MODELING DYNAMIC ADSORPTION OF AN ANIONIC SURFACTANT ON BEREA SANDSTONE WITH RADIAL FLOW

被引:31
作者
KWOK, W [1 ]
HAYES, RE [1 ]
NASRELDIN, HA [1 ]
机构
[1] UNIV ALBERTA,DEPT CHEM ENGN,EDMONTON,AB T6G 2G6,CANADA
基金
加拿大自然科学与工程研究理事会;
关键词
D O I
10.1016/0009-2509(94)00450-6
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
A study of the dynamic adsorption of an anionic surfactant, Neodol(R) 25-3S, on Berea sandstone is presented. Cylindrical cores with axisymmetric radial flow are used in order to simulate the flow pattern near an oilfield injection wellbore, and also to allow greater sensitivity in testing various transport and adsorption mechanism. Mathematical models based on the advective-dispersive transport equation of mass coupled with an adsorption model were applied. Numerical solutions of the coupled transport and adsorption equations were obtained using the Galerkin finite element method. Equilibrium and kinetic Langmuir, two-site, and bilayer adsorption models were evaluated. Linear (Henry's law) and non-linear (Langmuir) equilibrium adsorption models were found to be unsuitable for modelling the surfactant effluent profiles. Improved fits to the experimental data were obtained using a kinetic Langmuir model, but the total amount of adsorption was over-estimated by a factor of three. It was found that the two-site or bilayer model was required to produce consistent model parameters for the experimental conditions employed. The effect of salinity on the adsorption of surfactant was examined using the two-site model. A small decrease in the rate constant for the first type of adsorption kinetics and an increase for the second type were observed. At high salinity, the axisymmetric radial transport equation was not able to predict the tracer and surfactant profiles during the brine flood. At such conditions, the mobility ratio was not favourable and, as the result, the displacement front was not stable. The flow pattern became two-dimensional and could not be described by the one-dimensional model used. An increase in the rate of adsorption was observed with increasing injection flow rate. It is proposed that the adsorption kinetics depend strongly on the concentration of surfactant monomers in the bulk solution. The results from this study can be used to estimate surfactant loss due to adsorption during many surfactant-based EOR processes. The surfactant loss in the wellbore region is a very important parameter for determining surfactant propagation in the reservoir.
引用
收藏
页码:769 / 783
页数:15
相关论文
共 53 条
[1]
BADAKHSHAN A, 1991, AICHE S SERIES 280, V87, P98
[2]
ADSORPTION-RETENTION OF PETROLEUM SULFONATES IN BEREA CORES [J].
BAE, JH ;
PETRICK, CB .
SOCIETY OF PETROLEUM ENGINEERS JOURNAL, 1977, 17 (05) :353-357
[3]
EFFECTS OF DISPERSION AND DEAD-END PORE VOLUME IN MISCIBLE FLOODING [J].
BAKER, LE .
SOCIETY OF PETROLEUM ENGINEERS JOURNAL, 1977, 17 (03) :219-221
[4]
Bear J., 1972, DYNAMICS FLUIDS PORO
[5]
A GENERAL MODEL FOR CONVECTION-DISPERSION-DYNAMIC ADSORPTION IN POROUS MEDIA WITH STAGNANT VOLUME [J].
Bidner, M. S. ;
Vampa, V. C. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 1989, 3 (03) :267-281
[6]
Bird R B., 2007, TRANSPORT PHENOMENA
[7]
MIXING EQUATIONS IN SHORT LABORATORY CORES [J].
BRIGHAM, WE .
SOCIETY OF PETROLEUM ENGINEERS JOURNAL, 1974, 14 (01) :91-99
[8]
CAMERON A, 1990, UNPUB
[9]
CHEN CS, 1987, WATER RESOUR RES, V27, P1217
[10]
Chung F. T. H., 1991, MODELING SURFACTANT