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A two-stage circulated fluidized bed process to minimize tar generation of biomass gasification for fuel gas production

Author

Listed:
  • Wang, Chao
  • Zhu, Lianfeng
  • Zhang, Mengjuan
  • Han, Zhennan
  • Jia, Xin
  • Bai, Dingrong
  • Duo, Wenli
  • Bi, Xiaotao
  • Abudula, Abuliti
  • Guan, Guoqing
  • Xu, Guangwen

Abstract

This study tested a two-stage circulated fluidized bed process consisting of a downer for pyrolysis of biomass and a riser for char gasification and tar removal to produce fuel gas containing tar below 100 mg/Nm3 from pine chips using steam-oxygen (not N2-oxygen) as the agent. A pilot facility treating 15 kg/h biomass was run at different equivalent ratios (ERs) and steam-to-biomass ratios (S/Bs). Under the typical conditions of S/B = 0.15 and ER = 0.3, the produced fuel gas contained (in volume) 21.64% CO, 21.97% CO2, 15.34% H2, 18.59% CH4, 1.49% CnHm and 1.83 g/Nm3db tar. A long-tern running of the pilot pant realized a tar content low as 95.5 mg/Nm3db in the produced gas. These results thus well verified the technology feasibility for low-tar biomass fuel production via the two-stage circulated fluidized bed steam-oxygen gasification.

Suggested Citation

  • Wang, Chao & Zhu, Lianfeng & Zhang, Mengjuan & Han, Zhennan & Jia, Xin & Bai, Dingrong & Duo, Wenli & Bi, Xiaotao & Abudula, Abuliti & Guan, Guoqing & Xu, Guangwen, 2022. "A two-stage circulated fluidized bed process to minimize tar generation of biomass gasification for fuel gas production," Applied Energy, Elsevier, vol. 323(C).
    • Handle: RePEc:eee:appene:v:323:y:2022:i:c:s0306261922009412
    DOI: 10.1016/j.apenergy.2022.119639
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    References listed on IDEAS

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    Cited by:

    1. Marco Mancini & Andreas Schwabauer, 2023. "On the Thermal Stability of a Counter-Current Fixed-Bed Gasifier," Energies, MDPI, vol. 16(9), pages 1-36, April.

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