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A Condensation Temperature Model for Evaluating Early-period SAGD Performance

机译:用于评估早期SAGD性能的冷凝温度模型

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This paper proposes a new methodology using condensation model to evaluate the early-period SAGD by interpreting the temperature falloff data in injector or producer obtained from fiber optics or thermal couples after the wells are shut-in. Based on the non-condensation model proposed before, the condensation model also assumes a circular hot-zone shape since in the early stage of SAGD operation, and characterize the system as composed of a steam-zone of steam temperature, a cold-zone of reservoir temperature and a transition-zone in between as the initial temperature distribution. Besides, the condensation model incorporates the effect of steam condensation on the condensation-front. The movement of steam condensation-front is calculated to account for the steam-zone shrinkage. Sensitivity analysis over this models indicates that the sizes of steam- zone, transition-zone and the observing location directly affect the temperature behavior at observation point. Synthetic case study shows that the temperature falloffs from condensation model and from simulation are in good agreement and suggests that condensation model can be used to estimate the chamber size at the early stage of SAGD. As is known, it is important to obtain an even steam chamber distribution along the horizontal wellbore to shorten the ramp-up time so that maximized economics can be achieved. In reality, the reservoir heterogeneity, the wellbore undulation and the operation condition make the steam chamber conformance impossible. Because of the ready-to-use temperature data and the semi-analytic solution, the condensation model proposed in this paper can provide quick and reliable estimation of the steam chamber size to help the engineers to monitor and optimize the chamber development thereafter.
机译:本文提出了一种利用冷凝模型的新方法来评估早期SAGD,通过解释从光纤或井中的热耦合获得的喷射器或生产者中的温度降低数据来评估早期的SAGD。基于之前提出的非冷凝模型,冷凝模型还假设圆形热区形状,因为在SAGD操作的早期阶段,并根据蒸汽温度的蒸汽区,一个冷区表征系统的系统。作为初始温度分布的储层温度和过渡区。此外,冷凝模型包括蒸汽冷凝对凝结前的蒸汽凝结的影响。计算蒸汽冷凝前的运动,以考虑蒸汽区收缩。对该模型的敏感性分析表明蒸汽区,过渡区和观测位置的尺寸直接影响观察点的温度行为。综合性案例研究表明,来自冷凝模型和仿真的温度差异是良好的一致性,并表明冷凝模型可用于估计SAGD早期腔室的腔室尺寸。众所周知,重要的是沿水平井筒获得偶数蒸汽室分布,以缩短斜面时间,以便可以实现最大化的经济学。实际上,储层异质性,井眼波动和操作条件使蒸汽室一致性不可能。由于即用的温度数据和半分析解决方案,本文提出的冷凝模型可以提供快速可靠地估计蒸汽室尺寸,以帮助工程师在此后监测和优化腔室开发。

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