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    Convective Heat and Mass Transfer with Engineering Subscription Card

    ISBN-10: 0072990732
    ISBN-13: 9780072990737
    Author(s): William M. Kays, Michael E. Crawford, Bernhard Weigand
    Buy it from: $21.30
    This item will ship on Monday, December 29 .

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    List Price: $251.33
    Edition: 4th
    Publisher: McGraw-Hill Higher Education
    Binding: Mixed Media
    Pages: 576
    Size: 7.50" wide x 9.25" long x 1.00" tall
    Weight: 2.596
    Language: English

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

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