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    1. Naturvetenskap och teknik
    2. Teknik och industri
    3. Energiteknik

    Heat Transfer Basics

    A Concise Approach to Problem Solving

    AvJamil Ghojel

    Inbunden, Engelska, 2023

    1 211 kr

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    E-bok

    1 388 kr

    E-bok

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    Beskrivning

    HEAT TRANSFER BASICS Concise introduction to heat transfer, with a focus on worked example problems to aid in reader comprehension and student learning Heat Transfer Basics covers the essential topics of heat transfer in a focused manner, starting with an introduction to heat transfer that explains its relationship to thermodynamics and fluid mechanics and continuing on to key topics such as free convection, boiling and condensation, radiation, heat exchangers, and more, for an accessible and reader-friendly yet comprehensive treatment of the subject. Each chapter features multiple worked out example problems, including derivations of key governing equations and comparisons of worked solutions with computer modeled results, which helps students become familiar with the types of problems they will encounter in the field. Throughout the book, figures and diagrams liberally illustrate the concepts discussed, and practice problems allow students to test their understanding of the content. The text is accompanied by an online instructor’s manual. Heat Transfer Basics includes information on: One-dimensional, steady-state conduction, covering the plane wall, the composite wall, solid and hollow cylinders and sphere, conduction with and without internal energy generation, and conduction with constant and temperature-dependent thermal conductivity Heat transfer from extended surfaces, fins of uniform and variable cross-sectional area, fin performance, and overall fin efficiencyTransient conduction, covering general lumped capacitance solution method, one- and multi-dimensional transient conduction, and the finite-difference method for solving transient problemsFree and forced convection, covering hydrodynamic and thermal considerations, the energy balance, and thermal analysis and convection correlationsMore advanced than introductory textbooks yet not as overwhelming as textbooks targeted at specialists, Heat Transfer Basics is ideal for students in introductory and advanced heat transfer courses who do not intend to specialize in heat transfer, and is a helpful reference for advanced students and practicing engineers.

    Produktinformation

    • Utgivningsdatum:2023-11-17
    • Mått:185 x 257 x 36 mm
    • Vikt:930 g
    • Format:Inbunden
    • Språk:Engelska
    • Antal sidor:560
    • Förlag:John Wiley & Sons Inc
    • ISBN:9781119840268

    Utforska kategorier

    • Energiteknik inom Naturvetenskap och teknik

    Mer om författaren

    Jamil Ghojel, Ph.D. is a retired academic with 25 years’ experience of teaching undergraduate and graduate mechanical and aerospace engineering courses in heat engines and heat transfer. He has held positions at the University of Damascus (Syria), the University of Michigan (USA), the University of Melbourne (Australia), and Monash University (Australia). He has conducted extensive research on heat engines and is the author of the Wiley-ASME Press book Fundamentals of Heat Engines: Reciprocating and Gas Turbine Internal Combustion Engines.

    Innehållsförteckning

    • Preface xiiiAcknowledgements xvList of Symbols xviiAbout the Companion Website xxi1 Basic Concepts of Heat and Mass Transfer 11.1 Heat Transfer and Its Relationship With Thermodynamics 11.2 Heat Conduction 31.3 Heat Convection 61.4 Thermal Radiation 81.5 Mass Transfer 112 One-Dimensional Steady-State Heat Conduction 192.1 General Heat Conduction Equation 192.1.1 Cartesian Coordinate System 192.1.2 Cylindrical Coordinate System 222.1.3 Spherical Coordinate System 232.2 Special Conditions of the General Conduction Equation 252.2.1 Constant Thermal Conductivity k With Energy Storage and Generation 252.2.2 Variable Thermal Conductivity and No Internal Energy Storage and Generation 262.2.3 Variable Thermal Conductivity With Internal Energy Generation and No Energy Storage 262.3 One-Dimensional Steady-State Conduction 262.3.1 Plane Wall (or Plate) Without Heat Generation and Storage 262.3.1.1 Constant Thermal Conductivity 262.3.1.2 Temperature-Dependent Thermal Conductivity 282.3.1.3 Composite Plane Wall 312.3.2 Boundary Conditions 332.3.3 Hollow Cylinder (Tube) Without Heat Generation and Storage 362.3.3.1 Constant Thermal Conductivity 362.3.3.2 Temperature-Dependent Thermal Conductivity 382.3.3.3 Composite Cylinder 412.3.3.4 Critical Thickness of Cylinder Insulation 432.3.3.5 Effect of Order of Insulation Material 472.3.4 Hollow Spherical Shell Without Heat Generation and Storage 482.3.4.1 Constant Thermal Conductivity 482.3.4.2 Temperature-Dependent Thermal Conductivity 492.3.4.3 Composite Spherical Shell 512.3.5 Plate With Internal Heat Generation, No Heat Storage, and Uniform Heat Dissipation By Convection 542.3.5.1 Constant Thermal Conductivity 542.3.5.2 Temperature-Dependent Thermal Conductivity 562.3.6 Plate With Internal Heat Generation and Non-Uniform Heat Dissipation By Convection 572.3.6.1 Constant Thermal Conductivity 582.3.6.2 Temperature-Dependent Thermal Conductivity 592.3.7 Solid Cylinder With Internal Heat Generation and Heat Dissipation By Convection 602.3.7.1 Constant Thermal Conductivity 602.3.7.2 Temperature-Dependent Thermal Conductivity 622.3.8 Hollow Cylinder With Internal Heat Generation and Heat Dissipation By Convection From the Outer Surface 622.3.8.1 Constant Thermal Conductivity 622.3.8.2 Temperature-Dependent Thermal Conductivity 652.3.9 Hollow Cylinder With Internal Heat Generation and Heat Dissipation By Convection From the Inner Surface 652.3.9.1 Constant Thermal Conductivity 652.3.9.2 Temperature-Dependent Thermal Conductivity 672.3.10 Hollow Cylinder With Internal Heat Generation and Heat Dissipation By Convection From Both Inner and Outer Surfaces 682.3.10.1 Constant Thermal Conductivity 682.3.10.2 Temperature-Dependent Thermal Conductivity 712.3.11 Solid Sphere With Internal Heat Generation and Heat Dissipation By Convection and No Heat Storage 722.3.11.1 Constant Thermal Conductivity 732.3.11.2 Temperature-Dependent Thermal Conductivity 752.3.12 Hollow Sphere With Internal Heat Generation and Heat Dissipation By Convection From the Outer Surface and No Heat Storage 762.3.12.1 Constant Thermal Conductivity 762.3.12.2 Temperature-Dependent Thermal Conductivity 782.3.13 Hollow Sphere With Internal Heat Generation and Heat Dissipation By Convection From the Inner Surface and No Heat Storage 792.3.13.1 Constant Thermal Conductivity 792.3.13.2 Temperature-Dependent Thermal Conductivity 812.3.14 Hollow Sphere With Internal Heat Generation and Heat Dissipation By Convection From Both the Inner and Outer Surfaces and No Heat Storage 822.3.14.1 Constant Thermal Conductivity 832.3.14.2 Temperature-Dependent Thermal Conductivity With Specified Inner and Outer Surface Temperature 872.4 Interface Contact Resistance 893 Heat Transfer From Extended Surfaces 973.1 Pin Fin of Rectangular Profile and Circular Cross-Section 983.1.1 Pin Fin of Finite Length and Un-Insulated Tip 983.1.2 Pin Fin of Finite Length and Insulated Tip 1023.1.3 Pin Fin of Infinite Length 1033.1.4 Fin Efficiency 1053.2 Straight Fin of Rectangular Profile and Uniform Thickness 1063.3 Pin Fin of Triangular Profile and Circular Cross-Section (Conical Pin Fin) 1093.4 Straight Fins of Variable Cross-Sectional Area 1103.4.1 Fin of Trapezoidal Profile 1113.4.2 Direct Solution of the Straight Fin of Trapezoidal Profile 1153.4.3 Straight Fin of Triangular Profile 1173.4.4 Correction Factor Solution Method for Straight Fins of Variable Cross-Sectional Area 1193.4.5 Straight Fin of Convex Parabolic Profile 1213.4.6 Straight Fin of Concave Parabolic Profile 1253.5 Annular Fins 1263.5.1 Straight Annular Fin of Uniform Thickness 1263.5.2 Direct Solution of the Straight Annular Fin of Uniform Thickness 1293.5.3 Correction Factor Solution Method for Annular Fins of Uniform Thickness 1323.5.4 Circular (Annular) Fin of Triangular Profile 1343.5.5 Annular Fin of Hyperbolic Profile 1363.6 Other Fin Shapes 1373.7 Heat Transfer Through Finned Walls 1384 Two-Dimensional Steady-State Heat Conduction 1514.1 Analytical Method 1514.1.1 Two-Dimensional Plate With Finite Length and Width and Constant Boundary Conditions 1544.1.1.1 Temperature Distribution 1544.1.1.2 Rate of Heat Transfer 1574.1.2 Two-Dimensional Plate With Finite Length and Nonconstant Boundary Conditions 1594.1.2.1 Temperature Distribution 1594.1.2.2 Rate of Heat Transfer 1614.1.3 Two-Dimensional Plate With Semi-Infinite Length 1614.1.4 Other Boundary Conditions 1634.1.5 Two-Dimensional Semi-Circular Plate (Or Cylinder) With Prescribed Boundary Conditions 1654.2 Conduction Shape Factor Method 1664.3 Numerical Solution of Two-Dimensional Heat Conduction Problems 1724.3.1 Interior Node 1734.3.2 Plane-Surface Node 1754.3.3 Interior Node Near Curved Surface 1764.3.4 Finite Difference Formulation in Cylindrical Coordinates 1814.4 Solution Methods for Finite-Difference Models 1824.4.1 Matrix Inversion Method 1824.4.2 Iterative Methods (Gauss–Seidel Method) 1885 Transient Conduction 1955.1 Analytical Solutions of One-Dimensional Distributed Systems 1965.1.1 Heating or Cooling of an Infinite Plate 1965.1.2 Analysis of the Plate Solution 1995.1.2.1 Other Boundary Conditions 2015.1.3 Heating or Cooling of an Infinite Solid Cylinder 2025.1.4 Heating or Cooling of a Sphere 2065.1.5 Heisler Charts 2095.2 Time-Dependent and Spatially Uniform Temperature Distribution 2105.2.1 Lumped Capacitance Method 2115.3 Multi-Dimensional Transient Conduction Systems 2145.3.1 Long Rectangular Bar 2145.3.2 Short Cylinder 2165.3.3 Rectangular Parallelepiped 2185.4 Finite-Difference Method for Solving Transient Conduction Problems 2215.4.1 Explicit Finite-Difference Method 2215.4.1.1 One-Dimensional Transient Conduction 2225.4.1.2 Two-Dimensional Transient Conduction 2245.4.2 Implicit Finite-Difference Method 2265.4.2.1 One-Dimensional Transient Conduction 2265.4.2.2 Two-Dimensional Transient Conduction 2275.4.3 Finite Difference Formulation in Cylindrical Coordinates 2276 Fundamentals of Convection Heat Transfer 2436.1 Convection Governing Equation 2436.2 Viscosity 2446.3 Types of Flow 2446.4 The Hydrodynamic (Velocity) Boundary Layer 2456.4.1 Flow Over a Flat Plate 2456.4.2 Flow Inside a Cylindrical Tube 2466.4.3 Flow Over Tube or Sphere 2476.5 The Thermal Boundary Layer 2496.6 Dimensional Analysis 2506.6.1 The Rayleigh Method 2526.6.2 Buckingham Pi (Π or π) Theorem 2556.7 Geometric Similarity and Other Considerations 2587 Forced Convection – External Flows 2637.1 Flow Over a Flat Plate 2637.1.1 Laminar Flow Over a Flat Plate 2637.1.2 Turbulent Flow Over a Flat Plate 2687.2 Flow Over a Cylindrical Tube 2717.3 Tube Banks in Crossflow 2747.3.1 Banks of Smooth Tubes 2757.3.2 Banks of Rough Staggered Tubes 2777.4 Flow Over Non-Circular Tubes 2797.5 Flow Over Spheres 2798 Forced Convection – Internal Flows 2858.1 Forced Convection Inside Tubes 2858.2 Laminar Forced Convection (Region I) 2868.2.1 Fully Developed Flow 2878.2.2 Non-Circular Tubes 2908.2.3 Laminar Forced Convection Correlations 2918.3 Turbulent Forced Convection (Region III) 2948.3.1 Forced Convection for Flow in the Transition Region (Region II) 2999 Natural (Free) Convection 3059.1 Boundary Layer in Free Convection 3059.2 Governing Equation for Laminar Boundary Layer 3069.3 Application of Dimensional Analysis to Natural Convection 3089.4 Empirical Correlations for Natural Convection 3109.4.1 Vertical Plates 3119.4.2 Horizontal Plates 3129.4.3 Inclined Plates 3149.4.4 Long Horizontal Cylinder 3149.4.5 Spheres 3159.4.6 Flow in Channels 3159.4.7 Flow in Closed Spaces 3169.4.7.1 Vertical Rectangular Cavity 3169.4.7.2 Horizontal Fluid Layer 3179.4.7.3 Concentric Cylinders 3199.4.7.4 Concentric Spheres 3209.5 Mixed Free and Forced Convection 32310 Thermal Radiation 32710.1 The Electromagnetic Spectrum 32810.2 Definitions and Radiation Properties 32810.3 Shape Factors 33310.3.1 Reciprocity Rule 33410.3.2 Summation Rule 33510.3.3 Superposition Rule 33610.3.4 Symmetry Rule 33710.3.5 String Rule 33810.4 Determination of Shape Factors for Finite Surfaces 34010.5 Shape Factor Equations 34411 Thermal Radiation 36111.1 Radiation Exchange Between Two Grey Surfaces 36111.2 Thermal Radiation Networks 36311.2.1 Grey Object in Grey Enclosure 36311.2.2 Radiation Exchange Between Two Grey Surfaces 36411.2.3 Three Infinitely Long Parallel Planes 36411.2.4 Radiation Exchange Between Several Grey Surfaces 36611.2.5 Enclosure With Four Long Grey Surfaces That See Each Other 36811.2.6 Enclosure With Three Long Grey Surfaces That See Each Other 36911.2.7 Three Surfaces With One of Them Insulated 37011.2.8 Two Parallel Flat Plates of Equal Finite Size in Very Large Room 37111.2.9 Two Surfaces With One of Them Insulated in Large Room 37111.3 Radiation Exchange With Participating Medium 37411.3.1 Absorption of Radiation 37511.3.2 Gaseous Emission 37511.3.3 Gas-Mass to Surface Radiation Heat Transfer 37811.4 Combined Radiation and Convection 38412 Heat Exchangers 39112.1 Overall Heat Transfer Coefficient 39112.2 The LMTD Method of Heat Exchanger Analysis 39412.2.1 Double-Pipe Heat Exchangers 39412.2.2 Shell-and-Tube Heat Exchangers 39812.2.3 Cross-Flow Heat Exchangers 40212.2.4 LMTD Thermal Design Procedure 40512.3 The Effectiveness-NTU Method of Heat-Exchanger Analysis 40812.3.1 Effectiveness-NTU Relation for Parallel-Flow Exchanger 40912.3.2 Effectiveness-NTU Relation for Counter-Flow Exchanger 41112.3.3 Other Types of Heat Exchangers 41312.3.4 Effectiveness-NTU Thermal Design Procedure 41313 Heat Transfer With Phase Change 42513.1 Heat Transfer in Condensing Vapours 42513.1.1 Filmwise Condensation 42513.1.2 Flow Regimes of the Condensate Film 43013.1.2.1 Laminar Flow Regime 43113.1.2.2 Laminar Wavy Regime 43113.1.2.3 Turbulent Flow Regime 43313.1.3 Film Condensation Outside Horizontal Tubes 43513.1.4 Film Condensation Inside Horizontal Tubes 43813.1.4.1 Laminar Flow 43813.1.4.2 Turbulent Flow 43913.1.5 Dropwise Condensation 44113.2 Boiling Heat Transfer 44213.2.1 Pool Boiling 44213.2.2 Film Boiling 44613.2.3 Forced-Convection Boiling 44714 Mass Transfer 45314.1 Species Concentrations 45314.2 Diffusion Mass Transfer 45614.3 Steady Mass Diffusion Through a Plane Wall 46014.4 Diffusion of Vapour Through a Stationary Gas 46114.5 Steady-State Equimolar Counter Diffusion 46314.6 Mass Convection 46514.6.1 Forced Mass Convection Correlations 46614.6.2 Natural (Free) Mass Convection Correlations 46814.7 Simultaneous Mass and Heat Transfer 470AppendicesAppendix B 477Appendix C 491Appendix D 495Appendix N 501References 509Index 513