Page 278 - Bird R.B. Transport phenomena
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262   Chapter 8  Polymeric Liquids

                       8C.3  Verification  of  Giesekus viscosity function. 5
                            (a)  To check the shear-flow  entries in Table 8.5-1, introduce dimensionless  stress  tensor com-
                            ponents  Tj =  (\/T) )TJJ and a dimensionless  shear rate Г = Ay, and then show  that for  steady-
                                    t     0
                            state shear flow Eq. 8.5-4 becomes
                                                     T  -  2TT  -  a(T 2  +  7 p  = О           (8С.З-1)
                                                      xx    yx     xx
                                                            T  -  a(1% + T] ) = О               (8С.З-2)
                                                             yy          y
                                                    T  ~  TT  -  aT (T  4- T )  =  - f          (8C.3-3)
                                                     yx   yy    yx  xx  yy
                            There is also a fourth equation, which leads to T zz  = 0.
                            (b)  Rewrite these equations in terms  of  the dimensionless  normal-stress  differences  N^ = T xx
                            -  T  and N 2  = T yy  -  T , and  T .
                               yy
                                                     yx
                                              zz
                            (c)  It is difficult  to solve the equations in (b) to get the dimensionless shear stress  and normal-
                            stress  differences  in terms  of the dimensionless shear rate. Instead, solve for  N v  T , and Г as
                                                                                             yx
                            functions  of N :
                                       2
                                                   Г„,Ш^»                                       (SC.3-4,
                                                           a{\  -  Щ
                                                                      (1-2.)N P
                                                                    +        2
                                                               a(l  - N )  4
                                                                      2
                            (d)  Solve the last equation for N  as a function  of Г to get
                                                      2
                                                   N 2  = fix)  = (1 -  *)/[! + (1 "  ^OL) \    (8C.3-7)
                                                                              X
                            where
                                                л + 1 ^ Г 1 ^ 1       _    _      . . .           .
                                              =                    =  x  4 a ( 1  a ) r 2  +  ( 8 C 3  8 )
                                                    8 ( l  -  a)T 2
                            Then get the expression  for the non-Newtonian viscosity  and plot the curve  of 17(7).
                       8C.4  Tube Flow  for  the  Oldroyd  6-Constant Model.  Find the mass flow rate for  the steady  flow
                            in  a long circular tube  using  Eq. 8.5-3.
                                             6
                       8C.5  Chain  Models  with  Rigid-Rod  Connectors.  Read  and  discuss  the  following  publications:
                            M.  Gottlieb,  Computers in  Chemistry, 1,  155-160  (1977);  O.  Hassager,  /.  Chem.  Phys.,  60,
                            2111-2124  (1974);  X. J. Fan and  T. W.  Liu, /. Non-Newtonian Fluid Mech., 19, 303-321  (1986);
                            T.  W.  Liu, J. Chem. Phys., 90,  5826-5842  (1989);  H.  H.  Saab,  R.  B.  Bird,  and  С  F. Curtiss,
                            /.  Chem. Phys., 77, 4758-4766  (1982); J. D. Schieber, /. Chem. Phys., 87, 4917-4927,  4928-4936
                            (1987). Why  are rodlike connectors more difficult  to handle than springs?  What kinds  of prob-
                            lems can be solved  by computer simulations?














                                5
                                 H. Giesekus, /. Non-Newtonian  Fluid Mech., 11, 69-109  (1982).
                                6  M. C. Williams  and R. B. Bird, AIChE  Journal, 8, 378-382  (1962).
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