Energy Yields of Fuel Gas from Cassava Rhizome in a Fluidised-Bed Reactor
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Published:
Aug 31, 2018
Keywords:
Energy Yield; Gasification; Fuel Gas; Cassava Rhizomes; Fluidised - Bed
Main Article Content
Abstract
Gasification of cassava rhizomes in a fluidised-bed reactor is studied for investigate of product yields and energy yields of biomass gasification indifferent temperatures. The aim of this study is find the influence of temperature in five levels were 500, 600, 700, 800 and 900 °C on product yields and energy yields of biomass gasification in the fluidised - bed method. The liquefied petroleum gas (LPG) was used for the heating system before the experiment and air as a carrier gas during the experiment. The product yield was obtained by mass balance before and after the experiment. The gas chromatography (GC 8A) analysis method was used for analyze gas composition. The results show that maximum fuel gas yields from cassava rhizomes of 90.9 wt% at 900 °C. However, the gas with the lowest heating value were 12 MJ/kg. While the reaction temperature at 800 °C has gas yields and energy yields of 85 wt%, it is the ideal temperature for producing fuel gas.
Article Details
How to Cite
[1]
แดงทน ว. and ดวงอุปมา เ., “Energy Yields of Fuel Gas from Cassava Rhizome in a Fluidised-Bed Reactor”, RMUTI Journal, vol. 11, no. 2, pp. 88–99, Aug. 2018.
Section
บทความวิจัย (Research article)
References
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[5] Wang, Z., He, T., Qin, J., Wu, J., Li, J., and Zi, Z. (2015). Gasification of Biomass with Oxygen-Enriched Air in a Pilot Scale Two-Stage Gasifier. Fuel. Vol. 150, pp. 386-393. DOI: 10.1016/j.fuel.2015.02.056
[6] Ateş, F. and Erginel, N. (2012). The Regression Analysis of Fast Pyrolysis Product Yields and Determination of Product Quality. Fuel. Vol. 102, pp. 681-690. DOI: 10.1016/j.fuel.2012.05.051
[7] Kim, J. W., Lee, H. W., Lee, I. -G., Jeon, J. -K., Ryu, C., and Park, S. H. (2014). Influence of Reaction Conditions on Bio-Oil Production from Pyrolysis of Construction Waste Wood. Renewable Energy. Vol. 65, pp. 41-48. DOI: 10.1016/j.renene.2013.07.009
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[9] Yang, E., Jun, M., Haijun, H., and Wenfu, C. (2015). Chemical Composition and Potential Bioactivity of Volatile from Fast Pyrolysis of Rice Husk. Journal of Analytical and Applied Pyrolysis. Vol. 112, pp. 394-400. DOI: 10.1016/j.jaap.2015.02.021
[10] Yildiz, G., Ronsse, F., Venderbosch, R., Duren, R. V., Kersten, S. R. A., and Prins, W. (2015). Effect of Biomass Ash in Catalytic Fast Pyrolysis of Pine Wood. Applied Catalysis B: Environmental. Vol. 168-169, pp. 203-11. DOI: 10.1016/j.apcatb.2014.12.044
[11] Zhang, L., Li, T., Quyn, D., Dong, L., Qiu, P., and Li, C. -Z. (2015). Formation of Nascent Char Structure During the Fast Pyrolysis of Mallee Wood and Low-Rank Coals. Fuel. Vol. 150, pp. 486-492. DOI: 10.1016/j.fuel.2015.02.066
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[14] Du, S. -W., Chen, W. -H., and Lucas, J. A. (2014). Pretreatment of Biomass by Torrefaction and Carbonization for Coal Blend used in Pulverized Coal Injection. Bioresource Technology. Vol. 161, pp. 333-339. DOI: 10.1016/j.biortech.2014.03.090
[15] Sermyagina, E., Saari, J., Kaikko, J., and Vakkilainen, E. (2015). Hydrothermal Carbonization of Coniferous Biomass: Effect of Process Parameters on Mass and Energy Yields. Journal of Analytical and Applied Pyrolysis. Vol. 113, pp. 551-556
[16] Wu, Q., Zhang, S., Hou, B., Zheng, H., Deng, W., and Liu, D. (2015). Study on the Preparation of Wood Vinegar from Biomass Residues by Carbonization Process. Bioresource Technology. Vol. 179, pp. 98-103. DOI: 10.1016/j.biortech.2014.12.026
[17] Bridgwater, A. V., Toft, A. J., and Brammer, J. G. (2002). A Techno-Economic Comparison of Power Production by Biomass Fast Pyrolysis with Gasification and Combustion. Renewable and Sustainable Energy Reviews. Vol. 6, Issue 3, pp. 181-246. DOI: 10.1016/S1364-0321(01)00010-7
[18] Pattiya, A. (2011). Bio-Oil Production Via Fast Pyrolysis of Biomass Residues from Cassava Plants in a Fluidised-Bed Reactor. Bioresource Technology. Vol. 102, Issue 2, pp. 1959-67. DOI: 10.1016/j.biortech.2010.08.117
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[21] Lanza, R., Dalle Nogare, D., and Canu, P. (2009). Gas Phase Chemistry in Cellulose Fast Pyrolysis. Industrial & Engineering Chemistry Research. Vol. 48, Issue 3, pp. 1391-1399. DOI: 10.1021/ie801280g
[22] Billaud, J., Valin, S., Peyrot, M., and Salvador, S. (2016). Influence of H2O, CO2 and O2 Addition on Biomass Gasification in Entrained Flow Reactor Conditions: Experiments and Modelling. Fuel. Vol. 166, pp. 166-178. DOI: 10.1016/j.fuel.2015.10.046
[23] Chutichai, B., Patcharavorachot, Y., Assabumrungrat, S., and Arpornwichanop, A. (2015). Parametric Analysis of a Circulating Fluidized Bed Biomass Gasifier for Hydrogen Production. Energy. Vol. 82, pp. 406-13. DOI: 10.1016/j.energy.2015.01.051