Page 46 - Bird R.B. Transport phenomena
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§1.6  Viscosity  of Suspensions  and Emulsions  31

                            fluid  and  are simply  related  to the internal energy  of  vaporization  at the normal  boiling
                            point, as  follows: 3
                                                          AGj «  0.408 AU                        (1.5-8)
                                                                       vap
                            By using  this empiricism and setting 8/a  =  1, Eq. 1.5-7  becomes

                                                     11  = Щехр  0.408 ALZ /RT)                   (1.5-9)
                                                                         vap
                            The  energy  of  vaporization  at  the normal boiling  point  can be  estimated  roughly  from
                            Trouton's  rule

                                                     AL/ vap  -  AH vap  -  RT  =  9ART b       (1.5-10)
                                                                      b
                            With  this further  approximation, Eq. 1.5-9  becomes

                                                                 p V D                           (1.5-11)

                            Equations  1.5-9  and  11  are  in  agreement  with  the  long-used  and  apparently  successful
                            empiricism  jx = Л ехр(В/Т). The theory, although only approximate in nature, does give
                            the  observed  decrease  of  viscosity  with  temperature, but  errors  of  as  much  as  30%  are
                            common when  Eqs.  1.5-9  and  11 are used. They should  not be used  for  very long  slender
                            molecules, such as n-C oH 2.
                                               2  4
                                There are, in addition, many  empirical  formulas  available  for  predicting  the  viscos-
                            ity  of  liquids  and  liquid  mixtures.  For these, physical  chemistry  and  chemical  engineer-
                            ing textbooks  should  be consulted. 4


        EXAMPLE   1.5-1     Estimate the viscosity  of liquid benzene, QH , at 20°C (293.2K).
                                                                6
       Estimation  of  the  SOLUTION
       Viscosity  of  a Pure
       Liquid               Use Eq. 1.5-11 with  the following  information:
                                                                   3
                                                         V  =  89.0cm /g-mole
                                                        T b  = 80.1 °C
                            Since this  information  is  given  in  c.g.s. units, we  use  the values  of  Avogadro's  number and
                            Planck's constant in the same set  of units. Substituting into Eq. 1.5-11 gives:

                                                               27
                                                    23
                                           (6.023  X 10 )(6.624  X 10" )  /3.8  X  (273.2  + 80.1))
                                                                   r
                                                    (89.0)        ~ V      293.2
                                                   3
                                                                       4
                                         =  4.5  X 10" g/cm-s  or  4.5  X 10~  Pa •  s  or  0.45 mPa •  s
       §1.6  VISCOSITY    OF SUSPENSIONS AND        EMULSIONS
                            Up  to  this  point  we  have  been  discussing  fluids  that  consist  of  a  single  homogeneous
                            phase.  We  now  turn  our  attention briefly  to two-phase  systems.  The complete  descrip-
                            tion  of  such  systems  is, of  course, quite complex, but  it is  often  useful  to replace the sus-
                            pension  or  emulsion  by  a  hypothetical  one-phase  system,  which  we  then  describe  by


                                3  J. F. Kincaid, H. Eyring, and  A.  E. Stearn,  Chem. Revs., 28, 301-365  (1941).
                                 See, for  example, J. R. Partington, Treatise on Physical Chemistry, Longmans, Green (1949); or  R. C.
                                4
                            Reid, J. M. Prausnitz, and  В. Е. Poling, The Properties of Gases and Liquids, McGraw-Hill, New  York, 4th
                            edition (1987). See also  P. A.  Egelstaff, An  Introduction to the Liquid State, Oxford University Press,  2nd
                            edition (1994), Chapter 13; and  J. P. Hansen and  I. R. McDonald,  Theory of Simple Liquids, Academic  Press,
                            London  (1986), Chapter 8.
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