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By D. Lide, M. Paul

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1973, IEEE Trans. EI-8, 10. 11. , Sato, T. , 1960, Br. J. Appl. Phys. 11, 539. 12. Ahsmann, S. , 1947, Appl. Scient. Res. Al, 35. 13. Turnbull, R. , 1968, Physics Fluids 11, 2588. l Test cell arrangement and tube array (dashed) from v/hich it is derived 722 Symposium Series No. 2 Nu I I 100 1—I—I—I — I 1 Reynolds number, Re Comparison of test results for zero stress (0 = oil cooled, ^ = oil heated) with best fit line for those of ZukausKas (5). m, ^,9 I I I 1000 Fig. 3 Variation of oii-side neat transfer to oil with flow rate.

However, the equivalent view factor corresponding to an absorption coefficient of zero is also calculated. This should, ideally, be equal to the view factor calculated by the normal, accurate technique. The view factor with absorption is then corrected using the following equation: Accurate view factor with absorption = coarse view factor with absorption coarse view factor without absorption x accurate view factor (9) without absorption The sum of the modified view factors from any element will now be less than unity.

Symposium Series No. 86 CONCLUSIONS For single phase flow equation (1) summarises the data for pressure drop and equation (2) for heat transfer for flow over the bundles of finned tubes described in Table 1.

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