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Catalytic Coal Gasification Process Simulation with Alkaline Organic Wastewater in a Fluidized Bed Reactor Using Aspen Plus

Author

Listed:
  • Xianbin Xiao

    (National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China)

  • Xueying Wang

    (National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China)

  • Zongming Zheng

    (National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China)

  • Wu Qin

    (National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China)

  • Yumengqiu Zhou

    (National Engineering Laboratory for Biomass Power Generation Equipment, North China Electric Power University, Beijing 102206, China)

Abstract

A co-gasification process was proposed both for treating alkaline organic wastewater and to promote coal gasification by the alkaline substances in situ. A catalytic gasification model was developed by introducing a catalytic correction factor to describe the catalytic effects quantitatively. An integrated process simulation was carried out using Aspen Plus equipped with FORTRAN subroutines. The model was verified using the root mean square error between the simulation results and experimental data from the literature. Syngas composition, cold gas efficiency, and carbon conversion efficiency were analyzed with respect to different operating conditions (reaction temperature, steam/coal ratio, and equivalence ratio). The optimal conditions are summarized based on a self-sufficient system by using sensitivity analysis: Gasification temperature of 700 °C, steam/coal ratio = 1.0, and equivalence ratio = 0.4.

Suggested Citation

  • Xianbin Xiao & Xueying Wang & Zongming Zheng & Wu Qin & Yumengqiu Zhou, 2019. "Catalytic Coal Gasification Process Simulation with Alkaline Organic Wastewater in a Fluidized Bed Reactor Using Aspen Plus," Energies, MDPI, vol. 12(7), pages 1-18, April.
    • Handle: RePEc:gam:jeners:v:12:y:2019:i:7:p:1367-:d:221251
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    References listed on IDEAS

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    1. Sharmina Begum & Mohammad G. Rasul & Delwar Akbar & David Cork, 2013. "An Experimental and Numerical Investigation of Fluidized Bed Gasification of Solid Waste," Energies, MDPI, vol. 7(1), pages 1-19, December.
    2. Pala, Laxmi Prasad Rao & Wang, Qi & Kolb, Gunther & Hessel, Volker, 2017. "Steam gasification of biomass with subsequent syngas adjustment using shift reaction for syngas production: An Aspen Plus model," Renewable Energy, Elsevier, vol. 101(C), pages 484-492.
    3. Jorge E. Preciado & John J. Ortiz-Martinez & Juan C. Gonzalez-Rivera & Rocio Sierra-Ramirez & Gerardo Gordillo, 2012. "Simulation of Synthesis Gas Production from Steam Oxygen Gasification of Colombian Coal Using Aspen Plus ®," Energies, MDPI, vol. 5(12), pages 1-17, November.
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    Cited by:

    1. Qiu, Jianhua & Wu, Fujun & Chen, Fangzhou & Huang, Weijia & Cai, Yezheng & Jiang, Juantao, 2022. "Entire process simulation and thermodynamic analysis of the catalytic gasification for synthetic natural gas from biomass," Energy, Elsevier, vol. 255(C).
    2. Marcin Dębowski & Magda Dudek & Marcin Zieliński & Anna Nowicka & Joanna Kazimierowicz, 2021. "Microalgal Hydrogen Production in Relation to Other Biomass-Based Technologies—A Review," Energies, MDPI, vol. 14(19), pages 1-27, September.

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