Dimensionality-Dependent Foam Rheological Properties: How To Go From Linear to Radial Geometry for Foam Modeling and Simulation
- Woochan Lee (Louisiana State University) | Seungjun Lee (Louisiana State University) | Mohammad Izadi (Louisiana State University) | Seung I. Kam (Louisiana State University)
- Document ID
- Society of Petroleum Engineers
- SPE Journal
- Publication Date
- October 2016
- Document Type
- Journal Paper
- 1,669 - 1,687
- 2016.Society of Petroleum Engineers
- foam, dimensionality, mechanistic fractional flow analysis, foam EOR, mobility reduction factor
- 0 in the last 30 days
- 207 since 2007
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Numerous laboratory and field tests reveal that foam can effectively control gas mobility and improve sweep efficiency, if correctly designed. It is believed that there is a significant gap between small laboratory-scale experiments and large field-scale tests because of two main reasons: (1) Typical laboratory flow tests are conducted in linear systems, whereas field-scale foam enhanced-oil-recovery (EOR) processes are performed in radial (or spherical partly) systems and (2) through the complicated in-situ lamella creation/coalescence mechanisms and non-Newtonian behavior, foam rheology depends on the geometry and dimensionality. As a result, it is still an open question as to how to translate laboratory-measured data to field-scale treatments.
Motivated by earlier studies of Kovscek et al. (1994, 1997), this study investigates how such dimensionality-dependent foam rheological properties are affected by different injection conditions on small and large scales, with a mechanistic foam-modeling technique. Complex foam-flow characteristics such as three foam states (weak-foam, strong-foam, and intermediate states) and two steady-state strong-foam regimes (high-quality regime and low-quality regime) lie in the heart of this analysis.
The calculation results from small radial and spherical systems showed that (1) for strong foams in the low-quality regime injected, foam mobility decreased [or mobility reduction factor (MRF) increased] significantly with distance showing a good sweep efficiency; (2) for strong foams in the high-quality regime, the situation became more complicated--near the well, foam mobility decreased, but away from the well, foam mobility increased with distance, which eventually gave a relatively low sweep efficiency; and (3) for weak foams injected, foam mobility increased with distance showing a poor sweep efficiency. The results implied that the use of a fixed value of MRF, which is a common practice in field-scale reservoir simulations, might lead to a significant error. When the method was applied to a larger scale, it was shown that strong foams could propagate deeper into the reservoir at higher injection rate, higher injection pressure, and at lower injection foam quality. Foam-propagation distance was very sensitive to these injection conditions for strong foams in the high-quality regime, but much less sensitive for strong foams in the low-quality regime.
|File Size||2 MB||Number of Pages||19|
Afsharpoor, A., Lee, G. S., and Kam, S. I. 2010. Mechanistic Simulation of Continuous Gas Injection Period During Surfactant-Alternating-Gas (SAG) Processes Using Foam Catastrophe Theory. Chemical Engineering Science 65 (11): 3615–3631. http://dx.doi.org/10.1016/j.ces.2010.03.001.
Alvarez, J. M., Rivas, H. J., and Rossen, W. R. 2001. Unified Model for Steady-State Foam Behavior at High and Low Foam Qualities. SPE J. 6 (3): 325–333. SPE-74141-PA. http://dx.doi.org/10.2118/74141-PA.
Ashoori, E., Marchesin, D., and Rossen, W. R. 2012. Multiple Foam States and Long-Distance Foam Propagation in Porous Media. SPE J. 17 (4): 1231–1245. SPE-154024-PA. http://dx.doi.org/10.2118/154024-PA.
Bernard, G. G. and Holm, L. W. 1964. Effect of Foam on Permeability of Porous Media to Gas. SPE J. 4 (3): 267–274. SPE-983-PA. http://dx.doi.org/10.2118/983-PA.
Boud, D. C. and Holbrook, O. C. 1958. Gas Drive Oil Recovery Process. US Patent No. 2,866,507.
Buckley, S. E. and Leverett, M. C. 1941. Mechanism of Fluid Displacement in Sands. Trans. AIME 146 (1): 107–116. SPE-942107-G. http://dx.doi.org/10.2118/942107-G.
Dholkawala, Z. F., Sarma, H. K., and Kam, S. I. 2007. Application of Fractional Flow Theory to Foams in Porous Media. J. Petroleum Science and Engineering 57 (1): 152–165. http://dx.doi.org/10.1016/j.petrol.2005.10.012.
Falls, A. H., Hirasaki, G. J., Patzek, T. E. A. et al. 1988. Development of a Mechanistic Foam Simulator: The Population Balance and Generation by Snap-off. SPE Res Eng 3 (3): 884–892. SPE-14961-PA. http://dx.doi.org/10.2118/14961-PA.
Farajzadeh, R., Lotfollahi, M., Eftekhari, A. A. et al. 2015. Effect of Permeability on Implicit-Texture Foam Model Parameters and the Limiting Capillary Pressure. Energy & Fuels 29 (5): 3011–3018. http://dx.doi.org/10.1021/acs.energyfuels.5b00248.
Friedmann, F., Chen, W. H., and Gauglitz, P. A. 1991. Experimental and Simulation Study of High-Temperature Foam Displacement in Porous Media. SPE Res Eng 6 (1): 37–45. SPE-17357-PA. http://dx.doi.org/10.2118/17357-PA.
Friedmann, F., Smith, M. E., Guice, W. R. et al. 1994. Steam-Foam Mechanistic Field Trial in the Midway-Sunset Field. SPE Res Eng 9 (4): 297–304. SPE-21780-PA. http://dx.doi.org/10.2118/21780-PA.
Gauglitz, P. A., Friedmann, F., Kam, S. I. et al. 2002. Foam Generation in Homogeneous Porous Media. Chemical Engineering Science 57 (19): 4037–4052. http://dx.doi.org/10.1016/S0009-2509(02)00340-8.
Gillis, J. V. and Radke, C. J. 1990. A Dual-Gas Tracer Technique for Determining Trapped Gas Saturation During Steady Foam Flow in Porous Media. Presented at the 65th SPE Annual Technical Conference and Exhibition, New Orleans, 23–26 September, SPE-20519-MS. http://dx.doi.org/10.2118/20519-MS.
Hirasaki, G. J. and Lawson, J. B. 1985. Mechanisms of Foam Flow in Porous Media: Apparent Viscosity in Smooth Capillaries. SPE J. 25 (2): 176–190. SPE-12129-PA. http://dx.doi.org/10.2118/12129-PA.
Holm, L. W. 1970. Foam Injection Test in the Siggins Field, Illinois. J Pet Technol 22 (12): 1499–1506. SPE-2750-PA. http://dx.doi.org/10.2118/2750-PA.
Jonas, T. M., Chou, S. I., and Vasicek, S. L. 1990. Evaluation of a CO2 Foam Field Trial: Rangely Weber Sand Unit. Presented at the SPE Annual Technical Conference and Exhibition, New Orleans, 23–26 September. SPE-20468-MS. http://dx.doi.org/10.2118/20468-MS.
Kam, S. I. and Rossen, W. R. 2003. A Model for Foam Generation in Homogeneous Media. SPE J. 8 (4): 417–425. SPE-87334-PA. http://dx.doi.org/10.2118/87334-PA.
Kam, S. I. 2008. Improved Mechanistic Foam Simulation With Foam Catastrophe Theory. Colloids and Surfaces A: Physicochemical and Engineering Aspects 318 (1): 62–77. http://dx.doi.org/10.1016/j.colsurfa.2007.12.017.
Khatib, Z. I., Hirasaki, G. J., and Falls, A. H. 1988. Effects of Capillary Pressure on Coalescence and Phase Mobilities in Foams Flowing Through Porous Media. SPE Res Eng 3 (3): 919–926. SPE-15442-PA. http://dx.doi.org/10.2118/15442-PA.
Kovscek, A. R., Patzek, T. W., and Radke, C. J. 1994.Mechanistic Prediction of Foam Displacement in Multidimensions: A Population Balance Approach. Presented at the SPE/DOE ImprovedOil Recovery Symposium, Tulsa, 17–20 April. SPE-27789-MS. http://dx.doi.org/10.2118/27789-MS.
Kovscek, A. R. and Radke, C. J. 1994. Fundamentals of Foam Transport in Porous Media. ACS Advances in Chemistry Series 242: 115–164. http://dx.doi.org/10.1021/ba-1994-0242.ch003.
Kovscek, A. R., Patzek, T. W., and Radke, C. J. 1997. Mechanistic Foam Flow Simulation in Heterogeneous and Multidimensional Porous Media. SPE J. 2 (4). SPE-39102-PA. http://dx.doi.org/10.2118/39102-PA.
Lake, L. W. 1989. Enhanced Oil Recovery. Prentice Hall.
Lee, S. and Kam, S. I. 2013. Enhanced Oil Recovery by Using CO2 Foams: Fundamentals and Field Applications. In Enhanced Oil Recovery Field Case Studies (James Sheng), Gulf Professional Publishing (Elsevier).
Li, B., Hirasaki, G. J., and Miller, C. A. 2006. Upscaling of Foam Mobility Control to Three Dimensions. Presented at the SPE/DOE Symposium on Improved Oil Recovery, Tulsa, 22–26 April. SPE-99719-PA. http://dx.doi.org/10.2118/99719-PA.
Liu, S., Miller, C. A., Li, R. F. et al. 2010. Alkaline/Surfactant/Polymer Processes: Wide Range of Conditions for Good Recovery. SPE J. 15 (2). SPE-113936-PA. http://dx.doi.org/10.2118/113936-PA.
Ma, K., Lopez-Salinas, J. L., Puerto, M. C. et al. 2013. Estimation of Parameters for the Simulation of Foam Flow Through Porous Media. Part 1: The Dry-Out Effect. Energy and Fuels 27 (5): 2363–2375. http://dx.doi.org/10.1021/ef302036s.
Ma, K., Ren, G., Mateen, K. et al. 2015. Modeling Techniques for Foam Flow in Porous Media. SPE J. 20 (3): 453–470. SPE-169104-PA. http://dx.doi.org/10.2118/169104-PA.
Mohammadi, S. S., Van Slyke, D. C., and Ganong, B. L. 1989. Steam-Foam Pilot Project in Dome-Tumbador Midway-Sunset Field. SPE Res Eng 4 (1): 7–16. SPE-16736-PA. http://dx.doi.org/10.2118/16736-PA.
Osterloh, W. T. and Jante Jr.,M. J. 1992. Effects of Gas and Liquid Velocity on Steady-State Foam Flow at High Temperature. Presented at the SPE/DOE Enhanced Oil Recovery Symposium, Tulsa, 22–24 April. SPE-24179-MS. http://dx.doi.org/10.2118/24179-MS.
Ransohoff, T. C. and Radke, C. J. 1988. Mechanisms of Foam Generation in Glass-Bead Packs. SPE Res Eng 3 (2): 573–585. SPE-15441-PA. http://dx.doi.org/10.2118/15441-PA.
Roostapour, A. and Kam, S. I. 2013. Anomalous Foam Fractional Flow Solutions at High Injection Foam Quality. SPE Res Eval & Eng 16 (1): 40–50. SPE-152907-PA. http://dx.doi.org/10.2118/152907-PA.
Rossen, W. R. and Gauglitz, P. A. 1990. Percolation Theory of Creation and Mobilization of Foams in Porous Media. AICHE J. 36 (8): 1176–1188. http://dx.doi.org/10.1002/aic.690360807.
Rossen, W. R. and Wang, M. W. 1999. Modeling Foams for Acid Diversion. SPE J. 4 (2): 92–100. SPE-56396-PA. http://dx.doi.org/10.2118/56396-PA.
Rossen, W. R. and Boeije, C. S. 2015. Fitting Foam-Simulation-Model Parameters to Data: II. Surfactant-Alternating-Gas Foam Applications. SPE Res Eval & Eng 18 (2): 273–283. SPE-165282-PA. http://dx.doi.org/10.2118/165282-PA.
Tang, G.-Q. and Kovscek A. R. 2006. Trapped Gas Fraction During Steady-State Foam Flow. Transport in Porous Media 65: 287–307. http://dx.doi.org/10.1007/s11242-005-6093-4.
Worthen, A. J., Bagaria, H. G., Chen, Y. et al. 2013. Nanoparticle-Stabilized Carbon Dioxide-in-Water Foams With Fine Texture. J. Colloid and Interface Science 391 (1): 142–151. http://dx.doi.org/10.1016/j.jcis.2012.09.043.