화학공학소재연구정보센터
International Journal of Multiphase Flow, Vol.20, No.3, 453-479, 1994
Phase Distribution and Turbulence Structure for Solid Fluid Upflow in a Pipe
The phase distribution and turbulence structure for solid/fluid upflow in a vertical pipe were investigated. Spherical particles, approximately 2 mm in diameter, were used and runs were made with particles having two different specific gravities. In particular, ceramic particles, which were heavier than water, and expanded polystyrene particles, which were lighter than water, were used. A new method is presented for the measurement of the volume fraction in solid/fluid two-phase flows using a laser-Doppler anemometer (LDA). The measured local time fractions obtained with the LDA must be corrected, because bias is produced by the presence of natural seeding, the finite size of the measurement volume and interruptions of the laser beams by the dispersed particles. An analytical method has been developed which accounts for these effects. A single-beam traversing gamma-ray densitometer was used as a reference against which to assess the volume fraction correction method. Good agreement between the corrected LDA and gamma-ray densitometer results was obtained. The volume fraction profiles show that at low flow rates the ceramic particles have an almost uniform distribution, while increasing the flow rate causes coring. In contrast, the phase distribution of the light polystyrene particles had wall peaking for both the low and high flow rates. However, wall peaking was flattened as liquid flow rate was increased.