By Lienhard J.H.

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Sarofim. Radiative Transfer. McGraw-Hill Book Company, New York, 1967. 17] R. Siegel and J. R. Howell. Thermal Radiation Heat Transfer. , 4th edition, 2001. 18] M. F. Modest. Radiative Heat Transfer. McGraw-Hill, New York, 1993. 19] P. B. Whalley. Boiling, Condensation, and Gas-Liquid Flow. Oxford University Press, Oxford, 1987. 20] J. G. Collier and J. R. Thome. Convective Boiling and Condensation. Oxford University Press, Oxford, 3rd edition, 1994. 21] Y. Y. Hsu and R. W. Graham. Transport Processes in Boiling and Two-Phase Systems Including Near-Critical Systems.

The problem is that of assessing whether or not k is approximately constant in the range of interest. We could safely take k to be a constant for iron between 0◦ and 40◦ C (see Fig. 2), but we would incur error between −100◦ and 800◦ C. 1) that if k varies linearly with T , and if heat transfer is plane and steady, then q = k∆T /L, with k evaluated at the average temperature in the plane. If heat transfer is not planar or if k is not simply A + BT , it can be much more difficult to specify a single accurate effective value of k.

The heat conduction component of most heat exchanger problems is more complex than the simple planar analyses done in Chapter 1. To do such analyses, we must next derive the heat conduction equation and learn to solve it. Consider the general temperature distribution in a three-dimensional body as depicted in Fig. 1. For some reason (heating from one side, in this case), there is a space- and time-dependent temperature field in the body. 1 A three-dimensional, transient temperature field. isothermal surfaces, T1 , T2 , and so on.

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A heat transfer textbook by Lienhard J.H.


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