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§2.3  Flow Through a Circular Tube  51

                This first-order  separable  differential  equation may be integrated  to give




                The  constant C  is evaluated  from  the boundary condition
                             2
                B.C. 2:                       at r  = R,  v z  = 0                   (2.3-17)
                                                2
                                             (
                From this C  is found  to be  (SPQ —3> )R /4IJLL.  Hence the velocity  distribution  is
                          2
                                              L
                                                                                    (2.3-18)

                We  see  that  the  velocity  distribution  for  laminar, incompressible  flow  of  a Newtonian
                fluid  in  a long tube is parabolic  (see Fig. 2.3-2).
                    Once  the  velocity  profile  has  been  established,  various  derived  quantities  can  be
                obtained:
                    (i)  The maximum velocity v  occurs at r  = 0 and  is
                                           zmax
                                                                                    (2.3-19)

                    (ii)  The average velocity (v ) is obtained by dividing  the total volumetric flow rate by
                                           z
                        the  cross-sectional  area
                                             Г2тг  fR
                                                  v
                                            J   J rdrd6    (9  _ ^  )R2
                                             n     rdrdd  ~   Sal     ~  2  2 max
                                                   z
                                                                         '
                                             J  Q  J Q
                                                                                2
                    (iii)  The mass rate of flow w  is the product of  the cross-sectional  area  TTR , the density
                        p,  and the average velocity  (v )
                                                 z
                                                 „  = «»'-»№                        (2 .3-21)
                                                          SfJLL
                                                                      2
                        This rather famous  result  is  called  the Hagen-Poiseuille  equation.  It is  used,  along
                        with  experimental  data  for  the rate of flow and the modified  pressure  difference,
                        to  determine the viscosity  of  fluids  (see Example 2.3-1) in a "capillary  viscometer."
                    (iv)  The z-component  of  the force, F,, of  the fluid on  the wetted surface of  the pipe  is
                        just the shear stress r  integrated  over  the wetted  area
                                          rz
                                                                  2
                                        F 2  =    f  -/x,  ^ 4  =  TTR (%  - <3> )
                                                                          L
                                                           2
                                          =  TTR ( 2  PO  -  p )  + irR Lpg          (2.3-22)
                                                     L
                        This  result  states  that  the viscous  force  F z  is  counterbalanced  by  the net  pres-
                        sure  force  and  the  gravitational  force.  This  is  exactly  what  one  would  obtain
                        from  making  a force balance over  the  fluid  in the tube.


                    2  G. Hagen, Ann.  Phys. Chem., 46,423-442 (1839); J. L. Poiseuille, Comptes Rendus,  11, 961 and  1041
                (1841). Jean Louis Poiseuille (1799-1869) (pronounced "Pwa-ztf'-yuh,"  with б is roughly the "oo"  in
                book) was a physician interested in the flow of blood. Although  Hagen and Poiseuille established the
                dependence of the flow rate on the fourth  power  of the  tube radius, Eq.  2.3-21 was first derived by E.
                Hagenbach, Pogg. Annalen  der Physik u. Chemie, 108,385-426 (1860).
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