在低浓度二价离子油藏中实现无水软化的ASP

Samya Farsi, R. Bouwmeester, M. Brewer, J. Southwick, Dawood Mahruqi, V. Karpan, Diederik van Batenburg, Ian Carpenter, Sam Wilson
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引用次数: 2

摘要

事实证明,碱性表面活性剂聚合物驱是一种有效的水驱剩余油回收方法。然而,有几个复杂的问题限制了ASP的广泛实现。源水需要进行软化处理,以避免碱与二价阳离子混合时形成水垢而导致的注入性问题。即使使用软化水作为基础水,由于在现场混合了不同成分的水,在生产井中仍可能存在结垢问题。据报道,在某些情况下,通过在生产侧施加阻垢剂或在注入侧施加阻垢剂来控制结垢是成功的。当碳酸钠用作碱时,碳酸盐结垢问题最为严重。即使使用除碳酸盐以外的碱,碳酸盐垢仍然是一个问题,因为几乎存在于任何地层水中的碳酸氢盐都会在高pH值下转化为碳酸盐,并随后与存在的二价离子一起沉淀。乙醇胺被认为是一种有效的碱,可用于高TAN油藏,用于回注采出水中二价离子浓度相对较低的油藏。如果可以避免采出水的软化,ASP的实施将大大简化。研究结果包括确定结垢趋势、相容性测试、管堵塞测试以及添加和不添加阻垢剂的岩心注水,并将与现场实施的影响一起提出。在注入侧添加阻垢剂的另一个潜在优势是,阻垢剂会随待抑制的组分一起移动。这可能消除了在生产端采取规模控制措施的需要。
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Implementing ASP Without Water Softening in Reservoirs With Low Concentrations of Divalent Ions
Alkaline Surfactant Polymer (ASP) flooding has proven to be an effective method to recover residual oil after waterflood. Yet, there are several complications that limit a wide implementation of ASP. The source water needs to be softened to avoid injectivity issues due to scale formation when alkali is mixed with divalent cations. Even when softened water is used as base water, scaling can still be an issue in producing wells due to mixing of waters with different compositions in-situ. Scale control by means of scale inhibitor squeezes on the production side or scale inhibitor on the injection side have been reported to be successful for some cases. Carbonate scaling issues are most severe when sodium carbonate is used as alkali. Even if alkalis other than carbonate are used, carbonate scale remains an issue as bicarbonate that is present in almost any formation water, will convert to carbonate at high pH and will subsequently precipitate with the divalent ions present. Ethanolamine has been proposed as an effective alkali in ASP application with high TAN oils for reservoirs that contain relatively low concentrations of divalent ions in their produced water that is reinjected. ASP implementation could significantly be simplified if softening of the produced water could be avoided. Results of a study that involved determination of scaling tendencies, compatibility testing, tube blocking tests, and core floods with and without the addition of scale inhibitor will be presented together with implications for field implementation. A potential additional advantage of adding scale inhibitor on the injection side is that the scale inhibitor travels with the components to be inhibited. This might eliminate the need for scale control measures at the production side.
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