Page 103 - Bird R.B. Transport phenomena
P. 103

88  Chapter 3  The Equations of Change for Isothermal Systems

                              We  now turn to the illustrative  examples.  The first  two are problems  that were dis-
                           cussed  in the preceding  chapter; we rework  these just to illustrate  the use of the equa-
                           tions  of change. Then we consider some other problems  that would  be difficult  to set up
                           by the shell balance method of Chapter 2.


      EXAMPLE 3.6-1        Rework  the tube-flow  problem  of Example  2.3-1 using  the equations  of continuity and  mo-
                           tion.  This  illustrates  the use of the tabulated  equations  for constant viscosity and density in
     Steady  Flow in a Long  cylindrical  coordinates, given in Appendix B.
     Circular Tube
                           SOLUTION
                           We postulate that v = b v {r, z). This postulate implies  that there is no radial flow (v  = 0) and
                                                                                              r
                                               z
                                              z
                           no tangential flow (v  = 0), and that v  does not depend on 0. Consequently, we can discard
                                            e
                                                         z
                           many terms from the tabulated equations of change, leaving
                           equation of continuity                                               (3.6-1)
                           r-equation of motion                                                 (3.6-2)

                           0-equation of motion             0 =  -                              (3.6-3)
                                                                 дв
                           z-equation of motion                                                 (3.6-4)

                           The first equation indicates that v  depends only on r; hence the partial derivatives  in the sec-
                                                     z
                           ond term on the right  side  of Eq. 3.6-4 can be replaced by ordinary  derivatives.  By using the
                           modified  pressure & = p + pgh (where h is the height above  some arbitrary  datum plane), we
                           avoid  the necessity  of calculating the components of g in cylindrical  coordinates, and we ob-
                           tain a solution valid for any orientation of the axis of the tube.
                              Equations  3.6-2 and 3.6-3 show  that <3> is a function  of z alone, and the partial  derivative
                           in the first term of Eq. 3.6-4 may be replaced by an ordinary derivative.  The only way that we
                           can have a function  of r plus a function  of z equal to zero is for each term individually  to be a
                           constant—say, C —so that Eq. 3.6-4 reduces to
                                        o
                                                             dv
                                                                                                (3.6-5)

                           The ty equation can be integrated at once. The ^-equation can be integrated by merely  "peel-
                           ing  off"  one operation after  another on the left side  (do not "work  out" the compound deriva-
                           tive there). This gives
                                                           9  = Qz + C,                         (3.6-6)

                                                             2
                                                      v z  = ^  r  + C  In r + C 3              (3.6-7)
                                                                  2
                           The four  constants of integration can be found  from  the boundary conditions:
                           B.C.I                       at z =  0,                               (3.6-8)
                           B.C. 2                      at z =  L,                               (3.6-9)
                           B.C3                        at r =  R,                               (3.6-10)
                           B.C. 4                      at r =  0,  v 7  = finite                (3.6-11)
                           The resulting  solutions are:
                                                                                                (3.6-12)
                                                          P  -  <3> )R 2
                                                          o     L
                                                       = •                                      (3.6-13)
                                                     v 7
                                                           4/JLL
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