SPE Production & Operations
Volume 24,
Number 1,
February 2009,
pp. 171-179
Summary
Normal (hydrodynamic) slug flow in a pipeline/riser system was studied
theoretically and experimentally in this paper. Experimental data were obtained
for slug flow in which the length of liquid slugs was larger than the riser
height. A transient mechanistic model of this phenomenon was also developed. A
good agreement between the model predictions and experimental data was
achieved. Simulations of slug flow in an offshore production system with a
large-diameter pipeline were performed by use of the developed model. The
simulation revealed that long hydrodynamic slugs can accelerate in the riser to
a velocity five times greater than the average slug velocity in the pipeline.
This fact should be accounted for in the development of operating strategies
for such production systems.
© 2009. Society of Petroleum Engineers
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History
- Original manuscript received:
13 April 2007
- Meeting paper published:
27 June 2007
- Revised manuscript received:
17 June 2008
- Manuscript approved:
21 July 2008
- Published online:
2 March 2009
- Version of record:
26 February 2009