Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed
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 ga...
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th-cmuir.6653943832-523222018-09-04T09:23:33Z Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed Thanasit Wongsiriamnuay Nattakarn Kannang Nakorn Tippayawong Chemical Engineering 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. © 2013 Thanasit Wongsiriamnuay et al. 2018-09-04T09:23:33Z 2018-09-04T09:23:33Z 2013-07-19 Journal 16878078 1687806X 2-s2.0-84880168042 10.1155/2013/297941 https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84880168042&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/52322 |
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Chemical Engineering Thanasit Wongsiriamnuay Nattakarn Kannang Nakorn Tippayawong Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
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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. © 2013 Thanasit Wongsiriamnuay et al. |
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Thanasit Wongsiriamnuay Nattakarn Kannang Nakorn Tippayawong |
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Thanasit Wongsiriamnuay Nattakarn Kannang Nakorn Tippayawong |
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Thanasit Wongsiriamnuay |
title |
Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
title_short |
Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
title_full |
Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
title_fullStr |
Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
title_full_unstemmed |
Effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
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effect of operating conditions on catalytic gasification of bamboo in a fluidized bed |
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2018 |
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https://www.scopus.com/inward/record.uri?partnerID=HzOxMe3b&scp=84880168042&origin=inward http://cmuir.cmu.ac.th/jspui/handle/6653943832/52322 |
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