Page 135 - DJJ20063- Thermodynamics 1
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DJJ20063- Thermodynamics 1





                                           Feedback to Activity 3D





                      3.10    Neglecting the changes in potential energy, the steady flow energy equation is

                                                  C 2  −C  2   
                                                +
                              Q  −W  =   (h 2  − h 1 )   2  1   
                                                            
                                                  
                                                     2       
                                       
                              Q is negative since heat is lost from the steam to the surroundings
                                                       C 2  − C  2  
                                                     +
                              specific W = (h  − h  )   1    2   - Q
                                              1   2            
                                                          2    
                                                              2
                                                           ( 16 −  37 2 )
                                               = (2999-2530) +         −  25
                                                             2x 10 3
                                              = 434.443 kJ/kg


                              The steam flow rate = 324000/3600 = 90 kg/s

                               W = 434.443 x 90

                                       = 39099.97 kJ/s or kW

                                        39100 kW

                                        39.1 MW




                      3.11    The steady energy flow equation for nozzle gives

                                                             C  2  −C 2   
                                                           +
                                                   h
                                                                      
                                            0 = m   ( − h 1 )    2  1   
                                                     2
                                                                2      
                                                  

                                     On simplification,

                                            C =      ( 2 h − h +  1 2
                                                            ) C
                                              2
                                                      1
                                                           2

                                                                       3
                                                                              2
                                                             3
                                                  = 2(1200x 10 - 900x10 ) + 200
                                           = 800 m/s

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