Page 273 - Bird R.B. Transport phenomena
P. 273

.6  Molecular Theories for  Polymeric Liquids  257

                                                            Fig. 8.6-5.  Steady elongational
                   JUU  i  i  |  i  i  |  1  1  1  1  1  1  1
                                                            viscosity rjasa  function  of the
                                     / ^ ~  ~b =  1000      elongation rate s  according to
                                    /
                                                            the FENE-P dumbbell model.
                   100                                   -  The time constant is given
            V  - Зт],                /  ^   b =  100        byA e  = A b/(b  + 3). [From
                                                                    H
                                                            R. B. Bird, P. J. Dotson, and
                   10                                       N. L. Johnson, /. Non-Newton-
                                                            ian Fluid Mech., 7,213-235
                                                            (1980).]
                    1  ._!  L_=—4-" l  1  I  1  ,  1  1  I
                    0.01    0.1     1       10     100


           (b)  For steady-state elongational flow we  get
                                         +  r P/XX X H s  =                    (8.6-12)
                                    Z T P I X X
                                    ZTp,yy  + p,yi/H€ =  +ПКТ\ £               (8.6-13)
                                            T
                                                          Н
                                         -  2T PIZZ\ HS  =  -2пкТ\ н е         (8.6-14)
                                    ZT PIZZ
                                         3 Л _  V   Т Р,УУ  + P,Z2             (8.6-15)
                                                         T
                                                    ЗпкТ
           This set  of equations leads to a cubic equation for r pxx  -  r P/ZZ/  from which the elongational  vis-
           cosity  can be obtained  (see Fig. 8.6-5). Limited experimental data on polymer  solutions indi-
           cate that the shapes  of the curves  are probably approximately correct.
              The limiting expressions  for the elongational viscosity are

           For s  = 0:                г]  -  = ЗпкГЛ | н                       (8.6-16)
           For ir                           =  2пкТХ Ь                         (8.6-17)
                                                   н
           Having  found  the stresses  in the system, we  can then get the average  stretching  of  the mole-
           cules as a function  of the elongation rate; this is shown in Fig. 8.6-6.
              It is worth noting that for  a typical value  of b—say, 50—the elongational viscosity can in-
           crease by  a factor  of  about  30 as the elongation rate increases, thereby having  a profound  ef-
           fect  on flows in which there is a strong elongational component. 7


                          1  '  1  1  i  i  |  i  i  |  i

                 -1                                      Fig. 8.6-6.  Molecular stretching as
                             1-                          in steady  elongational flow, as
                       b =10                             a function  of the elongation rate e

                0.1 -              100                   predicted by the FENE-P dumb-
                                                         bell model. The time constant is
                                                                     H
                   -                                     given by  A, = \ b/(b  + 3). [From
               0 01       1  1  \  i  1  i  l  l  i  l  l  R. B. Bird, P. J. Dotson, and
                 0.01    0.1             10     100      N. L. Johnson, /. Non-Newtonian
                                                         Fluid Mech., 7,213-235 (1980).]


                The FENE-P and Giesekus models have been used successfully  to describe the details of turbulent
              7
           drag reduction, which is closely related to elongational viscosity, by R. Sureshkumar, A. N. Beris and
           R. A. Handler, Phys. Fluids, 9, 743-755 (1997), and C. D. Dimitropoulos, R. Sureshkumar, and A. N. Beris,
           /. Non-Newtonian Fluid Mechanics, 79, 433^68 (1998).
   268   269   270   271   272   273   274   275   276   277   278