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Fluidized bed reactor (FINEX R1)

Case Description

  • 1/2 Sector with internal cyclones for reducing computational load

Computational Mesh

  • ½ sector mesh for 2.2 million structured cells

Operating Condition​

  • ·  Volumetric gas flow rate : 450,000 Nm3/hr
  • ·  Gas flow rate of CPU : 0.9 kg/s
  • ·  Total mass inside reactor : 615 ton
  • ·  Particle density : 5000 kg/m3

Physical Models

  • Turbulence Model : Standard k-ε model
  • Particle motion : MP-PIC method (Multiphase Particle-in-Cell)

Results

  • Instantaneous images of gas volume fraction

  • Instantaneous images of particle inside cyclone