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Separator Design                                              281


                From Newton's  law  for  the  gravitation  force,  Archimedes  principle  for the
            buoyant  force,  and  the  definition  of  the  drag  force,  the  force  balance  on  a  drop
            becomes

                     Pv         PL v v
            m Lg = m L — g + C D A L ——                                 (6.10)
                     PL          2g
            where: m^  is the mass of a drop, g the acceleration of gravity, p the density of ei-
            ther liquid  or vapor,  C D the drag coefficient,  A L the projected  area  of a drop,  and
            v v, the maximum vapor velocity.

                Solving for the maximum vapor velocity, we find that




            v v =  l —————   I —————                                    (6.11)
                I  C D A L p L  )  \.  p v  )


                 Equation 6.11 does not  accurately describe the physical  situation.  In prac-
            tice, what is done is to set the coefficient  of Equation 6.11 equal to ky so that




                   I —————  I                                           (6.12)
            v v = k v
                   I  Pv    >/
            where k is an empirical constant that depends on the properties of  the fluids,  the
                  v
            design of the separator, the size of the drops, the vapor velocity, and the degree of
            separation required.

            Knock-Out Drums

            Knock-out drums, used when the liquid content of the incoming stream is low, is a
            special  case  of  a  gas-liquid  separator.  The  drum  is  placed  before  a  compressor
            inlet to prevent  liquid  drops from  entering and  damaging the compressor.  In this
            case, allowing a sufficient  residence time for the liquid is not a consideration.
                 To  determine  the  length  and  diameter  of  knock-out  drums,  Younger  [11]
            recommends using a value of k v of 0.2 ft/s (0.01  m/s) without a mist eliminator or
            35 ft/s (0.107 m/s) with  a  mist  eliminator,  and  an  L/D  ratio  of  2.  A  calculation
            procedure for solving the  equations listed in Table 6.7, is given in Table 6.8.  The




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