## Principles of Heat TransferPRINCIPLES OF HEAT TRANSFER was first published in 1959, and since then it has grown to be considered a classic within the field, setting the standards for coverage and organization within all other Heat Transfer texts. The book is designed for a one-semester course in heat transfer at the junior or senior level, however, flexibility in pedagogy has been provided. Following several recommendations of the ASME Committee on Heat Transfer Education, Kreith, Manglik, and Bohn present relevant and stimulating content in this fresh and comprehensive approach to heat transfer, acknowledging that in today's world classical mathematical solutions to heat transfer problems are often less influential than computational analysis. This acknowledgement is met with the emphasize that students must still learn to appreciate both the physics and the elegance of simple mathematics in addressing complex phenomena, aiming at presenting the principles of heat transfer both within the framework of classical mathematics and empirical correlations. Important Notice: Media content referenced within the product description or the product text may not be available in the ebook version. |

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### Table des matières

Basic Modes of Heat Transfer | 2 |

Heat Conduction | 70 |

Numerical Analysis of Heat Conduction | 166 |

Analysis of Convection Heat Transfer | 230 |

Natural Convection | 296 |

Forced Convection Inside Tubes and Ducts | 350 |

Forced Convection Over Exterior Surfaces | 420 |

Heat Exchangers | 484 |

Heat Transfer by Radiation | 540 |

Heat Transfer with Phase Change | 624 |

Appendixes | 1 |

58 | |

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### Expressions et termes fréquents

analysis applied approximately Assume average body boiling boundary layer Btu/h calculate Chapter consider constant control volume convection heat transfer cooling correlation cylinder depends determine diameter difference dimensionless direction effective electrical emissivity energy engineering equal equation estimate evaluated example experimental face factor FIGURE flat fluid forced geometry given gives heat exchanger heat flow heat flux heat transfer coefficient horizontal increase inside insulation laminar length liquid mass material method natural Nusselt number obtained physical pipe plate pressure Problem properties radiation range rate of heat ratio relation resistance Reynolds number shape shown in Fig shows side solution solve Source space specified sphere steam steel surface temperature Table temperature distribution thermal conductivity thickness tion tube turbulent uniform unit vapor velocity wall