Page 304 - Applied Process Design For Chemical And Petrochemical Plants Volume II
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Packed Towers                                           293








































                    0.02      0.04     0.07   0.10      0.2        0.4     0.7   1.0   1.5   2.0   30
           Figure 9-25A.  Pressure drop in inches of water per foot of height, drip point tile, shape 6295 with crossed flue arrangement. Used by permis-
           sion of General Refractories Co.


             Pressure Drop Design Criteria and Guide: Random           at 1.5 to 2.0 in. water/ft.  Select a design C,  above
                              Packings Only                            point C and below point D, Figure 9-22.
                                                                     2. Absorption  and  similar  systems; select  pressure
                                                                       drop of 0.1 to 0.4 in. water/ft  of packing, or 0.25
             A. Determine  the  height  of  packing  required  (not a
               function of diameter) from HETP in distillation sec-    to  0.4  for  non-foaming  systems.  For  “median”
               tion and Kga in absorption section. This provides the   foaming  systems  use  a  maximum  of  0.25  in.
               total  height  of  packing  required,  considering  the   water/ft  for  the  highest  loading  rate  [82],  see
               packing  efficiencies and minimum wetting require-      Table  9-27.  The  values  in  the  table  should  be
               ments, previously discussed. From this total height,    reduced for high viscosity fluids. At rates above 20,
               the  expected  total  column  pressure  drop  can  be   limit the gas rate to 85% of the rate which would
               established,  recognizing  the  pressure  loss  through   give a pressure drop of 1.5 in. water/ft  referring to
               support plates, distribution devices, etc.              the GPDC, Figure 9-21F.
                                                                     3. Atmospheric  or pressure  distillation, select pres-
             B.  Calculate the abscissa of Figure 9-21F; for example,   sure drop of 0.50-1.0  in. water/ft.
                                                                     4. Vacuum distillation varies with the system and par-
               L/G~L, other abscissa values.
                          or
                                                                       ticularly with the absolute pressure required at the
                                                                       bottom  of  the column; normally select low pres
             C. Select a  design/operating  pressure  drop,  as shown   sure drop in the range of 0.1 to 0.2 in. water/ft  of
               on the  curves of  Figure 9-21F.  Suggested selection
               basis is as follows:                                    packing. For in vacuum service of 75 mm Hg and
                                                                       lower, the pressure drop obtained from the GPDC,
               1. Low to medium pressure column operation, select
                 design pressure drop of 0.40 to 0.60 in. water/ft  of
                 packing height, although some towers will operate                               (lext continued on page 296)
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