| Symbols |
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xxi | |
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1 | (42) |
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2 | (1) |
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Physical Origins and Rate Equations |
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3 | (9) |
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3 | (2) |
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5 | (3) |
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8 | (4) |
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Relationship to Thermodynamics |
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12 | (1) |
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The Conservation of Energy Requirement |
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12 | (10) |
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Conservation of Energy for a Control Volume |
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12 | (7) |
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The Surface Energy Balance |
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19 | (2) |
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Application of the Conservation Laws: Methodology |
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21 | (1) |
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Analysis of Heat Transfer Problems: Methodology |
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22 | (3) |
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Relevance of Heat Transfer |
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25 | (1) |
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25 | (3) |
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28 | (15) |
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30 | (13) |
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Introduction to Conduction |
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43 | (30) |
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The Conduction Rate Equation |
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44 | (2) |
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The Thermal Properties of Matter |
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46 | (6) |
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46 | (3) |
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Other Relevant Properties |
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49 | (3) |
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The Heat Diffusion Equation |
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52 | (8) |
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Boundary and Initial Conditions |
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60 | (3) |
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63 | (10) |
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63 | (1) |
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63 | (10) |
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One-Dimensional, Steady-State Conduction |
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73 | (88) |
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74 | (12) |
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74 | (2) |
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76 | (1) |
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77 | (2) |
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79 | (7) |
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An Alternative Conduction Analysis |
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86 | (4) |
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90 | (9) |
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90 | (6) |
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96 | (3) |
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Summary of One-Dimensional Conduction Results |
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99 | (1) |
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Conduction with Thermal Energy Generation |
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100 | (10) |
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100 | (6) |
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106 | (4) |
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Application of Resistance Concepts |
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110 | (1) |
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Heat Transfer from Extended Surfaces |
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110 | (23) |
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A General Conduction Analysis |
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113 | (1) |
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Fins of Uniform Cross-Sectional Area |
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114 | (6) |
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120 | (4) |
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Fins of Nonuniform Cross-Sectional Area |
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124 | (2) |
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Overall Surface Efficiency |
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126 | (7) |
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133 | (28) |
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134 | (1) |
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134 | (27) |
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Two-Dimensional, Steady-State Conduction |
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161 | (50) |
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162 | (1) |
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The Method of Separation of Variables |
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163 | (4) |
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167 | (6) |
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Methodology of Constructing a Flux Plot |
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167 | (2) |
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Determination of the Heat Transfer Rate |
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169 | (1) |
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The Conduction Shape Factor |
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169 | (4) |
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Finite-Difference Equations |
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173 | (8) |
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173 | (1) |
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Finite-Difference Form of the Heat Equation |
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174 | (1) |
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The Energy Balance Method |
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175 | (6) |
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Finite-Difference Solutions |
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181 | (12) |
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The Matrix Inversion Method |
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181 | (1) |
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182 | (6) |
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188 | (5) |
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193 | (18) |
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193 | (1) |
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194 | (17) |
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211 | (72) |
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The Lumped Capacitance Method |
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212 | (3) |
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Validity of the Lumped Capacitance Method |
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215 | (3) |
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General Lumped Capacitance Analysis |
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218 | (5) |
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223 | (2) |
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The Plane Wall with Convection |
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225 | (4) |
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225 | (1) |
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226 | (1) |
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226 | (2) |
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Additional Considerations |
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228 | (1) |
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Radial Systems with Convection |
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229 | (7) |
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229 | (1) |
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230 | (1) |
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230 | (1) |
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Additional Considerations |
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231 | (5) |
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236 | (6) |
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242 | (6) |
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Finite-Difference Methods |
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248 | (15) |
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Discretization of the Heat Equation: The Explicit Method |
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248 | (8) |
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Discretization of the Heat Equation: The Implicit Method |
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256 | (7) |
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263 | (20) |
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263 | (1) |
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263 | (20) |
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Introduction to Convection |
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283 | (62) |
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The Convection Transfer Problem |
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284 | (5) |
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The Convection Boundary Layers |
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289 | (5) |
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The Velocity Boundary Layer |
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289 | (1) |
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The Thermal Boundary Layer |
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290 | (1) |
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The Concentration Boundary Layer |
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291 | (2) |
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Significance of the Boundary Layers |
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293 | (1) |
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Laminar and Turbulent Flow |
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294 | (2) |
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The Convection Transfer Equations |
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296 | (12) |
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The Velocity Boundary Layer |
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296 | (5) |
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The Thermal Boundary Layer |
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301 | (2) |
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The Concentration Boundary Layer |
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303 | (5) |
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Approximations and Special Conditions |
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308 | (3) |
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Boundary Layer Similarity: The Normalized Convection Transfer Equations |
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311 | (7) |
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Boundary Layer Similarity Parameters |
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311 | (2) |
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Functional Form of the Solutions |
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313 | (5) |
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Physical Significance of the Dimensionless Parameters |
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318 | (3) |
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321 | (7) |
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The Heat and Mass Transfer Analogy |
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321 | (4) |
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325 | (2) |
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327 | (1) |
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The Effects of Turbulence |
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328 | (3) |
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The Convection Coefficients |
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331 | (1) |
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332 | (13) |
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332 | (1) |
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333 | (12) |
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345 | (74) |
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347 | (1) |
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The Flat Plate in Parallel Flow |
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348 | (11) |
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Laminar Flow: A Similarity Solution |
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349 | (6) |
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355 | (1) |
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Mixed Boundary Layer Conditions |
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355 | (2) |
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357 | (2) |
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Methodology for a Convection Calculation |
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359 | (7) |
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The Cylinder in Cross Flow |
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366 | (8) |
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366 | (2) |
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Convection Heat and Mass Transfer |
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368 | (6) |
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374 | (3) |
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Flow Across Banks of Tubes |
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377 | (10) |
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387 | (6) |
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Hydrodynamic and Geometric Considerations |
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387 | (2) |
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Convection Heat and Mass Transfer |
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389 | (4) |
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393 | (1) |
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394 | (25) |
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396 | (1) |
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396 | (23) |
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419 | (62) |
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Hydrodynamic Considerations |
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420 | (5) |
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420 | (1) |
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421 | (1) |
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Velocity Profile in the Fully Developed Region |
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422 | (2) |
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Pressure Gradient and Friction Factor in Fully Developed Flow |
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424 | (1) |
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425 | (6) |
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426 | (1) |
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427 | (1) |
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Fully Developed Conditions |
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427 | (4) |
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431 | (8) |
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431 | (1) |
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Constant Surface Heat Flux |
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432 | (3) |
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Constant Surface Temperature |
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435 | (4) |
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Laminar Flow in Circular Tubes: Thermal Analysis and Convection Correlations |
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439 | (5) |
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The Fully Developed Region |
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439 | (4) |
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443 | (1) |
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Convection Correlations: Turbulent Flow in Circular Tubes |
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444 | (5) |
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Convection Correlations: Noncircular Tubes |
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449 | (5) |
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The Concentric Tube Annulus |
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454 | (2) |
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Heat Transfer Enhancement |
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456 | (1) |
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457 | (2) |
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459 | (22) |
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461 | (1) |
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461 | (20) |
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481 | (54) |
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482 | (2) |
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484 | (2) |
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Similarity Considerations |
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486 | (1) |
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Laminar Free Convection on a Vertical Surface |
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487 | (3) |
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The Effects of Turbulence |
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490 | (2) |
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Empirical Correlations: External Free Convection Flows |
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492 | (14) |
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493 | (3) |
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Inclined and Horizontal Plates |
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496 | (5) |
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The Long Horizontal Cylinder |
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501 | (3) |
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504 | (2) |
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Free Convection within Parallel Plate Channels |
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506 | (3) |
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506 | (2) |
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508 | (1) |
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Empirical Correlations: Enclosures |
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509 | (6) |
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509 | (3) |
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512 | (1) |
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513 | (2) |
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Combined Free and Forced Convection |
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515 | (1) |
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516 | (1) |
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516 | (19) |
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517 | (1) |
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518 | (17) |
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535 | (46) |
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Dimensionless Parameters in Boiling and Condensation |
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536 | (1) |
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537 | (1) |
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538 | (5) |
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538 | (2) |
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540 | (3) |
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Pool Boiling Correlations |
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543 | (9) |
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543 | (2) |
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Critical Heat Flux for Nucleate Pool Boiling |
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545 | (1) |
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545 | (1) |
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546 | (1) |
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Parametric Effects on Pool Boiling |
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547 | (5) |
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Forced-Convection Boiling |
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552 | (2) |
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External Forced-Convection Boiling |
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552 | (1) |
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553 | (1) |
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Condensation: Physical Mechanisms |
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554 | (2) |
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Laminar Film Condensation on a Vertical Plate |
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556 | (4) |
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Turbulent Film Condensation |
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560 | (5) |
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Film Condensation on Radial Systems |
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565 | (2) |
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Film Condensation in Horizontal Tubes |
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567 | (1) |
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568 | (1) |
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569 | (12) |
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569 | (2) |
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571 | (10) |
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581 | (52) |
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582 | (2) |
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The Overall Heat Transfer Coefficient |
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584 | (3) |
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Heat Exchanger Analysis: Use of the Log Mean Temperature Difference |
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587 | (12) |
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The Parallel-Flow Heat Exchanger |
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588 | (2) |
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The Counterflow Heat Exchanger |
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590 | (1) |
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Special Operating Conditions |
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591 | (1) |
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Multipass and Cross-Flow Heat Exchangers |
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592 | (7) |
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Heat Exchanger Analysis: The Effectiveness-NTU Method |
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599 | (8) |
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599 | (1) |
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Effectiveness-NTU Relations |
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600 | (7) |
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Methodology of a Heat Exchanger Calculation |
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607 | (6) |
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613 | (5) |
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618 | (15) |
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619 | (1) |
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619 | (14) |
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Radiation: Processes and Properties |
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633 | (84) |
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634 | (3) |
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637 | (9) |
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637 | (3) |
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640 | (3) |
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643 | (2) |
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645 | (1) |
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646 | (8) |
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647 | (1) |
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647 | (1) |
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648 | (1) |
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649 | (5) |
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654 | (8) |
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Surface Absorption, Reflection, and Transmission |
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662 | (10) |
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664 | (1) |
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665 | (1) |
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666 | (1) |
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667 | (5) |
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672 | (1) |
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673 | (7) |
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680 | (6) |
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686 | (31) |
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688 | (1) |
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689 | (28) |
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Radiation Exchange Between Surfaces |
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717 | (66) |
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718 | (10) |
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718 | (1) |
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719 | (9) |
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Blackbody Radiation Exchange |
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728 | (3) |
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Radiation Exchange Between Diffuse, Gray Surfaces in an Enclosure |
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731 | (15) |
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Net Radiation Exchange at a Surface |
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732 | (1) |
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Radiation Exchange Between Surfaces |
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732 | (6) |
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The Two-Surface Enclosure |
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738 | (1) |
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738 | (4) |
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742 | (4) |
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746 | (3) |
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749 | (5) |
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750 | (1) |
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Gaseous Emission and Absorption |
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750 | (4) |
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754 | (29) |
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755 | (1) |
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755 | (28) |
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783 | (42) |
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Physical Origins and Rate Equations |
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784 | (7) |
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784 | (1) |
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785 | (1) |
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786 | (1) |
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787 | (4) |
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Mass Diffusion Coefficient |
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791 | (1) |
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791 | (4) |
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Conservation of Species for a Control Volume |
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792 | (1) |
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The Mass Diffusion Equation |
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792 | (3) |
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Boundary and Initial Conditions |
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795 | (3) |
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Mass Diffusion Without Homogeneous Chemical Reactions |
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798 | (12) |
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Stationary Media with Specified Surface Concentrations |
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799 | (3) |
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Stationary Media with Catalytic Surface Reactions |
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802 | (3) |
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Equimolar Counterdiffusion |
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805 | (3) |
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808 | (2) |
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Mass Diffusion with Homogeneous Chemical Reactions |
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810 | (3) |
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813 | (12) |
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817 | (1) |
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818 | (7) |
| Appendix A Thermophysical Properties of Matter |
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825 | (30) |
| Appendix B Mathematical Relations and Functions |
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855 | (6) |
| Appendix C Thermal Conditions Associated with Uniform Energy Generation in One-Dimensional, Steady-State Systems |
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861 | (8) |
| Appendix D Graphical Representation of One-Dimensional, Transient Conduction in the Plane Wall, Long Cylinder, and Sphere |
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869 | (6) |
| Appendix E An Integral Laminar Boundary Layer Solution for Parallel Flow Over a Flat Plate |
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875 | (6) |
| Index |
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881 | |
