粘性反应性油的碱聚合物驱

R. Hincapie, Ante Borovina, T. Clemens, Markus Lüftenegger, E. Hoffmann, J. Wegner, Louis-Georgian Oprescu, Muhammad Tahir
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引用次数: 0

摘要

水驱稠油由于流度比高,指征粘稠,导致驱替效率不高。聚合物注入通过减少粘指和提高波及效率来提高采收率。我们展示了碱聚合物(AP)驱油如何显著提高罗马尼亚某油田反应性粘稠油的产量。利用IFT测量、岩心驱油和微观模型实验来了解和优化导致原油采收率增加的物理化学过程。在不同的碱和AP浓度下进行了广泛的IFT测量。此外,还进行了相行为试验。此外,微模型实验用于阐明在孔隙尺度上的影响,并作为筛选化学品使用的工具。单相和两相岩心驱替实验有助于确定岩心尺度上的驱替效率。注入不同顺序和浓度的碱和聚合物,以降低成本,最大限度地提高反应性粘性油的采收率。实验结果表明,油碱溶液界面皂化(110 μmol/g皂化酸)能有效降低IFT。随着时间的推移,由于生成的肥皂从界面扩散,IFT增加。相实验证实,乳剂在初始阶段形成。微观模型表明,注水时注入聚合物或碱只能带来有限的产油量增量。注碱时,由于粘指边缘处的原位皂化作用,油被乳化。水驱后注入AP非常有效。黏性手指边缘的乳化油被黏性流体有效地拖拽,大大提高了采收率。岩心洪水证实了微观模型的发现。此外,还考察了二价阳离子对聚合物浓度选择的影响。水软化导致AP段塞的粘度明显高于未软化的盐水。降低聚合物浓度以获得与含二价阳离子的聚合物溶液相同的粘度,驱替效率相似。因此,对于在注入聚合物之后计划注入AP的现场条件,可以实现显著的成本节约。结果表明,碱溶液导致反应性粘稠油初始IFT较低,这是由于油碱溶液界面处由于扩散而产生的肥皂随着时间的推移而增加。在反应性粘稠油中注入碱溶液不能有效降低剩余油饱和度,少量的油在粘稠指的边缘被动员。反应性粘稠油的AP驱油显著提高了原油的采收率。其原因是被动员的油与粘性流体的有效拖拽,以及随之而来的额外油暴露于碱溶液中。此外,通过调整聚合物浓度以适应含有软化水的AP段塞,可以大大提高AP驱油项目的经济性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Alkali Polymer Flooding of Viscous Reactive Oil
Displacing viscous oil by water leads to poor displacement efficiency owing to the high mobility ratio and viscous fingering. Polymer injection increases oil recovery by reducing viscous fingering and improving sweep efficiency. We are showing how Alkali-Polymer (AP) flooding is substantially improving production of reactive viscous oil from a Romanian oil field. IFT measurements, coreflood and micro-model experiments were used to understand and optimize the physico-chemical processes leading to incremental oil recovery. Extensive IFT measurements were performed at different alkali and AP concentrations. In addition, phase behavior tests were done. Furthermore, micro-model experiments were used to elucidate effects at the pore-scale and as screening tool for which chemicals to use. Single and two-phase coreflood experiments helped defining the displacement efficiency on a core scale. Various sequences and concentrations of alkali and polymers were injected to reduce costs and maximize incremental recovery of the reactive viscous oil. IFT measurements showed that saponification (110 μmol/g saponifiable acids) at the oil-alkali solution interface is very effectively reducing the IFT. With time, the IFT is increasing owing to diffusion of the generated soaps away from the interface. Phase experiments confirmed that emulsions are formed initially. Micro-models revealed that injection of polymers or alkali only leads to limited incremental oil recovery over waterflooding. For alkali injection, oil is emulsified due to in-situ saponification at the edges of viscous fingers. AP injection after waterflooding is very effective. The emulsified oil at the edges of the viscous fingers is effectively dragged by the viscous fluid substantially increasing recovery. Corefloods confirmed the findings of the micromodels. In addition, the effect of di-valent cations for the selection of the polymer concentration was investigated. Water softening leads to significantly higher viscosity of the AP slug than non-softened brine. Reducing the polymer concentration to obtain the same viscosity as the polymer solution containing divalent cations resulted in similar displacement efficiency. Hence, significant cost savings can be realized for the field conditions, for which AP injection is planned after polymer injection. The results show that alkali solutions lead to initial low IFT of reactive viscous oil owing to soap generation at the oil-alkali solution interface increasing with time due to diffusion. Injecting alkali solutions into reactive viscous oil is not effective to reduce remaining oil saturation, a limited amount of oil is mobilized at the edges of viscous fingers. AP flooding of reactive viscous oil is substantially increasing incremental oil recovery. The reason is the effective dragging of the mobilized oil with the viscous fluid and associated exposure of additional oil to the alkali solutions. Furthermore, the economics of AP flooding projects can be substantially improved by adjusting the polymer concentration to the AP slug containing softened water.
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