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4.5.  FLOW IN CIRCULAR PIPES                                         95


           reduces Eq.  (4.54) to

                                                                            (4.56)

           Engineering problems associated with pipe flow are classified as follows:
              0  Determine the pressure drop, IAPI, or the pump size, I@;  given the volumetric
                flow rate,  Q, the pipe diameter, D, and the physical properties of  the fluid,
                p  and p.

              0  Determine the volumetric flow rate,  Q; given the pressure drop,  IAPI, the
                pipe diameter, D, and the physical properties of  the fluid, p and p.

              0  Determine the pipe diameter, D; given the volumetric flow rate, &, the pres-
                sure drop, lAP(, and the physical properties of  the fluid, p  and p.


           4.5.1  Friction Factor Correlations
           4.5.1.1  Laminar flow correlation

           For laminar flow in a circular pipe, i.e.,  Re = D(v)p/p < 2100, the solution of  the
           equations of  change gives4
                                                                            (4.5-7)

              The friction factor f appearing in Eqs.  (4.56) and  (4.57) is also called the
           Fanning fiction factor.  However, this is not  the only definition for f available
           in the literature.  Another  commonly used  definition for f  is the  Darcy fraction
           factor, fo, which is four times larger than the Fanning friction factor, i.e., fo = 4 f.
           Therefore, for laminar flow
                                                64
                                          fD = Re                           (4.5-8)

           4.5.1.2  Turbulent flow correlation
           Since no theoretical solution exists for turbulent flow, the friction factor is usually
           determined  from the  Moody chart  (1944) in which it is expressed as a  function
           of  the Reynolds number, Re, and the relative pipe wall roughness, &ID. Moody
           prepared this chart by using the equation proposed by Colebrook (1938)

                                 1
                                --                                          (4.59)
                                d7
           where E  is the surface roughness of  the pipe wall in meters.

             4See Section 9.1.3.1 in Chapter 9.
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