalyst temperatures and to largely
CO and CO2 at the higher catalyst temperatures. The molecular weight distri
bution of the oils was decreased after catalysis and further decreased with
increasing temperature of catalysis. The catalysed oils were markedly incr
eased in single ring and PAH compared to uncatalysed biomass pyrolysis oils
. The concentration of aromatic and polycyclic aromatic species increased w
ith increasing catalyst temperature. (C) 2000 Elsevier Science Ltd. All rig
hts reserved.