Fundamentals of Convective Heat Transfer

Cover
Half Title
Title Page
Copyright Page
Table of Contents
Authors
Preface
Acknowledgments
CHAPTER 1: Preliminary Concepts and Basic Equations
	1.1 REYNOLDS TRANSPORT THEOREM
	1.2 COMPRESSIBLE AND INCOMPRESSIBLE FLOWS
	1.3 ENERGY EQUATION USING SPECIFIC COORDINATE SYSTEM
	1.4 GENERALIZED APPROACH FOR DERIVATION OF ENERGY EQUATION
	1.5 IMPORTANT DIMENSIONLESS NUMBERS
	1.6 BOUNDARY LAYERS
		1.6.1 Velocity Boundary Layer
		1.6.2 Thermal Boundary Layer
		1.6.3 More about Velocity Boundary Layer and Thermal Boundary Layer
		1.6.4 Steady Flow over Flat Plate
		1.6.5 Derivation of the Equation for Thermal Boundary Layer
	1.7 IMPORTANT DEFINITIONS
	1.8 PRANDTL NUMBER AND RATIO OF BOUNDARY LAYERS
CHAPTER 2: External Flows
	2.1 BLASIUS SOLUTION
	2.2 TEMPERATURE DISTRIBUTION OVER FLAT PLATE BOUNDARY LAYER
	2.3 ANALYTICAL SOLUTION FOR . = 0
	2.4 MORE DISCUSSIONS ON SOLUTION VIA NUMERICAL ROUTE
	2.5 APPROXIMATE METHODS FOR FLAT PLATE BOUNDARY LAYER
	2.6 VISCOUS DISSIPATION EFFECTS ON LAMINAR BOUNDARY LAYER FLOW OVER FLAT PLATE
	2.7 MORE ABOUT SIMILARITY SOLUTION (VELOCITY BOUNDARY LAYER)
		2.7.1 Derivation of Falkner Skan Equation
	2.8 MORE ABOUT SIMILARITY SOLUTION OF ENERGY EQUATION
	2.9 APPROXIMATE METHOD FOR BOUNDARY LAYER FLOWS OVER NON-ZERO PRESSURE GRADIENT SURFACES
	2.10 EFFECT OF PRESSURE GRADIENT ON EXTERNAL FLOWS
	2.11 DESCRIPTION OF FLOW PAST CIRCULAR CYLINDER
	2.12 EXPERIMENTAL RESULTS FOR CIRCULAR CYLINDER FLOW
	2.13 OTHER IMPORTANT CORRELATIONS
CHAPTER 3: Internal Flows
	3.1 ENTRY FLOW IN DUCT
	3.2 VELOCITY PROFILE IN FULLY DEVELOPED PIPE FLOW
	3.3 THERMAL CONSIDERATIONS DURING INTERNAL FLOWS
		3.3.1 Newton’s Law of Cooling for Internal Flows
		3.3.2 Fully Developed Thermal Conditions
		3.3.3 Energy Balance in Ducted Flows
	3.4 LAMINAR FLOW IN CIRCULAR TUBE
		3.4.1 Heat Transfer through Circular Tube for Hydrodynamically and Thermally Developed Flow with Uniform Wall Heat Flux (UHF) Condition
		3.4.2 Heat Transfer through Circular Tube for Thermally Fully Developed Laminar Slug Flow with Uniform Wall Temperature (UWT) Condition
		3.4.3 Heat Transfer in Circular Tube for Hydrodynamically and Thermally Developed Flow with Uniform Wall Temperature (UWT) Condition
		3.4.4 Calculation of Nusselt Number for UWT
	3.5 GRAETZ PROBLEM
	3.6 SUMMARY OF SOLUTIONS FOR VARIOUS FLOW AND HEAT TRANSFER SITUATIONS IN PIPE FLOWS
	3.7 HEAT TRANSFER IN COUETTE FLOW
	3.8 CONVECTION CORRELATIONS FOR NON-CIRCULAR TUBES
CHAPTER 4: Solution of Complete Navier–Stokes and Energy Equations for Incompressible Internal Flows
	4.1 INTRODUCTION
	4.2 SOLUTION OF NAVIER STOKES EQUATIONS IN CARTESIAN COORDINATE
		4.2.1 Staggered Grid
		4.2.2 Introduction to MAC method
	4.3 SOLUTION OF ENERGY EQUATION IN CARTESIAN COORDINATE
		4.3.1 Solution Procedure
		4.3.2 Flow Chart
CHAPTER 5: Fluid Flow Solutions in Complex Geometry
	5.1 INTRODUCTION
	5.2 BOUNDARY-FITTED MESHES
	5.3 MAPPING
	5.4 COORDINATE TRANSFORMATION RELATIONS
	5.5 GOVERNING EQUATIONS IN BOUNDARY-FITTED COORDINATE SYSTEMS
	5.6 DISCRETIZATION
	5.7 STEADY CALCULATION USING PSEUDO-TRANSIENT
	5.8 NON-ORTHOGONAL PRESSURE CORRECTION EQUATION
	5.9 BOUNDARY CONDITIONS
CHAPTER 6: Turbulent Flow and Heat Transfer
	6.1 INTRODUCTION
	6.2 CLASSICAL IDEALIZATION OF TURBULENT FLOWS
	6.3 REYNOLDS AVERAGED FORM OF ENERGY EQUATION
	6.4 PRANDTL’S MIXING LENGTH
	6.5 UNIVERSAL VELOCITY PROFILE (ON FLAT PLATE)
	6.6 LAW OF THE WALL AND IMPACT OF PRESSURE GRADIENT
	6.7 TURBULENT HEAT TRANSFER IN PIPE (SIMPLIFIED ANALYSIS )
	6.8 COMPUTATIONAL APPROACH AND .-e MODEL OF TURBULENCE
		6.8.1 k-. Model
		6.8.2 Special Features of Near Wall Flow
		6.8.3 Near Wall Treatment in Transport Equation based Models
	6.9 RNG k-e MODEL AND KATO-LAUNDER MODEL
	6.10 SUMMARY
CHAPTER 7: Free Convection
	7.1 INTRODUCTION
	7.2 FREE CONVECTION OVER VERTICAL FLAT PLATE
		7.2.1 Heat transfer coefficient
	7.3 VERTICAL CYLINDER
	7.4 PLUMES
		7.4.1 Integral Analysis of Steady Plume
	7.5 MIXED CONVECTION IN RECTANGULAR CHANNEL
	7.6 MIXED CONVECTION INCLUDING BUOYANCY AIDED AND BUOYANCY DRIVEN FLOWS
CHAPTER 8: Introduction to Boiling
	8.1 POOL BOILING
		8.1.1 Boiling Regimes
	8.2 NUCLEATION AND BUBBLE GROWTH
		8.2.1 Homogeneous Nucleation
		8.2.2 Heterogeneous Nucleation
		8.2.3 Waiting Period
		8.2.4 Bubble Growth without Heat or Mass Transfer
		8.2.5 Dynamics of Bubble Growth on Wall
		8.2.6 Bubble Growth with Heat and Mass Transfer
	8.3 BUBBLE DEPARTURE DIAMETER AND RELEASE FREQUENCY
	8.4 BUBBLE MERGER AND TRANSITION FROM PARTIAL TO FULLY DEVELOPED NUCLEATE BOILING
	8.5 BUBBLE SITE DENSITY
	8.6 HEAT TRANSFER MECHANISMS
	8.7 PARTIAL NUCLEATE BOILING
	8.8 FULLY DEVELOPED NUCLEATE BOILING
CHAPTER 9: Maximum and Minimum Heat Fluxes, Film and Transition Boiling
	9.1 TAYLOR INSTABILITY
	9.2 INSTABILITYOF PLANE INTERFACE BETWEEN TWO PARALLEL FLOWING STREAMS
	9.3 MAXIMUM HEAT FLUX
	9.4 MINIMUM HEAT FLUX
	9.5 FILM BOILING HEAT TRANSFER COEFFICIENT
	9.6 TRANSITION BOILING
CHAPTER 10: Laminar Film Condensation
	10.1 CONDENSATION ON PLANE AND AXISYMMETRIC BODIES
	10.2 GENERALIZED SPARROW AND GREGG SOLUTION
		10.2.1 Vertical Plate
	10.3 SYNCHONOUSLY ROTATING PLATE
		10.3.1 Limitations on Similarity Solution for Curved Surfaces Shown in Fig. 10.2
Index