Fluid Particle Technology: Analysis and ApplicationsAlan Wesley Weimer |
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Page 8
... region of decreased particle concentration has developed , in the neighborhood of which there is a closed vortex in the fluid flow field . Though the particle streamlines have not been shown , their velocity is directed downward ...
... region of decreased particle concentration has developed , in the neighborhood of which there is a closed vortex in the fluid flow field . Though the particle streamlines have not been shown , their velocity is directed downward ...
Page 61
... region are not physically realisable . Calculations using the Wake flow field , which simulates a hypothetical wake region , show almost identical trajectories upstream of the cylinder , as the wake has little effect on the flow field ...
... region are not physically realisable . Calculations using the Wake flow field , which simulates a hypothetical wake region , show almost identical trajectories upstream of the cylinder , as the wake has little effect on the flow field ...
Page 63
... region was predicted in front of the cylinder for all cases , except for upflows at the lowest stream velocities . For the upflow cases the depth of the bubble - free region increased as the stream velocity increased , and decreased ...
... region was predicted in front of the cylinder for all cases , except for upflows at the lowest stream velocities . For the upflow cases the depth of the bubble - free region increased as the stream velocity increased , and decreased ...
Contents
Foreword | 1 |
Expansion Behavior of Gas Fluidized Beds in the Turbulent Regime | 31 |
The Introduction and Measurement of Rheological Parameters for the Characterization of Emulsion Phase | 45 |
Copyright | |
7 other sections not shown
Common terms and phrases
added mass annulus Auton average axial bed expansion bed voidage behavior bottom zone bubble trajectories calculated carbon centrifugal fluidized bed char Chem circulating fluidized bed coefficient combustion crossing cylinder dense phase density Diatomaceous earth dimensional distributor drag coefficient effect emulsion phase equations of motion fast bed flow field fluid Fluidized Bed Combustion fluidized bed reactor furnace gas and solids gas fluidized beds Geldart glass beads H₂ increase interparticle force Jaraiz kg/m³ MAJFM measured method minimum fluidization Multiphase Flow Odar packed bed parameters phase-space trajectories potential flow predicted radial profiles reaction recirculation zone region Reynolds number riser shown in Figure shows silicon nitride slip velocity slugging solids concentration solids volume concentration solution soot sorbent splash zone spray zone superficial gas velocity temperature terminal velocity tracer turbulent bed Unconverted H2S upflow values variation vibration Werther zeolite