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By John H Lienhard

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3 prediction, and his work included the initial formulation of quantum mechanics. 3806503× 10−23 J/K. Radiant heat exchange. Suppose that a heated object (1 in Fig. 16a) radiates only to some other object (2) and that both objects are thermally black. All heat leaving object 1 arrives at object 2, and all heat arriving at object 1 comes from object 2. 31) If the first object “sees” other objects in addition to object 2, as indicated in Fig. 16b, then a view factor (sometimes called a configuration factor or a shape factor ), F1–2 , must be included in eqn.

Hsu and R. W. Graham. Transport Processes in Boiling and Two-Phase Systems Including Near-Critical Systems. American Nuclear Society, LaGrange Park, IL, 1986. 22] W. M. Kays and A. L. London. Compact Heat Exchangers. McGrawHill Book Company, New York, 3rd edition, 1984. 23] G. F. Hewitt, editor. Heat Exchanger Design Handbook 1998. Begell House, New York, 1998. 24] R. B. Bird, W. E. Stewart, and E. N. Lightfoot. Transport Phenomena. , New York, 1960. 25] A. F. Mills. Mass Transfer. , Upper Saddle River, 2001.

Thus we can usually write k = k(T ). The assumption that we really want to make is that k is constant. Whether or not that is legitimate must be determined in each case. As is apparent from Fig. 2 and Fig. 3, k almost always varies with temperature. It always rises with T in gases at low pressures, but it may rise or fall in metals or liquids. 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.

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