[1] A. Bera, A. Mandal, G.B. Guha, Synergistic effect of surfactant and salt mixture on interfacial tension reduction between crude oil and water in enhanced oil recovery, J. Chem. Eng. Data 59(1) (2013) 89-96. [2] S. Kumar, P. Panigrahi, Kumar Saw, A. Mandal, Interfacial interaction of cationic surfactants and its effect on wettability alteration of oil-wet carbonate rock, Energy Fuel 30(2016) 2846-2857. [3] N. Kumar, A. Mandal, Surfactant stabilized oil-in-water nanoemulsion:stability, interfacial tension and rheology study for enhanced oil recovery application, Energy Fuel 32(6) (2018) 6452-6466. [4] M. Riazi, A. Golkari, The influence of spreading coefficient on carbonated water alternating gas injection in a heavy crude oil, Fuel 178(2016) 1-9. [5] M. Riazi, M.S. Sohrabi, M. Jamiolahmady, S. Ireland, C. Brown, Oil recovery improvement using CO2-enriched water injection, 71st European Association of Geoscientists and Engineers Conference and Exhibition 2009, pp. 1915-1925. [6] L.L. Handy, A laboratory study of oil recovery by solution gas drive, AIME, Transactions 213(1958) 310-315. [7] L.W. Holm, L.J. O'Brien, Carbon dioxide test at the mead-strawn field, J. Pet. Technol. 23(04) (1971) 431-442. [8] L.W. Holm, V.A. Josendal, Mechanisms of oil displacement by carbon dioxide, J. Pet. Technol. 26(12) (1974) 1-427. [9] J.C. Moulu, Solution-gas drive:experiments and simulation, J. Pet. Sci. Eng. 2(4) (1989) 379-386. [10] F. RCK Wong, J.S. Guo, W.E. Barr Weaver, Heavy oil flow under solution-gas drive:pressure depletion tests, J. Can. Pet. Technol. 38(1999) 31-37. [11] R. Kumar, M. Pooladi-Darvish, T. Okazawa, An investigation into enhanced recovery under solution gas drive in heavy oil reservoirs, paper SPE 59336 the SPE/DOE IOR Symposium, Tulsa, 20003-5, https://doi.org/10.2118/59336-MS. [12] P. Arora, A. Kovscek, Mechanistic modeling of solution-gas drive in viscous oils, J. Pet. Technol. 53(6) (2001) 48-49. [13] S. Akin, A.R. Kovscek, Heavy-oil solution gas drive:a laboratory study, J. Pet. Sci. Eng. 35(1-2) (2002) 33-48. [14] G.Q. Tang, Y.T. Leung, L.M. Castanier, A. Sahni, F. Gadelle, M. Kumar, A.R. Kovscek, An investigation of the effect of oil composition on heavy oil solution-gas drive, SPE J. 11(01) (2006) 58-70. [15] A. Sahni, F. Gadelle, M. Kumar, L. Tomutsa, A.R. Kovscek, Experiments and analysis of heavy-oil solution-gas drive, SPE Reserv. Eval. Eng. 7(03) (2004) 217-229. [16] M. Shahvali, M. Pooladi-Darvish, Dynamic modelling of solution-gas drive in heavy oils, J. Can. Pet. Technol. 48(12) (2009) 39-46. [17] T. Lu, Z. Li, S. Li, S. Liu, X. Li, P. Wang, Z. Wang, Behaviors of foamy oil flow in solution gas drive at different temperatures, Transp. Porous Media 109(1) (2015) 25-42. [18] A. Bera, T. Babadagli, Relative permeability of foamy oil for different types of dissolved gases, SPE Reserv. Eval. Eng. 19(04) (2016) 604-619. [19] T. Lu, Z. Li, S. Li, P. Wang, Z. Wang, S. Liu, Enhanced heavy oil recovery after solution gas drive by water flooding, J. Pet. Sci. Eng. 137(2016) 113-124. [20] X. Zhou, F. Zeng, L. Zhang, H. Wang, Foamy oil flow in heavy oil-solvent systems tested by pressure depletion in a sandpack, Fuel 171(2016) 210-223. [21] B.S. Abusahmin, R.R. Karri, B.B. Maini, Influence of fluid and operating parameters on the recovery factors and gas oil ratio in high viscous reservoirs under foamy solution gas drive, Fuel 197(2017) 497-517. [22] W. Dong, X. Wang, J. Wang, A new method to calculate the early performance of solution-gas-drive reservoirs, J. Pet. Sci. Eng. 171(2018) 153-163. [23] U. Bagudu, S.R. McDougall, E.J. Mackay, Network modelling analysis of a depressurization experiment on a North Sea reservoir core sample, J. Pet. Sci. Eng. 162(2018) 63-75. [24] Y. Zhang, H. Zhao, X. Sun, S. Zhang, Z. Gai, Y. Liu. Experimental study of foamy oil solution gas drive process in an etched glass micromodel. IOP Conference Series:Earth and Environmental Science. vol. 223(1)(2019)012035. [25] Y.B. Chang, B.K. Coats, J.S. Nolen, A compositional model for CO2 floods including CO2 solubility in water, SPE Reserv. Eval. Eng. 1(02) (1998) 155-160. [26] R. Wiebe, The binary system carbon dioxide-water under pressure, Chem. Rev. 29(3) (1941) 475-481. [27] Z. Duan, R. Sun, An improved model calculating CO2 solubility in pure water and aqueous NaCl solutions from 273 K to 533 K and from 0 MPa to 200 MPa, Chem. Geol. 193(3) (2003) 257-271. [28] Z. Duan, R. Sun, C. Zhu, An improved model for the calculation of CO2 solubility in aqueous solutions containing Na+, K+, Ca2+, Mg2+, Cl-, and SO42-, Mar. Chem. 98(2) (2006) 131-139. [29] M. Shakiba, S. Ayatollahi, M. Riazi, Investigation of oil recovery and CO2 storage during secondary and tertiary injection of carbonated water in an Iranian carbonate oil reservoir, J. Pet. Sci. Eng. 137(2016) 134-143. [30] A. Golkari, M. Riazi, Comparative study of oil spreading characteristics for water and carbonated water systems using live and dead oils, J. Pet. Sci. Eng. 171(2018) 242-252. [31] M. Riazi, Pore scale mechanisms of carbonated water injection in oil reservoirs, PhD thesis, Heriot-Watt University, UK, 2011. [32] C. Du, Y.C. Yortsos, A numerical study of the critical gas saturation in a porous medium, Transp. Porous Media 35(2) (1999) 205-225. [33] G.Q. Tang, A. Firoozabadi, Wettability alteration to intermediate gas-wetting in porous media at elevated temperatures, Transp. Porous Media 52(2) (2003) 185-211. [34] M. Shakiba, M. Riazi, S. Ayatollahi, M. Takband, The impact of connate water saturation and salinity on oil recovery and CO2 storage capacity during carbonated water injection in carbonate rock, Chin. J. Chem. Eng. 27(7) (2019) 1699-1707. |