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Systematic Calcium Carbonate Scale Risk Evaluation from Downhole toTopside Flowline

机译:系统的碳酸钙尺度从井下流动线上的风险评估

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The formation of CaCO3 mineral scale is a persistent flow assurance problem in the oil and gas industry. Itdeposits at various locations with different levels from reservoir to topside flowline. It could restrict wellintervention, block flowline and reduce production. To make an effective mitigation strategy, it is essentialto understand the location and severity of scaling, and the performance of scale inhibitor under specificoperation conditions. In the work reported herein, the dynamic scale loop tests were performed to evaluate the severity of scaledeposition at different locations from the reservoir to transport flowline in the absence and in the presenceof scale inhibitors under dynamic conditions. The tests are carried out at various temperatures (20-130°C)and pH (6.0-8.3), which are major factors contributing to calcium carbonate formation and representativeof the operating conditions at different locations from reservoir to topside flowline. The results showed low calcium carbonate risk from reservoir to wellhead under tested conditions.Although the high reservoir temperature favors calcium carbonate formation in downhole, the low pHreduces the risk of calcium carbonate formation at downhole conditions. Harsher calcium carbonatedeposition is evaluated at the conditions of phase separator/degasser units due to the higher pH of producedwater after released CO2 from fluid. Calcium carbonate scale can also deposit in transport flowline,especially at high temperature during summer in the desert area, along with higher pH of the produced water.Calcium carbonate scale prevention and mitigation treatments are required to inhibit scale deposition. Thetested phosphonate scale inhibitor provides low dose rate to effectively inhibit calcium carbonate formationat high temperature. The corrosion inhibitor could have a negative impact on the performance of scaleinhibitor, and this must be considered when designing the scale inhibitor treatment. This paper gives a comprehensive study of scaling risk evaluation from downhole to topside flowline inthe absence and in the presence of scale inhibitor. It contributes to the understanding of calcium carbonateformation and inhibition in the whole production system and recommends effective scale mitigationstrategies.
机译:CaCO3矿物规模的形成是石油和天然气工业中持续的流动保证问题。 itdeposits在各个地点,从水库到顶部流线的不同水平。它可能会限制完全,阻止流线并减少生产。为了提出有效的缓解策略,必须了解缩放的位置和严重程度,以及在特定操作条件下的规模抑制剂的性能。在本文报道的工作中,进行动态刻度环试验以评估来自储库的不同位置处的分级沉积的严重程度,以在动态条件下在不存在的情况下和在抑制剂的情况下运输流动线。该试验在各种温度(20-130℃)和pH(6.0-8.3)处进行,这是碳酸钙形成的主要因素,以及从水库到顶部流线的不同地点的操作条件的主要因素。结果表明,在经过测试的条件下,从储层到井口的碳酸钙风险低。虽然高层储层温度较井下碳酸钙形成,但低分化井下条件下碳酸钙形成的风险。在从流体释放的CO 2之后,在相分离器/脱气机单元的条件下评价Harsher钙碳酸钙沉积。碳酸钙尺度还可以存放在运输流线中,特别是在沙漠区域的夏季期间的高温下,以及所产生的水的pH值。需要碳酸盐量定预防和减缓处理来抑制尺度沉积。鉴定的膦酸盐量表抑制剂提供低剂量率,以有效抑制碳酸钙形成高温。腐蚀抑制剂可能对展示抑制性的性能产生负面影响,并且在设计规模抑制剂治疗时必须考虑这一点。本文综合研究了从井下扩大风险评估,以缺席并在规模抑制剂存在下。它有助于了解整个生产系统中碳酸钙形成和抑制,并推荐有效的缓解策略。

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