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FLUID MECHANICS


                Example 4.16





                      An orifice meter consists of a 100 mm diameter in a 250 mm diameter pipe (Figure 4.15),

                       and has a coefficient discharge of 0.65. The pipe conveys oil of specific gravity 0.9. The
                       pressure difference between the two sides of the orifice plate is measured by a mercury

                       manometer, that leads to the gauge being filled with oil. If the difference in mercury levels

                       in the gauge is 760 mm, calculate the flow rate of oil in the pipeline.




                                 Pipe Area, A1









                                        P1             P2


                                        V1
                                                      Figure 4.15 : Orifice
                                                       V2

                                                                                                       X
                       Solution to Example 4.16
                                                   Orifice area A2                            C                C

                                     Let  v1  be  the  velocity  and  p1  the  pressure  immediately  upstream  of  the

                              orifice, and v2 and p2 are the corresponding values in the orifice. Then, ignoring

                              losses, by Bernoulli’s theorem,





                                      p 1  +  v 1 2  =  p 2  +  v 2 2       ——————(1)
                                          2 g       2 g






                                      v 2 2  − v 1 2  =  p −  p 2       ——————(2)
                                                  1
                                        2g         








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