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216                            8.  Flow assurance stability issues

                                            Vacuum condition in flow

                   Vacuum condition and pressure surge may occur during stock oil flow.
                   In oil export pipelines going through mountainous terrain, or in deepwater during dis-
                 placement of the flowline live oil with stock oil there may be a vacuum condition at the high-
                 est point of the flow system.
                   If pressure at a pipeline pumping station downstream of a mountain or at the bottom of the
                 flowline riser is lower than hydrostatic head pressure for stock oil, vacuum may occur at the
                 crest of the mountain or at the riser top.
                   Vacuum condition has to be taken into account for design of flexible lines and flexible parts
                 and materials on topsides system.
                   Vacuum can also occur at top of chemical injection lines causing flashing off of solvent and
                 deposition of active ingredient in the chemical tubing.
                   Higher than normal flowing pressure or deadheading may occur during start-up of stock
                 oil flow to move the stationary fluids in the pipeline or in the flowline such as during dead
                 oil displacement.

                 References

                 Hill, T.J., Wood, D.G., 1994. Slug flow: occurrence, consequences and prediction. In: SPE 27960, University of Tulsa
                   Centennial Petroleum Engineering Symposium, Tulsa, 29–31 August.
                 Hou, D.Q., Tijsseling, A.S., Bozkus, Z., 2014. Dynamic force on an elbow caused by a traveling liquid slug. J. Press.
                   Vessel. Technol. 136.
                 Makogon, T.Y., Estanga, D., Sarica, C., 2011. A new passive technique for severe slugging attenuation. In: 15th
                   Multiphase Production Technology Conference, Cannes, France, 15–17 June.
                 Montgomery, J.A., 2002. Severe Slugging and Unstable Flows in an S-Shaped Riser. PhD. Thesis, Cranfield University.
                 Sancho, A.M., 2015. Severe Slugging in Pipelines. Master Sc. Thesis, Instituto Superior Tecnico, Lisboa.
                 Taitel, Y., 1986. Stability of severe slugging. Int. J. Multiphase Flow 12 (2), 203–217.
                 Tay, B.L., Thorpe, R.B., 2015. Statistical analysis of the hydrodynamic forces acting on pipe bends in gas–liquid slug
                   flow and their relation to fatigue. Chem. Eng. Res. Des. 104, 457–471.
                 Zakarian, E., 2000. Analysis of two-phase flow instabilities in pipe-riser system. In: Proceedings PVP2000, ASME
                   Pressure Vessels and Piping Conference, July 23–27, Seattle.

                 Further reading
                 Boe, A., 1981. Severe Slugging Characteristics, Part I, Flow Regime for Severe Slugging, Presented at Special Topics
                   in Two-Phase Flow, Trondheim, Norway.
                 Joukowsky, N., 1898. “Über den hydraulischen Stoss in Wasserleitungsröhren.” (“On the hydraulic hammer in water
                   supply pipes.”). Mémoires de l'Académie Impériale des Sciences de St.-Pétersbourg (1900), Series 8 9 (5), 1–71. (in
                   German); Sections presented to the Division of Physical Sciences of O.L.E., 26 September 1897, to the Physical-
                   Mathematical Commission of the Society, 30 January 1898, to the Polytechnic Society of the Moscow Imperial
                   Institute, 21 February 1898; complete paper to the Russian Technical Society, 24 April 1898, to the Physical-
                   Mathematical Division of the Academy of Sciences, 13 May 1898. Also: Жуковский, Н.Е. (1899). “О гидравлическом
                   ударе  в  водопроводных  трубах.”  (“On  hydraulic  hammer  in  water  mains.”),  Proc.,  4th  Russian  Water  Pipes
                   Congress, pp. 78–173, printed in Moscow (1901), April 1899, Odessa, Russia.
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