Page 283 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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Mechanical  Separations                                   253
















                     EVAPORATO�S         HORIZONTAL  SEPARATORS      HORIZONTAL  SEPARATORS   FRACTIONATIN6  rDWERS



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                  OPEN  SEPARATORS       IN-LINE  GAS  SCRUBBERS     Oil-GAS  SEPARATORS     OVER-SIZE  VESSEL

                       Figure 4-24. Typical  mesh installations in process equipment.  Courtesy of Metal  Textile Corp.,  Bulletin  ME-7.

            selected,  the heads normally available for such vessels run   Use  stainless  304 mesh  due  to  low  temperature  opera-
            in 6-inch increments  ( either O.D.  or I.D.).       tion.  Carbon  steel  is  too  brittle  in wire  form  at  this  tem-
              Net inside diameter at support ring:               perature.
                                                                    The  check or specification form  of Figure  4-2fi  is  nec-
              30" O.D.  - 4" - 3/4"  =  25 1/4"                  essary  and  helpful  when  inquiry.ing  wire  mesh  entrain-
                                                                 ment units,  either as  the  mesh  alone,  or as  a  complete
              Note  that vessel wall assumed %-inch thick.       turnkey unit including vessel.
              Net area  =  3.46 sq ft                               For services where solids are present or evaporation of
                                                                 droplets  on the mesh might leave a  solid crust,  it is usual
                                 2 83                            practice to install sprays above or below the mesh to cover
              Actual velocity at ring:   ·  (2. 74)  =  2. 24 ft/ sec
                                 3.46                            the unit with water (or suitable solvent)  on scheduled (or
                                                                 necessary)  operating  times,  as  the  plugging  builds  up.
              Percent design velocity:  2.24(100)/3.66  =  61.3%. This   This is checked by a manometer or other differential pres-
            is  acceptable operating point.                      sure meter placed with taps on the top and bottom side of
              Note that if 28-inch O.D.  X  %-inch wall pipe is available   the mesh installation.
            this  could be  used with  weld  cap  ends,  or dished  heads.   A few case examples for guidance include:
            The percent design velocity would be =  71.8%.
              This  is also an  acceptable design.
              Pressure  drop  is in  the order of 0.1  inch  to  0.5 inches   • 2-3%  caustic  solution  with  10%  sodium  carbonate.
           water.                                                    This  condition  might  plug  the  wire  mesh.  Sprays
                                                                     would be recommended.
            Notes:  Since this vessel will operate as a flash drum with
            a  iiquid  level  at  approximately  Yi  of its  height up  from   • Raw river water.  This presents no plugging problem
            bottom,  place the inlet at about center of vessel.  See Fig-   • Light hydrocarbon  mist.  This  presents  no  plugging
            ure 4-25.                                                problem
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