Accurate prediction of slug length distribution and the maximum slug length in a hilly terrain pipeline is crucial for designing downstream separation facilities. A hilly terrain pipeline consists of interconnected uphill and downhill pipe sections, where slugs can dissipate in the downhill sections and grow in the uphill sections. Furthermore, new slugs can be generated at the dips (bottom elbows) and dissipate at the top elbows. Although existing steady-state models are capable of predicting the average slug length for pressure drop calculations and pipeline design, they are incapable of predicting detailed flow characteristics such as the maximum slug length expected at the exit of a hilly terrain pipeline. A transient slug tracking model based on a quasi-equilibrium formulation was developed to track the front and back of each individual slug, from which individual slug lengths are calculated. The model was verified with large-scale two-phase flow hilly terrain experimental data acquired at the Tulsa University Fluid Flow Projects (TUFFP). The results show a fairly accurate match between the model predictions and experimental data.

1.
Brill
,
J.
,
Schmidt
,
Z.
,
Coberly
,
W.
,
Herring
,
J.
, and
Moore
,
D.
,
1981
, “
Analysis of Two-Phase Tests in Large Diamtere Prudhoe Bay Field
,” SPEJ, June, pp. 363–378.
2.
Norris, L., 1981, “Correlation of Prudhoe Bay Liquid Slug Lengths and Holdups Including 1981 Large Diameter Flowline Tests,” Internal Report, Exxon Production Research Co, Houston, TX.
3.
Scott
,
S.
,
Shoham
,
O.
, and
Brill
,
J.
,
1989
, “
Prediction of Slug Length in Horizontal, Large-Diameter Pipes
,”
SPE Prod. Facil.
4
, pp.
335
340
.
4.
Scott, S., 1987, “Modeling Slug Growth in pipelines,” Ph.D. dissertation, The University of Tulsa.
5.
Scott, S., and Kouba, G., 1990, “Advances in Slug Flow Characterization for Horizontal and Slightly Inclined Pipelines,” SPE 20628, New Orleans, LA.
6.
Gopal, M., 1998, “Development of a Mechanistic Model for the Prediction of Slug Length in Horizontal Multiphase Flow,” BHRG Multiphase 1998 proceedings, Banff, Canada.
7.
Nydal
,
O.
,
Pintus
,
S.
, and
Andreussi
,
P.
,
1992
, “
Statistical Characterization of Slug Flow in Horizontal Pipes
,”
Int. J. Multiphase Flow
,
18
(
3
), pp.
439
453
.
8.
Dhulesia, H., Bernicot, M., and Deheuvels, P. Y., 1991, “Statistical Analysis and Modeling of Slug Lengths,” BHRG Multiphase 1991 proceedings, Canes, France.
9.
Zheng
,
G.
,
Brill
,
J. P.
, and
Taitel
,
Y.
,
1994
, “
Slug Flow Behavior in a Hilly-Terrain Pipeline
,”
Int. J. Multiphase Flow
,
20
(
1
), pp.
63
79
.
10.
Al-safran, E., Jayawadena, S., Zhang, H., Redus, C., and Brill, J., 2000, “An Experimental Study of Two-Phase Flow in a Hilly-Terrain Pipeline,” ASME/ETCE, New Orleans, LA. Feb.
11.
Taitel
,
Y.
, and
Barnea
,
D.
,
1998
, “
Effect of Gas Compressibility on a Slug Tracking Model
,”
Chem. Eng. Sci.
,
2089
2097
.
12.
Nicklin
,
D. J.
,
1962
, “
Two-phase Bubble Flow
,”
Chem. Eng. Sci.
,
17
, pp.
693
702
.
13.
Bendiksen
,
K. H.
,
1984
, “
An Experimental Investigation of the Motion of Long Bubbles in Inclined Tubes
,”
Int. J. Multiphase Flow
,
10
(
4
), pp.
467
483
.
14.
Talvy
,
C. Aladjem
,
Shemer
,
L.
, and
Barnea
,
D.
,
2000
, “
On the Interaction between Two Consecutive Elongated Bubbles in a Vertical Pipe
,”
Int. J. Multiphase Flow
,
26
, pp.
1905
1923
.
15.
Gregory
,
G. A.
,
Nicholson
,
M. K.
, and
Aziz
,
K.
,
1978
, “
Correlation of the Liquid Volume Fraction in the Slug for Horizontal Gas-Liquid Slug Flow
,”
Int. J. Multiphase Flow
,
4
, pp.
33
39
.
16.
Taitel
,
Y.
, and
Barnea
,
D.
,
1990
, “
Two-phase Slug Flow
,”
Adv. Heat Transfer
,
20
, pp.
83
132
.
17.
Cohen
,
S. L.
, and
Hanratty
,
T. J.
,
1968
, “
Effects of Waves at a Gas-Liquid Interface on a Turbulent Air Flow
,”
J. Fluid Mech.
,
31
, pp.
467
469
.
You do not currently have access to this content.