The severe slugging phenomenon is illustrated in the
animation below. The phenomenon is a cyclical production of liquid
and gas coupled with cyclical flowline pressure fluctuations. The
first phase of the cycle is referred to as slug formation.
Here the base of the riser has become blocked with liquid preventing
free passage of gas. The pressure in the pipeline then increases
as more liquid runs down to the base of the pipeline increasing the
size of the liquid slug. The system continues in this fashion until
the pressure has built sufficiently to overcome the gravitational
head associated with the liquid slug. The system is then hydrodynamically
unstable and the liquid slug is discharge rapidly up the riser followed
immediately by a gas surge as the pipeline blows down. The pressure
in the pipeline then returns to a low value, leading to insufficient
gas velocities to carry the liquids up the riser, and the process
is repeated.
The animation below shows
results of a transient multiphase flowline simulation in the slug
flow regime. The animation shows how the liquid periodically builds
up in several dips near the riser base and are then purged, dropping
the flowline pressure.
Severe Slugging (Animated GIF 222K)
The
normalised limit cycles for such an unstable system is shown in
the figures below. The flowline inlet pressure changes by ~35%
and the liquid content by ~25% during the cycle, however the sudden
changes in gas and liquid flow rates could cause serious difficulties
for downstream equipment.
For
a more detailed discussion of how to analyse the effect of the severe
slugging region on the operability of a flowline system,
please see the Life
of Field Stability in a Deepwater Development case study.


