[1]. Nourozieh H, Kariznovi M, Guan JG, Abedi J (2013) Measurement of thermophysical properties and modeling for pseudo-binary mixtures of n -decane and Athabasca bitumen, Fluid Phase Equilib 347: 62–75.##
[2]. Nourozieh H, Kariznovi M, Abedi J (2012) Liquid-Liquid Equilibria of Solvent / Heavy Crude Systems : In Situ Upgrading and Measurements of Physical Properties, SPE Western Regional Meeting California 1–7. ##
[3]. Nourozieh H, Kariznovi M, Abedi J (2012) Development and evaluation of a modified experimental apparatus for phase behavior study of solvent – heavy crude systems, Fuel Process. Technol. 102: 116–123. ##
[4]. Kariznovi M, Nourozieh H, Abedi J (2014) Volumetric Properties of Athabasca Bitumen + n ‑ Hexane Mixtures, Energy & Fules 28, 12: 7418-7425. ##
[5]. Curtis C, Kopper R, Decoster E, Guzman-Garcia A, Huggins C, Knauer L, Minner M, Kupsch N, Linares LM, Rough H, Waite M. (2002) Heavy-oil reservoirs, Oilfield Review, 14, 3: 30–51. ##
[6]. Das SK, Butler RM (1998) Mechanism of the vapor extraction process for heavy oil and bitumen, Journal of Petroleum Science and Engineering, 21, 1–2: 43–59. ##
[7]. Nourozieh H, Kariznovi M, Abedi J (2017) Solubility of n -butane in athabasca bitumen and saturated densities and viscosities at temperatures up to 200 oC, SPE Journal, 22, 01: 94–102. ##
[8]. Butler RM (1985) A New approach to the modelling of steam-assisted gravity drainage, Journal of Canadian Petroleum Technology 24, 03: 42–51. ##
[9]. Butler RM, Stephens DJ (1981) The gravity drainage of steam-heated heavy oil to parallel horizontal wells, Journal of Canadian Petroleum Technology 20, 02. ##
[10]. Kariznovi M, Nourozieh H, Abedi J (2011) Experimental and modeling study of vapor-liquid equilibrium for propane-heavy crude systems at high temperature conditions, In SPE Annual Technical Conference and Exhibition, Society of Petroleum Engineers.
[11]. Butler R M (1991) Thermal recovery of oil and bitumen, Old Tappan, NJ (United States); Prentice Hall Inc. ##
[12]. Farouq Ali SM (2013) All you need is darcy’s equation to determine eor success or failure, SPE Western Regional & AAPG Pacific Section, California. ##
[13]. Nourozieh H, Kariznovi M, Abedi J (2015) Viscosity measurement and modeling for mixtures of athabasca bitumen/n-pentane at temperatures up to 200°C, SPE Journal 20, 02: 226–238. ##
[14]. Johnston KA, Satyro MA, Taylor SD, Yarranton HW (2017) Can a cubic equation of state model bitumen-solvent phase behavior?, Energy and Fuels, 31, 8: 7967–7981. ##
[15]. Mancilla-Polanco A, Schoeggl FF, Johnston K, Richardson WDL, Yarranton HW, Taylor SD (2017) The phase behavior of heavy oil and propane mixtures, SPE Canada Heavy Oil Technology Conf.,Canada. ##
[16]. Drive P, Suite A, Canada ATG (2004) The paradox of asphaltene precipitation, 2: 557–558. ##
[17]. Mannistu KD, Yarranton HW, Masliyah JH (1997) Solubility modeling of asphaltenes in organic solvents, Energy & Fuels, 11, 03: 615–622. ##
[18]. Hu YF, Guo TM (2001) Effect of temperature and molecular weight of n-alkane precipitants on asphaltene precipitation, Fluid Phase Equilibria 192, 1–2: 13–25. ##
[19]. Andersen SI, Birdl KS (1990) Influence of temperature and solvent on the precipitation of asphaltenes, Petroleum Science and Technology 08, 06: 593–615. ##
[20]. Ali LH, Al-Ghannam KA (1981) Investigations into asphaltenes in heavy crude oils. I. Effect of temperature on precipitation by alkane solvents, Fuel 60, 11: 1043–1046. ##
[21]. Agrawal P, Schoeggl FF, Satyro MA, Taylor SD, Yarranton HW (2012) Measurement and modeling of the phase behavior of solvent diluted bitumens, Fluid Phase Equilibria 334: 51–64. ##
[22]. Gao J, Okuno R, Li HA (2017) An Experimental study of multiphase behavior for <em>n</em>-butane/bitumen/water mixtures, SPE Journal 22, 03: 0783–0798. ##
[23]. Johnston KA, Schoeggl FF, Satyro MA, Taylor SD, Yarranton HW (2017) Fluid phase equilibria phase behavior of bitumen and n- pentane, Fluid Phase Equilibria 442: 1–19. ##
[24]. Nourozieh H, Kariznovi M, Abedi J (2014) Pentane as a potential candidate for ES-SAGD and hybrid processes: its phase behavior with bitumen, SPE Heavy Oil Conference, Alberta, 1–17. ##
[25]. Li H, Zheng S, Yang D (2013) Enhanced swelling effect and viscosity reduction of solvents-CO2 -heavy oil Systems, SPE Journal 18, 04: 695–707. ##
[26]. Li H, Yang D (2013) Phase behaviour of C3H8/n-C4H10/ and heavy-oil systems at high pressures and elevated temperatures, Journal of Canadian Petroleum Technology 52:01 30–40. ##
[27]. Zirrahi M, Hassanzadeh H, Abedi J (2015) Prediction of CO2 solubility in bitumen using the cubic-plus-association equation of state (CPA-EoS), The Journal of supercritical fluids prediction of CO2 solubility in bitumen using the cubic-plus-association equation of state (cpa-eos) 98, 44–49. ##
[28]. Svrcek WY, Mehrotra AK (1982) Gas solubility , viscosity and density measurements for athabasca bitumen, Journal of Canadian Petroleum Technology 21, 09. ##
[29]. Fu CT, Puttangunla R, Vilcsak G (1986) Vapour-Liquid equilibrium properties For gas - cold lake bitumen, In Annual Technical Meeting. Petroleum Society of Canada. ##
[30]. Mehrotra AK, Svrcek WY (1988) Properties of cold lake bitumen saturated with pure gases and gas mixtures, The Canadian Journal of Chemical Engineering 66, 4: 656–665. ##
[31]. Yu JM, Huang SH, Radosz M (1989) Phase behavior of reservoir fluids: supercritical carbon dioxide and cold lake bitumen, Fluid Phase Equilibria, 53: 429–438. ##
[32]. Sayegh SG, Rao DN, Kokal S, Najman J (1990) Phase behaviour and physical properties of lindbergh heavy oil/Co2 mixtures, Journal of Canadian Petroleum Technology, 29, 06: 31–39. ##
[33]. Eastick RR, Svrcek WY, Mehrotra AK (1992) Phase behaviour of Co2 -bitumen fractions, The Canadian Journal of Chemical Engineering 70, 01: 159–164. ##
[34]. Han B, Peng DY, Fu CT, Vilcsak G (1992) An apparatus for phase equilibrium studies of carbon dioxide + heavy hydrocarbon systems, Journal of Chemical Engineering 70, 06, 1164–1171. ##
[35]. Das SK, Butler RM (1996) Diffusion coefficients of propane and butane in peace river bitumen, Journal of Chemical Engineering 74, 06: 985–992. ##
[36]. Han B, Yang G, Ke J, Mao C, Yan H (1998) Phase equilibria of supercritical propane–fengcheng bitumen system and the density and viscosity of the liquid phase, Fluid Phase Equilibria 143, 1–2: 205–211. ##
[37]. Zhang X, Shaw JM (2006) The impact of multiphase behavior on coke deposition in heavy oil hydroprocessing catalysts, Energy & Fules 20, 02: 473-480. ##
[38]. Luo P, Yang C, Gu Y (2007) Enhanced solvent dissolution into in-situ upgraded heavy oil under different pressures, Fluid Phase Equilibria 252, 1–2: 143–151. ##
[39]. Badamchi-Zadeh A, Yarranton HW, Svrcek WY, Maini BB (2009) Phase behaviour and physical property measurements for VAPEX solvents: Part I. Propane and Athabasca bitumen, Journal of Canadian Petroleum Technology 48, 01: 54–61. ##
[40]. Badamchi-Zadeh A, Yarranton HW, Maini BB, Satyro MA (2009) Phase behaviour and physical property measurements for VAPEX solvents: Part II. propane, carbon dioxide and athabasca bitumen, Journal of Canadian Petroleum Technology 48, 03: 57–65. ##
[41]. Luo P, Gu Y (2009) Characterization of a heavy oil-propane system in the presence or absence of asphaltene precipitation, Fluid Phase Equilibria 277, 01: 1–8. ##
[42]. Yazdani A, Maini BB (2010) Measurements and modelling of phase behaviour and viscosity of a heavy oil/butane system, Journal of Canadian Petroleum Technology 49, 02: 9–14. ##
[43]. Badamchizadeh A, Yarranton H, Maini B (2013) Phase behavior and physical property modeling for vapex solvents: propane, carbon dioxide, and athabasca bitumen, SPE Heavy Oil Conference-Canada. Society of Petroleum Engineers. ##
[44]. Li H, Yang DT (2013) Phase behaviour of C3H8/n-C4H10/heavy-oil systems at high pressures and elevated temperatures, Journal of Canadian Petroleum Technology 52, 01: 30–40. ##
[45]. Li X, Li H, Yang D (2013) Determination of multiphase boundaries and swelling factors of solvent(s)-Co2-heavy oil systems at high pressures and elevated temperatures, Energy and Fuels 27, 03: 1293– 1306. ##
[46]. Varet G, Montel F, Nasri D, Daridon J (2013) Gas solubility measurement in heavy oil and extra heavy oil at vapor extraction (vapex) conditions, Energy & Fuels 27, 05: 2528–2535. ##
[47]. Nourozieh H, Kariznovi M, Abedi J (2016) Measurement and modeling of solubility and saturated-liquid density and viscosity for methane/athabasca-bitumen mixtures, SPE Journal 21, 01: 180–189. ##
[48]. Li X, Yang D, Fan Z (2014) Phase behaviour and viscosity reduction of co 2 -heavy oil systems at high pressures and elevated temperatures, SPE Heavy Oil Conference-Canada, Alberta 1–17. ##
[49]. Nourozieh H, Kariznovi M, Abedi J (2015) Experimental and modeling studies of phase behavior for propane/athabasca bitumen mixtures, Fluid Phase Equilibria, 397, 37–43. ##
[50]. Dini Y, Becerra M, Shaw JM (2016) Phase behavior and thermophysical properties of peace river bitumen + propane mixtures from 303 k to 393 k, Journal of Chemical & Engineering Data 61, 8, 2659–2668. ##
[51]. Hu R, Crawshaw JP, Trusler JPM, Boek ES (2016) Rheology and phase behavior of carbon dioxide and crude oil mixtures, Energy and Fuels 31, 6: 5776–5784. ##
[52]. Nourozieh H, Kariznovi M, Abedi J (2016) Measurement and correlation of solubility and physical properties for gas-saturated athabasca bitumen, SPE Production and Operations 31, 03: 207–218. ##
[53]. Eghbali S, Dehghanpour H (2017) An Experimental and modeling study of solvent-bitumen phase behavior at elevated temperatures using cold lake bitumen, SPE Annual Technical Conference and Exibition, Texas, 9–11. ##
[54]. Eghbali S, Dehghanpour H, Dragani J, Zhang X (2018) Phase behaviour and viscosity of bitumen-CO2/light hydrocarbon mixtures at elevated temperatures: a cold lake case study, In SPE Canada Heavy Oil Technical Conference. ##
[55]. Mehrotra AK, Nighswander JA, Kalogerakis N (1989) Data and correlation for CO2-peace river bitumen phase behaviour at 22-200 c, AOSTRA Journal of Research 05, 04: 351–358. ##
[56]. Mehrotra AK, Svrcek WY (1985) Viscosity, density and gas solubility data for oil sand bitumens. part i: athabasca bitumen saturated with co and C2H6, AOSTRA Journal of Research, 1, 04: 263–268. ##
[57]. Mehrotra AK, Svrcek WY (1988) Properties of cold lake bitumen saturated with pure gases and gas mixtures, The Canadian Journal of Chemical Engineering 66, 04: 656–665. ##
[58]. Mehrotra AK, Svrcek WY (1985) Viscosity, density and gas solubility data for oilsand bitumens. Part II: wabasca bitumen saturated with n2, CO, CH4, CO2 and C2H6, AOSTRA Journal of Research, 83–93. ##
[59]. Van Konynenburg PH, Scott RL (1980) Critical Lines and phase equilibria in binary van Der waals mixtures, Philosophical Transactions of the Royal Society of London. Series A, Mathematical and Physical Sciences 298, 1442: 495-540. ##
[60]. Smith JM, Van Ness HC, Abbott MM (1950) Introduction to chemical engineering thermodynamics, 7th ed., McGraw-Hill, 1-584. ##
[61]. Peng DY, Robinson DB (1982) A new two-constant equation of state, Industrial and Engineering Chemistry Fundamentals 15, 1: 59–64, 1976. ##
[62]. Péneloux A, Rauzy E, Fréze R (1982) A consistent correction for Redlich-Kwong-Soave volumes, Fluid Phase Equilibria 8, 1: 7–23. ##
[63]. Mathias PM, Naheiri T, Edwin M Oh (1989) A density correction for the Peng-Robinson equation of state, F luid Phase Equilibria 47, 1: 77–87. ##
[64]. Danesh A (1998) PVT and Phase Behaviour of Petroleum Reservoir Fluids, 1st ed., Elsevier, Edinburg, Scotland, 1-385.
[65]. Gao G, Daridon J, Saint-Guirons H, Xans P, Montel F (1992) A simple correlation to evaluate binary interaction parameters of the Peng-Robinson equation of state: binary light hydrocarbon systems, Fluid Phase Equilibria 74: 85–93. ##
[66]. Twu CH (1984) An internally consistent correlation for predicting the critical properties and molecular weights of petroleum and coal-tar liquids, Fluid Phase Equilibria 16, 2: 137–150. ##
[67]. Riazi MR (2005) Characterization and properties of petroleum fractions 50. ASTM international. ##
[68]. Wilson GM (1969) A modified Redlich-Kwong equation of state, application to general physical data calculations, in 65th National AIChE Meeting, Cleveland, OH 16, 6: 991-998.
[69]. Michelsen ML (1982) The isothermal flash problem. Part I. Stability, Fluid Phase Equilibria 9, 1: 1–19. ##
[70]. Díaz OC, Modaresghazani J, Satyro MA, Yarranton HW (2011) Modeling the Phase Behavior of Heavy Oil and Solvent Mixtures, Fluid Phase Equilibria 304, 1–2: 74–85. ##
[71]. Kontogeorgis GM, Folas GK (2010) Thermodynamic models for industrial applications from classical and advanced, John Wiley & Sons. ##
[72]. Firoozabadi A (1999) Thermodynamics of hydrocarbon reservoirs, 1st ed., Mc Graw-Hill. ##