Cargando…

Gas fluidization /

This book is a much-needed fluidization handbook for practising engineers. There are few plants which do not have a fluid bed process operating somewhere on the site, yet engineers rarely have any formal training in the subject. College courses often emphasize academic issues rather than industrial...

Descripción completa

Detalles Bibliográficos
Clasificación:Libro Electrónico
Autor principal: Pell, Melvyn
Formato: Electrónico eBook
Idioma:Inglés
Publicado: Amsterdam ; New York : Elsevier, 1990.
Colección:Handbook of powder technology ; v. 8.
Temas:
Acceso en línea:Texto completo
Texto completo
Tabla de Contenidos:
  • Front Cover; Gas Fluidization; Copyright Page; Dedication; Acknowledgements; Preface; Table of Contents; Chapter 1. INTRODUCTION TO GAS FLUIDIZATION; 1.1 Introduction; 1.2 Regimes of Fluidization; 1.3 Effects of Particle Size and Density; 1.4 Effects of Gas Density and Viscosity; 1.5 References; Chapter 2. FIRST CALCULATIONS; 2.1 Average Particle Size; 2.2 Experimental Evaluation vs. Calculation; 2.3 Minimum Fluidization Velocity; 2.4 Minimum Bubbling Velocity; 2.5 Terminal Velocity; 2.6 Bed Expansion; 2.7 A Second Look at the Minimum Bubbling Condition; 2.8 Bed Pressure Drop; 2.9 References
  • Chapter 3. GAS DISTRIBUTOR DESIGN3.1 Functions of the Grid; 3.2 Grid Pressure Drop; 3.3 Hole Size and Number; 3.4 Jet Length; 3.5 Particle Attrition; 3.6 Grid Variations; 3.7 Grid Seals; 3.8 Plenum Design; 3.9 References; Chapter 4. BUBBLE GROWTH AND STABILITY; 4.1 Overview; 4.2 Bubble Growth; 4.3 Slugging; 4.4 Maximum Stable Bubble Size; 4.5 Effect of Bubble Size on Bed Expansion; 4.6 References; Chapter 5. MIXING AND SEGREGATION; 5.1 Solids Mixing; 5.2 Mechanism of Vertical Mixing; 5.3 Radial Mixing; 5.4 Diffusion Model for Solids and Gas Backmixing; 5.5 Segregation; 5.6 References
  • Chapter 6. HEAT TRANSFER6.1 Introduction; 6.2 Particle to Gas Heat Transfer; 6.3 Particle to Wall and Tube Heat Transfer; 6.4 Design Considerations for Tube Banks; 6.5 Radiation; 6.6 Heat Transfer by Entrained Solids; 6.7 References; Chapter 7. DRYING AND SOLVENT STRIPPING; 7.1 Introduction; 7.2 The Drying Curve; 7.3 Design Considerations; 7.4 Designing for Residence Time Effects; 7.5 Vibrated Bed Drying; 7.6 Vendor Assistance; 7.7 References; Chapter 8. ENTRAINMENT; 8.1 Introduction; 8.2 Particle Ejection from the Bed; 8.3 Transport Disengaging Height, TDH
  • 8.4 Correlations for Entrainment Above TDH8.5 Entrainment Below TDH; 8.6 References; Chapter 9. CHEMICAL REACTION MODELING; 9.1 Introduction; 9.2 Historical Background and Evolution of the Model; 9.3 Description of the Model; 9.4 Effect of Fines; 9.5 Grid Region Effects; 9.6 Freeboard Region; 9.7 Baffles; 9.8 References; Chapter 10. SCALE UP AND SCALE DOWN; 10.1 Introduction; 10.2 The Scaleup Sequence; 10.3 Large Scale Effects; 10.4 References; Chapter 11. DEFLUIDIZATION AND AGGLOMERATION; 11.1 Introduction; 11.2 Defluidization from Thermal Sintering; 11.3 Intentional Agglomeration
  • 11.4 ReferencesChapter 12. ATTRITION IN FLUIDIZED BEDS; 12.1 Attrition Fundamentals; 12.2 Time Effects on Attrition; 12.3 Attrition Tests; 12.4 Design Procedures; 12.5 Designing to Minimize Attrition; 12.6 References; Chapter 13. PHYSICAL FORCES; 13.1 Effect on Particles; 13.2 Effect on Internals; 13.3 Effect on the Vessel and Associated Equipment; 13.4 References; App A. UNITS AND SYMBOLS; A-1 SI Base Units and Prefixes; A-2 Derived SI Units with Special Names; A-3 Conversions from Non-SI Units; A-4 Universal Constants; A-5 Roman Font; A-6 Greek Font; A-7 Subscripts; INDEX