Volume 49 Issue 12
Dec.  2021
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ZHANG Hai-feng, CHEN Lu, LIU Xian-yu, GE Hui-jun, SONG Tao, SHEN Lai-hong. Characteristics of cyanobacteria pyrolysis and gasification during chemical looping process with red mud oxygen carrier[J]. Journal of Fuel Chemistry and Technology, 2021, 49(12): 1802-1811. doi: 10.1016/S1872-5813(21)60087-7
Citation: ZHANG Hai-feng, CHEN Lu, LIU Xian-yu, GE Hui-jun, SONG Tao, SHEN Lai-hong. Characteristics of cyanobacteria pyrolysis and gasification during chemical looping process with red mud oxygen carrier[J]. Journal of Fuel Chemistry and Technology, 2021, 49(12): 1802-1811. doi: 10.1016/S1872-5813(21)60087-7

Characteristics of cyanobacteria pyrolysis and gasification during chemical looping process with red mud oxygen carrier

doi: 10.1016/S1872-5813(21)60087-7
Funds:  The project was supported by the National Natural Science Foundation of China (52076044, 52006108) and Natural Science Foundation of Jiangsu Province (BK20190707)
  • Received Date: 2021-03-16
  • Rev Recd Date: 2021-04-13
  • Available Online: 2021-04-30
  • Publish Date: 2021-12-29
  • The pyrolysis and gasification characteristics of pelletized cyanobacteria during chemical looping process with red mud oxygen carrier were investigated. The objective is to evaluate influence of red mud oxygen carrier on the pyrolysis and gasification behavior. In a fluidized bed reactor effects of reaction temperature (750−900 ℃) and oxygen carrier to fuel ratio (0.1−0.7) on syngas distribution, carbon conversion and its conversion rate, syngas content and ratio of H2/CO in syngas were investigated. The results indicate that the presence of oxygen carrier has remarkably positive effect on the pyrolysis and gasification processes. It improves pressure gradient caused by devolatilization of the sample. Consequently, the volatiles could be released gradually through the relatively developed channels. During chemical looping gasification H2 content in the syngas has the highest concentration of higher than 45%, followed by CO2, CH4 and CO. The increase of reaction temperature or oxygen carrier to fuel ratio leads to increase in carbon conversion. When reaction temperature increases from 750 to 950 ℃, ratio of H2/CO in the syngas decreases from 7.26 to 4.83. Meanwhile, with increasing oxygen carrier to fuel ratio, ratio of H2/CO first increases and then decreases, and the peak is 5.6 as oxygen carrier to fuel ratio is 0.5.
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