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Biomass steam-reforming in a low throughput fluidized bed reactor

Research output: Contribution to conference - Without ISBN/ISSN Conference paperpeer-review

Published
Publication date1/12/2004
Number of pages8
Pages6179-6186
<mark>Original language</mark>English
Event2004 AIChE Annual Meeting - Austin, TX, United States
Duration: 7/11/200412/11/2004

Conference

Conference2004 AIChE Annual Meeting
CountryUnited States
CityAustin, TX
Period7/11/0412/11/04

Abstract

This work presents the results from biomass gasification tests in a low throughput fluidized bed membrane reactor (FBMR) and compares them with two-phase model predictions. The operating temperature was decreased to 550°C, while an equimolar steam/cellulose ratio was used. The profiles of kinetics limitation and biomass conversion were analysed when a palladium (Pd) membrane for hydrogen separation was used. The produced gases were analysed by gas chromatography, while steam composition and temperature profiles were retrieved by near-infrared imaging (NIRI) technique. As a single membrane tube did not show high permeability rates, the changes in conversions and temperatures profiles were not significant when a Pd membrane was incorporated. The experimental design and procedure allowed us to visualize low radial dispersions in the FBMR.