Page 291 - Applied Process Design For Chemical And Petrochemical Plants Volume II
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280                      Applied Process Design for Chemical and Petrochemical Plants

                               Table 9-23                        many plastics will  deform, thereby changing the packing
                HEW Comparison of 2-h-Dia. Slotted Rings         bed  characteristics, and the column pressure drop. As a
                                                                 general rule, do not select a plastic to operate at any time
                                                      Averaged   within 50°F of the softening or deflection temperature of
                             Top p~ss~, Bed depth,     mTP,      the plastic.
           System              =Hg             ft       in.
           Acetone/water         740           5         18      Particle versus Cmpact Prejimd Structured Packings
                                               -
                                              10         20
           Iso-octane/ toluene   740           3         24        Particle packings (random) are usually (not always) less
                                               10        30      efficient  than  the  pre-packaged/preformed  assemblies;
                                              20         32      however, particle types are generally more flexible in load-
                                 100           5         24      ing and the ability to handle “dirty” fluids.
                                               10        26        Cost of  the packing and its effect on the system costs
                                              20         28      must  be  considered, as  some  packings are  much  more
           Methanol/water        740           10        21      expensive than  others, yet  produce very little improved
           Iso-propanol/water    740           10        24      performance. Table 9-1  7 presents some comparative infor-
           Para/ortho xylene     100           10        33
                                  50           10        31      mation. The most common packings and hence the ones
                                  16           10        28      with  the most available data are Raschig rings, Berl sad-
           Ethylbenzene/styrene   100          10        22      dles, several saddle types and Pall Rings@ (Norton Co.) or
                                               20        26      equivalent.
           Basis: Test-column diameter: 24-42 in.                  As a guide with  only rough  experimental backing, the
           Used by permission: Chen,  G.  IC,  Chem. En6  Mar. 5  (1984), p.  40, all   ratio of maximum random packing size to tower diameter is
            rights reserved.
                                                                 Raschig rings:   1:20 (Reference  5)
                                                                                 1:8 (Reference 52)
             The packing sizes listed relate to ceramic (where avail-   Berl saddles:   1:lO
           able), metal, and  plastics.  The plastic  random  packing   Intalox saddles:  1:8 to 1:lO  (Reference 6)
           must be used well under its softening temperature. Due to
           packing weight of  the bed, the packing can compress as   The 1:8 ratio is in more common use for most packings;
           the temperature increases and thereby become less effec-   however recent data indicated that Raschig rings require a
           tive and increase the system pressure drop to the point of   larger ratio approaching 1:20.
           causing flooding. Therefore, the manufacturer should be   These ratios are useful in dealing with small towers, and
           consulted for upper limits of operating temperatures for   serve as guides for the borderline cases of  others. There
           design selection of the particular plastic suited for perfor-   are no guides to the smallest sized packing to place in a
           mance  requirements  and  corrosion  resistance.  Under   tower. However, %in. is about the smallest ceramic used
           these conditions it is important that the plastic packing   with %in. and 1-in. being the most popular. Operating and
           surface be “wetted” to allow film formation.          pressure drop factors will usually control this selection.
                                                                   Packed towers are not limited to small units; in fact the
           Pressure Drop                                         largest  processing  towers  for  absorption and  stripping
                                                                 operations are probably in these towers. Some units are 40
             This is  important  to most column designs. Recognize   and 50 ft in diameter using 2-in. and larger packings to
           that pressure drop will increase due to:              heights of 20-30  ft. Other units are 5-6  ft in diameter with
                                                                 60 ft of packing. Towers with a 24in. dia. and smaller are
             1. Unsteady column operations                       most  often used  with  packing rather  than  trays  due  to
             2. Increased liquid/vapor loads                     mechanical limitations of trays in small towers.
             3. Breakage of ceramic packings (this can be serious)
             4. Compaction/deflection of plastic packings        Fouling of Packing


           Materials of Construction                               Random and structured packings are susceptible to sur-
                                                                 face fouling due to process conditions and/or  the pres
             Give careful consideration to fluids, temperatures of sys-   ence  of  oxygen  as  may  be  related  to  bacterial  growth.
           tems, aeration. Plastic materials may be quite good for the   Some systems will precipitate solids or crystals from solu-
           application;  however,  carefully  determine  the  recom-   tion  usually due  to  the  temperature and  concentration
           mended long-term heat &fiction  characteristics. With time,   effects. Bravo [ 1351 discusses air-water stripping and illus-
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