Effect of the blend ratio on the co-gasification of biomass and coal in a bubbling fluidized bed with CFD-DEM

  • Juhui Chen*
  • , Shilin Zhong
  • , Dan Li*
  • , Chenxi Zhao
  • , Changliang Han
  • , Guangbin Yu
  • , Meiqi Song
  • *Corresponding author for this work

Research output: Contribution to journalArticlepeer-review

Abstract

Computational Fluid Dynamics-Discrete Element Method (CFD-DEM) is employed to describe the co-gasification of biomass and coal in bubbling fluidized bed coupled with chemical reaction kinetic model. Six sets of simulations are set up to study the effect of blend ratio on the amount of gasification products compared with experiments. The calorific value of syngas, carbon conversion efficiency, hydrogen conversion efficiency and cold gas efficiency are calculated. Compared with the separate gasification, the hydrogen efficiency and cold gas efficiency in the co-gasification are enhanced. When biomass accounts for 75%, the contents of CO gas and CO2 gas are the lowest, while the contents of H2 gas and CH4 gas are the highest. The high calorific value, carbon conversion efficiency and hydrogen conversion efficiency reach the maximum under this blend ratio. The cold gas efficiency is not obviously affected by the blend ratio, and reaches the maximum when the biomass content is 50%.

Original languageEnglish
Pages (from-to)22328-22339
Number of pages12
JournalInternational Journal of Hydrogen Energy
Volume47
Issue number53
DOIs
StatePublished - 26 Jun 2022
Externally publishedYes

UN SDGs

This output contributes to the following UN Sustainable Development Goals (SDGs)

  1. SDG 7 - Affordable and Clean Energy
    SDG 7 Affordable and Clean Energy

Keywords

  • Biomass/coal co-gasification
  • Blend ratio
  • Bubbling fluidized bed
  • CFD-DEM

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