Page 309 - Chemical process engineering design and economics
P. 309

288                                                      Chapter 6

           Figure 6.5. This diameter might result in a short separator length if the liquid flow
           rate is small. If this occurs it may be necessary to increase the separator length, or
           employ  other  designs  for  reducing  the  diameter  as  given  by  Sigales  [73]. The
            equations are listed in Table 6.11, and the calculation procedure for calculating L
            and D is given in Table 6.12. As was the case for vertical gas-liquid  separators,  if
            L/D < 3,  increase L so that L/D > 3, even if the  liquid  surge volume  is increased.
            Similarly, if L/D > 5 increase D  so that L/D < 5. Increasing D will reduce the gas
            velocity and increase the liquid  surge volume, which is in the right direction. The
            volume of the dished heads is not  included in the design procedure. Example  6.3
            illustrates the calculation procedure for sizing horizontal gas-liquid separators.
            Table 6.12  Calculation Procedure for Sizing Horizontal Gas-Liquid
            Separators__________________________________

            1. Select k v from Equation 6.11.3.

            2. Calculate the maximum vapor velocity, v v, from Equation 6.11.2.

            3. Calculate the cross-sectional area, A, from Equation 6.11.1.

            4. Calculate D using Equation 6.11.4. Round off D in 6 in (0.152 m) intervals,
            starting at 30 in (0.762 m). If  D is less then 30 in (0.762), use standard pipe.

            5. Select a liquid phase surge time, t s, from Equation 6.11.6.

            6. Calculate the separator length from Equation 6.11.5. Round off  L in 3 in
            (0.0762 m) intervals (for example, in feet, 5.0, 5.25, 5.5, 5.75 etc.)

            7. If L/D < 3.0, then recalculate L so that L/D > 3.0 by setting L/D = 3.2. If L/D >
            5.0,  then recalculate D so that L/D < 5.0 by setting L/D = 4.8.



            Example 6.3  Sizing a Gas-Liquid Separator___________________

            Calculate  the  length  and  diameter  of  a  gas-liquid  separator  to  separate  200.7
                        3
             3
                                                          3
            ft /min (5.68 m /min) of vapor from 5.0 gal/min (0.0189 m /min) of  a liquid.
            Data
                                                    3
                                         3
            vapor density        1.372 Ib/ft  (21.98 kg/m )
                                                    3
            liquid density       31.15 Ib/ft 3  (499.0 kg/m )
            design pressure      50 psig (3.45 barg)
            design temperature   200 °F (93.3 °C)
            material             carbon steel


         Copyright © 2003 by Taylor & Francis Group LLC
   304   305   306   307   308   309   310   311   312   313   314