Page 589 - Bird R.B. Transport phenomena
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Problems  569

                                   -R  = 1.4 cm       Fig. 18A.4.  Schematic drawing  of a  wetted-wall
                                   - Water  film  runs  column.
                                    down  the wall




                                   - Film thickness 8

                    L = 13 cm
                                  — Surface  concentration
                                    assumed  equal to the
                                   saturation concentration





                                Chlorine-bearing
                                     gas



              18A.2o  Sublimitation  of  small  iodine  spheres  in  still  air.  A  sphere  of  iodine, 1 cm in diameter, is
                    placed  in still  air at 40°C and  747 mm Hg pressure.  At  this temperature the vapor pressure  of
                    iodine is about  1.03 mm Hg. We want to determine the diffusivity  of the iodine-air system  by
                    measuring the sublimation rate. To help determine reasonable experimental conditions,
                    (a)  Estimate the diffusivity  for  the iodine-air  system  at the temperature and  pressure  given
                    above, using  the intermolecular force parameters in Table E.I.
                    (b)  Estimate the rate of sublimation, basing  your calculations on Eq. 18.2-27. (Hint: Assume  r 2
                    to be very  large.)
                        This  method has  been  used  for  measuring  the diffusivity,  but  it is  open to question  be-
                    cause  of the possible  importance of  free  convection.
                                            2
                    Answer:  (a) 2>,_  = 0.0887 cm /s;  (b) W  = 2.43  X 10" 3  g-mole/hr
                                                    h
                                2 air
              18A.3.  Estimating the error in calculating the absorption rate.  What  is the maximum possible  error
                    in  computing the absorption  rate from  Eq. 18.5-18,  if  the solubility  of Л in В is known  within
                    ±5% and the diffusivity  of Л in В is known within  ±15%? Assume  that the geometric quanti-
                    ties and the velocity  are known very  accurately.
              18A.4.  Chlorine absorption in a falling  film  (Fig. 18A.4).  Chlorine is being  absorbed  from  a gas  in a
                    small  experimental  wetted-wall  tower  as  shown  in  the figure.  The absorbing  fluid  is  water,
                    which  is  moving  with  an  average  velocity  of  17.7  cm/s.  What  is  the  absorption  rate  in  g-
                                                                                            2
                                                                                        5
                    moles/hr,  if  the liquid-phase  diffusivity  of  the chlorine-water  system  is  1.26  X  10~  cm /s,
                    and  if  the saturation  concentration of  chlorine  in  water  is  0.823 g  chlorine per  100  g  water
                    (these are the experimental values  at 16°C). The dimensions  of the column are given  in the  fig-
                    ure.  (Hint: Ignore the chemical reaction between  chlorine and water.)
                    Answer: 0.273 g-moles/hr
              18A.5.  Measurement  of  diffusivity  by  the point-source method  (Fig. 18C.1). 1  We  wish to design  a
                    flow  system  to utilize  the results  of  Problem  18C.1  for  the measure  of  ЯЬ .  The approaching
                                                                               АВ


                        1
                         This is the most precise  method yet developed  for measurements  of diffusivity  at high
                    temperatures.  For a detailed  description  of the method, see R. E. Walker and A. A. Westenberg,  /. Chetn.
                    Phys., 29,1139-1146,1147-1153 (1958). For a summary  of measured  values and comparisons  with the
                    Chapman-Enskog  theory, see R. M. Fristrom and A. A. Westenberg,  Flame Structure, McGraw-Hill, New
                    York (1965), Chapter XIII.
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