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A NEW MODEL FOR STEAM CIRCULATION PREHEATING STAGE OF SAGD PRODUCTION

机译:SAGD生产蒸汽循环预热阶段的新模型

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The whole steam assisted gravity drainage (SAGD) production can be divided into two stages: the pre-heating stage and the production stage. Earlier researchers focused more on the production stage of SAGD, ignoring the importance of the pre-heating stage. Although several investigations have been carried out with the help of commercial reservoir simulator to probe the influences of reservoir properties, wellbore configurations and injection parameters, the simulation process takes too much computational time and the simulation results are greatly affected by the mesh size of the numerical model. In this paper, we build a new model to calculate the instantaneous heat loss rate and reservoir temperature distribution during the pre-heating stage. In the pre-heating stage, steam is injected through both the production well and injection well. Unlike SAGD production stage, heat is mainly transferred by thermal conduction. Therefore, the problem can be expressed as a transient conductive heat transfer equation with constant temperature inner boundary condition and well interference. First, Duhamel 's principle is used to convert the constant temperature inner boundary into variable heat flow rates inner boundary to deal with the well interference effects. By applying Laplace transformation to the basic function system, the analytical solutions for instantaneous heat loss rate and temperature distribution in Laplace space can be obtained. Then, with Stephest numerical inverse transformation method, the heat loss rate and temperature distribution can be calculated numerically. At last, we compare the results of our new model with that of two commercial simulators, and great agreement is observed. The quick and accurate solution for heat loss rate and temperature distribution can help people determine a proper steam injection rate and reasonable pre-heating days.
机译:整个蒸汽辅助重力排水(SAGD)生产可以分为两个阶段:预热阶段和生产阶段。早期的研究人员将更多的精力放在SAGD的生产阶段,而忽略了预热阶段的重要性。尽管已经借助商用油藏模拟器进行了一些研究来探究油藏性质,井眼配置和注入参数的影响,但是模拟过程花费了太多的计算时间,并且模拟结果受到数值网格尺寸的很大影响。模型。在本文中,我们建立了一个新模型来计算预热阶段的瞬时热量损失率和储层温度分布。在预热阶段,通过生产井和注入井注入蒸汽。与SAGD生产阶段不同,热量主要通过热传导传递。因此,该问题可以表示为具有恒定温度内边界条件和良好干涉的瞬态传导热传递方程。首先,利用杜哈默(Duhamel)原理将恒温内边界转换为热流量可变内边界,以处理井的干扰效应。通过将拉普拉斯变换应用于基本函数系统,可以获得拉普拉斯空间中瞬时热损失率和温度分布的解析解。然后,使用Stephest数值逆变换方法,可以数值计算热损失率和温度分布。最后,我们将新模型的结果与两个商业模拟器的结果进行了比较,并观察到了很好的一致性。快速,准确的热损失率和温度分布解决方案可以帮助人们确定合适的蒸汽注入率和合理的预热天数。

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