Gas-liquid-solid fluidization engineering
This book provides a comprehensive mechanistic interpretation of the transport phenomena involved in various basic modes of gas-liquid-solid fluidization. These modes include, for example, those for three-phase fluidized beds, slurry columns, turbulent contact absorbers, and three-phase fluidized beds, slurry columns, turbulent contact absorbers, and three-phase transport. It summarizes the empirical correlations useful for predicting transport properties for each mode of of operation. Gas-Liquid-Solid Fluidization Engineering provides a comprehensive account of the state-of-the-art applications of the three-phase fluidization systems that are important in both small-and large-scale operations. These applications include fermentation, biological wastewater treatment, flue gas desulfurization and particulates removal, and resid hydrotreating. This book highlights the industrial implications of these applications. In addition, it discusses information gaps and future directions for research in this field.
69 pages matching flow rate in this book
Results 1-3 of 69
What people are saying - Write a review
We haven't found any reviews in the usual places.
Classification and Significance
5 Countercurrent and LiquidBatch Fluidized Bed Systems
Hydrodynamics of Cocurrent Upward Fluidized Bed Systems
12 other sections not shown
activated carbon adipic acid AIChE axial dispersion coefficient bed expansion bed height bed porosity behavior biofilm bioreactor Biotech bubble rise velocity bubble wake catalyst Chem cm/s coalesced bubble regime contact angle correlation decreases density dispersed bubble regime distribution distributor DTFB ebullated effects equation Figure fixed bed flow rate flow regime Fukuma gas and liquid gas holdup gas phase gas-liquid mass transfer gas-liquid-solid fluidized bed glass beads heat transfer coefficient hydrodynamic immobilized cell interfacial area Japan liquid flow liquid holdup liquid phase liquid velocity liquid-solid fluidized bed mass transfer coefficient Mode Muroyama operation Ostergaard overall oxygen packed bed Peclet Peclet number phase holdups porosity pressure drop primary wake radial reaction Reynolds number shown in Fig slurry bubble column solids concentration solids holdup solids mixing substrate surface tension surfactant temperature terminal velocity three-phase fluidized bed two-phase volumetric vortex vortices wake model