Page 54 - DJJ20063- Thermodynamics 1
P. 54

DJJ20063- Thermodynamics 1



                      Example 2.7


                        Determine the specific enthalpy of dry saturated steam at 103 bar.



                      Solution to Example 2.7


                                                                         h − 2725    2715 − 2725
                                 P                                        g        =
                                                                         103 −100     105 −100
                               105

                               103                                                   3 (−10 )
                                                                                      h =   + 2725
                                                                                 g
                               100                                                      5

                                                              hg
                                       2725  hg   2715                               h  =  2719 kJ/kg


                                                                                 g

                      Example 2.8


                                                                                o
                        Determine the specific volume of steam at 8 bar and 220 C.


                      Solution to Example 2.8

                                                                                            o
                      From the Steam Tables at 8 bar, the saturated temperature (ts) is 170.4  C.
                                                                                                    o
                      The steam is at superheated condition as the temperature of the steam is 220 C > ts.

                      An extract from the Steam Tables,

                           p / (bar)        t              200            220           250

                                             o
                               o
                           (ts /  C)        ( C)
                               8        v                0.2610           v           0.2933
                           (170.4)



                                      P
                                                                              .
                                                                                       .
                                                                                                .
                                    250                                  v − 0 2610  =  0 2933 − 0 2610
                                                                         220 − 200       250 − 200
                                    220

                                    200
                                                                                                3
                                                                                   v = 0 27392.   m /kg
                                                                   v
                                          0.2610  v    0.2933
                                                                                                 45 | P a g e
   49   50   51   52   53   54   55   56   57   58   59