CONVECTION HEAT TRANSFER

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CONVECTION HEAT TRANSFER SECOND EDITION Adrian Bejan J. A. Jones Professor of Mechanical Engineering Duke University Durham, North Carolina A WILEY-INTERSCIENCE PUBUCATION JOHN WILEY & SONS, INC. New York / Chichester / Brisbane / Toronto / Singapore

List of Symbols xxi 1 Fundamental Principles 1 1.1 Mass conservation / 2 1.2 Force balances (momentum equations) / 4 1.3 The first law of thermodynamics / 9 1.4 The second law of thermodynamics / 16 1.5 The rules of scale analysis / 18 1.6 Heatlines for visualizing convection / 21 References / 23 Problems / 24 2 Laminar Boundary Layer Flow 28 2.1 The fundamental problem in convective heat transfer / 29 2.2 The concept of boundary layer / 32 2.3 Velocity and thermal boundary layers / 35 2.4 Integral Solutions / 39 2.5 Similiarity Solutions / 46 2.5.1 Themethod / 46 2.5.2 The flow Solution / 48 2.5.3 The heat transfer Solution / 51 2.6 Other wall heating conditions / 55 2.6.1 Unheated starting length / 55 2.6.2 Arbitrary wall temperature / 56 2.6.3 Uniform heat flux / 58 2.6.4 Film temperature / 59 2.7 The effect of longitudinal pressure gradient: Flow past a wedge, and Stagnation flow / 59 2.8 The effect of flow through the wall: Blowing and suction / 63 xiii

XiV CONTENTS 2.9 The effect of conduction across a solid coating deposited on the wall / 66 2.10 Entropy generation minimization in laminar boundary layer flow / 70 2.11 The heatlines in laminar boundary layer flow / 72 References / 76 Problems / 78 3 Laminar Duct Flow 92 3.1 Hydrodynamic entrance length / 93 3.2 Fully developed flow / 97 3.3 Hydraulic diameter and pressure drop / 100 3.4 Heat transfer to fully developed duct flow / 107 3.4.1 Mean temperature / 107 3.4.2 Fully developed temperature profile / 109 3.4.3 Uniform wall heat flux / 112 3.4.4 Uniform wall temperature / 115 3.4.5 Tube surrounded by isothermal fluid / 118 3.5 Heat transfer to developing flow / 121 3.5.1 Scale analysis / 122 3.5.2 Thermally developed uniform (slug) flow / 124 3.5.3 Thermally developing Hagen-Poiseuille flow / 126 3.5.4 Thermally and hydraulically developing flow / 130 3.6 The optimal cooling of a Stack of parallel heat generating boards / 132 3.7 The heatlines in fully developed duct flow / 136 3.8 The optimal duct shape for minimum flow resistance / 139 References / 142 Problems / 144 4 External Natural Convection 156 4.1 Natural convection versus forced convection / 157 4.2 Laminar boundary layer equations / 159 4.3 Scale analysis / 161 4.3.1 High-Pr fluids / 163 4.3.2 Low-Pr fluids / 165 4.3.3 Observations / 166 4.4 Integral Solution / 168 4.4.1 High-Pr fluids / 169 4.4.2 Low-Pr fluids / 170

XV 4.5 Similarity Solution / 172 4.6 Uniform wall heat flux / 177 4.7 The effect of thermal stratification / 180 4.8 Conjugate boundary layers / 183 4.9 Vertical Channel flow / 185 4.10 Combined natural and forced convection (mixed convection) / 188 4.11 Heat transfer results including the effect of turbulence / 192 4.11.1 Vertical walls / 192 4.11.2 Inclined walls / 194 4.11.3 Horizontal walls / 196 4.11.4 Horizontal cylinder / 198 4.11.5 Sphere / 199 4.11.6 Vertical cylinder / 199 4.11.7 Other immersed bodies / 200 4.12 The optimal cooling of a Stack of vertical heat generating boards / 202 References / 205 Problems / 209 Internal Natural Convection 219 5.1 Transient heating from the side / 220 5.1.1 Scale analysis / 220 5.1.2 Criterion for distinct vertical layers / 225 5.1.3 Criterion for distinct horizontal jets / 225 5.2 The boundary layer regime / 228 5.3 The shallow enclosure limit / 235 5.4 Summary of results for heating from the side / 243 5.4.1 Isothermal side walls / 243 5.4.2 Side walls with uniform heat flux / 247 5.4.3 Partially divided enclosures / 247 5.4.4 Triangulär enclosures / 251 5.5 Enclosures heated from below / 252 5.6 Inclined enclosures / 256 5.7 Annular space between horizontal cylinders / 257 5.8 Annular space between concentric spheres / 259 References / 260 Problems / 263 Transition to Turbulence 268 6.1 Empirical transition data / 268 6.2 The scaling laws of transition / 270

XVI CONTENTS 6.3 The buckling of inviscid streams / 274 6.4 The local Reynolds number criterion for transition / 278 6.5 The instability of inviscid flow / 281 References / 287 Problems / 290 7 Turbulent Boundary Layer Flow 293 7.1 The large-scale structure / 293 7.2 The time-averaged equations / 296 7.3 The boundary layer equations / 299 7.4 The mixing length model / 302 7.5 The velocity distribution / 303 7.6 Wall friction in boundary layer flow / 311 7.7 Heat transfer in boundary layer flow / 313 7.8 Theory of heat transfer in turbulent boundary layer flow / 317 7.9 Other external flows / 323 7.9.1 Single cylinder in cross-flow / 323 7.9.2 Sphere / 325 7.9.3 Other body shapes / 326 7.9.4 Arrays of cylinders in cross-flow / 326 7.10 Natural convection along vertical walls / 331 References / 335 Problems / 336 8 Turbulent Duct Flow 343 8.1 Velocity distribution / 343 8.2 Friction factor and pressure drop / 345 8.3 Heat-transfer coefficient / 350 8.4 Total heat transfer rate / 354 8.4.1 Isothermal wall / 355 8.4.2 Uniform wall heating / 356 8.5 More refined turbulence modeis / 357 8.6 The heatlines in turbulent flow near a wall / 361 References / 364 Problems / 365 9 Free Turbulent Flows 371 9.1 Free shear layers / 372 9.1.1 Features of the free turbulent flow model / 372 9.1.2 The velocity distribution / 375 9.1.3 The structure of free turbulent flows / 376 9.1.4 The temperature distribution / 378

XVII 9.2 Jets / 379 9.2.1 Two-dimensional jets / 379 9.2.2 Round jets / 383 9.2.3 Jet in density stratified reservoir / 385 9.3 Plumes / 387 9.3.1 The round plume and the entrainment hypothesis / 387 9.3.2 The pulsating frequency of pool fires / 392 9.3.3 The geometric similarity of free turbulent flows / 396 9.4 Thermal wakes behind concentrated sources / 398 References / 400 Problems / 401 10 Convection with Change of Phase 403 10.1 Condensation / 403 10.1.1 Laminar film on a vertical surface / 403 10.1.2 Turbulent film on a vertical surface / 410 10.1.3 Film condensation in other configurations / 412 10.1.4 Drop condensation / 421 10.2 Boiling / 423 10.2.1 Pool boiling regimes / 423 10.2.2 Nucleate boiling and peak heat flux / 427 10.2.3 Film boiling and minimum heat flux / 430 10.2.4 Flow boiling / 433 10.3 Contact melting and lubrication / 434 10.3.1 Plane surfaces with relative motion / 434 10.3.2 Other contact melting configurations / 438 10.3.3 Scale analysis and correlation / 441 10.3.4 Melting due to viscous heating in the liquid film / 443 10.4 Melting by natural convection / 446 10.4.1 The transition from the conduction regime to the convection regime / 446 10.4.2 The quasisteady convection regime / 449 10.4.3 The horizontal spreading of the melt layer / 452 References / 455 Problems / 459 11 Mass transfer 466 11.1 Properties of mixtures / 467 11.2 Mass conservation / 470 11.3 Mass diffusivities / 475

11.4 Boundary conditions / 477 11.5 Laminar forced convection / 479 11.6 The impermeable surface model / 483 11.7 Other external forced convection configurations / 484 11.8 Internal forced convection / 486 11.9 Natural convection / 488 11.9.1 Mass-transfer-driven flow / 490 11.9.2 Heat-transfer-driven flow / 491 11.10 Turbulent flow / 494 11.10.1 The time-averaged concentration equation / 494 11.10.2 Forced convection results / 495 11.10.3 Contaminant removal from a ventilated enclosure / 498 11.11 Massfunction and masslines / 505 11.12 The effect of chemical reaction / 506 References / 509 Problems / 511 Convection in Porous Media 12.1 Mass conservation / 516 12.2 The Darcy flow model and the Forchheimer modification / 520 12.3 The flrst law of thermodynamics / 523 12.4 The second law of thermodynamics / 527 12.5 Forced convection / 527 12.5.1 Boundary layers / 527 12.5.2 Concentrated heat sources / 532 12.5.3 Sphere and cylinder in cross-flow / 534 12.5.4 Channel filled with porous medium / 534 12.6 Natural convection boundary layers / 535 12.6.1 The boundary layer equations: Vertical wall / 535 12.6.2 Uniform wall temperature / 537 12.6.3 Uniform wall heat flux / 538 12.6.4 The effect of wall inclination / 539 12.6.5 Conjugate boundary layers / 540 12.6.6 Thermal stratification / 541 12.6.7 Sphere and horizontal cylinder / 544 12.6.8 Horizontal walls / 545 12.6.9 Concentrated heat sources / 546 12.7 Enclosed porous media heated from the side / 550 12.7.1 The four heat transfer regimes / 550 12.7.2 Convection results / 555

XJX 12.8 Penetrative convection / 557 12.8.1 Lateral penetration / 558 12.8.2 Vertical penetration / 558 12.9 Enclosed porous media heated from below / 559 12.9.1 The onset of convection / 559 12.9.2 Darcy flow / 564 12.9.3 Forchheimer flow / 565 References / 568 Problems / 570 Appendixes 577 A Constants and conversion factors / 579 B Properties of solids / 585 C Properties of liquids / 595 D Properties of gases / 603 E Mathematical formulas / 609 Author Index 611 Subject Index 619