Page 474 - Pipeline Pigging Technology
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Pigging  research





















               Fig.3. Flow velocity vs pressure to move a sphere.
      the numerous interesting observations was: "that the actual pressure  required
      for  transporting two  spheres simultaneously is 10% smaller than the  sum of
      the pressures for transporting a single sphere".
         They also noted that the 5D bends showed  no increase in the  differential
      pressure across the sphere, and "can be assumed as parts of the straight line".
         Of particular interest, however, was the reduction of differential  pressure
      across  a sphere,  with  an  increase  in velocity. This is shown  graphically in
      Fig.3, which is reproduced from their paper. Although these reductions were
                                            2
      only of the  order  of O.Tpsig (O.OSkg/cm ), when  the  velocity was  doubled
      (from  Im/sec to 2m/sec),  it may well have a significant impact on the results
      of  some  further  research  which  they  carried  out,  details  of which  were
      published early in  1979[5].
        This later work was designed to study the mixing of dissimilar fluids when
      separated by spheres at the interface. It produced a great  deal of  interesting
      data concerning  sphere performance in general.
         It confirmed that although the frictional resistance (and hence  differential
      pressure) is nearly constant, it does decrease slightly with increasing velocity.
         It was noted  that flow forward and flow back was equal at a velocity of
      about 1.3m/sec (4.3ft/sec). At lower velocities, flow back decreased, but flow
      forward  increased while at higher velocities, the reverse applied; the  graph
      showing this is reproduced  in Fig.4.
        They made the reasonable assumption that product flows forward due to
      the frictional resistance of the sphere (i.e. the differential  pressure) and flows
      back due to product  viscosity.
        In pigging, it is generally the flow back which needs to be minimized (e.g.
      for  dewatering, condensate  removal, etc.)  so for optimum liquids' removal
      using a sphere,  these tests indicate that speeds should probably not exceed



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