Journal
ENERGY
Volume 66, Issue -, Pages 849-859Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.energy.2013.12.035
Keywords
Biomass; Torrefaction; Fluidized bed reactor; Tar; Steam/O-2 gasification
Categories
Funding
- European Regional Development Funds (ERDF, FEDER Programa de Competitivitat de Catalunya)
- Spanish Government [CTQ2011-22767]
- ERDF program
- Norwegian Research Council
- RENERGI Programme (Gasbio: Gasification for Biofuels) [199902/S60]
- Spanish Ministry of Economy and Competitivity [RYC-2011-09202]
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This work investigates the effect of temperature and bed material on the yields and composition of gas and tar produced from gasification of two types of biomass feedstock previously torrefied at 275 degrees C. Special attention was devoted to the evolution of tar composition under the different experimental conditions. Experiments were conducted in a fluidized bed reactor using two different types of bed material (sand and dolomite) under a constant pressure of 0.5 MPa and at two temperature levels (750 and 850 degrees C). Tar destruction reactions promoted by the catalyst (dolomite) enhanced the production of some of the gas components (H-2, CO2, CO and CH4) whereas C-2 hydrocarbons decreased, this effect being slightly more relevant at 850 C. Comparable trends were observed with increasing temperature, which had a positive effect on cracking reactions and tar destruction. For both feedstocks, the increase in temperature resulted in (i) higher gas yields, and (ii) enhanced char gasification rate. On the other hand the evolution of tar yield and composition revealed a possible competition between two tar reaction pathways during gasification, (i) tar polymerization, and (ii) de-alkylation, dehydration and cracking of tars, depending on the experimental conditions and feedstock used. (c) 2013 Elsevier Ltd. All rights reserved.
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