Page 76 - ebook fluid mechanics_finalize
P. 76

FLUID MECHANICS


                              b)     Discharge at section A = Discharge at section B


                                            Q =   Q
                                                    B
                                              A

                                              A  v =  A  v
                                           A  A    B  B

                                                  A  v
                                             v =   A  A
                                              B
                                                   A B

                                                   . 0  318 ( ) 4
                                                 =
                                                   ( ) 3.0  2



                                                  4=  5 .  m  s /



                                     For continuity of flow


                                     Q =   Q +  Q
                                             C
                                       B
                                                  D
                                     Q =   Q −  Q
                                                  C
                                       D
                                             B
                                            (A =  B  v B ) (A−  C v C  )


                                            ( ) 3.0  2     ( ) 2.0  2  
                                                     4
                                                       .
                                                                        
                                           =        5  −          4
                                              4              4       
                                            0=  . 192  m 3  s /



                                     For pipe BD



                                     Q =   A   v
                                                 D
                                             D
                                       D
                                               0=  . 192 m 3  s /


                                           Q
                                     v =    D
                                       D
                                           A D

                                           . 0  192 4
                                          =             10=  . 86 m  s /
                                           ( 15.0  ) 2








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