Heat and Mass TransferCRC Press, 1995 M02 13 - 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. |
Contents
CONTENTS | 5 |
7 | 38 |
2 | 99 |
| 123 | |
MULTIDIMENSIONAL AND UNSTEADY CONDUCTION | 124 |
CONVECTION FUNDAMENTALS AND CORRELATIONS | 244 |
CONTENTS | 251 |
1 Laminar Flow of Oil | 277 |
15 Pressure Drop in a MultipleTube Exchanger | 762 |
9 | 808 |
L | 820 |
HIGH MASS TRANSFER RATE THEORY | 921 |
5 Evaporation of a Water Droplet | 949 |
MASS EXCHANGERS | 1044 |
Incinerator | 1063 |
APPENDIX | 1137 |
Receiver | 298 |
CONVECTION ANALYSIS | 372 |
4 A NaturalConvection Water Boundary Layer | 417 |
6 | 476 |
6 | 488 |
2 Shape Factor Determination | 502 |
8 Effective Temperature of the Sun | 526 |
CONDENSATION EVAPORATION AND BOILING | 596 |
HEAT EXCHANGERS | 705 |
1043 | 1156 |
pressures | 1186 |
B UNITS CONVERSION FACTORS AND MATHEMATICS | 1199 |
CHARTS | 1209 |
| 1217 | |
Nomenclature | 1227 |
| 1233 | |
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Common terms and phrases
analysis 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 natural convection negligible Nusselt number obtained overall heat transfer particle Prandtl number pressure drop problem properties radiation resistance Reynolds number Section shape factor shown in Fig Solution Given solved species stream surface T₁ Table temperature profile thermal conductivity thermocouple thickness Tsat tube vapor velocity viscosity W/m² W/m² K ρι ди ду дх
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