Impact of WAG Design on Calcite Scaling Risk in Coupled CO2-EOR and Storage Projects in Carbonate Reservoirs

H. Rodrigues, E. Mackay, D. Arnold
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引用次数: 3

Abstract

WAG (Water-Alternating-Gas) schemes have been applied in Brazilian carbonate reservoirs aiming to minimize residual oil saturation and gas flaring by recycling CO2 naturally being produced alongside hydrocarbon gas. However, applying WAG injection in highly reactive and heterogeneous carbonate rocks can potentially create severe scaling problems. This work develops a reactive transport simulation-based workflow to evaluate the impact of key WAG design parameters on oil recovery, scale deposition risk and CO2 storage to support multi-objective decision-making. Compositional simulations of WAG scenarios were performed as part of a sensitivity study followed by statistical analysis in order to quantify to what extent the outcomes of interest are sensitive to variations on four WAG design parameters: WAG ratio, CO2 concentration in the injection gas stream, injection rate and solvent slug-size. We established an Equation-of-State (EoS) using PVT data, a representative geochemical model and well constrains designed to control production of injected fluids. Scale risk was assessed by calcite changes around the wells, precipitation in well tubing and surface facilities, and water breakthrough. Results of this study showed that values of calcite rate constant (Ksp) and reactive surface area (A0) assigned in numerical simulations can impact relative calcite changes in the reservoir. Using reactive surface areas from BET studies of crushed rocks can lead to prediction of unrealistic amounts of calcite dissolution. Cases with lower values of (Ksp×A0) appeared to be more numerically stable and more consistent with dissolution/precipitation rates of silicate minerals. Simulation results also suggested that calcite dissolution close to injection wells and precipitation in production wells and surface facilities become more severe as CO2 concentration in injection gas and WAG ratio increases. Based on the design variables and reservoir conditions studied, the most to least crucial factors affecting oil recovery were: CO2 concentration in the injection gas stream, injection rate, WAG ratio and solvent slug-size. From a storage perspective, the impact of the design variables had considerably more impact, with the most influential factor being again CO2 concentration in the injection gas stream, followed by WAG ratio, injection rate and solvent slug-size. Optimization study results suggested that low WAG ratio values combined with low to intermediate gas slug sizes could result in superior profitability and CO2 storage outcomes for this pilot. Ultimately, we demonstrate the importance of integrating multiphase miscible displacement with geochemical reactions while modeling complex CO2-EOR in carbonate reservoirs and address how key design parameters impact our desired outcomes, knowledge that promotes a more robust decision-making framework.
碳酸盐岩油藏CO2-EOR - Storage耦合项目中WAG设计对方解石结垢风险的影响
WAG(水-气交替)方案已应用于巴西的碳酸盐岩储层,旨在通过回收碳氢化合物气中自然产生的二氧化碳来降低残余油饱和度和天然气燃烧。然而,在高活性和非均质碳酸盐岩中注入WAG可能会产生严重的结垢问题。这项工作开发了一个基于反应输运模拟的工作流程,以评估WAG关键设计参数对采收率、结垢风险和二氧化碳储存的影响,以支持多目标决策。WAG方案的成分模拟作为敏感性研究的一部分,随后进行了统计分析,以量化对四个WAG设计参数(WAG比、注入气流中的CO2浓度、注入速率和溶剂段塞大小)变化的敏感程度。我们利用PVT数据建立了状态方程(EoS),这是一种典型的地球化学模型,旨在控制注入流体的产量。通过井周围方解石的变化、油管和地面设施的沉淀以及水的突破来评估结垢风险。研究结果表明,数值模拟中方解石速率常数(Ksp)和反应表面积(A0)的取值会影响储层中方解石的相对变化。利用BET对碎石的反应表面积研究,可以预测出不切实际的方解石溶解度。(Ksp×A0)值较低的情况似乎在数值上更稳定,更符合硅酸盐矿物的溶解/沉淀速率。模拟结果还表明,随着注入气中CO2浓度和WAG比的增加,注入井附近方解石溶解和生产井及地面设施的沉淀更加严重。根据所研究的设计变量和储层条件,影响采收率的关键因素依次为:注入气流中的CO2浓度、注入速率、WAG比和溶剂段塞尺寸。从储气角度来看,设计变量的影响要大得多,影响最大的因素仍然是注入气流中的CO2浓度,其次是WAG比、注入速度和溶剂段塞尺寸。优化研究结果表明,低WAG比率值与低至中等气段塞尺寸相结合,可以为该试验带来卓越的盈利能力和二氧化碳储存效果。最后,我们证明了在模拟碳酸盐岩储层复杂的CO2-EOR时,将多相混相驱与地球化学反应相结合的重要性,并解决了关键设计参数如何影响我们的预期结果,这些知识促进了更强大的决策框架。
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