In-depth study of rice husk torrefaction: Characterization of solid, liquid and gaseous products, oxygen migration and energy yield

•The liquid and gaseous products play a crucial role in the torrefaction of biomass.•Water and gaseous products are the major contributors to deoxygenation of rice husk.•In temperature range of 210–300 °C, 9.5–63.2% of oxygen is removed from rice husk.•Formation of H2O, CO2 and CO is important for i...

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Veröffentlicht in:Bioresource technology 2018-04, Vol.253, p.148-153
Hauptverfasser: Chen, Dengyu, Gao, Anjiang, Ma, Zhongqing, Fei, Dayi, Chang, Yu, Shen, Chao
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Sprache:eng
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Zusammenfassung:•The liquid and gaseous products play a crucial role in the torrefaction of biomass.•Water and gaseous products are the major contributors to deoxygenation of rice husk.•In temperature range of 210–300 °C, 9.5–63.2% of oxygen is removed from rice husk.•Formation of H2O, CO2 and CO is important for intense torrefaction deoxygenation.•Energy yields of gaseous and liquid products increase with increasing temperature. Torrefaction is a promising method for biomass upgrading, and analysis of all products is the essential way to reveal torrefaction mechanism. In this study, torrefaction of rice husk was performed at 210–300 °C. Results showed that the fuel properties of solid products were greatly enhanced upon removal of oxygen. The gaseous products were mainly CO2 (52.9–73.8 vol%), followed by CO (26.3–39.2 vol%). The liquid product was mainly water and some tar, and the latter contained acids, furans, ketones, aldehydes, and phenols, among which the relative content of acids was the highest. Torrefaction temperature has obvious effects on the oxygen migration. Within the temperature range of 210–300 °C, 9.5–63.2% of oxygen in rice husk was migrated to the gaseous and liquid products. The H2O was the major contributor to deoxygenation, followed by CO2 and CO. Thus, formation of H2O, CO2, and CO during torrefaction is important as it achieves the purpose of intense deoxygenation.
ISSN:0960-8524
1873-2976
DOI:10.1016/j.biortech.2018.01.009