Page 105 - Bird R.B. Transport phenomena
P. 105

90  Chapter 3  The Equations of Change for Isothermal Systems

                                                                               Fixed
                                                                            Torsion wire with torsion constant k
                                                                                                     t
                                                       Bob is suspended     Mirror
              Outer cylinder   v  is a function  of r  and free to rotate
                                0
                 rotating  /
                      A,


                                                   In this  У                             Fixed
                                                  region the\                           cylindrical
                                                   fluid is                              surfaces
                                                  moving
                                                    with
                  Inner cylinder                  v  = v (r)
                   stationary                      e  e                                Rotating
                                                                                       cylindrical
                                                                                         cup
                                                         Fluid inside
                                                        is stationary
                                (a)                                    (b)
              Fig. 3.6-1.  (fl)Tangential laminar flow  of an incompressible fluid  in the space between two cylinders; the outer
              one is moving with an angular velocity  il .  (b) A diagram  of a Couette viscometer. One measures the angular
                                               0
              velocity  Cl  of the cup and the deflection  6  of the bob at steady-state operation. Equation 3.6-31 gives the vis-
                       0
                                               B
              cosity /л in terms of Д, and the torque T  = k 6 .
                                                   B
                                              z
                                                  t
                            shown  in the figure.  Because  of  the arrangement used, end  effects  over  the region  including
                            the bob height L are  negligible.
                               To analyze  this measurement, we  apply  the equations  of  continuity and motion for con-
                            stant p and fi  to the tangential flow in the annular region around the bob. Ultimately we  want
                            an  expression  for  the viscosity  in  terms  of  (the z-component of)  the torque  7\  on  the inner
                            cylinder, the angular velocity  fl 0  of the rotating cup, the bob height  L, and the radii KR and R
                            of the bob and cup, respectively.
      SOLUTION              In the portion  of  the annulus under consideration the fluid  moves  in a circular pattern. Rea-
                            sonable postulates  for  the velocity  and pressure  are: v  = v {r), v  = 0, V-.  = 0, and p  = p{r, z).
                                                                       ()  n   r
                            We expect p to depend on z because of gravity and on r because  of the centrifugal  force.
                               For these postulates all the terms in the equation of continuity are zero, and the compo-
                            nents  of the equation of motion simplify  to
                                                               Щ    dp
                                                                =
                            r-component                     ~PT ~~a~                            (3.6-20)
                                                                  d
                            ^-component                                                         (3.6-21)

                            z-component                                                         (3.6-22)

                            The  second  equation gives  the  velocity  distribution.  The  third  equation  gives  the  effect  of
                            gravity on the pressure (the hydrostatic effect), and the first equation tells how the centrifugal
                            force  affects  the pressure.  For the  problem  at  hand  we  need  only  the  ^-component of  the
                            equation  of motion. 2



                               2  See R. B. Bird, С  F. Curtiss, and W. E. Stewart, Chem. Eng. Sci., 11,114-117 (1959) for a method of
                            getting p(r, z) for this system. The time-dependent buildup to the steady-state profiles is given by R.  B.
                            Bird and С  F. Curtiss, Chem. Eng. Sci., 11,108-113 (1959).
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