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Measurement of  density using hydrostatic head  117




                                          9 Overflow                                     Inlet



             Densii  ’*
             signal



                                Outlet                    (Relative density= p,)  outlet
             Figure 8.7  Density measurement with constant head
                                                      Figure 8.9  Density measurement with purge liquid
             However,  all require  the dimensions of  the pro-
             cess vessel to provide a sufficient change of head
             to satisfy the minimum span of the transmitter.

             8.4.2  Dlp transmitter with overflow tank
             Constant-level  overflow  tanks  permit  the  sim-
             plest  instrumentation,  as  shown  in  Figure  8.7.
             Only one dip transmitter  is required.  With H  as
             the  height  of  liquid  above  the  transmitter,  the
             equations are still:
                 span = H(p2 - PI)
                 zero suppression value = H . pi

             8.4.3  Dlp transmitter with a wet leg
             Applications  with  level  or  static  pressure  vari-   Figure 8.1 0  Purge system with gooseneck and trap.
             ations require compensation. There are three basic
             arrangements  for  density  measurement  under
             these conditions. First, when a seal fluid can be
             chosen  that  is  always  denser  than  the  process   span = Wpz - PI)
                                                          zero elevation value = H(ps - PI 1
             fluid and  ill not mix with it, the method shown
             in  Figure  8.8  is  adequate.  This  method  is used   When  there is no  suitable wet-leg seal fluid, but
             extensively on  hydrocarbons  with  water  in  the   the process liquid will tolerate a liquid purge, the
             wet  leg.  For  a  wet-leg  fluid  of  specific gravity   method  shown  in  Figure  8.9  can  be  used.  To
             ps,  an  elevated  zero  transmitter  must  be  used.   ensure that the process liquid does not enter the
             The equations become:                    purged wet leg, piping to the process vessel should
                                                      include  an  appropriate  barrier,  either  goose-
                                                      neck or trap, as shown in Figure  8.10. Elevation
                                                      or suppression of the transmitter  will  depend on
                                                      the  difference in  specific gravity of  the  seal and
                     B                       3 Inlet   process liquids. Here, the equations are:
             Wet leg
             (Relative
                                                          span = H(p2 - PI)
                                                          zero suppression value = H(pl - ps),
                                                                                  when PI > ps
                                                          zero elevation value = H(ps - PI).
                                                                                  when PS > PI
                                                      Ideally,  the  purge  liquid  has  a  specific  gravity
                                   Outlet             equal to PI, which eliminates the need for either
             Figure 8.8  Densitymeasurement with wet leg   suppression or elevation.
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