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A new comprehensive model to estimate the steam chamber expansion and recovery performance of entire SAGD process

机译:一种新的综合模型来估算整个SAGD过程的蒸汽室扩展和恢复性能

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Steam-Assisted gravity drainage (SAGD) technique has been successfully applied to unlock the oilsands resources in Canada. But to accurately estimate the steam chamber expansion and productivity of the entire lifetime of a SAGD well pair is still challenging. In this paper, a new comprehensive model is proposed encompassing the different stages of SAGD. Firstly, for the rising stage, based on the theory of volumetric displacement, an analytical model is developed for the rise speed and oil rate. Thereafter, based on Butler's theory, a 2D numerical approach is modelled for predicting the lateral spreading and confinement stage of steam chamber. Thus, combining the two different mathematical models, the steam chamber shape and recovery performance of a SAGD process can be calculated. The calculation results are also compared against 3D experimental results and field data to confirm the accuracy of this model. Then, a sensitivity analysis is performed to discuss the effects of operation parameters on steam chamber expansion and recovery performance of SAGD process. Results indicate that the calculated results can match the experiment results and field date very well. The calculated peak oil production rate causes a large error and the plateau time of SAGD process obviously is shortened if the pre-heating stage is neglected. A higher steam chamber pressure results in a narrower inverted triangle interface shape in the rising stage and a more concave-like interface in the sideways expansion stage. In addition, the oil rate increases with steam chamber pressure allowing for varying steam injection rate, whereas the increasing trend of ultimate recovery decreases with the steam chamber pressure increases, which indicates that a proper steam chamber pressure to be chosen can not only achieve a preferable ultimate recovery but also benefit for project economics.
机译:蒸汽辅助重力排水(SAGD)技术已成功应用于解锁加拿大的油脂资源。但要准确估计蒸汽室的蒸汽室膨胀和生产率的整个寿命,仍然具有挑战性。在本文中,提出了一种新的综合模型,包括SAGD的不同阶段。首先,对于上升阶段,基于体积位移理论,为上升速度和油速开发了分析模型。此后,基于Butler的理论,建模了一种2D数值方法,用于预测蒸汽室的横向扩散和限制阶段。因此,可以计算两个不同的数学模型,可以计算SAGD过程的蒸汽室形状和恢复性能。计算结果也与3D实验结果和现场数据进行比较,以确认该模型的准确性。然后,进行灵敏度分析以讨论操作参数对SAGD过程的蒸汽室扩展和恢复性能的影响。结果表明,计算结果可以很好地匹配实验结果和场日期。计算出的峰值油生产率导致大误差,并且如果忽略了预热阶段,显然会缩短SAGD过程的平台时间。较高的蒸汽室压力在上升阶段中的较窄的三角形界面形状和侧向膨胀阶段中的更凹入的界面。此外,油速仪随蒸汽室压力而增加,允许不同的蒸汽喷射速率,而最终回收的趋势随着蒸汽室压力的增加而降低,这表明要选择的适当蒸汽室压力不能达到优选的蒸汽室压力最终的恢复,但也有利于项目经济学。

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