Experiments were carried out in three-phase fluidized beds containing solid particles
contacted by upward co-current flow of air and water, to study flow patterns of gas-liquid-solid
systems.
The minimum fluidization velocity and the particle transport velocity in a gas-hquid-solid
mixture delineate the boundaries between three types of flow systems — fixed bed, fluidized bed
and transport flow. Both of these transition velocities were measured for a variety of particles. A
theoretical model, the Gas-Perturbed Liquid Model, was developed to predict the minimum liquid
fluidization velocity of a bed of solid particles in the presence of a fixed co-current superficial gas
velocity. This model, together with an appropriate equation for the gas holdup on a solids-free
basis, shows almost as good agreement with the present experimental data and those from the
literature as the best available empirical equation for the minimum hquid fluidization velocity at
low to intermediate superficial gas velocity, and has the advantage of correctly reducing to the
Wen-Yu equation for minimum two-phase fluidization as the superficial gas velocity goes to zero.
Two types of particle movement were observed as the superficial liquid velocity approaches the
particle transport velocity. For 1.2 mm steel shot, clusters of particles were found in both liquidsolid
and gas-hquid-solid systems. For 1.5 and 4.5 mm glass beads, on the other hand, no particle
clusters were observed. In the latter case, a mathematical model the Particle Transport Velocity
Model, was developed to predict the superficial hquid velocity for particle transport in upward
gas-hquid flow. An empirical correlation was also proposed for the transition from fluidized bed
to particle transport flow. Both predictions showed good agreement with experimental data
obtained in the present work and in the literature for a wide range of superficial gas velocities.
Within the fluidized bed, based on bubble characteristics, dispersed bubble flow, discrete
bubble flow, coalesced bubble flow, slug flow, churn flow, bridging flow and annular flow regimes were identified and characterized, at different combinations of gas and liquid superficial velocities.
These flow regimes were also observed for two-phase air-water systems.
A comprehensive measurement method using a conductivity probe was developed to
determine flow regime transitions based on bubble frequency, Sauter mean bubble chord length
and the time taken by a bubble to pass a given point. Criteria for determining flow regime
transitions were developed in an air-water two-phase system and then successfully applied to gasliquid-
solid three-phase fluidized beds. Flow regime maps were derived based on experimental
data for three different three-phase systems. As in two-phase gas-liquid systems, chum flow,
bridging flow and annular flow can be observed at high gas velocities in three-phase fluidized
beds. Empirical correlations were developed to predict the flow regime boundaries in the three phase
fluidized systems investigated. / Applied Science, Faculty of / Chemical and Biological Engineering, Department of / Graduate
| Identifer | oai:union.ndltd.org:UBC/oai:circle.library.ubc.ca:2429/6176 |
| Date | 11 1900 |
| Creators | Zhang, Junping |
| Source Sets | University of British Columbia |
| Language | English |
| Detected Language | English |
| Type | Text, Thesis/Dissertation |
| Format | 13417316 bytes, application/pdf |
| Rights | For non-commercial purposes only, such as research, private study and education. Additional conditions apply, see Terms of Use https://open.library.ubc.ca/terms_of_use. |
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