Pressure and temperature variations of natural gas flows in a pipeline may cause partial gas condensation. Fluid phase behavior and prevailing conditions often make liquid appearance inevitable, which subjects the pipe flow to a higher pressure loss. This study focuses on the hydrodynamic behavior of the common scenarios that may occur in natural gas pipelines. For this purpose, a two-fluid model is used. The expected flow patterns as well as their transitions are modeled with emphasis on the low-liquid loading character of such systems. In addition, the work re-examines previous implementations of two-flow model for gas-condensate flow.
Issue Section:
Technical Papers
1.
Coulter
, D. M.
, 1979
, “New Equation Accurately Predicts Flowing Gas Temperature
,” Pipeline Industry
, 50
(5
), pp. 71
–73
.2.
Vincent
, P. A.
, and Adewumi
, M. A.
, 1990
, “Engineering Design of Gas-Condensate Pipelines With a Compositional Hydrodynamic Model
,” SPEPE
, 5
(4
), pp. 381
–386
.3.
Ayala, L. F., 2001, “A Unified Two-Fluid Model for Multiphase Flow in Natural Gas Pipelines,” MS Thesis, Pennsylvania State U., University Park.
4.
Adewumi
, M. A.
, and Mucharam
, L.
, 1990
, “Compositional Modeling of Gas/Gas-Condensate Dispersed Flow in Gas Pipelines
,” SPEPE
, 5
(1
), pp. 85
–90
.5.
Chen
, N. H.
, 1979
, “An Explicit Equation for Friction Factor in Pipe
,” Ind. Eng. Chem. Fundam.
, 18
(3
), pp. 296
–297
.6.
Taitel
, Y.
, and Dukler
, A. E.
, 1976
, “A Model for Predicting Flow Regime Transitions in Horizontal and Near Horizontal Gas Liquid Flow
,” AIChE J.
, 22
(1
), pp. 47
–55
.7.
Chen
, X.
, Cai
, X.
, and Brill
, J. P.
, 1997
, “Gas-Liquid Stratified Wavy Flow in Horizontal Pipelines
,” ASME J. Energy Resour. Technol.
, 119
(4
), pp. 209
–216
.8.
Grolman
, E.
, and Fortuin
, J. M. H.
, 1997
, “Gas-Liquid Flow in Slightly Inclined Pipes
,” Chem. Eng. Sci.
, 52
(24
), pp. 4461
–4471
.9.
Ishii
, M.
, and Mishima
, K.
, 1989
, “Droplet Entrainment Correlation in Annular Two-Phase Flow
,” Int. J. Heat Mass Transfer
, 32
(10
), pp. 1835
–1846
.10.
Wallis, G. B., 1969, “One-Dimensional Two-Phase Flow,” McGraw-Hill Book Company, New York.
11.
Hinze
, J.
, 1955
, “Fundamentals of the Hydrodynamic Mechanism of Splitting in Dispersion Processes
,” AIChE J.
, 1
(3
), pp. 289
–295
.12.
Brauner
, N.
, 2001
, “The Prediction of Dispersed Flows Boundaries in Liquid-Liquid and Gas-Liquid Systems
,” Int. J. Multiphase Flow
, 27
, pp. 885
–910
.13.
Barnea
, D.
, 1987
, “A Unified Model for Predicting Flow-Pattern Transitions for the Whole Range of Pipe Inclinations
,” Int. J. Multiphase Flow
, 13
(1
), pp. 1
–12
.14.
Baker
, A.
, Nielsen
, K.
, and Gabb
, A.
, 1988
, “Pressure Loss, Liquid Holdup Calculations Developed
,” Oil & Gas J.
, 86
(11
), pp. 55
–69
.15.
Meng
, W.
, Chen
, X. T.
, Kouba
, G. E.
, Sarica
, C.
, and Brill
, J. P.
, 2001
, “Experimental Study of Low Liquid Loading Gas-Liquid Flow in Near-Horizontal Pipes
,” SPE Prod. Facil.
, 16
(4
), p. 240
240
.16.
Cliff, R., Grace, J. R., and Weber, M. E., 1978, “Bubbles, Drops, and Particles,” Academic Press, New York.
17.
Peng
, D.
, and Robinson
, D. B.
, 1976
, “A New Two-Constant Equation of State
,” Ind. Eng. Chem. Fundam.
, 15
(1
), pp. 59
–64
.18.
Lorentz
, J.
, Bray
, B.
, and Clark
, C.
, 1964
, “Calculating Viscosities of Reservoir Fluids From Their Composition
,” JPT, Trans. AIME
, , 231
, pp. 1171
–1176
.19.
Lee
, A.
, Gonzalez
, M.
, and Eakin
, B.
, 1966
, “The Viscosity of Natural Gases,” JPT
, Trans. AIME
, 237
, pp. 997
–1000
.20.
Katz, D., et al., 1959, “Handbook of Natural Gas Engineering,” McGraw Hill, New York, p. 125.
21.
Passut
, C.
, and Danner
, R.
, 1972
, “Correlation of Ideal Gas Enthalpy, Heat Capacity, and Entropy
,” Ind. Eng. Chem. Process Des. Dev.
, 11
(4
), pp. 543
–546
.22.
Press, W. H., Teukolsky, S. A., Vetterling, W. T., and Flannery, B. P., 1994, “Numerical Recipes in Fortran: The Art of Scientific Computing,” Cambridge University Press, Second edition, pp. 701–716.
23.
Cash
, J. R.
, and Karp
, A. H.
, 1990
, “A Variable Order Runge-Kutta Method for Initial Value Problems With Rapidly Varying Right-Hand Sides
,” ACM Trans. Math. Softw.
, 16
, pp. 201
–222
.24.
Mucharam, L., 1990, “One-Dimensional Compositional Modeling of Gas and Condensate Flow in Pipelines,” PhD dissertation, Pennsylvania State U., University Park.
25.
Furukawa
, H.
, Shoham
, O.
, and Brill
, J. P.
, 1986
, “Predicting Compositional Two-Phase Flow Behavior in Pipelines
,” ASME J. Energy Resour. Technol.
, 108
, pp. 207
–210
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