SAGD的下一步是什么?:低温室气体和高效第三次回收方案的评价

R. Pratama, T. Babadagli
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引用次数: 1

摘要

几十年来,注汽技术以不同形式被广泛应用于稠油和沥青的开采。尽管这种方法是一种经过验证的有效技术,但蒸汽产生过程本身可能会导致环境问题和低经济可行性。此外,世界上许多蒸汽项目,包括加拿大的SAGD项目,已经达到成熟阶段,尽管持续注蒸汽,但产量仍严重下降。不断上升的温室气体(GHG)排放是蒸汽注入应用的另一个重要缺点,导致全球排放增长率约为1.1%,加拿大每年增长0.8%。这要求我们寻找不同的技术,以有效和环保的方式消耗剩余的(条件)油。本文重点介绍了一种新技术的测试,该技术可以最大限度地减少蒸汽产生的温室气体排放,同时提高sagd后的最终采收率。本实验研究采用~50,000 cP重质原油和成品油(用于视觉模型)样品作为油相。可冷凝气体作为单一和多种组分(与甲烷混合)被包括作为潜在的溶剂,应用于已经蒸熟的模型。采用可视化Hele-Shaw模型和glass-bead-pack模型研究了多孔介质中的驱替机理、驱替效率和相分布。所有实验均在成熟SAGD油藏的现有温度下进行,以进一步评估稠油/蒸汽系统中可冷凝溶剂的相行为敏感性,以及现有凝结水与烃类溶剂不相容的情况。我们观察到,可冷凝溶剂可以通过动员残余油和提供良好的蒸汽室一致性来提高驱替效率/增加重油采收率超过30%。更重要的是,蒸汽的使用可以完全停止,能源效率可以提高到几乎100%。此外,在给定的sagd后温度下,确定了应用可冷凝溶剂的类型(和组成)。此外,还研究了可冷凝溶剂与油的回收潜力,以寻求一种高效的工艺。引入不同成分的可冷凝气体作为潜在的溶剂,用于回收重油和沥青,减少甚至完全切断SAGD后期的蒸汽注入,减少温室气体排放,提高能源效率。这些有价值的发现为低排放和高效的后期稠油开采提供了有益的建议,如sagd后的应用,以及其他类型的注汽工艺。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
What is Next for SAGD?: Evaluation of Low GHG and High-Efficiency Tertiary Recovery Options
Steam injection has been widely applied in different forms to recover heavy-oil and bitumen for decades. Even though this method is a proven and effective technology, the steam generation process itself may lead to environmental issues and low economic viability. Also, many worldwide steam projects, including SAGD projects in Canada, have already reached their maturity with a severe decline in production despite continuous steam injection. Escalating greenhouse gas (GHG) emissions is another crucial downside of steam injection application, contributing to an emission growth rate of about 1.1% worldwide and 0.8% annually in Canada. This requires us to search for different techniques to deplete the remaining (conditioned) oil efficiently and in an eco-friendly manner. This paper focuses on the testing of a new technique to minimize GHG emissions resulting from steam generation while enhancing the ultimate recovery post-SAGD. ~50,000 cP heavy crude and processed oil (for visual models) samples were used as an oleic phase in this experimental research. Condensable gases as single and multiple (mixed with methane) components were included as potential solvents to be applied to the already steamed models. Visual Hele-Shaw and glass-bead-pack models were employed to investigate the displacement mechanism, displacement efficiency, and phase distribution in porous media. All experiments were performed at currently existing temperatures in matured SAGD reservoirs to further evaluate the sensitivity of phase behavior of condensable solvents in a heavy-oil/steam system, as well as existing condensed water of which is not compatible with hydrocarbon solvents. We observed that condensable solvents could improve the displacement efficiency/incremental heavy-oil recovery over 30% by mobilizing residual oil and providing favorable conformance to the steam chamber. More importantly, the steam usage was able to be entirely cut off, and the energy efficiency could be ramped up to almost 100%. Additionally, the type (and composition) for applying condensable solvents were determined at a given post-SAGD temperature. Also, the retrieval potential of the condensable solvent with oil was investigated for an efficient process. Condensable gases with different compositions were introduced as potential solvents to recuperate heavy-oil and bitumen recovery and reduce or even completely cut off the steam injection at late-stage SAGD, diminishing its GHG emission and improving energy efficiency. Valuable findings present beneficial recommendations for low-emission and high-efficiency late-stage heavy-oil recovery as post-SAGD applications, as well as other types of steam injection processes.
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