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The article contains sections titled: 1. Introduction 2. Bubble Columns 2.1. Design and Applications 2.2. Gas Distribution 2.3. Flow Regimes 2.4. Bubble Size 2.5. Bubble Rise Velocity 2.6. Axial Dispersion 2.7. Gas Holdup 2.8. Specific Interfacial Area 2.9. Mass Transfer 2.10. Heat Transfer 2.11. Fluid Dynamics 3. Airlift Loop Reactors 3.1. Design and Applications 3.2. Mixing Behavior and Fluid Dynamics 3.3. Gas Holdup 3.4. Mass Transfer and Mixing 3.5. Heat Transfer 3.6. Computational Fluid Dynamics
The article contains sections titled: 1. Introduction 2. Bubble Columns 2.1. Design and Applications 2.2. Gas Distribution 2.3. Flow Regimes 2.4. Bubble Size 2.5. Bubble Rise Velocity 2.6. Axial Dispersion 2.7. Gas Holdup 2.8. Specific Interfacial Area 2.9. Mass Transfer 2.10. Heat Transfer 2.11. Fluid Dynamics 3. Airlift Loop Reactors 3.1. Design and Applications 3.2. Mixing Behavior and Fluid Dynamics 3.3. Gas Holdup 3.4. Mass Transfer and Mixing 3.5. Heat Transfer 3.6. Computational Fluid Dynamics
Correspondence concerning this paper should be addrmed to Pio Farzatti. deactivation kinetics, so that they cannot be taken as conclusive evidence of nonseparability. It appears also that the separable representation provides a systematic overestimation of activity. These mults have been related to their chemical causes, and are expected to apply as well to other reacting systems exhibiting similar chemical behavior. Finally, TPD has proven to be a suitable technique for studying the separability of reaction-deactivation kinetics.
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