Abstract
Catalytic pyrolysis of pine biomass was carried out in a fluidized bed reactor at 450 degrees C. The acidic catalysts used as bed material in the reactor were B-zeolites with varying silica to alumina ratio, thus having different acid strengths. Quartz sand was used as bed material in the non-catalytic experiment. The yield of the different product phases was clearly influenced by the zeolites acidity. The chemical composition of the bio-oil was dependent on the catalyst. Zeolites with stronger acidity formed less organic oil, and respectively more water and polyaromatic hydrocarbons than less acidic zeolites.
Original language | Undefined/Unknown |
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Pages (from-to) | 473–480 |
Number of pages | 8 |
Journal | Process Safety and Environmental Protection |
Volume | 85 |
Issue number | B5 |
DOIs | |
Publication status | Published - 2007 |
MoE publication type | A1 Journal article-refereed |
Keywords
- bio-oil
- biomass
- fluidized bed reactor
- pyrolysis
- zeolites