相对渗透率
超临界流体
润湿
碳酸盐
石油工程
溶解
注水(采油)
提高采收率
火花塞
磁导率
残余油
材料科学
地质学
化学
热力学
复合材料
多孔性
冶金
有机化学
物理化学
膜
物理
生物化学
作者
Xianmin Zhou,Fawaz M. AlOtaibi,Sunil Kokal
出处
期刊:Energy & Fuels
[American Chemical Society]
日期:2019-05-07
卷期号:33 (6): 5464-5475
被引量:21
标识
DOI:10.1021/acs.energyfuels.9b01053
摘要
Relative permeability characteristic and wetting behavior of reservoir rocks are crucial for oil recovery. Supercritical CO2 (sc-CO2) miscible flooding as an enhanced oil recovery (EOR) method has been successfully used in both sandstone and carbonate reservoirs. The sc-CO2 is miscible with the remaining oil left after water flooding at injection pressures above MMP, and then higher recovery can be achieved. To describe the flow characteristics and performance of sc-CO2 displacing remaining oil and water, characteristic parameters such as the water (Krw) and miscible phase (Krm) relative permeability curves and wetting behavior are required, which applies to reservoir numerical simulation for predicting production performance of sc-CO2 miscible injection. Surprisingly, publications of experimental data including water and miscible phases are relatively rare due to the lack of proper experimental methods in laboratory. In this paper, we proposed a modified method based on the Corey model to calculate water and miscible phase relative permeability using endpoint values of oil/water system and water/miscible phase (sc-CO2 dissolving into oil) system. In addition, relative permeability reduction and the change of wetting behavior of core plug after sc-CO2 miscible injection were evaluated. Four core flooding experiments were carried out on carbonate composite cores using live oil at reservoir conditions. The experiments included seawater injection and sc-CO2 injection for each core plug to obtain the endpoint values from both injections. The Corey model was used directly to calculate oil/water relative permeability of the carbonate composite cores. A modified Corey model proposed in this paper was used to calculate water and miscible phase relative permeability and obtain the relationship of relative permeability vs miscible phase saturation. The co-flow characteristics in water and miscible phase system were described using these endpoints and relative permeability curves. As a result, relative permeability to water and miscible phases can be calculated using the modified Corey model based on endpoint values during co-flow of water and miscible phases in core plug. The evaluation of relative permeability reduction of core plugs was made by comparing endpoint relative permeability of sc-CO2 at residual state of water/phase phase system with that of water at residual oil saturation of oil/water system. The values of endpoint relative permeability to sc-CO2 are extremely low, which are in the range of 1.57–5% after sc-CO2 injection. The wetting behavior had slightly changed by observing photographs of water droplets and oil droplets on the surface of core plugs before and after sc-CO2 injection. The relationship between relative permeability to water and miscible phases vs miscible saturation has been developed when the water saturation is decreasing during sc-CO2 miscible injection process. There is an obvious influence of water and miscible phase relative permeability when the Corey exponents, Nw and Nm, are changed.
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