دسترسی نامحدود
برای کاربرانی که ثبت نام کرده اند
برای ارتباط با ما می توانید از طریق شماره موبایل زیر از طریق تماس و پیامک با ما در ارتباط باشید
در صورت عدم پاسخ گویی از طریق پیامک با پشتیبان در ارتباط باشید
برای کاربرانی که ثبت نام کرده اند
درصورت عدم همخوانی توضیحات با کتاب
از ساعت 7 صبح تا 10 شب
ویرایش: 3
نویسندگان: S. P. Venkateshan
سری:
ISBN (شابک) : 9783030583378, 9789385462078
ناشر: Springer
سال نشر: 2021
تعداد صفحات: 1026
زبان: English
فرمت فایل : PDF (درصورت درخواست کاربر به PDF، EPUB یا AZW3 تبدیل می شود)
حجم فایل: 24 مگابایت
در صورت تبدیل فایل کتاب Heat Transfer به فرمت های PDF، EPUB، AZW3، MOBI و یا DJVU می توانید به پشتیبان اطلاع دهید تا فایل مورد نظر را تبدیل نمایند.
توجه داشته باشید کتاب انتقال حرارت نسخه زبان اصلی می باشد و کتاب ترجمه شده به فارسی نمی باشد. وبسایت اینترنشنال لایبرری ارائه دهنده کتاب های زبان اصلی می باشد و هیچ گونه کتاب ترجمه شده یا نوشته شده به فارسی را ارائه نمی دهد.
Preface to the Springer Edition Preface to the Second Edition Acknowledgements Contents About the Author Nomenclature Latin Alphabet Symbols Greek Symbols Subscripts 1 Introduction to the Study of Heat Transfer 1.1 Introduction 1.2 Basic Assumptions in the Study of Heat Transfer 1.3 Basic Heat Transfer Processes and Examples 1.3.1 Basic Definitions 1.4 Exercises 2 Steady Conduction in One Dimension 2.1 Preliminaries 2.1.1 On Thermal Conductivity Values 2.1.2 Approaches to the Study of Conduction Heat Transfer 2.2 Steady One Dimensional Conduction 2.2.1 One-Dimensional Conduction in a Uniform Area Bar 2.2.2 Steady One-Dimensional Conduction in Cylindrical Coordinates 2.2.3 Steady Radial Conduction in a Solid Cylinder with Internal Heat Generation 2.2.4 One-Dimensional Radial Conduction in Spherical Coordinates 2.3 Generalization 2.4 Exercises 3 Unsteady Heat Transfer in Lumped Systems 3.1 Preliminaries 3.2 Governing Equation and the General Solution 3.2.1 Governing Equation 3.2.2 Electrical Analogy 3.2.3 Characteristic Length Scale 3.2.4 General Solution 3.2.5 Response of a First-Order System in Particular Cases 3.3 Second-Order Thermal System: Response to Step Input 3.4 Exercises 4 Heat Transfer from Extended Surfaces 4.1 Introduction 4.2 Fins of Uniform Area 4.2.1 Analysis 4.2.2 Solution to the Fin Equation 4.2.3 Uniform Area Fin Subject to Third Kind Boundary Condition at the Tip 4.3 Variable Area Fins 4.3.1 General Analysis of Variable Area Fins 4.3.2 Particular Cases of Variable Area Fins 4.4 Fins of Minimum Mass 4.4.1 Uniform Fin of Optimum Proportions 4.4.2 Uniform Spine (pin Fin) of Optimum Proportions 4.5 Heat Transfer from Fin Arrays 4.5.1 Overall Surface Efficiency of a fin array 4.5.2 Effectiveness of a Fin Array 4.5.3 Fin Array Applications 4.6 Exercises 5 Multidimensional Conduction Part I 5.1 Introduction 5.1.1 Integral Form of Governing Equation 5.1.2 Differential Form of Governing Equation 5.1.3 Simplified Form of Energy Equation 5.1.4 Thermal Diffusivity 5.2 One-Dimensional Transient Conduction 5.2.1 Transients in a Semi-infinite Solid 5.2.2 Approximate Integral Method Due to Goodman 5.2.3 One-Dimensional Transient Problem: Space Domain Finite 5.3 Steady Conduction in Two Dimensions 5.3.1 Steady Conduction in a Rectangle 5.3.2 Steady Conduction in a Rectangle With Heat Generation 5.3.3 Steady Two-Dimensional Conduction in Cylindrical Co-Ordinates 5.3.4 Shape Factors for Some Useful Configurations 5.3.5 Solution to Laplace Equation in a Cylinder 5.3.6 Solution to a Practical Problem 5.3.7 Solution to Laplace Equation in Spherical Co-ordinates 5.4 Exercises 6 Multidimensional Conduction Part II 6.1 Preliminaries 6.1.1 Introduction 6.1.2 Basic Problem in Cartesian Coordinates 6.1.3 Basic Problem in Cylindrical Coordinates 6.1.4 Basic Problem in Spherical Co-Ordinates 6.2 One-Term Approximation and Heisler Charts 6.3 Transient Conduction in More Than One Dimension 6.3.1 Introduction 6.3.2 Transient Conduction in an Infinitely Long Rectangular Bar 6.3.3 Transient Heat Conduction in a Rectangular Block in the form of a brick 6.3.4 Transient Heat Conduction in a Circular Cylinder of Finite Length 6.4 Exercises 7 Numerical Solution of Conduction Problems 7.1 Introduction 7.1.1 A Simple Example: One-Dimensional Steady Conduction 7.1.2 Numerical Solution of a Fin Problem 7.1.3 Solution of Nodal Equations by TDMA 7.1.4 Steady Radial Conduction in a Cylinder 7.1.5 Steady Radial Conduction in a Spherical Shell 7.2 Conduction in Two Dimensions 7.2.1 Steady Heat Conduction in Two Dimensions: Cartesian Coordinates 7.2.2 Steady Heat Conduction in Two Dimensions: Cylindrical Coordinates 7.2.3 One-Dimensional Transient in a Bar 7.2.4 Transient Heat Transfer in a Conducting Convecting Fin 7.2.5 One-Dimensional Transient in a Solid Cylinder 7.2.6 One-Dimensional Transient in a Solid Sphere 7.3 Transient Conduction in Two and Three Dimensions 7.3.1 Transient Conduction in a Rectangle: Explicit Formulation 7.3.2 ADI Method 7.3.3 Modification of the ADI Method for Three Dimensional Transient Conduction 7.4 Exercises 8 Basics of Thermal Radiation 8.1 Introduction 8.1.1 Fundamental Ideas 8.1.2 Preliminaries and Definitions 8.2 Cavity or Black Body Radiation 8.2.1 Basic Ideas 8.2.2 Thermodynamics of Black Body Radiation 8.3 Wavelength Distribution of Black Body Radiation 8.3.1 About Waves 8.3.2 Number of Degenerates Modes in a Three-Dimensional Cavity 8.3.3 Planck Distribution 8.3.4 Properties of the Planck Distribution Function 8.4 Exercises 9 Surface Radiation 9.1 Introduction 9.1.1 Surface Types 9.2 Spectral and Hemispherical Surface Properties 9.2.1 Spectral Hemispherical Quantities 9.2.2 Total Hemispherical Quantities 9.2.3 Band Model for a Non-gray Surface 9.2.4 Equilibrium Temperature of a Surface 9.2.5 Selective Surfaces 9.3 Angle-Dependent Surface Properties 9.3.1 Some Results from Electromagnetic Theory 9.3.2 Specular Surface 9.3.3 Hemispherical Reflectance 9.3.4 Real or Engineering Surfaces 9.4 Exercises 10 Radiation in Enclosures 10.1 Introduction 10.2 Evacuated Enclosure with Gray Diffuse Walls 10.2.1 Assumptions 10.2.2 Diffuse Radiation Interchange Between Two Surfaces 10.2.3 Angle Factor Algebra and Its Applications 10.2.4 Three-Dimensional Enclosures 10.3 Radiation Heat Transfer in Enclosures with Gray Diffuse Walls 10.3.1 Method of Detailed Balancing 10.3.2 Radiation Shields 10.3.3 Radiosity Irradiation Method of Enclosure Analysis 10.3.4 Electrical Analogy 10.4 Enclosure Analysis Under Special Circumstances 10.4.1 Enclosure Containing Diffuse Non-gray Surfaces 10.4.2 Gray Enclosures Containing Diffuse and Specular Surfaces 10.4.3 Enclosure Analysis with Surfaces of Non-uniform Radiosity 10.5 Exercises 11 Radiation in Participating Media 11.1 Introduction 11.2 Preliminaries 11.2.1 Definitions 11.2.2 Equation of Transfer 11.3 Absorption of Radiation in Different Media 11.3.1 Transmittance of a Solid Slab 11.3.2 Absorption of Radiation by Liquids 11.3.3 Absorption of Radiation by Gases 11.3.4 Radiation in an Isothermal Gray Gas Slab and the Concept of Mean Beam Length 11.4 Modeling of Gas Radiation 11.4.1 Basics of Gas Radiation Modeling 11.4.2 Band Models 11.5 Radiation in a Non-isothermal Participating Medium 11.5.1 Radiation Transfer in a Gray Slab: 11.5.2 Radiation Equilibrium 11.5.3 Solution of Integral Equation 11.5.4 Discrete Ordinate Method 11.6 Enclosure Analysis in the Presence of an Absorbing and Emitting Gas 11.6.1 Zone Method 11.6.2 Example of Zone Analysis 11.6.3 Application of DOM to Two-Surface Enclosure with a Non-isothermal Participating Medium 11.7 Exercises 12 Laminar Convection In Internal Flow 12.1 Introduction 12.1.1 Classification of Flows 12.1.2 Fluid Properties and Their Variation 12.2 Dimensional Analysis and Similarity 12.2.1 Dimensional Analysis of a Flow Problem 12.2.2 Notion of ``Similarity\'\' 12.2.3 Dimensional Analysis of Heat Transfer Problem 12.3 Internal Flow Fundamentals 12.3.1 Fundamentals of Steady Laminar Tube Flow 12.3.2 Governing Equation Starting from First Principles 12.3.3 Governing Equation Starting with the NS Equations 12.3.4 Solution 12.3.5 Fully Developed Flow in a Parallel Plate Channel 12.3.6 Concept of Fluid Resistance 12.4 Laminar Heat Transfer in Tube Flow 12.4.1 Bulk Mean Temperature 12.4.2 Variation of the Bulk Mean Temperature 12.4.3 Tube Flow with Uniform Wall Heat Flux 12.4.4 Fully Developed Temperature with Uniform Wall Heat Flux 12.4.5 Tube Flow with Constant Wall Temperature 12.4.6 Fully Developed Tube Flow with Constant Wall Temperature 12.5 Laminar Fully Developed Flow and Heat Transfer in Non-circular Tubes and Ducts 12.5.1 Introduction 12.5.2 Parallel Plate Channel with Asymmetric Heating 12.5.3 Parallel Plate Channel with Symmetric Heating 12.5.4 Fully Developed Flow in a Rectangular Duct 12.5.5 Fully Developed Heat Transfer in a Rectangular Duct: Uniform Wall Heat Flux Case 12.5.6 Fully Developed Flow and Heat Transfer Results in Several Important Geometries 12.6 Laminar Fully Developed Heat Transfer to Fluid Flowing in an Annulus 12.6.1 Fully Developed Flow in an Annulus 12.6.2 Fully Developed Temperature in an Annulus 12.7 Flow and Heat Transfer in Laminar Entry Region 12.7.1 Heat Transfer in Entry Region of Fully Developed Tube Flow 12.7.2 Mean Nusselt Number and Useful Correlations 12.8 Exercises 13 Laminar Convection in External Flow 13.1 Introduction 13.2 Laminar Boundary Layer Flow Past a Surface 13.2.1 Order of Magnitude Analysis and the Boundary Layer Approximation 13.2.2 Laminar Boundary Layer over a Flat Plate: Velocity Boundary Layer 13.2.3 Laminar Thermal Boundary Layer over a Flat Plate 13.3 Boundary Layer Flow in the Presence of Stream-Wise Pressure Variation 13.3.1 Inviscid Flow Past the Wedge 13.3.2 Flow Within the Boundary Layer 13.3.3 Temperature Profiles in Falkner–Skan Flows 13.4 Integral Form of Boundary Layer Equations 13.4.1 Momentum and Energy Integral Equations 13.4.2 Approximate Solution for Boundary Layer Flow Past a Flat Plate Using a Polynomial Profile for Velocity 13.4.3 Approximate Solution for Boundary Layer Temperature Profile for Flow Past a Flat Plate Using a Polynomial Profile for Temperature 13.4.4 Integral Method Applied to Boundary Layer Flow with Axial Pressure Gradient 13.4.5 Thwaites\'s Method 13.5 Cylinder in Cross Flow 13.5.1 Introduction 13.5.2 Laminar Flow Normal to a Cylinder 13.5.3 Laminar Boundary Layer Flow Past a Cylinder 13.5.4 Effect of Pressure Gradient on Boundary Layer Flow 13.5.5 Drag Force on a Cylinder in Cross Flow 13.6 Exercises 14 Convection in Turbulent Flow 14.1 Introduction 14.2 Time-Averaged Equations 14.2.1 Turbulent Shear Stress and Turbulent Heat Flux 14.2.2 Turbulent Boundary Layer Equations 14.3 Turbulence Models 14.3.1 Prandtl\'s Mixing Length Theory 14.3.2 Universal Velocity Distribution 14.3.3 Velocity Profiles in Pipe Flow 14.4 Pressure Drop and Heat Transfer in Turbulent Pipe Flow 14.4.1 Pressure Drop in Turbulent Pipe Flow 14.4.2 Heat Transfer in Turbulent Pipe Flow 14.4.3 Application of Average Heat Transfer Coefficient Concept to a Practical Application 14.5 Turbulent Boundary Layer over a Flat Plate 14.5.1 Approximate Analysis of Turbulent Flow Parallel to a Flat Plate 14.5.2 Heat Transfer in the Turbulent Boundary Layer over a Flat Plate 14.5.3 Calculation of Drag with Flow Being Partly Laminar and Partly Turbulent 14.6 Cylinder in Cross Flow 14.6.1 Heat Transfer for Flow Normal to a Tube Bank 14.7 Exercises 15 Heat Exchangers 15.1 Introduction 15.2 Analysis of Heat Exchangers 15.2.1 Thermodynamic Analysis of a Co-Current Heat Exchanger 15.2.2 Thermal Analysis of a Co-Current Heat Exchanger 15.2.3 Overall Heat Transfer Coefficient 15.2.4 Alternate Approach—ε-NTU Relationship for a Co-Current Heat Exchanger 15.2.5 Counter-Current Heat Exchanger 15.3 Other Types of Heat Exchangers 15.3.1 Analysis of Shell and Tube Heat Exchanger 15.3.2 Analysis of a Cross Flow Heat Exchanger by the ε-NTU Approach 15.3.3 Analysis of a Cross Flow Heat Exchanger by LMTD Correction Factor Approach 15.3.4 General Remarks on Heat Exchangers 15.4 Exercises 16 Natural Convection 16.1 Introduction 16.2 Laminar Natural Convection from a Vertical Isothermal Plate 16.2.1 Isothermal Vertical Plate—Integral Solution 16.2.2 Exact Solution of Ostrach 16.2.3 Comparison with Experimental Results 16.3 Turbulent Natural Convection from a Vertical Isothermal Plate 16.3.1 Approximate Integral Analysis 16.3.2 Useful Nusselt Number Correlations 16.4 Natural Convection from Other Geometries 16.4.1 Correlation for Horizontal Plates 16.4.2 Correlation for Vertical Cylinders 16.4.3 Correlation for Horizontal Cylinders 16.5 Heat Transfer Across Fluid Layers 16.5.1 Horizontal Fluid Layers 16.5.2 Vertical Fluid Layers 16.5.3 Inclined Air Layers 16.6 Exercises 17 Special Topics in Heat Transfer 17.1 Introduction 17.2 Multi-mode Problem Involving Radiation 17.2.1 Transient Cooling of a Lumped System 17.2.2 Radiation Error in Thermometry 17.2.3 Duct Type Space Radiator 17.2.4 Uniform Area Fin Losing Heat by Convection and Radiation 17.2.5 Radiating-Conducting-Convecting Fin With Linearized Radiation 17.3 Heat Transfer During Melting or Solidification 17.3.1 Stefan Problem 17.3.2 Neumann Problem 17.3.3 Phase Change in a Finite Domain 17.4 Heat Transfer During Condensation 17.4.1 Film Condensation Over An Isothermal Vertical Surface 17.4.2 Film Condensation Inside and Outside Tubes 17.4.3 Condensation in the Presence of Flowing Vapor 17.5 Heat Transfer During Boiling 17.5.1 Pool Boiling 17.5.2 Some Useful Relations in Pool Boiling 17.5.3 Flow Boiling 17.5.4 Heat Transfer Correlation in Flow Boiling 17.6 Mixed Convection 17.6.1 Laminar Mixed Convection For Flow Over A Vertical Isothermal Flat Plate 17.6.2 Laminar Mixed Convection in a Parallel Plate Channel 17.6.3 Laminar Mixed Convection in a Vertical Parallel Plate Channel: Fully Developed Solution 17.7 Heat Transfer in a Particle Bed 17.7.1 Flow Characteristics of a Particle Bed 17.7.2 Heat Transfer Characteristics of a Particle Bed 17.8 Heat Transfer in High Speed Flows 17.8.1 Compressible Boundary Layer Flow Parallel to a Flat Plate 17.9 Current Topics of Interest in Heat Transfer 17.10 Exercises Appendix A Note on Bessel Functions A.1 Background A.1.1 Bessel Equation with Non-integer ν A.1.2 Gamma Function: A Short Digression A.1.3 Bessel Function of the First Kind A.2 Bessel Equation When ν is an Integer: Bessel Function of the Second Kind A.3 Asymptotic Behavior of Bessel Functions A.4 Orthogonal Property of Bessel Functions A.5 Modified Bessel Functions A.6 General Form of Equation Solvable in Terms of Bessel Functions A.7 Some Useful Results A.8 Tables of Bessel Functions and Modified Bessel Functions Appendix B Note on Legendre Functions B.1 Background B.1.1 Special Simple Case of Legendre Equation B.1.2 Legendre Equation with nge1 B.1.3 Legendre Function of Second Kind B.1.4 Some Useful Relations Involving Legendre Polynomials B.1.5 Orthogonality property and Fourier Legendre series Appendix C Basics of Complex Variables C.1 Introduction C.1.1 Definitions C.1.2 Conditions for the Existence of Derivative of w C.1.3 Complex Potential C.2 Examples of Complex Potentials C.2.1 Complex Potential w=z C.2.2 Complex Potential w=Ln(z) C.2.3 Complex Potential w=ez C.3 Superposition of Complex Potentials C.3.1 Combination of Complex Potentials Considered in Sects. C.2.1 and C.2.2 C.3.2 Flow Past a Cylinder C.3.3 General Comments Appendix D Heisler Charts D.1 One Term Approximation of the Slab Transient D.2 One Term Approximation of the Cylinder Transient D.3 One Term Approximation of the Sphere Transient Appendix E Numerical Solution of Algebraic and Differential Equations E.1 Introduction E.2 Solution of Algebraic Equations E.2.1 Solution of a Single Algebraic Equation E.2.2 Solution of Several Algebraic Equations E.2.3 Solution of Equations Involving Sparse Matrix—TDMA E.2.4 Point by Point Iteration Methods E.2.5 Iteration With Over or Under Relaxation E.3 Solution of Ordinary Differential Equations (ODE) E.3.1 First Order ODE E.4 Higher Order ODE E.4.1 Second-Order ODE: Initial Value Problem E.4.2 Second-Order ODE: Boundary Value Problem Appendix F Exponential Integrals F.1 Introduction F.2 Useful Ways of Calculating Exponential Integrals F.2.1 Approximation of E3(t): Appendix G Angle Factors and Mean Beam Lengths G.1 Angle Factors G.1.1 Angle Factors Between Rectangles G.1.2 Angle Factor Between Equal and Parallel Rectangles G.1.3 Angle Factor Between Perpendicular Rectangles G.1.4 Angle Factor Between Coaxial Disks G.2 Mean Beam Lengths in a Parallelepiped Enclosure G.2.1 Mean Beam Length Between Equal and Parallel Rectangles G.2.2 Mean Beam Length Between Perpendicular Rectangles Sharing a Common Edge Appendix H Basic Equations of Convection Heat Transfer H.1 Introduction H.1.1 NS Equations in Cartesian Coordinates H.1.2 Ideal Fluid Flow H.2 NS Equations in Cylindrical and Spherical Coordinates H.2.1 NS Equations in Cylindrical Coordinates H.2.2 NS Equations in Spherical Coordinates Appendix I Useful Tables Index