Page 559 - Bird R.B. Transport phenomena
        P. 559
     Problems  539
                        7.  Compare and contrast the relation between  binary  diffusivity  and viscosity  for  gases and  for
                           liquids.
                        8.  How are the Maxwell-Stefan  equations  for  multicomponent diffusion  in gases related  to the
                           Fick equations for binary  systems?
                        9.  In a multicomponent mixture, does the vanishing  of N a  imply  the vanishing  of Vx ?
                                                                                            a
                     17A.1.  Prediction of  a low-density  binary  diffusivity.  Estimate ЯЬ  for  the system methane-ethane
                                                                           АВ
                           at  293K and 1 atm by  the following  methods:
                           (a)  Equation 17.2-1.
                           (b)  The corresponding-states chart in Fig. 17.2-1 along with  Eq. 17.2-3.
                           (c)  The  Chapman-Enskog  relation  (Eq.  17.3-12)  with  Lennard-Jones  parameters  from
                           Appendix  E.
                           (d)  The  Chapman-Enskog  relation  (Eq.  17.3-12)  with  the  Lennard-Jones  parameters  esti-
                           mated from  critical properties.
                                         2
                           Answers (all in cm /s): (a) 0.152;  (b) 0.138;  (c) 0.146;  (d) 0.138.
                     17A.2.  Extrapolation of binary diffusivity  to a very high temperature. A value  of ЯЬ  = 0.151 cm /s
                                                                                                   2
                                                                                         АВ
                           has been reported  1  for  the system  CO -air at 293K and 1 atm. Extrapolate ЯЬ  to 1500K by the
                                                                                        АВ
                                                         2
                           following  methods:
                           (a)  Equation 17.2-1.
                           (b)  Equation 17.3-10.
                           (c)  Equations 17.3-12 and 15, with Table E.2,
                               What  do  you  conclude  from  comparing  these  results  with  the  experimental  value  1  of
                           2.45  cm7s?
                                          2
                           Answers (all in cm /s): (a) 2.96;  (b) 1.75;  (c) 2.51
                     17A.3.  Self-diffusion  in liquid  mercury.  The diffusivity  of Hg  203  in normal liquid  Hg has been mea-
                           sured, 2  along  with  viscosity  and  volume  per  unit  mass.  Compare the  experimentally  mea-
                           sured Q) * with the values  calculated with Eq. 17.4-5.
                                  AA
                                            2
                           T  (K)   % *  (cm /s)   /x (cp)  V  (crnVg)
                                     AA
                           275.7     1.52  X 10" 5  1.68     0.0736
                           289.6     1.68  X  1 0  s  1.56   0.0737
                           364.2    2.57  X 10" 5  1.27      0.0748
                     17A.4.  Schmidt  numbers  for  binary  gas  mixtures  at  low  density.  Use  Eq.  17.3-11  and  the  data
                           given  in Problem  1A.4  to compute Sc  = /л/рЯЬ  for  binary  mixtures  of  hydrogen  and  Freon-
                                                                 АВ
                           12 at x A  = 0.00, 0.25, 0.50, 0.75, and  1.00, at 25°C and 1 atm.
                           Sample answers: At x A  = 0.00, Sc = 3.43; at x A  = 1.00,  Sc = 0.407
                     17A.5.  Estimation of  diffusivity  for  a binary  mixture at high  density.  Predict сЯЬ АВ  for  an equimo-
                           lar mixture of N  and C H  at 288.2K and 40 atm.
                                                6
                                              2
                                        2
                           (a)  Use the value  of 4b  at 1 atm from  Table  17.1-1, along with  Fig. 17.2-1.
                                             AB
                           (b)  Use Eq. 17.2-3 and Fig. 17.2-1.
                                            6
                           Answers: (a) 5.8  X 10"  g-mole/cm  • s;  (b) 5.3  X 10"  g-mole/cm  • s
                                                                     6
                               1  Ts. M. Klibanova, V. V. Pomerantsev, and  D. A. Frank-Kamenetskii, /. Tech. Phys.  (USSR),  12,14-30
                           (1942), as quoted by С  R. Wilke and  C. Y. Lee, Ind. Eng.  Chem., 47,1253  (1955).
                               2  R. E. Hoffman,  /. Chem.  Phys.,  20,1567-1570  (1952).





