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- W2955273603 abstract "Bubbles play a significant role in the performance of the bubbling fluidized bed. By incorporating the CFD-DEM coupling model with heat transfer and chemical reactions, biomass gasification in the three-dimensional bubbling fluidized bed is numerically simulated to explore the bubble dynamics and the relationship between bubble phase and the resulting chemical reactions. After validating the numerical results, the spatial distribution, effect of operating parameters on the bubble characteristics, and the relationship between voidage and gas species concentration are discussed. Small bubbles at the bed bottom are elongated laterally. As the bubbles rise, they coalesce and enlarge, and the bubble rise velocity increases as the bubbles become more elongated axially. The reaction rates of the water–gas shift reaction and methane steam reaction are larger in the bubble phase, compared to oxidation reactions of H2, CH4, and CO. The mass concentrations of CH4, CO, CO2, and H2O in the bubble phase are higher than in the emulsion phase." @default.
- W2955273603 created "2019-07-12" @default.
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- W2955273603 date "2019-07-03" @default.
- W2955273603 modified "2023-10-16" @default.
- W2955273603 title "Numerical Investigation of Bubble Dynamics during Biomass Gasification in a Bubbling Fluidized Bed" @default.
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- W2955273603 doi "https://doi.org/10.1021/acssuschemeng.9b01628" @default.
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