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7.7 PROBLEMS       159





                 Table 7.1 Excerpt from Steam Tables, Showing Values on the Saturated Liquid and Vapour
                Lines (Rogers and Mayhew (1994)).
                                             Specific    Change of     Entropy of     Enthalpy of
                  Temperature    Pressure    Volume      Specific       Liquid, s f    Liquid, h f
                                               3
                     ( C)         (bar)      (m /kg)    Volume, v fg   (kJ/kg K)      (kJ/kg K)

                      115         1.691
                      120         1.985      0.001060     0.8845        1.530           505
                      125         2.321


                                                       dp   2:321   1:691
                                                                                       3
                                                                            5
                  At 120 C, the slope of the saturation line is  z        10 ¼ 6:30   10 .

                                                       dT       10
                  From the Clausius–Clapeyron equation, Eqn (7.82)
                                              s 2   s 1  dp  s g   s f
                                                    ¼    ¼       ;
                                                v fg  dT     v fg
               giving
                                             dp                          3   3
                                  s g ¼ s f þ v fg  ¼ 1:530 þ 0:8845   6:30   10 =10
                                             dT
                                         ¼ 1:530 þ 5:57235 ¼ 7:102 kJ=kg K
                  The specific enthalpy on the saturated vapour line is

                                        h g ¼ h f þ Ts fg
                                           ¼ 505 þð120 þ 273Þ  5:57235
                                           ¼ 2694:9kJ=kg K
                  These values are in good agreement with the tables of properties; the value of s g ¼ 7.127 kJ/kg K,
               while h g ¼ 2707 kJ/kg at a temperature of 120.2 C.


               7.6 CONCLUDING REMARKS
               Thermodynamic relationships between properties have been developed which are independent of a
               particular fluid. These can be used to evaluate derived properties from primitive ones and to extend
               empirical data.


               7.7 PROBLEMS

               P7.1 For a van der Waals gas that obeys the state equation

                                                      RT     a
                                                  p ¼
                                                      v   b  v 2
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