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Clean bio-oil production from fast pyrolysis of sewage sludge: effects of reaction conditions and metal oxide catalysts.

Bioresource technology (2009-07-29)
Hyun Ju Park, Hyeon Su Heo, Young-Kwon Park, Jin-Heong Yim, Jong-Ki Jeon, Junhong Park, Changkook Ryu, Seung-Soo Kim
RESUMEN

Fast pyrolysis of sewage sludge was carried out under different reaction conditions, and its effects on bio-oil characteristics were studied. The effect of metal oxide catalysts on the removal of chlorine in the bio-oil was also investigated for four types of catalysts. The optimal pyrolysis temperature for bio-oil production was found to be 450 degrees C, while much smaller and larger feed sizes adversely influenced production. Higher flow and feeding rates were more effective but did not greatly affect bio-oil yields. The use of the product gas as the fluidizing medium gave an increased bio-oil yield. Metal oxide catalysts (CaO and La2O3) contributed to a slight decrease in bio-oil yield and an increase in water content but were significantly effective in removal of chlorine from the bio-oil. The fixed catalyst bed system exhibited a higher removal rate than when metal oxide-supported alumina was used as the fluidized bed material.

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Sigma-Aldrich
Lanthanum(III) oxide, ≥99.9%
Sigma-Aldrich
Lanthanum(III) oxide, 99.99% trace metals basis
Supelco
Lanthanum(III) oxide, suitable for AAS, ≥99.9%
Sigma-Aldrich
Lanthanum(III) oxide, nanopowder, <100 nm particle size (TEM), 99% trace metals basis
Sigma-Aldrich
Lanthanum(III) oxide, 99.999% trace metals basis