Corrosion in deadlegs occurs as a result of water separation due to the very low flow velocity. This work aims to investigate the effect of geometry and orientation on flow field and oil/water separation in deadlegs in an attempt for the development of a deadleg criterion. The investigation is based on the solution of the mass and momentum conservation equations of an oil/water mixture together with the volume fraction equation for the secondary phase. Results are obtained for two main deadleg orientations and for different lengths of the deadleg in each orientation. The considered fluid mixture contains 90% oil and 10% water (by volume). The deadleg length to diameter ratio (L/D) ranges from 1 to 9. The results show that the size of the stagnant fluid region increases with the increase of L/D. For the case of a vertical deadleg, it is found that the region of the deadleg close to the header is characterized by circulating vortical motions for a length l3D while the remaining part of the deadleg occupied by a stagnant fluid. In the case of a horizontal deadleg, the region of circulating flow extends to 3–5 D. The results also indicated that the water volumetric concentration increases with the increase of L/D and is influenced by the deadleg orientation. The streamline patterns for a number of cases were obtained from flow visualization experiments (using 200 mW Argon laser) with the objective of validating the computational model.

1.
Craig, B. C., 1996, “Corrosion in Oil/Water Systems,” Mater. Selection Design, Aug.
2.
Lotz, U., Van Bodegom, L., and Ouwehand, C., 1990, “Effect of Type of Oil or Gas Condensate on Carbon Acid Corrosion,” Corrosion/90, Paper no. 41, NACE, Houston TX.
3.
Ricca
,
P. M.
,
1991a
, “
Ultrasonic Inspection Prompts Chemical Inhibitor Program
,”
Oil & Gas Journal
,
22
, pp.
73
82
.
4.
Ricca, P. M., 1991b, “Control of Deadleg Corrosion in a Crude Oil Pipeline,” PD-Vol. 34, Pipeline Engineering, ASME, pp. 34–39.
5.
Charles
,
M. E.
,
Govier
,
G. W.
, and
Hodgson
,
G. W.
,
1961
, “
The Horizontal Pipeline Flow of Equal Density Oil-Water Mixture
,”
Can. J. Chem. Eng.
,
39
(
1
), pp.
27
36
.
6.
Charles
,
M. E.
, and
Lilleleht
,
L. U.
,
1966
, “
Correlations of Pressure Gradients for the Stratified Laminar-Turbulent Pipeline Flow of Two Immiscible Liquids
,”
Can. J. Chem. Eng.
,
44
(
1
), pp.
47
49
.
7.
Lockhart
,
R. W.
, and
Martinelli
,
R. C.
,
1949
,
Chem. Eng. Prog.
,
45
, pp.
39
48
.
8.
Barnea
,
D.
,
1986
, “
Transition From Annular Flow and From Dispersed Bubble Flow-Unified Models for the Whole Range of Pipe Inclinations
,”
Int. J. Multiphase Flow
,
12, 5
, pp.
733
744
.
9.
Brauner
,
N.
, and
Maron
,
D. M.
,
1992
, “
Stability Analysis of Stratified Liquid-Liquid Flow
,”
Int. J. Multiphase Flow
,
18, 1
, pp.
103
121
.
10.
Schmidt
,
H.
, and
Loth
,
R.
,
1994
, “
Predictive Methods for Two-Phase Flow Pressure Loss in Tee Junctions With Combining Ducts
,”
Int. J. Multiphase Flow
,
20, 4
, pp.
703
720
.
11.
Plaxton, B. L., 1995, “Pipeflow Experiments for Analysis of Pressure Drop in Horizontal Wells,” SPE Annual Technical Conference and Exhibition, October 22–25, Dallas, TX, SPE Int L. Stdnt. Pap. Cntst., pp. 635–650.
12.
Brill, J., and Beggs, H., 1994, Two-Phase Flow in Pipes, University of Tulsa Press, Tulsa, OK.
13.
Asheim
,
H.
,
Kolnes
,
J.
, and
Oudeman
,
P.
,
1992
, “
A Flow Resistance Correlation for Completed Wellbore
,”
J. Pet. Sci. Eng.
,
8, 2
, pp.
97
104
.
14.
Angeli, P., and Hewitt, G. F., 1996, “Pressure Gradient Phenomena During Horizontal Oil-Water Flow,” 1996 OMAE—Pipeline Technology, Vol. V, ASME, pp. 287–295.
15.
Hwang
,
C. J.
, and
Pal
,
R.
,
1997
, “
Flow of Two-Phase Oil/Water Mixtures Through Sudden Expansions and Contractions
,”
Chem. Eng. J.
,
68
, pp.
157
163
.
16.
Schabacker, J., Bolcs, A., and Johnson, B. V., 1998, “PIV Investigation of the Flow Characteristics in an Internal Coolant Passage With Two Ducts Connected by a Sharp 180° Bend,” ASME Paper No. 98-GT-544, Fairfield, NJ.
17.
Hafskjold
,
B.
,
Celius
,
H. K.
, and
Aamo
,
O. M.
,
1999
, “
A New Mathematical Model for Oil/Water Separation in Pipes and Tanks
,”
SPE Prod. Facil.
,
14, 1
, pp.
30
36
.
18.
Fluent, 1988, CD-Rom Fluent 5, User’s Guide, section 14.2.
19.
Wilson, W., 1999, “The Development of a Droplet Formation and Entrainment Model for Simulations of Immiscible Liquid-Liquid Flows,” MS thesis, Weat Virginia University.
20.
Celik, I. B., Badeau, A. E., Burt, A., and Kandil, S., 2001, “A Single Fluid Transport Model for Computation of Stratified Immiscible Liquid-Liquid Flows,” Proceedings of the XXIX IAHR Congress, Sep., Beijing, China, pp. 1–18.
21.
Dluska, E., Wronski, S., and Rudnaik, L., 2001, “Two-Phase Gas-Liquid Coutte-Taylor Eccentric Reactor. Computational Calculation of Reactor Hydrodynamics,” Proceedings of the 2nd International Conference on Computational Heat and Mass Transfer COPPE/UFRJ, Federal University of Rio de Janeiro, Brazil, Oct. 22–26.
22.
Vigil
,
R. D.
, and
Zhu
,
X.
,
2001
, “
Banded Liquid-Liquid Taylor-Coutte-Posuille Flow
,”
AICHE J.
,
47
(
9
), pp.
1932
1940
.
23.
Manninen, M., Taivassalo V., and Kallio, S., 1996, On the Mixture Model for Multiphase Flow, Technical Research Center of Finland, VTT Publication No. 288.
24.
Maron
,
D. M.
,
1992
, “
Flow Pattern Transitions in Two-Phase Liq-Liq Flow in Horizontal Tubes
,”
Int. J. Multiphase Flow
,
18, 1
, pp.
123
140
.
25.
Versteeg, H. K., and Malalasekera, W., 1995, An Introduction to Computational Fluid Dynamics: The Finite Volume Method, Longman Scientific and Technical, Essex, England.
26.
Reynolds, W. C., 1987, “Fundamentals of Turbulence for Turbulence Modeling and Simulation,” Lecture Notes for Von Karman Institute, Agard Report No. 755, pp. 1–11.
27.
Shih
,
T. H.
,
Liou
,
W. W.
,
Shabbir
,
A.
, and
Zhu
,
J.
,
1995
, “
A New k-ε Eddy-Viscosity Model for High Reynolds Number Turbulent Flows—Model Development and Validation
,”
Comput. Fluids
,
24, 3
, pp.
227
238
.
28.
Launder
,
B. E.
, and
Spalding
,
D. B.
,
1974
, “
The Numerical Computation of Turbulent Flows
,”
Comput. Methods Appl. Mech. Eng.
,
3
, pp.
269
289
.
29.
Habib
,
M. A.
,
Attya
,
A. M.
, and
McEligot
,
D. M.
,
1989
, “
Calculation of Turbulent Flow and Heat Transfer in Channels With Streamwise Periodic Flow
,”
ASME J. Turbomach.
,
110
, pp.
405
411
.
30.
Patankar, S. V., 1980, Numerical Heat Transfer and Fluid Flow, Hemisphere Publishing Corporation, New York.
31.
Chiang
,
T. P.
,
Sheu
,
W. H.
, and
Hwang
,
R. R.
,
1998
, “
Effect of Reynolds Number on the Eddy Structure in a Lid-Driven Cavity
,”
Int. J. Numer. Methods Fluids
,
26
, pp.
557
579
.
You do not currently have access to this content.