Incropera's Principles of Heat and Mass Transfer, Global Edition - Frank P. Incropera, David P. DeWitt, Theodore L. Bergman, Adrienne S. Lavine

Incropera's Principles of Heat and Mass Transfer, Global Edition

Buch | Softcover
1008 Seiten
2017 | 8th edition
John Wiley & Sons Inc (Verlag)
978-1-119-38291-1 (ISBN)
50,24 inkl. MwSt
Sonderpreis bis 30.11.2024
Listenpreis bisher: 62,80 €
Incropera's Fundamentals of Heat and Mass Transfer has been the gold standard of heat transfer pedagogy for many decades, with a commitment to continuous improvement by four authors’ with more than 150 years of combined experience in heat transfer education, research and practice. Applying the rigorous and systematic problem-solving methodology that this text pioneered an abundance of examples and problems reveal the richness and beauty of the discipline. This edition makes heat and mass transfer more approachable by giving additional emphasis to fundamental concepts, while highlighting the relevance of two of today’s most critical issues: energy and the environment.

Symbols xix

Chapter 1 Introduction 1

1.1 What and How? 2

1.2 Physical Origins and Rate Equations 3

1.2.1 Conduction 3

1.2.2 Convection 6

1.2.3 Radiation 8

1.2.4 The Thermal Resistance Concept 12

1.3 Relationship to Thermodynamics 12

1.3.1 Relationship to the First Law of Thermodynamics (Conservation of Energy) 13

1.3.2 Relationship to the Second Law of Thermodynamics and the Efficiency of Heat Engines 28

1.4 Units and Dimensions 33

1.5 Analysis of Heat Transfer Problems: Methodology 35

1.6 Relevance of Heat Transfer 38

1.7 Summary 42

References 45

Problems 45

Chapter 2 Introduction to Conduction 59

2.1 The Conduction Rate Equation 60

2.2 The Thermal Properties of Matter 62

2.2.1 Thermal Conductivity 63

2.2.2 Other Relevant Properties 70

2.3 The Heat Diffusion Equation 74

2.4 Boundary and Initial Conditions 82

2.5 Summary 86

References 87

Problems 87

Chapter 3 One-Dimensional, Steady-State Conduction 99

3.1 The Plane Wall 100

3.1.1 Temperature Distribution 100

3.1.2 Thermal Resistance 102

3.1.3 The Composite Wall 103

3.1.4 Contact Resistance 105

3.1.5 Porous Media 107

3.2 An Alternative Conduction Analysis 121

3.3 Radial Systems 125

3.3.1 The Cylinder 125

3.3.2 The Sphere 130

3.4 Summary of One-Dimensional Conduction Results 131

3.5 Conduction with Thermal Energy Generation 131

3.5.1 The Plane Wall 132

3.5.2 Radial Systems 138

3.5.3 Tabulated Solutions 139

3.5.4 Application of Resistance Concepts 139

3.6 Heat Transfer from Extended Surfaces 143

3.6.1 A General Conduction Analysis 145

3.6.2 Fins of Uniform Cross-Sectional Area 147

3.6.3 Fin Performance Parameters 153

3.6.4 Fins of Nonuniform Cross-Sectional Area 156

3.6.5 Overall Surface Efficiency 159

3.7 Other Applications of One-Dimensional, Steady-State Conduction 163

3.7.1 The Bioheat Equation 163

3.7.2 Thermoelectric Power Generation 167

3.7.3 Nanoscale Conduction 175

3.8 Summary 179

References 181

Problems 182

Chapter 4 Two-Dimensional, Steady-State Conduction 209

4.1 General Considerations and Solution Techniques 210

4.2 The Method of Separation of Variables 211

4.3 The Conduction Shape Factor and the Dimensionless Conduction Heat Rate 215

4.4 Finite-Difference Equations 221

4.4.1 The Nodal Network 221

4.4.2 Finite-Difference Form of the Heat Equation: No Generation and Constant Properties 222

4.4.3 Finite-Difference Form of the Heat Equation: The Energy Balance Method 223

4.5 Solving the Finite-Difference Equations 230

4.5.1 Formulation as a Matrix Equation 230

4.5.2 Verifying the Accuracy of the Solution 231

4.6 Summary 236

References 237

Problems 237

4S.1 The Graphical Method W-1

4S.1.1 Methodology of Constructing a Flux Plot W-1

4S.1.2 Determination of the Heat Transfer Rate W-2

4S.1.3 The Conduction Shape Factor W-3

4S.2 The Gauss-Seidel Method: Example of Usage W-5

References W-10

Problems W-10

Chapter 5 Transient Conduction 253

5.1 The Lumped Capacitance Method 254

5.2 Validity of the Lumped Capacitance Method 257

5.3 General Lumped Capacitance Analysis 261

5.3.1 Radiation Only 262

5.3.2 Negligible Radiation 262

5.3.3 Convection Only with Variable Convection Coefficient 263

5.3.4 Additional Considerations 263

5.4 Spatial Effects 272

5.5 The Plane Wall with Convection 273

5.5.1 Exact Solution 274

5.5.2 Approximate Solution 274

5.5.3 Total Energy Transfer: Approximate Solution 276

5.5.4 Additional Considerations 276

5.6 Radial Systems with Convection 277

5.6.1 Exact Solutions 277

5.6.2 Approximate Solutions 278

5.6.3 Total Energy Transfer: Approximate Solutions 278

5.6.4 Additional Considerations 279

5.7 The Semi-Infinite Solid 284

5.8 Objects with Constant Surface Temperatures or Surface Heat Fluxes 291

5.8.1 Constant Temperature Boundary Conditions 291

5.8.2 Constant Heat Flux Boundary Conditions 293

5.8.3 Approximate Solutions 294

5.9 Periodic Heating 301

5.10 Finite-Difference Methods 304

5.10.1 Discretization of the Heat Equation: The Explicit Method 304

5.10.2 Discretization of the Heat Equation: The Implicit Method 311

5.11 Summary 318

References 319

Problems 319

5S.1 Graphical Representation of One-Dimensional, Transient Conduction in the Plane Wall, Long Cylinder, and Sphere W-12

5S.2 Analytical Solutions of Multidimensional Effects W-16

References W-22

Problems W-22

Chapter 6 Introduction to Convection 343

6.1 The Convection Boundary Layers 344

6.1.1 The Velocity Boundary Layer 344

6.1.2 The Thermal Boundary Layer 345

6.1.3 The Concentration Boundary Layer 347

6.1.4 Significance of the Boundary Layers 348

6.2 Local and Average Convection Coefficients 348

6.2.1 Heat Transfer 348

6.2.2 Mass Transfer 349

6.3 Laminar and Turbulent Flow 355

6.3.1 Laminar and Turbulent Velocity Boundary Layers 355

6.3.2 Laminar and Turbulent Thermal and Species Concentration Boundary Layers 357

6.4 The Boundary Layer Equations 360

6.4.1 Boundary Layer Equations for Laminar Flow 361

6.4.2 Compressible Flow 364

6.5 Boundary Layer Similarity: The Normalized Boundary Layer Equations 364

6.5.1 Boundary Layer Similarity Parameters 365

6.5.2 Dependent Dimensionless Parameters 365

6.6 Physical Interpretation of the Dimensionless Parameters 374

6.7 Boundary Layer Analogies 376

6.7.1 The Heat and Mass Transfer Analogy 377

6.7.2 Evaporative Cooling 380

6.7.3 The Reynolds Analogy 383

6.8 Summary 384

References 385

Problems 386

6S.1 Derivation of the Convection Transfer Equations W-25

6S.1.1 Conservation of Mass W-25

6S.1.2 Newton’s Second Law of Motion W-26

6S.1.3 Conservation of Energy W-29

6S.1.4 Conservation of Species W-32

References W-36

Problems W-36

Chapter 7 External Flow 399

7.1 The Empirical Method 401

7.2 The Flat Plate in Parallel Flow 402

7.2.1 Laminar Flow over an Isothermal Plate: A Similarity Solution 403

7.2.2 Turbulent Flow over an Isothermal Plate 409

7.2.3 Mixed Boundary Layer Conditions 410

7.2.4 Unheated Starting Length 411

7.2.5 Flat Plates with Constant Heat Flux Conditions 412

7.2.6 Limitations on Use of Convection Coefficients 413

7.3 Methodology for a Convection Calculation 413

7.4 The Cylinder in Cross Flow 421

7.4.1 Flow Considerations 421

7.4.2 Convection Heat and Mass Transfer 423

7.5 The Sphere 431

7.6 Flow Across Banks of Tubes 434

7.7 Impinging Jets 443

7.7.1 Hydrodynamic and Geometric Considerations 443

7.7.2 Convection Heat and Mass Transfer 444

7.8 Packed Beds 448

7.9 Summary 449

References 452

Problems 452

Chapter 8 Internal Flow 475

8.1 Hydrodynamic Considerations 476

8.1.1 Flow Conditions 476

8.1.2 The Mean Velocity 477

8.1.3 Velocity Profile in the Fully Developed Region 478

8.1.4 Pressure Gradient and Friction Factor in Fully Developed Flow 480

8.2 Thermal Considerations 481

8.2.1 The Mean Temperature 482

8.2.2 Newton’s Law of Cooling 483

8.2.3 Fully Developed Conditions 483

8.3 The Energy Balance 487

8.3.1 General Considerations 487

8.3.2 Constant Surface Heat Flux 488

8.3.3 Constant Surface Temperature 491

8.4 Laminar Flow in Circular Tubes: Thermal Analysis and Convection Correlations 495

8.4.1 The Fully Developed Region 495

8.4.2 The Entry Region 500

8.4.3 Temperature-Dependent Properties 502

8.5 Convection Correlations: Turbulent Flow in Circular Tubes 502

8.6 Convection Correlations: Noncircular Tubes and the Concentric Tube Annulus 510

8.7 Heat Transfer Enhancement 513

8.8 Forced Convection in Small Channels 516

8.8.1 Microscale Convection in Gases (0.1 μm ≲ Dh ≲ 100 μm) 516

8.8.2 Microscale Convection in Liquids 517

8.8.3 Nanoscale Convection (Dh ≲ 100 nm) 518

8.9 Convection Mass Transfer 521

8.10 Summary 523

References 526

Problems 527

Chapter 9 Free Convection 547

9.1 Physical Considerations 548

9.2 The Governing Equations for Laminar Boundary Layers 550

9.3 Similarity Considerations 552

9.4 Laminar Free Convection on a Vertical Surface 553

9.5 The Effects of Turbulence 556

9.6 Empirical Correlations: External Free Convection Flows 558

9.6.1 The Vertical Plate 559

9.6.2 Inclined and Horizontal Plates 562

9.6.3 The Long Horizontal Cylinder 567

9.6.4 Spheres 571

9.7 Free Convection Within Parallel Plate Channels 572

9.7.1 Vertical Channels 573

9.7.2 Inclined Channels 575

9.8 Empirical Correlations: Enclosures 575

9.8.1 Rectangular Cavities 575

9.8.2 Concentric Cylinders 578

9.8.3 Concentric Spheres 579

9.9 Combined Free and Forced Convection 581

9.10 Convection Mass Transfer 582

9.11 Summary 583

References 584

Problems 585

Chapter 10 Boiling and Condensation 603

10.1 Dimensionless Parameters in Boiling and Condensation 604

10.2 Boiling Modes 605

10.3 Pool Boiling 606

10.3.1 The Boiling Curve 606

10.3.2 Modes of Pool Boiling 607

10.4 Pool Boiling Correlations 610

10.4.1 Nucleate Pool Boiling 610

10.4.2 Critical Heat Flux for Nucleate Pool Boiling 612

10.4.3 Minimum Heat Flux 613

10.4.4 Film Pool Boiling 613

10.4.5 Parametric Effects on Pool Boiling 614

10.5 Forced Convection Boiling 619

10.5.1 External Forced Convection Boiling 620

10.5.2 Two-Phase Flow 620

10.5.3 Two-Phase Flow in Microchannels 623

10.6 Condensation: Physical Mechanisms 623

10.7 Laminar Film Condensation on a Vertical Plate 625

10.8 Turbulent Film Condensation 629

10.9 Film Condensation on Radial Systems 634

10.10 Condensation in Horizontal Tubes 639

10.11 Dropwise Condensation 640

10.12 Summary 641

References 641

Problems 643

Chapter 11 Heat Exchangers 653

11.1 Heat Exchanger Types 654

11.2 The Overall Heat Transfer Coefficient 656

11.3 Heat Exchanger Analysis: Use of the Log Mean Temperature Difference 659

11.3.1 The Parallel-Flow Heat Exchanger 660

11.3.2 The Counterflow Heat Exchanger 662

11.3.3 Special Operating Conditions 663

11.4 Heat Exchanger Analysis: The Effectiveness–NTU Method 670

11.4.1 Definitions 670

11.4.2 Effectiveness–NTU Relations 671

11.5 Heat Exchanger Design and Performance Calculations 678

11.6 Additional Considerations 687

11.7 Summary 695

References 696

Problems 696

11S.1 Log Mean Temperature Difference Method for Multipass and Cross-Flow Heat Exchangers W-40

11S.2 Compact Heat Exchangers W-44

References W-49

Problems W-50

Chapter 12 Radiation: Processes and Properties 711

12.1 Fundamental Concepts 712

12.2 Radiation Heat Fluxes 715

12.3 Radiation Intensity 717

12.3.1 Mathematical Definitions 717

12.3.2 Radiation Intensity and Its Relation to Emission 718

12.3.3 Relation to Irradiation 723

12.3.4 Relation to Radiosity for an Opaque Surface 725

12.3.5 Relation to the Net Radiative Flux for an Opaque Surface 726

12.4 Blackbody Radiation 726

12.4.1 The Planck Distribution 727

12.4.2 Wien’s Displacement Law 728

12.4.3 The Stefan–Boltzmann Law 728

12.4.4 Band Emission 729

12.5 Emission from Real Surfaces 736

12.6 Absorption, Reflection, and Transmission by Real Surfaces 745

12.6.1 Absorptivity 746

12.6.2 Reflectivity 747

12.6.3 Transmissivity 749

12.6.4 Special Considerations 749

12.7 Kirchhoff’s Law 754

12.8 The Gray Surface 756

12.9 Environmental Radiation 762

12.9.1 Solar Radiation 763

12.9.2 The Atmospheric Radiation Balance 765

12.9.3 Terrestrial Solar Irradiation 767

12.10 Summary 770

References 774

Problems 774

Chapter 13 Radiation Exchange Between Surfaces 797

13.1 The View Factor 798

13.1.1 The View Factor Integral 798

13.1.2 View Factor Relations 799

13.2 Blackbody Radiation Exchange 808

13.3 Radiation Exchange Between Opaque, Diffuse, Gray Surfaces in an Enclosure 812

13.3.1 Net Radiation Exchange at a Surface 813

13.3.2 Radiation Exchange Between Surfaces 814

13.3.3 The Two-Surface Enclosure 820

13.3.4 Two-Surface Enclosures in Series and Radiation Shields 822

13.3.5 The Reradiating Surface 824

13.4 Multimode Heat Transfer 829

13.5 Implications of the Simplifying Assumptions 832

13.6 Radiation Exchange with Participating Media 832

13.6.1 Volumetric Absorption 832

13.6.2 Gaseous Emission and Absorption 833

13.7 Summary 837

References 838

Problems 839

Chapter 14 Diffusion Mass Transfer 863

14.1 Physical Origins and Rate Equations 864

14.1.1 Physical Origins 864

14.1.2 Mixture Composition 865

14.1.3 Fick’s Law of Diffusion 866

14.1.4 Mass Diffusivity 867

14.2 Mass Transfer in Nonstationary Media 869

14.2.1 Absolute and Diffusive Species Fluxes 869

14.2.2 Evaporation in a Column 872

14.3 The Stationary Medium Approximation 877

14.4 Conservation of Species for a Stationary Medium 877

14.4.1 Conservation of Species for a Control Volume 878

14.4.2 The Mass Diffusion Equation 878

14.4.3 Stationary Media with Specified Surface Concentrations 880

14.5 Boundary Conditions and Discontinuous Concentrations at Interfaces 884

14.5.1 Evaporation and Sublimation 885

14.5.2 Solubility of Gases in Liquids and Solids 885

14.5.3 Catalytic Surface Reactions 890

14.6 Mass Diffusion with Homogeneous Chemical Reactions 892

14.7 Transient Diffusion 895

14.8 Summary 901

References 902

Problems 902

Appendix A Thermophysical Properties of Matter 911

Appendix B Mathematical Relations and Functions 943

Appendix C Thermal Conditions Associated with Uniform Energy Generation in One-Dimensional, Steady-State Systems 949

Appendix D The Gauss–Seidel Method 955

Appendix E The Convection Transfer Equations 957

E.1 Conservation of Mass 958

E.2 Newton’s Second Law of Motion 958

E.3 Conservation of Energy 959

E.4 Conservation of Species 960

Appendix F Boundary Layer Equations for Turbulent Flow 961

Appendix G An Integral Laminar Boundary Layer Solution for Parallel Flow over a Flat Plate 965

Index 969

Erscheinungsdatum
Verlagsort New York
Sprache englisch
Maße 10 x 10 mm
Gewicht 1814 g
Themenwelt Naturwissenschaften Physik / Astronomie Thermodynamik
Technik Maschinenbau
ISBN-10 1-119-38291-2 / 1119382912
ISBN-13 978-1-119-38291-1 / 9781119382911
Zustand Neuware
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