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              Raschig Ring              Pall Ring               Structured
                                                             Source: Reference  78


            Figure 6.14 Examples of random and structure packings.


            liquid  is  poor,  reducing  the  mass-transfer  rate.  Also,  at  low  gas  velocity,  liquid
            will  leak -  called  weeping -  through the openings in the tray to the tray below,
            reducing the column efficiency.  Both of these effects  cause the efficiency  to  drop
            sharply.

            Packed Columns

            In packed columns, liquid spreads over the packing and flows  downward. The  gas
            flows  upward  through  the  void  space  in  the packing  countercurrent  to  the  liquid
            flow.  Like trays, the purpose  of the packing is to provide  surface  area to  enhance
            mass  transfer  between  gas  and  liquid.  There  are  two broad  classes  of  packing,
            random and structured packing.  Random packing is loaded  into the  separator by
            first  filling  the separator with water. Then, the packing is gradually loaded into the
            separator. After  settling the packing will assume random positions within the col-
            umn.  Also, the water prevents  breaking  fragile  packing.  For  structured packing,
            the position of the packing is definite.  Three types of random packing are  shown
            in Figure 6.14, the oldest being the Raschig ring, which is a hollow cylinder. Later,
            more  efficient  packings  were  developed,  like  the  Pall  ring,  which  is  the  most
            widely used packing [6]. An example of structure packing is given in Figure 6.14.
            Because of low liquid holdup and pressure drop,  structured packing is suitable for
            vacuum separations. There are numerous packing types on the market. For exam-
            ple,  see Walas [6].
                 Similar  to  tray  columns,  packed  columns  operated  at  high  gas  velocities
            causes backmixing, and low gas velocities reduce the mass transfer rate. If the gas
            velocity is too high, the column will flood.  In addition, at low liquid flow rates the
            packing will not wet completely, resulting in a reduction in mass-transfer. Another
            problem is the  tendency  for the  liquid  to  channel. To  minimize this  effect,  redis-
            tributors have to be installed every  5 to  10 m (16.4 to 30.5 ft) [23] to even out the
            liquid flow.




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