1. 西南石油大学,四川 成都610500中国石化江苏油田分公司,江苏,扬州,225009
2. 中国石化江苏油田分公司,江苏,扬州,225009
[ "郭德明(1995—),男,硕士,从事注气提高采收率及油气藏流体相态研究。地址:四川省成都市新都区新都大道8号西南石油大学,邮政编码:610500。E-mail: 873224527@qq.com" ]
[ "潘毅 E-mail:873224527@qq.com" ]
纸质出版:2022
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郭德明, 潘毅, 孙扬, 等. 低渗稠油油藏降黏剂-CO2复合驱提高采收率机理研究[J]. 油气藏评价与开发, 2022,(5):794-802.
GUO Deming, PAN Yi, SUN Yang, et al. EOR mechanism of viscosity reducer-CO2 combined flooding in heavy oil reservoir with low permeability[J]. Petroleum Reservoir Evaluation and Development, 2022, (5): 794-802.
郭德明, 潘毅, 孙扬, 等. 低渗稠油油藏降黏剂-CO2复合驱提高采收率机理研究[J]. 油气藏评价与开发, 2022,(5):794-802. DOI: 10.13809/j.cnki.cn32-1825/te.2022.05.011.
GUO Deming, PAN Yi, SUN Yang, et al. EOR mechanism of viscosity reducer-CO2 combined flooding in heavy oil reservoir with low permeability[J]. Petroleum Reservoir Evaluation and Development, 2022, (5): 794-802. DOI: 10.13809/j.cnki.cn32-1825/te.2022.05.011.
低渗稠油油藏实施CO
2
驱是目前发展的主要提高采收率综合利用的技术
但受CO
2
低黏度、高流度的影响
稠油油藏CO
2
驱易过早气窜
为此探索了低渗稠油油藏CO
2
-降黏剂降黏改善流度比调驱可行性
明确了低渗稠油油藏CO
2
-水溶性降黏剂复合驱提高采收率机理。结果表明:KD-45A水溶性降黏剂在缺少外力搅拌的情况下
只能乳化原油表层以起到降黏效果
降黏效果较差
但降黏剂段塞能够改善因黏度差引起的油气过大的流度比
有效地控制CO
2
沿气流通道突进;水溶性降黏剂乳化形成的O/W形乳状液过渡带黏度接近水相
能够防止水溶性降黏剂的指进
使降黏剂段塞对CO
2
的调驱作用更加明显、CO
2
的波及面积更大;CO
2
在降黏剂中的溶解会降低CO
2
-降黏体系剂的界面张力
充分发挥二者的协同驱油作用;CO
2
溶于降黏剂后形成碳化水可以大幅降低重力和黏度差异对波及面积的影响
形成较为稳定连续的驱替界面
复合驱油体系的驱油机理相互协同、叠加
可大幅提高稠油采收率。
The implementation of CO
2
flooding in heavy oil reservoirs with low-permeability is currently the main comprehensive utilization technology for enhanced oil recovery. However
due to the low viscosity and high mobility of CO
2
CO
2
flooding in heavy oil reservoirs is prone to premature gas channeling. For this reason
the feasibility of low permeability heavy oil reservoirs with CO
2
-viscosity reducer to reduce viscosity and improve mobility ratio has been explored
and the mechanism of the combined flooding of CO
2
and water-soluble viscosity reducer for low-permeability heavy oil reservoirs to EOR is obtained. The results show that the KD-45A water-soluble viscosity reducer can only emulsify the surface of crude oil to reduce the viscosity without external stirring. The viscosity reduction effect is poor
but the viscosity reducer slug can improve the mobility ratio caused by viscosity differences
which can effectively control the CO
2
rushing along the airflow channel. The O/W-shaped emulsion transition zone formed by the emulsification of the water-soluble viscosity reducer has a viscosity close to the water phase
which can prevent the fingering of the water-soluble viscosity reducer
so that the viscosity reducer slug has a more obvious control and displacement effect on CO
2
and the swept area of CO
2
is larger. The dissolution of CO
2
in the viscosity reducer will reduce the interfacial tension of the CO
2
-viscosity reducer system
which can give full play to the synergy between the two displacement effect. The formation of carbonized water after CO
2
dissolves in the viscosity reducer can greatly reduce the influence of gravity and viscosity differences on the swept area
forming a relatively stable and continuous displacement interface. The displacement mechanisms of the combined flooding system are synergistic and superimposed
which can significantly improve the recovery rate of heavy oil.
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