Page 225 - Chemical engineering design
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                                                        2
                           where P f D pressure drop, N/m ,
                                    f D friction factor,  CHEMICAL ENGINEERING
                                    L D pipe length, m,
                                   d i D pipe inside diameter, m,
                                                        3
                                      D fluid density, kg/m ,
                                    u D fluid velocity, m/s.
                           The friction factor is a dependent on the Reynolds number and pipe roughness. The
                           friction factor for use in equation 5.3 can be found from Figure 5.7.
                                         The Renolds number is given by Re D    ð u ð d i  /      5.4

                           Values for the absolute surface roughness of commonly used pipes are given in Table 5.2.
                           The parameter to use with Figure 5.7 is the relative roughness, given by:

                                      relative roughness,e D absolute roughness/pipe inside diameter
                           Note: the friction factor used in equation 5.3 is related to the shear stress at the pipe wall,
                                                     2
                           R, by the equation f D  R/ u  . Other workers use different relationships. Their charts
                           for friction factor will give values that are multiples of those given by Figure 5.7. So, it is
                           important to make sure that the pressure drop equation used matches the friction factor chart.

                                                       Table 5.2.  Pipe roughness
                                              Material            Absolute roughness, mm
                                              Drawn tubing        0.0015
                                              Commercial steel pipe  0.046
                                              Cast iron pipe      0.26
                                              Concrete pipe       0.3 to 3.0

                           Non-Newtonian fluids
                           In equation 5.3, and when calculating the Reynolds number for use with Figure 5.7, the
                           fluid viscosity and density are taken to be constant. This will be true for Newtonian liquids
                           but not for non-Newtonian liquids, where the apparent viscosity will be a function of the
                           shear stress.
                             More complex methods are needed to determine the pressure drop of non-Newtonian
                           fluids in pipelines. Suitable methods are given in Volume 2, Chapter 4, and in Chabbra
                           and Richardson (1999); see also Darby (2001).

                           Gases
                           When a gas flows through a pipe the gas density is a function of the pressure and so is deter-
                           mined by the pressure drop. Equation 5.3 and Figure 5.7 can be used to estimate the pressure
                           drop, but it may be necessary to divide the pipeline into short sections and sum the results.
                           Miscellaneous pressure losses
                           Any obstruction to flow will generate turbulence and cause a pressure drop. So, pipe
                           fittings, such as: bends, elbows, reducing or enlargement sections, and tee junctions, will
                           increase the pressure drop in a pipeline.
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