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Separator Design                                              315


            Tray Columns

            The purpose of a tray is to provide thorough contact between gas and liquid, facili-
            tating  mass  transfer  between  the  two  phases  on  each  tray.  Gas  bubbles  through
            liquid flowing  across the tray.  The most common designs are the sieve, valve, and
            bubble-cap trays shown in Figure 6.13.  According to Harrison and France  [32],  the
            sieve  and  valve  tray have mostly displaced  the  bubble-cap  tray because  they  are
            less expensive and have a higher capacity. The  sieve tray is the most widely used
            and should be considered  first  because of its lower installed cost, well known de-
            sign procedures, low fouling tendency, large capacity, and high efficiency  [33].
                 When comparing tray designs the turndown ratio is important because it is a
            measure of the  flexibility  of a column in  dealing with a change in flow rate. The
            turndown ratio is defined  as the ratio of the maximum to minimum operating flow
            rate. For bubble  cap and valve trays, the turndown ratio is  about ten whereas for
            sieve trays it is only about three.
                 Engineers  realize  that  all  equipment  have  a  maximum  operating  capacity,
            and because  of uncertainty  in  system property  data,  the  equipment  will be  over-
            designed  to insure  that  adequate  capacity will be  available.  Overdesigning,  how-
            ever, -  besides being  costly -  can cause  operating  difficulties  because all equip-
            ment have a turndown ratio.  Below the minimum or above the maximum capac-
            ity,  equipment  may become  inoperable  or  very  inefficient.  This  is  illustrated  in
            Figure  6.15  which shows that the tray efficiency,  expressed as a percentage of the
            flooding  gas velocity,  is relatively constant over a range of gas velocities.  Close
            to  the flooding point the gas velocity is high so that an excessive amount of liquid
            drops are carried to the tray above.  This form of  backmixing causes the tray effi-
            ciency to decrease. On the other hand, at low gas velocities,  mixing  of  gas  with












                  Vapor Flow
                                                             Vapor Flow


                  Bubble Cap             Sieve                 Valve




            Figure  6.13  Bubble  cap,  sieve, and valve trays.




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