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Experimental and Analytical Modeling of Gravity Drainage Dominated Heavy-Oil Recovery Under Non-Isothermal Conditions:A Microscale Approach

机译:在非等温条件下的重力排水的实验和分析建模在非等温条件下的重质 - 恢复:微观方法

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Steam assisted gravity drainage(SAGD)is a well-known example of a non-isothermal gravity dominated recovery application.It is commonly observed that field scale applications of this process yield less recovery than estimated.This requires |in-depth analysis of the problem at the pore scale to account for the residual oil saturation in the swept zone.It is still uncertain to what extent pore scale mechanisms,such as the counter and co-current nature of multiphase flow,the trapping mechanism and the distribution of phases,the formation and flow of emulsions,and heat transfer mechanisms affect the process of non-isothermal gravity drainage dominated heavy-oil recovery.Alteration of wettability due to phase change under steam heating and how wettability interacts with spreading coefficients are still enigmatic.In this paper,we used a single capillary tube to mimic an elementary volume in the swept area during gravity dominated displacement under non-isothermal applications.We carned out two-phase(air-oil)and three phase(air-oil-initial water saturation)flow displacements in a capillary tube under isothermal and non-isothermal conditions,varying the air injection rate and the capillary properties.Detailed visualization experiments were carried out to analyze:(1)The effects of oil viscosity,wettability and the spreading coefficient on isothermal and non-isothermal displacement.(2)the interplay among capillary.gravity and viscous(steam injection rates)forces and wettability'using different size capillaries,and(3)residual oil saturation and phase distribution in the capillaries(mainly the thicknesses of the wetting and non wetting phases).The analytical calculations based on the experimental observations(measured displacement rates)suggest that at low capillary numbers,the temperature does not have a significant influence in the residual saturation of processed and crude oil.For heavy crude oil this is true for the capillary numbers less than 0.02.Above this threshold capillary number,the oil recovery(and therefore residual oil saturation)is very sensitive to the capillary number,i.e..the injection rate,interfacial tension,and wettability,and to temperature.
机译:蒸汽辅助重力排水(SAGD)是非等温重力占据恢复应用的众所周知的例子。通常观察到该过程的场比例应用比估计更少的恢复。这需要对问题进行深入分析在孔隙刻度下,考虑扫掠区域中的残余油饱和度。仍然不确定孔隙率机制在多大程度上,例如多相流动的计数器和共流性质,捕获机制和阶段的分布,乳液的形成和流动,传热机制影响非等温重力排放的过程主导的重油恢复。由于蒸汽加热下的相变,如何与扩散系数相互作用,润湿性的润湿性仍然是神秘的。本文,我们使用单个毛细管在非等温应用下的重力主导位移期间模拟扫掠区域中的基本体积。我们克确了TW在等温和非等温条件下,毛细管中的O相(空气油)和三相(空气油初始水饱和度)流离失所,改变空气喷射率和毛细血管性能。进行了测定的可视化实验分析:(1)油粘度,润湿性和扩散系数对等温和非等温位移的影响。(2)毛细血管中的相互作用和粘性(蒸汽注射率)力和润湿性的不同尺寸毛细血管, (3)毛细血管中的残留油饱和和相分布(主要是润湿和非润湿阶段的厚度)。基于实验观察的分析计算(测量的位移率)表明,在低毛细管数,温度不会对加工和原油的残留饱和度有显着影响。对于大于0.02的毛细管数,这是真正的毛细管数量。这个阈值钙LARY数量,油回收(以及因此残留的油饱和度)对毛细数字非常敏感,即注射速率,界面张力和润湿性,以及温度。

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