Page 353 - Chemical engineering design
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                                                        CHEMICAL ENGINEERING
                           Example 8.9
                           Estimate the specific heat capacity of isopropyl alcohol at 500 K.
                           Solution
                           Structural formula
                                                               CH 3

                                                         CH 3  CH    OH

                                Group       No. of       a        b ð 10 2    c ð 10 4    d ð 10 6
                                              2         5.0970    17.9480     0.7134      0.0095
                                   CH 3
                                              1       14.7516     14.3020     1.1791      0.03356
                                   CH

                                   OH         1        27.2691     0.5640      0.1733     0.0068
                                Total                  17.6145    31.6860     1.7190      0.0363

                                                                           4 2
                                                           2
                                                                                              3
                                                                                            6
                                 Ž
                                C D 17.6145 C 31.6860 ð 10 T   1.7192 ð 10 T C 0.0363 ð 10 T .
                                 p
                           At 500 K, substitution gives:
                                                                        Ž
                                                       C p D 137.6 kJ/kmol C
                                                                         Ž
                                                        Ž
                           Experimental value, 31.78 cal/mol C D 132.8 kJ/kmol C, error 4 per cent.
                                  8.10. ENTHALPY OF VAPORISATION (LATENT HEAT)
                           The latent heats of vaporisation of the more commonly used materials can be found in
                           the handbooks and in Appendix C.
                             A very rough estimate can be obtained from Trouton’s rule (Trouton, 1884), one of the
                           oldest prediction methods.
                                                           L v
                                                              D constant                         8.15
                                                           T b
                           where L v D latent heat of vaporisation, kJ/kmol,
                                 T b D normal boiling point, K.
                           For organic liquids the constant can be taken as 100.
                             More accurate estimates, suitable for most engineering purposes, can be made from
                           a knowledge of the vapour pressure-temperature relationship for the substance. Several
                           correlations have been proposed; see Reid et al. (1987).
                             The equation presented here, due to Haggenmacher (1946), is derived from the Antoine
                           vapour pressure equation (see Section 8.11).
                                                                    2
                                                              8.32 BT z
                                                         L v D                                   8.16
                                                                T C C  2
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