Single- and Two-Phase Flow Pressure Drop and Heat Transfer in Tubes

Preface
Acknowledgments
Contents
About the Author
Nomenclature
Part I: Single-Phase Flow Pressure Drop and Heat Transfer in Tubes
	Chapter 1: Introduction
		Background
		Need for Single-Phase Flow Study in the Transition Region
	Chapter 2: Single-Phase Flow Experimental Setup for Plain and Micro-fin Tubes
		Background
		Details of the Single-Phase Flow Experimental Setup
	Chapter 3: Effect of Inlet Configuration and Heating on Plain Tube Friction Factor
		Background
		Fully Developed Friction Factor
		Entrance and Fully Developed Friction Factors
	Chapter 4: Proposed Correlations for Laminar and Transition Friction Factors in Plain Tubes with Different Inlet Configurations
		Background
		Laminar Region
		Transition Region
		An Illustrative Example
	Chapter 5: Heat Transfer Results in Plain Tubes with Different Inlet Configurations
		Background
		Effect of Inlet Configuration on Plain Tube Heat Transfer
		Effect of Buoyancy (Secondary Flow) on Plain Tube Heat Transfer Coefficient
		Variation of Local Nusselt Number Along the Plain Tube with Different Inlet Configuration in Different Flow Regimes
		Simultaneous Heat Transfer and Friction Factor for Plain Tube with Different Inlet Configurations
	Chapter 6: Proposed Correlations and Flow Regime Map for Laminar, Transition, and Turbulent Heat Transfer in Plain Tubes with ...
		Background
		Proposed Correlations for All Flow Regimes
		Flow Regime Map for Forced and Mixed Convection
		An Illustrative Example
	Chapter 7: Friction Factor Results for Micro-fin Tubes
		Background
		Effect of Inlet Configuration and Heating on Micro-fin Tubes´ Fully Developed Friction Factors
		Effect of Inlet Configuration and Heating on Micro-fin Tubes´ Entrance and Fully Developed Friction Factors
		Effect of Fin Geometry of Micro-fin Tubes on Friction Factor
		Effect of Change in Spiral Angle on Friction Factor
		Effect of Change in Fin Height-to-Diameter Ratio on Friction Factor
		Effect of Change in Number of Starts on Friction Factor
	Chapter 8: Proposed Correlations for Laminar, Transition, and Turbulent Friction Factors in Micro-fin Tubes with Different Inl...
		Background
		Laminar Region
		Transitional Region
		Turbulent Region
	Chapter 9: Heat Transfer Results in Micro-fin Tubes
		Background
		Effect of Inlet Configuration and Buoyancy on Micro-fin Tubes´ Heat Transfer
		Effect of Fin Geometry of Micro-fin Tubes on Heat Transfer
		Effect of Change in Spiral Angle on Heat Transfer
		Effect of Change in Fin Height-to-Diameter Ratio on Heat Transfer
		Effect of Change in Number of Starts on Heat Transfer
		Simultaneous Heat Transfer and Friction Factor for Micro-fin Tubes with Different Inlet Configurations
	Chapter 10: Proposed Correlations for Laminar, Turbulent, and Transition Heat Transfer in Micro-fin Tubes with Different Inlet...
		Background
		Laminar Region
		Turbulent Region
		Transition Region
	Chapter 11: Friction Factor in the Transition Region of Mini- and Micro-tubes
		Background
		Details of the Single-Phase Flow Pressure Drop Experimental Setup for Mini- and Micro-tubes
		Effect of Mini- and Micro-tube Diameter on the Start and End of the Transition Region of the Friction Factor: The Work of Ghaj...
		A Brief Summary of the Extensions to the Work of Ghajar et al. (2010)
Part II: Two-Phase Flow Pressure Drop and Heat Transfer in Tubes
	Chapter 12: Introduction
		Background
		Need of Two-Phase Flow Study in Inclined Systems
		Basic Definitions in Gas-Liquid Two-Phase Flow
	Chapter 13: Two-Phase Flow Experimental Setup for Inclined Systems
		Background
		Details of the Two-Phase Flow Experimental Setup
	Chapter 14: Flow Patterns, Flow Pattern Maps, and Flow Pattern Transition Models
		Background
		Flow Patterns
		Flow Pattern Maps
		Flow Pattern Transitions
	Chapter 15: Void Fraction
		Background
		Effect of Pipe Orientation on Void Fraction
		Effect of Phase Flow Rates on Void Fraction
		Effect of Fluid Properties on Void Fraction
		Effect of Pipe Diameter on Void Fraction
		Modeling of Void Fraction
		An Illustrative Example
	Chapter 16: Pressure Drop
		Background
		Effect of Pipe Orientation on Pressure Drop
		Effect of Phase Flow Rates on Pressure Drop
		Effect of Pipe Diameter on Pressure Drop
		Effect of Fluid Properties on Pressure Drop
		Effect of Surface Roughness on Pressure Drop
		Pressure Gradient Minimum and Flow Reversal in Upward Inclined Flow
		Two-Phase Pressure Drop Modeling
		An Illustrative Example
	Chapter 17: Modeling of Stratified Flow
		Background
		Taitel and Dukler (1976) Model
		Apparent Rough Surface Model
		Double Circle Model
		An Illustrative Example
	Chapter 18: Entrainment
		Background
		Entrainment Mechanisms
		Liquid Entrainment Fraction Correlations
		An Illustrative Example
	Chapter 19: Modeling of Annular Flow
		Background
		Triangular Relationship in Annular Flow
		An Illustrative Example
	Chapter 20: Non-boiling Two-Phase Heat Transfer
		Background
		Effect of Pipe Inclination and Phase Flow Rates on Heat Transfer Coefficient
		Circumferential Variation of Heat Transfer Coefficient with Pipe Inclination
		Modeling of Non-boiling Two-Phase Heat Transfer
		Application of Reynolds Analogy to Non-boiling Two-Phase Heat Transfer
		An Illustrative Example
References
Index