• Title of article

    Dispersion of a particle-laden air jet in a confined rectangular crossflow

  • Author/Authors

    Yi، نويسنده , , J and Plesniak، نويسنده , , M.W، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2002
  • Pages
    11
  • From page
    168
  • To page
    178
  • Abstract
    Dispersion of a particle-laden air jet issuing into a confined rectangular crossflow has been studied experimentally by means of a planar light-scattering technique. Experiments were run for a jet injected at 24° to the crossflow, using three jet-to-crossflow velocity ratios (Vr=0.5, 1.0 and 1.5), five downstream measurement locations (x/D=7.5, 12, 16, 20, 25) and mass fractions (σ) of particles-to-jet air ranging from 3.5×10−2 to 1.8×10−1. Spherical particles with a mean diameter of dp=130–200 μm and material density ρp=1050 kg/m3 and nonspherical particles with a mean diameter of dp=200 μm and ρp=1200 kg/m3 were studied. The distribution of the 200-μm spherical particles downstream of the jet-crossflow intersection is more uniform than that of nonspherical particles, indicating that particle shape affects dispersion. The dispersion of both types of 200-μm particles in the crossflow is generally greater with increasing downstream distance. However, dispersion of 130-μm spherical particles becomes non-uniform with increasing downstream distance due to the action of a large-scale counter-rotating vortex pair. Dispersion of the particle-laden air jet in the crossflow is not greatly dependent on loading rate over the range of loadings studied. For both spherical and nonspherical particles, the penetration of particle-laden air jet issuing into the crossflow is greater than that of a single-phase air jet. Measurements of static pressure along the top of the main duct (crossflow) indicate that the effect of particles on the air-phase static pressure downstream of the jet-crossflow intersection is significant only for the higher particle loading rates.
  • Keywords
    Particle Dispersion , Jet-crossflow , Gas–solid flow , two-phase
  • Journal title
    Powder Technology
  • Serial Year
    2002
  • Journal title
    Powder Technology
  • Record number

    1691971