CO2-WAG水-气交替注入条件下碳酸盐岩储层压垢长期治理策略优化

V. Azari, H. Rodrigues, Alina Suieshova, O. Vazquez, E. Mackay
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引用次数: 2

摘要

本研究的目的是为巴西盐下碳酸盐岩类似油藏设计一系列挤压处理方法,以最大限度地降低阻垢策略的成本。在储层中进行CO2-WAG(水-气交替)注入以提高采收率,但也可能增加结垢的风险。在CO2注入过程中,由于pH值的降低,CaCO3的溶解可能会导致生产系统中碳酸钙沉淀的风险增加。这些沉积物可能出现在从生产井底到地面设施的任何位置。挤压处理被认为是防止CaCO3沉积在储层中最有效的技术。因此,四分之一5点模型的最佳WAG设计,即从油藏优化过程中确定的最大净现值(NPV)和二氧化碳储存量,被认为是优化挤压处理策略的基础,并将结果与基本情况水驱情景的结果进行了比较。采用梯度下降算法确定了总生命周期的最佳挤压寿命。挤压策略优化的主要目标是确定处理的频率和寿命,从而在井的整个生命周期内以尽可能低的成本实现水保护。WAG案例的模拟结果表明,在生产井见水后的最后10年的生产中,尺度窗口延长了。考虑了不同的挤压目标寿命,从50万桶到600万桶产出水,以优化其使用寿命。确定了最佳挤压寿命为200万桶保护水,并将其用于后续的挤压处理。根据产水速率和饱和度随时间的变化,计算出最佳的化学剂部署方案。优化结果表明,在WAG情况下,为了保护生产井,需要进行7次挤压处理,而在水驱情况下,由于生产窗口的含水率较高,需要进行10次挤压处理。该方法的新颖之处在于能够针对长期生产周期优化一系列挤压处理设计。它为油田的前端工程设计(FEED)阶段增加了有价值的信息,规模控制可能对油田的经济可行性产生重大影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Long-term Strategy Optimization of Scale Squeeze Treatment in a Carbonate Reservoir Under CO2-WAG Water-Alternating-Gas Injection
The objective of this study is to design a series of squeeze treatments for 20 years of production of a Brazilian pre-salt carbonate reservoir analogue, minimizing the cost of scale inhibition strategy. CO2-WAG (Water-Alternating-Gas) injection is implemented in the reservoir to increase oil recovery, but it may also increase the risk of scale deposition. Dissolution of CaCO3 as a consequence of pH decrease during the CO2 injection may result in a higher risk of calcium carbonate precipitation in the production system. The deposits may occur at any location from production bottom-hole to surface facilities. Squeeze treatment is thought to be the most efficient technique to prevent CaCO3 deposition in this reservoir. Therefore, the optimum WAG design for a quarter 5-spot model, with the maximum Net Present Value (NPV) and CO2 storage volume identified from a reservoir optimization process, was considered as the basis for optimizing the squeeze treatment strategy, and the results were compared with those for a base-case waterflooding scenario. Gradient Descent algorithm was used to identify the optimum squeeze lifetime duration for the total lifecycle. The main objective of squeeze strategy optimization is to identify the frequency and lifetime of treatments, resulting in the lowest possible expenditure to achieve water protection over the well's lifecycle. The simulation results for the WAG case showed that the scale window elongates over the last 10 years of production after water breakthrough in the production well. Different squeeze target lifetimes, ranging from 0.5 to 6 million bbl of produced water were considered to optimize the lifetime duration. The optimum squeeze lifetime was identified as being 2 million bbl of protected water, which was implemented for the subsequent squeeze treatments. Based on the water production rate and saturation ratio over time, the optimum chemical deployment plan was calculated. The optimization results showed that seven squeeze treatments were needed to protect the production well in the WAG scenario, while ten treatments were necessary in the waterflooding case, due to the higher water rate in the production window. The novelty of this approach is the ability to optimize a series of squeeze treatment designs for a long-term production period. It adds valuable information at the Front-End Engineering and Design (FEED) stage in a field, where scale control may have a significant impact on the field's economic viability.
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