加速恢复

重油

蒸汽辅助重力泄油 (SAGD) 技术在数值模拟、流入控制技术、光纤监测和实时生产优化等方面的改进推动下,持续快速发展。

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蒸汽辅助重力泄油(SAGD)技术持续快速发展,这得益于数值模拟、进水控制技术、光纤监测和实时生产优化等方面的进步。目前,行业关注的重点是后期性能优化,特别是泄压阶段的气体控制以及通过在泄压前后实施进水控制装置(ICD)来提高蒸汽的稳定性。

在SAGD(蒸汽辅助重力泄油)装置的后期运行中,气体管理和合规性控制成为主要的优化挑战。一个明显的趋势是,通过策略性地布置ICD(集成控制装置)来改善流入分布,并减少泄压阶段的过量产气。

在SPE 230259号论文中,探讨了在接近蒸汽闪蒸条件下模拟ICD性能的关键挑战。成功运行需要深入了解ICD在高温热力条件下的行为,因为在高温热力条件下,阻塞加剧和高于预期的流动阻力可能会对安装后的油井产能产生负面影响。该研究表明,平衡的流入分布对于SAGD中ICD的有效运行至关重要。理想情况下,ICD应限制高温、易产生蒸汽区域的流动,同时允许从温度较低、富含液体的层段进行生产。

如果ICD引起的压降显著高于周围液池的压降,则流入会受到过度限制,导致整体生产率下降。相反,如果ICD压降过低,则该装置如同一个开放式端口,无法提供有效的流量控制。作为一项实用的设计指南,建议最大压降比约为0.3,以防止过度阻塞,同时保持有效的流量控制。

SPE 230265号论文评估了自主流入控制阀(AICV)在泄压阶段阻断天然气生产的潜力。在SAGD(蒸汽辅助重力泄油)装置的后期运行阶段,运营商通常会过渡到泄压阶段,将不可凝结气体(通常为天然气)注入蒸汽室,以维持压力并在蒸汽室顶部提供隔热。蒸汽室聚结后,加密井和生产井的天然气产量可能会大幅增加,导致与天然气处理、压缩和回注相关的运营成本居高不下。因此,将天然气保留在储层内是关键目标。

AICV(气冷式通风阀)已成功应用于北海等海上环境中,用于降低常规(非热式)作业中的天然气产量。人们越来越关注将这项技术应用于SAGD(蒸汽辅助重力泄油)工艺,以防止泄压过程中产生天然气。然而,目前仍存在一个重大挑战:大多数AICV是为非热式应用设计的,需要进行改造才能承受SAGD的作业条件,因为SAGD作业中的温度通常超过200℃。

最后,SPE 230260号论文重点研究了如何防止气体进入电潜泵(ESP)。气锁现象显著缩短了ESP的运行寿命,并导致SAGD作业中生产不稳定。对无流量事件的分析表明,气油比被低估了约500%,凸显了气体干扰的严重性。虽然倒置式导流罩已被广泛用于减少气体进入ESP,但本研究首次在SAGD应用中引入了上串联式气体分离器(UT-GS)作为一种替代的气体处理方案。现场实例表明,与更换ESP之前相比,UT-GS提高了生产稳定性并实现了更高的产量。

本期(2026年4月)论文摘要

SPE 230259 蒸汽敏感流量控制装置在 Surmont SAGD 项目中实施, 作者为 Matthew French, SPE 和 Alex Colleaux, SPE(康菲石油公司)、Marco Melo Llanos, SPE(贝克休斯公司)等。

SPE 230265 SAGD 泄压阶段性能通过自主流入控制阀优化, 作者 Maria A. Roa、SPE、Ismarullizam M. Ismail、SPE 和 Einar Gisholt、InflowControl AS 等。

SPE 230260 动态气体分离技术集成到SAGD中以提高ESP性能, 作者:Shadi Gabasa(SPE,SLB)和Rejish Joseph(SPE,Suncor Energy)。

推荐延伸阅读

SPE 230272 消除热井表面套管排气:水泥特性至关重要, 作者:ZR Lin、Sanjel Energy Services 等。

Sahar Ghannadi, SPE(美国石油工程师协会会员),现任Ashaw Energy总裁,负责领导蒸汽辅助重力泄油(SAGD)和地热井的设计与优化项目。她拥有阿尔伯塔大学石油工程博士学位。Ghannadi的工作重点是开发先进软件,将油井和油藏数据整合到一个统一的平台,供运营使用。在担任现职之前,她曾在BP、Suncor Energy和E2E Energy担任技术职位。Ghannadi撰写并发表了30余篇关于SAGD作业各个方面的技术论文,并且是SPE的活跃成员。

原文链接/JPT
Enhanced recovery

Heavy Oil

Steam-assisted gravity drainage (SAGD) technology continues to advance rapidly, driven by improvements in numerical simulation, inflow-control technologies, fiber-optic monitoring, and real-time production optimization.

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Steam-assisted gravity drainage (SAGD) technology continues to advance rapidly, driven by improvements in numerical simulation, inflow-control technologies, fiber-optic monitoring, and real-time production optimization. A major industry focus today is on late-life performance optimization, particularly gas control during the blowdown phase and improved steam conformance through the implementation of inflow control devices (ICDs), both pre- and post‑blowdown.

In late-life SAGD operations, gas management and conformance control become the primary optimization challenges. One clear trend is the strategic placement of ICDs to improve inflow distribution and mitigate excessive gas production during the blowdown phase.

In paper SPE 230259, the critical challenge of modeling ICD performance at temperatures approaching steam-flashing conditions is discussed. Successful operation requires a thorough understanding of ICD behavior under high-temperature thermal conditions, where increased choking and higher-than-expected flow resistance may affect well productivity negatively following installation. The study demonstrates that balanced inflow distribution is essential for effective ICD performance in SAGD. Ideally, ICDs should restrict flow in high-temperature, steam-prone zones while allowing production from cooler, liquid-rich intervals.

If the ICD-induced pressure drop significantly exceeds that of the surrounding liquid pool, inflow becomes overly restricted, resulting in reduced overall productivity. Conversely, if the ICD pressure drop is too low, the device behaves like an open port and fails to provide meaningful flow control. As a practical design guideline, a maximum pressure drop ratio of approximately 0.3 is recommended to prevent excessive choking while maintaining effective conformance control.

Paper SPE 230265 evaluates the potential of autonomous inflow-control valves (AICVs) to block gas production during the blowdown phase. In late-life SAGD, operators typically transition to blowdown, injecting noncondensable gas—commonly natural gas—into the steam chamber to maintain pressure and provide thermal insulation at the chamber crest. After steam-chamber coalescence, gas production from infill wells and producers can increase substantially, leading to high operational costs associated with gas handling, compression, and reinjection. Retaining gas within the reservoir, therefore, is a key objective.

AICVs have been successfully implemented in offshore environments such as the North Sea to reduce gas cut in conventional (nonthermal) operations. There is growing interest in adapting this technology for SAGD to prevent gas production during blowdown. A significant challenge remains, however; most AICVs are designed for nonthermal applications and require modification to withstand SAGD conditions, where temperatures commonly exceed 200°C.

Finally, paper SPE 230260 focuses on preventing gas entry into the electric submersible pump (ESP). Gas locking has reduced ESP run life significantly and caused unstable production in SAGD operations. Analysis of no-flow events revealed that gas/oil ratios were underestimated by approximately 500%, highlighting the severity of gas interference. While inverted shrouds have been deployed widely to reduce gas intake into ESPs, this study introduces, for the first time in SAGD applications, an upper tandem gas separator (UT-GS) as an alternative gas-handling solution. Field examples demonstrate that the UT-GS improved production stability and delivered higher production rates compared with performance before ESP replacement.

Summarized Papers in This April 2026 Issue

SPE 230259 Steam-Sensitive Flow-Control Device Implemented in Surmont SAGD Project by Matthew French, SPE, and Alex Colleaux, SPE, ConocoPhillips, and Marco Melo Llanos, SPE, Baker Hughes, et al.

SPE 230265 SAGD Performance at Blowdown Phase Optimized With Autonomous Inflow Control Valves by Maria A. Roa, SPE, Ismarullizam M. Ismail, SPE, and Einar Gisholt, SPE, InflowControl AS, et al.

SPE 230260 Dynamic Gas Separation Integrated Into SAGD for Improved ESP Performance by Shadi Gabasa, SPE, SLB, and Rejish Joseph, SPE, Suncor Energy

Recommended Additional Reading

SPE 230272 Toward Elimination of Surface Casing Vent Flow in Thermal Wells: Cement Properties That Matter by Z.R. Lin, Sanjel Energy Services, et al.

Sahar Ghannadi, SPE, is president of Ashaw Energy, where she leads initiatives in the design and optimization of steam-assisted gravity drainage (SAGD) and geothermal wells. She holds a PhD degree in petroleum engineering from the University of Alberta. A key focus of Ghannadi’s work is the development of advanced software to integrate well and reservoir data into a single platform for operational use. Before taking her current role, she held technical positions at BP, Suncor Energy, and E2E Energy. Ghannadi has authored and presented more than 30 technical papers on various aspects of SAGD operations and is an active member of SPE.