Viscous oil recovery and in-situ deasphalting in fractured reservoirs - Part 2: Effect of solvent type and temperature

被引:13
作者
Sie, Chao-Yu [1 ]
Nguyen, Bradley [1 ]
Diaz, Orlando Castellanos [3 ,4 ]
Verlaan, Marco [2 ]
Nguyen, Quoc P. [1 ]
机构
[1] Univ Texas Austin, Dept Petr & Geosyst Engn, 200 East Dean Keeton St,Stop C0300, Austin, TX 78712 USA
[2] Shell Kuwait Ltd, 20th Floor,Sahab Tower Salhiya, Salhiya, Kuwait
[3] Shell Canada Ltd, POB 100,STN M, Calgary, AB T2P 2H5, Canada
[4] Dow Chem Canada, Calgary, AB, Canada
关键词
Enhanced oil recovery; Solvent process; Miscible injection; Deasphalting; Viscous oil; Bitumen; Fractured reservoirs; HEAVY-OIL; ASPHALTENE PRECIPITATION; BITUMEN RECOVERY; INJECTION; DEPOSITION; VISCOSITY; BEHAVIOR;
D O I
10.1016/j.fuel.2019.03.044
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This paper advances the understanding of the solvent-based EOR methods from our previous work by investigating the effect of solvent type and temperature on the recovery of viscous oil by liquid extraction using sandstone cores with an artificial fracture. The production mechanisms were identified through the analysis of oil production rate, ultimate recovery, and in-situ deasphalting in different sections of the core. The use of dichloromethane (DCM) was introduced as the reference to study the production without in-situ deasphalting whereas n-pentane injection was compared to that of n-butane injection to study the effect of paraffin length on production with in-situ deasphalting. Sustained high production rates, which deviate from the behavior of typical gravity drainage processes, were observed in the cases with in-situ deasphalting. This discrepancy was attributed to the enhanced convection in the matrix due to the alteration of fracture aperture by asphaltene precipitation and deposition. Temperature has a significant impact on oil production through its effect on mass diffusivity as well as asphaltene rheology. The result of this work indicates that solvent selection is a key factor in the optimizing solvent EOR process and potential asphaltene deposition should be taken into consideration.
引用
收藏
页码:294 / 301
页数:8
相关论文
共 44 条
  • [1] Measurement and modeling of the phase behavior of solvent diluted bitumens
    Agrawal, P.
    Schoeggl, F. F.
    Satyro, M. A.
    Taylor, S. D.
    Yarranton, H. W.
    [J]. FLUID PHASE EQUILIBRIA, 2012, 334 : 51 - 64
  • [2] Akbarzadeh K, 2004, CAN INT PETR C, DOI [10.2118/2004-026-EA, DOI 10.2118/2004-026-EA]
  • [3] Al Yousef Z., 2013, Journal of Petroleum Science Research, V3 issue, DOI [DOI 10.14355/JPSR.2014.0303.01, 10.14355/jpsr.2014.0303.01]
  • [4] Al-Bahlani A.M., 2009, SPE-117626-MS, DOI [10.2118/117626-ms, DOI 10.2118/117626-MS, 10.2118/117626-MS]
  • [5] Alkindi AS, 2010, SPE EOR C OIL GAS 20, DOI [10.2523/IPTC-12710-MS, DOI 10.2523/IPTC-12710-MS]
  • [6] Anand N., 2018, SPE190350MS, DOI [10.2118/190350-MS, DOI 10.2118/190350-MS]
  • [7] Quantitative and visual characterization of asphaltenic components of heavy-oil after solvent interaction at different temperatures and pressures
    Arciniegas, Laura Moreno
    Babadagli, Tayfun
    [J]. FLUID PHASE EQUILIBRIA, 2014, 366 : 74 - 87
  • [8] Asphaltene precipitation, flocculation and deposition during solvent injection at elevated temperatures for heavy oil recovery
    Arciniegas, Laura Moreno
    Babadagli, Tayfun
    [J]. FUEL, 2014, 124 : 202 - 211
  • [9] Bird RB, 2007, TRANSPORT PHENOMENA, P558
  • [10] Physical factors affecting the transport and fate of colloids in saturated porous media
    Bradford, SA
    Yates, SR
    Bettahar, M
    Simunek, J
    [J]. WATER RESOURCES RESEARCH, 2002, 38 (12) : 63 - 1