The use of core-annular flow pattern may be attractive as an artificial lift method in heavy oil wells. This flow pattern can be induced by the lateral injection of relatively small quantities of water, in order to get a lubricated oil core along the pipe. Frictional pressure drop measurements for upward vertical core flow in a 1-in. pipe, using a 17.6-Pa.s, 963-kg/m3 oil and water at room temperature reported a decrease by over 1000-fold with respect to single-phase oil flow, being comparable to the flow of water alone in the pipe at mixture flow rate. The total pressure drop was reduced by over 45-fold. The frictional pressure drop model proposed includes both irreversible and buoyancy terms. The model was adjusted to fit our data and shows excellent agreement with laboratory data available.

1.
Oliemans, R. V. A., and Ooms, G., 1986, “Core-Annular Flow of Oil and Water Through a Pipeline,” Multiphase Science and Technology, eds., G. F. Hewitt, J. M. Delhaye, and N. Zuber, Vol. 2.
2.
Russel
,
T. W. F.
, and
Charles
,
M. E.
,
1959
, “
The Effect of the Less Viscous Liquid in the Laminar Flow of Two Immiscible Liquids
,”
Can. J. Chem. Eng.
,
37
, pp.
18
24
.
3.
Charles
,
M. E.
,
Govier
,
G. W.
, and
Hodgson
,
G. W.
,
1961
, “
The Horizontal Pipeline Flow of Equal Density Oil-Water Mixtures
,”
Can. J. Chem. Eng.
,
39
, No.
1
, pp.
27
36
.
4.
Arney
,
M. S.
,
Bai
,
R.
,
Guevara
,
E.
,
Joseph
,
D. D.
, and
Liu
,
K.
,
1993
, “
Friction Factor and Holdup Studies for Lubricated Pipeline—I: Experiments and Correlations
,”
Int. J. Multiphase Flow
,
19
, pp.
1061
1076
.
5.
Ribeiro
,
G. S.
,
Arney
,
M. S.
,
Bai
,
R.
,
Guevara
,
E.
, and
Joseph
,
D. D.
,
1996
, “
Cemented Lined Pipes for Water Lubricated Transport of Heavy Oil
,”
Int. J. Multiphase Flow
,
22
, pp.
207
221
.
6.
Bannwart
,
A. C.
,
1999
, “
A Simple Model for Pressure Drop in Horizontal Core Annular Flow
,”
J. Brazilian Soc. Mech. Sciences
,
21
, No.
2
, pp.
233
244
.
7.
Shertok, J. T., 1975, “Velocity Profiles in Core-Annular Flow Using a Laser-Doppler Velocimeter,” Ph.D. thesis, Princeton University, Department of Chemical Engineering, Princeton, NJ.
8.
Bai
,
R.
,
Kelkar
,
K.
, and
Joseph
,
D. D.
,
1996
, “
Direct Simulation of Interfacial Waves in a High-Viscosity-Ratio and Axisymmetric Core-Annular Flow
,”
J. Fluid Mech.
,
327
, pp.
1
34
.
9.
Bai, R., 1995, “Traveling Waves in a High-Viscosity Ratio and Axisymmetric Core Annular Flow,” Ph.D. thesis, University of Minnesota, Minneapolis, MN.
10.
Ho
,
W. S.
, and
Li
,
N. N.
,
1994
, “
Core-Annular Flow of Liquid Membrane Emulsion
,”
AIChE J.
,
40
, pp.
1961
1968
.
11.
Bannwart, A. C., and Vanegas Prada, J. W., 1999, “Production of Heavy Oil Via Core Flow,” Latin American and Caribbean Petroleum Engineering-LACPEC, Paper SPE 63588, Caracas, Venezuela.
12.
Bannwart
,
A. C.
,
1998
, “
Wavespeed and Volumetric Fraction in Core Annular Flow
,”
Int. J. Multiphase Flow
,
24
, pp.
961
974
.
13.
Vanegas Prada, J. W., 1999, “Experimental Study of Core Flow for Heavy Oil Lifting” (in Portuguese), MSc. thesis, Department of Petroleum Engineering—FEM, State University of Campinas—UNICAMP, Brazil.
14.
Shell
Oil Co.
,
1972
, “
Oil-Water Line Moves Highly Viscous Crude
,”
Oil Gas J.
,
70
, p.
37
37
.
15.
Anon.
,
1988
, “
Venezuelan Line to Carry Heavy Oil in Water Film
,”
Oil Gas J.
,
86
, p.
112
112
.
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