泡沫水泥浆在11900英尺水深超深水井成功应用(创世界纪录)

Degaul Nana Nzoutchoua, C. Johnson, Jean Yengoua Tenin, Matthieu Lonca, Edevaldo Andrade e Sousa, Jamel Zghal
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引用次数: 0

摘要

泡沫水泥成功应用于水深11,900英尺的超深水井的无隔水管段。选择泡沫水泥是为了最大限度地降低运营成本,并在短时间内灵活调整泥浆密度。海水柱对环空施加了5319.1 psi的静水压力。因此,氮(N2)密度不能再被忽视。本文介绍了在作业准备、操作考虑和作业后评估中进行的模拟。铅浆的密度为1.25 SG, 48小时内抗压强度至少为300 psi。考虑到当前新冠疫情限制下外包资源的成本和挑战,泡沫水泥体系比化学或颗粒扩展水泥或混合体系更受青睐。泡沫水泥浆体系的氮气比为700立方英尺/桶。在基础泥浆泵送速率为5桶/分钟的情况下,所需的氮气泵送速率为3500 scf/分钟,大于单个氮气泵(3000 scf/分钟)的能力。由于钻井平台空间无法容纳3台N2泵,因此需要一台作为备用泵;因此,最终的方案是同时使用两台氮气泵。安装了两条平行的泡沫泥浆处理管线,以降低单线中的流体速度。所有化验均在本地进行。泡沫浆中使用的添加剂是环保的。在固井作业过程中,使用了专有的过程控制系统,可以自动同步氮气泵和泡沫泵的速率与基础泥浆速率。固井工作人员共有11人,其中包括2名客户代表。整个泵送作业在10小时内完成。连续混合1016.2桶的基浆,并以13.35磅/加仑(1.60 SG)的密度泵送。所得泡沫浆体积为1387.0桶,平均泡沫质量为27.8%,泡沫浆密度为10.5磅/加仑(1.26 SG)。在泵送作业期间,共消耗了119公吨G类水泥和30,711 L氮气。铅浆之后是603.9桶15.86磅/加仑(1.90 SG)的G级水泥尾浆和349.7桶海水进行驱替。最终的表面压力为594.6 psi。铅浆到达海底,浮鞋检查是积极的。没有观察到套管下沉。在这种极端条件下使用泡沫水泥浆证明了其坚固性和可靠性。通过形式化和系统化的风险评估,团队能够识别并实施导致突出结果的缓解措施。该应用还证实,当涉及高静水压力时,N2密度不应被忽视。
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Successful Application of Foamed Cement Slurry in an Ultradeepwater Well of 11,900-ft Water Depth (Claiming World Record)
Foamed cement was successfully used in the riserless section of an ultradeepwater well located in 11,900ft water depth. Foamed cement was selected to minimize operating costs and provide flexibility to adjust slurry density on a short notice. The seawater column exerted 5,319.1-psi hydrostatic pressure on the annulus. Consequently, nitrogen (N2) density could no longer be neglected. This paper presents simulations performed in preparation for the job, operational considerations, and post-job evaluation. The lead slurry needed a density of 1.25 SG and develops a compressive strength of at least 300 psi within 48 hr. Considering the cost and challenges associated with outsourcing resources under current Covid-19 pandemic restrictions, the foamed cement system was preferred over chemical- or particle- extended cement or blend systems. The N2 ratio for the foamed cement slurry system was 700 scf/bbl. With a base slurry pumping rate of 5 bbl/min, the required N2 pumping rate was 3,500 scf/min, which was greater than the capability of a single N2 pump (3,000-scf/min rate). Because the rig deck space could not accommodate three N2 pumps, one pump would serve as backup; thus, the final plan consisted of using two N2 pumps simultaneously. Two parallel foamed slurry treating lines were rigged up to reduce the fluid velocity in a single line. All laboratory testing was conducted locally. Additives used in the foamed slurry were environmentally friendly. A proprietary process-control system was used during the cementing operation and automatically synchronized the N2 pumps and foam pump rates with the base slurry rate. The cementing crew consisted of 11 individuals, including 2 client representatives. The entire pumping operation was completed in 10 hr. A total base slurry volume of 1016.2 bbl was continuously mixed and pumped at the density of 13.35 lbm/gal (1.60 SG). The resulting foamed slurry volume was 1387.0 bbl with an average foam quality of 27.8% and foamed slurry density of 10.5 lbm/gal (1.26 SG). A total of 119 metric tonne of class G cement and 30,711 L of N2 were consumed during the pumping operation. The lead slurry was followed by 603.9 bbl of 15.86 lbm/gal (1.90 SG) class G cement tail slurry and 349.7 bbl of seawater for displacement. The final surface pressure was 594.6 psi. The lead slurry reached the seabed and the float shoe check was positive. No casing subsidence was observed. Using foamed cement slurry in such extreme conditions demonstrated its robustness and reliability. Through formalized and methodical risk assessment, the team was able to identify and implement mitigating measures that led to an outstanding result. This application also confirmed that N2 density should not be neglected when high-hydrostatic pressure is involved.
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