U An extension of the general method for correlating forcedconvection heat transfer data is proposed for the case of a coil and the inside surface of a vessel with the fluid agitated by a flat paddle.
Substitution in Equation 1gives: logo = XtXi (7.30-,.151,,g,m+ 17!14( ) (4) Tin• accuracy of Equation 4 is shown in Table 1 by comparing t lie calculated value of a with the ratio of the vapor pressures for a series of binary mixtures at pressures ranging from 10 to 1200 mm.Deviations between the two values become appreciable only at large boiling point differences, where the value' of (1 also deviates appreciably from true relative volatility.
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