Page 229 - Pipeline Pigging Technology
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Pipeline  Pigging  Technology



      works had a significant impact on the way the valve assembly was installed.
      These  indicated that all flanged joints should be  leak  tested  at  1.1  MAOP,
      whereas a minimum number of new welds could be inspected by 100% NDT.
      This meant that in order to avoid pressure  testing the whole line, the flanged
      valve had to be pre-tested with flanged pup  pieces  already in place, rather
      than welding-in the two flanges offshore and then bolting in the new valve.
         In practice,  the  differential  pressure  across the  pig train in the  offshore
      phase was slightly less than that anticipated from the trials; this may have been
      due to condensate present in the line. The pressure required to 'flip' the entire
      train  to return it back to the  platform  on completion of the  operation  was
      lO.Sbarg. Combined with the static head of diesel available, this meant that
      the pig train would have held back a DP of up to  ISbarg.




         SUBSEA VALVES


         Following the  success  of the  high-DP pig train for pipeline  isolation  for
      topsides'  valve installation, its application for  subsea valve installation was
      studied. The application for subsea works introduced several new factors into
      the pig train design concept.
         Firstly, because the construction  work would be carried out subsea, it was
      necessary to launch the pig train with water to provide the necessary working
      environment  for  the  divers.  This would  be  advantageous for  control  and
      positioning  of the  pig train, as water  is largely incompressible  and  easy to
      meter. It would, however,  mean that some method of recommissioning the
      pipeline  would be  required.
         The design premise for the pig train was also altered by the  construction
      work being subsea. It was always intended that the pipeline would be vented
      down to static head pressure  subsea, i.e. approximately  13bar. With the pig
      train  in position  and the  pipeline  cut,  the  pig train would  be  in dynamic
      balance,  with  13bar gas pressure on one  side and  13bar  static  head  on  the
      other.
         The differential pressure  capability of the pig train would only come into
      play in an emergency  situation.  Initially, this was  taken to  be  inadvertent
      pressurization from the far end with gas moving the pigs towards the divers.
      However, this was found to be highly unlikely as, in this case, gas injection was
      not possible. Further examination of the system gave a worst-case scenario of
      a topsides' leak or rupture at the far end leading to pipeline depressurization.
         The full static head would then be acting across the pig train, and the divers
      could potentially be sucked into the pipeline  if the pig train moved. It was

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