Experimental Comparative Investigation of Hot Solvent/Steam-Assisted Gravity Drainage in Oil Sand Reservoirs

被引:4
|
作者
Bai, Yu [1 ]
Liu, Jianbo [2 ]
Liu, Shangqi [1 ]
Xia, Zhaohui [1 ]
Chen, Yuxin [1 ]
Liang, Guangyue [1 ]
Shen, Yang [1 ]
机构
[1] PetroChina Res Inst Petr Explorat & Dev, Beijing 100083, Peoples R China
[2] Univ Calgary, Dept Chem & Petr Engn, Calgary, AB T2N 1N4, Canada
来源
ACS OMEGA | 2021年 / 6卷 / 34期
关键词
HEAVY-OIL; DIFFUSION-COEFFICIENTS; GAS DIFFUSIVITY; VAPEX; EXTRACTION; BITUMEN; STEAM; RECOVERY; METHANE;
D O I
10.1021/acsomega.1c03090
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Hot solvent-assisted gravity drainage (HS-AGD) is an effective way to exploit oil sands and heavy oil both economically and environmentally. The visualized microscopic seepage experiments and two-dimensional (2-D) macroscopic simulation experiments of HS-AGD are carried out, and the results are compared with that of steam-assisted gravity drainage (SAGD) in detail for the first time in order to compare their development effects of the oil sand reservoir. MacKay River oil sand bitumen is taken as an oil sample in the experiments, with n-hexane as the solvent. Micro seepage characteristics of the hot solvent and steam and the remaining oil distribution of the solvent and steam drive are investigated through microseepage experiments. The expanding process of the solvent/steam chamber and production performance of HS-SAGD and SAGD are investigated through macrosimulation experiments. The study found that the sweep efficiency of hot solvent is higher than that of steam at the same temperature due to the small interfacial tension between the condensed solvent and heated bitumen. Due to the severe gravity segregation, the steam accumulated at the top of the model during the 2-D physical simulation experiment, which results in the huge heat loss at the top of the model. The temperature of the steam chamber is significantly lower than that of the solvent chamber. The oil recovery of 200 degrees C hot solvent vapor is twice as much as that of 300 degrees C steam owing to the different drainage mechanisms of the HS-AGD and SAGD. In SAGD, only heat transfer reduces the viscosity of oil sand bitumen. The components of oil produced in SAGD have little difference compared with that of the original bitumen. In HS-AGD, both mass transfer and the sensible heat transfer reduce the viscosity of oil sand bitumen. The in situ asphaltene precipitation induced by heated-solvent extraction also upgrades the bitumen. The results of component analysis show that in HS-AGD, the content of heavy components in the oil sand bitumen is obviously reduced. This paper aims to reveal the oil drainage mechanism of HS-AGD and SAGD from the macroscopic and microscopic view and to provide theoretical guidance for the field application of this technology.
引用
收藏
页码:22333 / 22343
页数:11
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