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| Preface to the Fourth Edition | |
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| Preface to the Third Edition | |
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| Preface to the Second Edition | |
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| Preface to the First Edition | |
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| List of Symbols | |
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| Introduction | |
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| Conservation Principles | |
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| The Control Volume | |
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| Principle of Conservation of Mass | |
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| The Momentum Theorem | |
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| Principle of Conservation of Energy | |
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| Fluid Stresses and Flux Laws | |
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| Viscous Fluid Stresses | |
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| Fourier's Law of Heat Conduction | |
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| Fick's Law of Diffusion | |
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| Dimensionless Groups of Transport Properties | |
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| Turbulent-Flow Transport Coefficients | |
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| References | |
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| Differential Equations for the Laminar Boundary Layer | |
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| The Concept of the Boundary Layer | |
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| The Continuity Equations | |
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| The Momentum Equations | |
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| The Mass-Diffusion Equations | |
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| The Energy Equations | |
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| Problems | |
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| References | |
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| Integral Equations for the Boundary Layer | |
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| The Momentum Integral Equation | |
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| The Displacement and Momentum Thicknesses | |
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| Alternative Forms of the Momentum Integral Equation | |
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| The Energy Integral Equation | |
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| The Enthalpy and Conduction Thicknesses | |
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| Alternative Forms of the Energy Integral Equation | |
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| Problems | |
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| Reference | |
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| Differential Equations for the Turbulent Boundary Layer | |
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| Momentum and Thermodynamic Variables | |
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| Newtonian Stress and Fourier Heat-Flux Models | |
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| Instantaneous Equations of Turbulence | |
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| Reynolds Decomposition | |
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| Time-Averaging and Turbulence Statistics | |
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| Reynolds-Averaged Transport Equations of Turbulence | |
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| Problems | |
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| References | |
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| Laminar Internal Flows: Momentum Transfer | |
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| Fully Developed Laminar Flow in Circular Tubes | |
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| Fully Developed Laminar Flow in Other Cross-Sectional Shape Tubes | |
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| The Laminar Hydrodynamic Entry Length | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Laminar Internal Flows: Heat Transfer | |
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| The Energy Differential Equations for Flow through a Circular Tube | |
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| The Circular Tube with Fully Developed Velocity and Temperature Profiles | |
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| The Concentric Circular-Tube Annulus with Fully Developed Velocity and Temperature Profiles, Asymmetric Heating | |
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| Solutions for Tubes of Noncircular Cross Section with Fully Developed Velocity and Temperature Profiles | |
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| Circular-Tube Thermal-Entry-Length Solutions | |
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| Thermal-Entry-Length Solutions for the Rectangular Tube and Annulus | |
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| The Effect of Axial Variation of the Surface Temperature with Hydrodynamically Fully Developed Flow | |
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| The Effect of Axial Variation of Heat Flux | |
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| Combined Hydrodynamic and Thermal Entry Length | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Laminar External Boundary Layers: Momentum Transfer | |
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| Similarity Solutions: The Laminar Incompressible Boundary Layer with Constant Properties and Constant Free-Stream Velocity | |
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| Similarity Solutions for the Laminar Incompressible Boundary Layer for u[subscript infinity] = Cx[superscript m] | |
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| Similarity Solutions for the Laminar Incompressible Boundary Layer for v[subscript s] [not equal] 0 | |
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| Nonsimilar Momentum Boundary Layers | |
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| An Approximate Laminar Boundary-Layer Solution for Constant Free-Stream Velocity Developed from the Momentum Integral Equation | |
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| An Approximate Laminar Boundary-Layer Solution for Arbitrarily Varying Free-Stream Velocity over a Body of Revolution | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Laminar External Boundary Layers: Heat Transfer | |
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| Constant Free-Stream Velocity Flow along a Constant-Temperature Semi-Infinite Plate | |
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| Flow with u[subscript infinity] = Cx[superscript m] along a Constant-Temperature Semi-Infinite Plate | |
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| Flow along a Constant-Temperature Semi-Infinite Plate with Injection or Suction | |
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| Nonsimilar Thermal Boundary Layers | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Unheated Starting Length | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Arbitrarily Specified Surface Temperature | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Arbitrarily Specified Surface Heat Flux | |
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| Flow Over a Constant-Temperature Body of Arbitrary Shape | |
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| Flow Over a Body of Arbitrary Shape and Arbitrarily Specified Surface Temperature | |
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| Flow Over Bodies with Boundary-Layer Separation | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Turbulent External Boundary Layers: Momentum Transfer | |
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| Transition of a Laminar Boundary Layer to a Turbulent Boundary Layer | |
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| The Qualitative Structure of the Turbulent Boundary Layer | |
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| The Concepts of Eddy Diffusivity and Eddy Viscosity | |
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| The Prandtl Mixing-Length Theory | |
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| Wall Coordinates | |
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| The Law of the Wall for the Case of p[superscript +] = 0.0 and v[superscript + subscript s] = 0.0 | |
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| An Approximate Solution for the Turbulent Momentum Boundary Layer | |
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| A Continuous Law of the Wall: The Van Driest Model | |
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| Summary of a Complete Mixing-Length Theory | |
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| A Model Based on the Turbulence Kinetic Energy Equation | |
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| The [kappa]-[epsilon] Model | |
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| Equilibrium Turbulent Boundary Layers | |
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| The Transpired Turbulent Boundary Layer | |
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| The Effects of Surface Roughness | |
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| The Effects of Axial Curvature | |
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| The Effects of Free-Stream Turbulence | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Turbulent External Boundary Layers: Heat Transfer | |
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| The Concepts of Eddy Diffusivity for Heat Transfer, Eddy Conductivity, and Turbulent Prandtl Number | |
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| The Reynolds Analogy | |
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| Turbulent Prandtl Number | |
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| A Conduction Model for Turbulent Prandtl Number | |
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| Complete Solution of the Energy Equation | |
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| A Law of the Wall for the Thermal Boundary Layer | |
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| Effect of Pressure Gradient on Temperature Profiles | |
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| A Heat-Transfer Solution for Constant Free-Stream Velocity and Surface Temperature | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Unheated Starting Length | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Arbitrarily Specified Surface Temperature | |
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| Constant Free-Stream Velocity Flow along a Semi-Infinite Plate with Arbitrarily Specified Heat Flux | |
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| An Approximate Solution for Varying Free-Stream Velocity | |
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| Strongly Accelerated Boundary Layers | |
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| The Transpired Turbulent Boundary Layer | |
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| Full-Coverage Film Cooling | |
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| Film Cooling | |
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| The Effects of Surface Roughness | |
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| The Effects of Axial Curvature | |
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| The Effects of Free-Stream Turbulence | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Turbulent Internal Flows: Momentum Transfer | |
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| Fully Developed Flow in a Circular Tube | |
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| Tubes of Noncircular Cross Section | |
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| Effects of Surface Roughness | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Turbulent Internal Flows: Heat Transfer | |
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| Circular Tube with Fully Developed Velocity and Temperature Profiles, Constant Heat Rate, Prandtl Numbers 0.6-6.0 | |
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| Circular Tube with Fully Developed Flow, Higher Prandtl Numbers | |
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| Very Low-Prandtl-Number Heat Transfer, Liquid Metals | |
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| Circular Tube, Fully Developed Profiles, Constant Surface Temperature | |
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| Effect of Peripheral Heat-Flux Variation | |
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| Fully Developed Turbulent Flow between Parallel Planes and in Concentric Circular-Tube Annuli | |
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| Fully Developed Turbulent Flow in Other Tube Geometries | |
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| Experimental Correlations for Flow in Tubes | |
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| Thermal-Entry Length for Turbulent Flow in a Circular Tube | |
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| Thermal-Entry Length for Turbulent Flow between Parallel Planes | |
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| The Effects of Axial Variations of Surface Temperature and Heat Flux | |
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| Combined Hydrodynamic- and Thermal-Entry Length | |
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| The Influence of Surface Roughness | |
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| Problems | |
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| TEXSTAN Problems | |
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| References | |
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| Influence of Temperature-Dependent Fluid Properties | |
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| Laminar Flow in Tubes: Liquids | |
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| Laminar Flow in Tubes: Gases | |
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| Turbulent Flow in Tubes: Liquids | |
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| Turbulent Flow in Tubes: Gases | |
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| The Laminar External Boundary Layer: Gases | |
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| The Laminar External Boundary Layer: Liquids | |
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| The Turbulent External Boundary Layer: Liquids | |
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| The Turbulent External Boundary Layer: Gases | |
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| Problems | |
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| References | |
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| Convective Heat Transfer at High Velocities | |
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| The Stagnation Enthalpy Equation | |
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| The High-Velocity Thermal Boundary Layer for a Fluid with Pr = 1 | |
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| The Laminar Constant-Property Boundary Layer for Pr [not equal] 1 | |
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| The Laminar Boundary Layer for a Gas with Variable Properties | |
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| The Use of Reference Properties for High-Velocity Laminar Boundary-Layer Calculations | |
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| The Turbulent Boundary Layer for a Gas with Variable Properties | |
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| Reference Properties for High-Velocity Turbulent Boundary-Layer Calculations | |
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| Mach Number and Large-Temperature-Difference Corrections for Variable Free-Stream Velocity and Variable Temperature Differences | |
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| Problems | |
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| References | |
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| Convective Heat Transfer with Body Forces | |
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| Boundary-Layer Equations for Free Convection | |
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| Scaling and Flow Regimes in Free Convection | |
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| Similarity Solutions: Laminar Flow on a Constant-Temperature, Vertical, and Semi-Infinite Flat Plate | |
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| Similarity Solutions with Variable Surface Temperature | |
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| Similarity Solutions with Wall Suction or Blowing | |
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| Approximate Integral Solution: Laminar Flow on a Constant-Temperature, Vertical, and Semi-Infinite Flat Plate | |
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| The Effect of Variable Properties | |
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| Turbulent Flow on a Vertical and Semi-Infinite Flat Plate | |
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| Heat-Transfer Solutions for Other Geometries | |
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| Mixed Free and Forced Convection | |
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| Natural Convection in Enclosures | |
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| Problems | |
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| References | |
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| Convective Mass Transfer: Basic Definitions and Formulation of a Simplified Theory | |
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| Definitions | |
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| The Differential Equations of the Concentration Boundary Layer | |
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| Simplified Equations for the Concentration Boundary Layer | |
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| Boundary Conditions | |
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| Definition of the Mass-Transfer Conductance and Driving Force | |
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| Problems | |
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| References | |
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| Convective Mass Transfer: Evaluation of the Mass-Transfer Conductance from the Conserved-Property (P) Equation | |
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| The Prediction of the Mass-Transfer Conductance g for Low Mass-Transfer Rates | |
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| The Laminar Constant-Property Boundary Layer for Low Mass-Transfer Rates | |
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| The Turbulent Constant-Property Boundary Layer for Low Mass-Transfer Rates | |
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| The Prediction of the Mass-Transfer Conductance g for High Mass-Transfer Rates | |
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| High Mass-Transfer-Rate Convection in a Laminar Couette Flow | |
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| The Laminar Constant-Property Boundary Layer, Similarity Solutions for High Mass-Transfer Rates | |
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| The Laminar Boundary Layer for High Mass-Transfer Rates: Some Variable-Property Solutions | |
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| The Laminar Constant-Property Boundary Layer with Arbitrary Varying Free-Stream Velocity and High Mass-Transfer Rates | |
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| The Turbulent Constant-Property Boundary Layer with Constant Free-Stream Velocity and High Mass-Transfer Rates | |
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| The Turbulent Boundary Layer: Some Variable-Property Solutions | |
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| Problems | |
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| References | |
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| Convective Mass Transfer: Examples for Application of the Simplified Method | |
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| General Problem Solution Procedure | |
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| Thermodynamics of the Air-Water-Vapor System | |
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| Analysis of the Wet-Bulb Psychrometer | |
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| Drying | |
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| Evaporative Cooling | |
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| Naphthalene Sublimation from a Flat Plate | |
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| Burning of a Volatile Fuel in Air | |
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| Simple Graphite Burning in Air | |
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| Graphite Ablation with More than One Reaction | |
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| The High-Temperature Boundary Layer with Dissociation | |
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| Transpiration Cooling by Gas Injection | |
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| Problems | |
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| References | |
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| Property Values | |
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| Dimensions and Conversion to SI | |
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| Some Tables of Functions Useful in Boundary-Layer Analysis | |
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| Operations Implied by the [down triangle, open] Operator | |
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| Detailed Derivation of the Simplified Mass-Diffusion and Energy Equation (P Equation) for Convective Mass Transfer Problems and the Corresponding Boundary Conditions | |
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| The Texstan Boundary-Layer Code | |
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| Blasius Flow--A Sample Data Set for Texstan | |
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| Texstan Data Sets | |
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| Index | |