4.5 Article

Syngas production by chemical looping gasification of rice husk using Fe-based oxygen carrier

期刊

JOURNAL OF THE ENERGY INSTITUTE
卷 93, 期 4, 页码 1261-1270

出版社

ELSEVIER SCI LTD
DOI: 10.1016/j.joei.2019.11.009

关键词

Chemical looping gasification; Rice husk; Biomass; Oxygen carrier; Syngas

资金

  1. National Natural Science Foundation of China [51806068, 51706074]
  2. Guangdong Natural Science Foundation [2017A030310370]
  3. Guangzhou Science and Technology Project [201804010205]
  4. Guangdong Key Laboratory of Clean Energy Technology [2017B030314127]

向作者/读者索取更多资源

The chemical looping gasification (CLG) of rice husk was conducted in a fixed bed reactor to analyze the effects of the ratio of oxygen carrier to rice husk (O/C), temperature, residence time and preparation methods of Fe-based oxygen carriers. The yield of gas, H-2/CO, lower heating value of syngas (LHV), conversion efficiency and performance parameters were analyzed to obtain CLG reaction characterization and optimal reaction conditions. Results showed that when O/C increased from 0.5 to 3.0, the gas production, H-2/CO, CO2 yield and carbon conversion efficiency gradually increased, while the yield of H-2 , CO and CH4 and LHV gradually decreased. At the same time, a highest gasification efficiency was obtained when O/C was 1.5. As increasing temperature, the gas production, CO yield, carbon conversion efficiency and gasification efficiency gradually increased, while the yield of H-2 , CH4 and CO2 , H-2/CO and LHV gradually decreased. Sintering and agglomeration was obvious when the temperature was higher than 850 degrees C. When the reaction time increased from 10 min to 60 min, the gas production, CO yield, carbon conversion efficiency and gasification efficiency gradually increased, but the yield of H-2, H-2/CO and LHV decreased, among which 30 min was the best reaction residence time. In addition, coprecipitation was the best preparation method among several preparation methods of oxygen carrier. Finally, O/C of 1.5, 800 degrees C, 30 min and coprecipitation preparation method of oxygen carrier were the optimal parameters to obtain a gasification efficiency of 26.88%, H-2 content of 35.64%, syngas content of 56.40%, H-2/CO ratio of 1.72 and LHV of 12.25 MJ/Nm(3) . (C) 2019 Energy Institute. Published by Elsevier Ltd. All rights reserved.

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