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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 | |