Heat TransferCambridge University Press, 2009 - 1107 páginas The single objective of this book is to provide engineers with the capability, tools, and confidence to solve real-world heat transfer problems. It includes many advanced topics, such as Bessel functions, Laplace transforms, separation of variables, Duhamel's theorem, and complex combination, as well as high order explicit and implicit numerical integration algorithms. These analytical and numerical solution methods are applied to topics not considered in most textbooks. Examples are heat exchangers involving fluids with varying specific heats or phase changes; heat exchangers in which axial conduction is a concern; and regenerators. To improve readability, derivations of important results are presented completely, without skipping steps, which reduces student frustration and improves retention. The examples in the book are ubiquitous, not trivial "textbook" exercises. They are rather complex and timely real-world problems that are inherently interesting. This textbook integrates the computational software packages Maple, MATLAB, FEHT, and Engineering Equation Solver (EES) directly with the heat transfer material. |
Contenido
1 OneDimensional SteadyState Conduction | 1 |
2 TwoDimensional SteadyState Conduction | 202 |
3 Transient Conduction | 302 |
4 External Forced Convection | 483 |
5 Internal Forced Convection | 635 |
6 Natural Convection | 735 |
7 Boiling and Condensation | 778 |
8 Heat Exchangers | 823 |
9 Mass Transfer | 974 |
10 Radiation | 979 |
Appendices | 1089 |
| 1091 | |
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analytical solution approximately average heat transfer average Nusselt number axial conduction Biot number boundary conditions boundary layer C₁ capacitance rate cold-fluid cold-side computed condensation constant control volume convection correlations cylinder diameter differential equation dimensionless discussed in Section duct energy balance EXAMPLE friction factor function heat exchanger heat flux heat transfer coefficient heat transfer rate Heun's method inlet Inputs integration internal flow kg/s laminar Laplace transform leads length liquid Maple mass flow rate MATLAB matrix momentum number of nodes numerical model numerical solution obtained parameter plot position Prandtl number pressure problem rate of heat ratio regenerator Reynolds number separation of variables shown in Figure solve specific heat capacity step Substituting Eq surface temperature Tabstops TC,in technique temperature difference temperature distribution TH,in thermal conductivity thermal energy thermal resistance Tlumped tube turbulent volumetric W/m² wall y-direction
