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International Journal of Chemical Engineering
Volume 2013, Article ID 297941, 9 pages
Research Article

Effect of Operating Conditions on Catalytic Gasification of Bamboo in a Fluidized Bed

1Division of Agricultural Engineering, Faculty of Engineering and Agro-Industry, Maejo University, Chiang Mai 50290, Thailand
2Department of Mechanical Engineering, Faculty of Engineering, Chiang Mai University, Chiang Mai 50200, Thailand

Received 19 March 2013; Revised 3 June 2013; Accepted 3 June 2013

Academic Editor: Deepak Kunzru

Copyright © 2013 Thanasit Wongsiriamnuay et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.


Catalytic gasification of bamboo in a laboratory-scale, fluidized bed reactor was investigated. Experiments were performed to determine the effects of reactor temperature (400, 500, and 600°C), gasifying medium (air and air/steam), and catalyst to biomass ratio (0 : 1, 1 : 1, and 1.5 : 1) on product gas composition, H2/CO ratio, carbon conversion efficiency, heating value, and tar conversion. From the results obtained, it was shown that at 400°C with air/steam gasification, maximum hydrogen content of 16.5% v/v, carbon conversion efficiency of 98.5%, and tar conversion of 80% were obtained. The presence of catalyst was found to promote the tar reforming reaction and resulted in improvement of heating value, carbon conversion efficiency, and gas yield due to increases in H2, CO, and CH4. The presence of steam and dolomite had an effect on the increasing of tar conversion.