Parametric analysis of biomass fast pyrolysis in a downer fluidized bed reactor

Yassir Makkawi, Xi Yu, Raffaella Ocone

Research output: Contribution to journalArticle

Abstract

This study presents a theoretical parametric analysis of biomass fast pyrolysis in a downer reactor, as part of a dual fluidized bed system. The model framework uses a Eulerian-Eulerian CFD approach and incorporates a user-defined function (UDF) for the thermochemical conversion of biomass. The downer reactor consists of a novel gas-solid separator, which is employed to control the gas residence time within the reactor. The parameters investigated included the reactor temperature, the particle (heat carrier and biomass) size and the gas residence time. The product yield was found to be strongly dependent on the reactor temperature (varied through changing the heat carrier flow rate), intermediately dependent on the sweeping gas (N 2) flow rate and the sand particle size, and much less dependent on the biomass particle size (within the range of 1 mm diameter). The developed model and the results demonstrate the advantage and robustness of employing the model for parameters optimization and sensitivity investigation when dealing with complex multiphase flow reactive system. This conclusion will benefit future development and scale-up studies of downer reactors for biomass fast pyrolysis.

Original languageEnglish
Pages (from-to)1225-1234
Number of pages10
JournalRenewable Energy
Volume143
Early online date24 May 2019
DOIs
Publication statusE-pub ahead of print - 24 May 2019

Fingerprint

Fluidized beds
Biomass
Pyrolysis
Gases
Particle size
Flow rate
Multiphase flow
Separators
Computational fluid dynamics
Sand
Temperature
Hot Temperature

Keywords

  • Biomass
  • CFD
  • Downer reactor
  • Eulerian-Eulerian
  • Fast pyrolysis
  • Parametric analysis

ASJC Scopus subject areas

  • Renewable Energy, Sustainability and the Environment

Cite this

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abstract = "This study presents a theoretical parametric analysis of biomass fast pyrolysis in a downer reactor, as part of a dual fluidized bed system. The model framework uses a Eulerian-Eulerian CFD approach and incorporates a user-defined function (UDF) for the thermochemical conversion of biomass. The downer reactor consists of a novel gas-solid separator, which is employed to control the gas residence time within the reactor. The parameters investigated included the reactor temperature, the particle (heat carrier and biomass) size and the gas residence time. The product yield was found to be strongly dependent on the reactor temperature (varied through changing the heat carrier flow rate), intermediately dependent on the sweeping gas (N 2) flow rate and the sand particle size, and much less dependent on the biomass particle size (within the range of 1 mm diameter). The developed model and the results demonstrate the advantage and robustness of employing the model for parameters optimization and sensitivity investigation when dealing with complex multiphase flow reactive system. This conclusion will benefit future development and scale-up studies of downer reactors for biomass fast pyrolysis.",
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Parametric analysis of biomass fast pyrolysis in a downer fluidized bed reactor. / Makkawi, Yassir; Yu, Xi; Ocone, Raffaella.

In: Renewable Energy, Vol. 143, 12.2019, p. 1225-1234.

Research output: Contribution to journalArticle

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