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Steam Alternating Solvent Process

机译:蒸汽交替溶剂法

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摘要

A new heavy-oil-recovery process, the steam alternating solvent (SAS) process, is proposed and studied using numerical simulation. The process is intended to combine the advantages of the steam-assisted gravity drainage (SAGD) and vapor-extraction (va-pex) processes to minimize the energy input per unit oil recovered. The SAS process involves injecting steam and solvent alternately, and the basic well configurations are the same as those in the SAGD process. Field-scale simulations were conducted to assess the SAS process performance under typical Cold Lake, Alberta, reservoir conditions. These results suggested that the oil-production rate of an SAS process could be higher than that of a SAGD process, while the energy input was 18% less than that of a SAGD process. By varying the length of the steam- and solvent-injection periods in a cycle, a different set of steam/oil and solvent/oil ratios may be obtained because the temperature profiles and solvent-concentration distributions in the vapor chamber can be affected by the injection pattern. The process therefore can be optimized for a specific reservoir under certain economic conditions.
机译:提出了一种新的稠油回收工艺,即蒸汽交替溶剂(SAS)工艺,并通过数值模拟对其进行了研究。该工艺旨在结合蒸汽辅助重力排水(SAGD)和蒸汽萃取(va-pex)工艺的优势,以最大程度地减少每单位采油量的能量输入。 SAS工艺涉及交替注入蒸汽和溶剂,其基本井配置与SAGD工艺中的井配置相同。进行了现场规模的仿真,以评估典型的艾伯塔省冷湖水库条件下的SAS工艺性能。这些结果表明,SAS工艺的产油率可能高于SAGD工艺的产油率,而能量输入却比SAGD工艺的产油量低18%。通过改变一个周期中蒸汽和溶剂注入周期的长度,可以获得不同组的蒸汽/油和溶剂/油比,因为蒸汽室中的温度曲线和溶剂浓度分布会受到温度的影响。注射模式。因此,可以在某些经济条件下针对特定油藏优化该过程。

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