Heat and Mass TransferCRC Press, 13 févr. 1995 - 300 pages This complete reference book covers topics in heat and mass transfer, containing extensive information in the form of interesting and realistic examples, problems, charts, tables, illustrations, and more. Heat and Mass Transfer emphasizes practical processes and provides the resources necessary for performing accurate and efficient calculations. This excellent reference comes with a complete set of fully integrated software available for download at crcpress.com, consisting of 21 computer programs that facilitate calculations, using procedures developed in the text. Easy-to-follow instructions for software implementation make this a valuable tool for effective problem-solving. |
Table des matières
CHAPTER | 2 |
STEADY ONEDIMENSIONAL HEAT CONDUCTION | 62 |
MULTIDIMENSIONAL AND UNSTEADY CONDUCTION | 124 |
8 Temperature Fluctuations in a Diesel Engine Cylinder | 166 |
15 Convective Heating of a Resin Slab | 206 |
CONVECTION FUNDAMENTALS AND CORRELATIONS | 244 |
CONTENTS | 251 |
Receiver | 298 |
16 Heat Transfer in a VerticalTube Water | 659 |
HEAT EXCHANGERS | 705 |
ELEMENTARY MASS TRANSFER | 808 |
HIGH MASS TRANSFER RATE THEORY | 921 |
MASS EXCHANGERS | 1044 |
APPENDIX | 1137 |
1043 | 1156 |
807 | 1167 |
12 A Tube Bank Water Heater | 321 |
CONVECTION ANALYSIS | 372 |
3 A Plate with an Unheated Starting Length | 403 |
THERMAL RADIATION | 488 |
9 Calculation of Sky Emittance and Effective | 527 |
Directional Characteristics of Surface Radiation | 533 |
CONDENSATION EVAPORATION AND BOILING | 596 |
pressures | 1186 |
B UNITS CONVERSION FACTORS AND MATHEMATICS | 1199 |
CHARTS | 1209 |
| 1217 | |
Nomenclature | 1227 |
| 1233 | |
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Expressions et termes fréquents
analysis approximately assumed Assumptions average boiling boundary conditions boundary layer calculate constant control volume convective heat transfer cooling correlations counterflow cylinder determine diameter differential equation diffusion coefficient dimensionless dimensionless groups droplet effect emittance engineering enthalpy estimate evaluated example Figure flat plate fluid Fourier's law fraction gases gives gradient heat conduction heat exchanger heat flow heat flux heat loss heat transfer coefficient heatpipe insulated isothermal J/kg kg/m³ kg/s laminar flow length liquid m²/s mass transfer molecules momentum natural convection negligible Nusselt number obtained overall heat transfer particle Prandtl number pressure drop problem properties radiation resistance result Reynolds number Section shape factor shown in Fig Solution Given solved species sphere stream surface T₁ Table temperature profile thermal conductivity thermocouple thickness Tsat tube turbulent flow vapor viscosity W/m² W/m² K ди ду дх
Fréquemment cités
Page 371 - The lower plate is stationary, and the upper plate moves with a uniform velocity ue.