Catalytic pyrolysis of biomass in a fluidized bed reactor: Influence of the acidity of H-beta zeolite

A1 Journal article (refereed)


Internal Authors/Editors


Publication Details

List of Authors: Aho A, Kumar N, Eranen K, Salmi T, Hupa M, Murzin DY
Publisher: INST CHEMICAL ENGINEERS
Publication year: 2007
Journal: Process Safety and Environmental Protection
Journal acronym: PROCESS SAF ENVIRON
Volume number: 85
Issue number: B5
Start page: 473
End page: 480
Number of pages: 8
ISSN: 0957-5820


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.


Keywords

biomass, bio-oil, fluidized bed reactor, pyrolysis, zeolites

Last updated on 2019-19-06 at 04:45