重油生产蒸汽辅助重力泄油的新型压力控制方案

IF 1.6 4区 工程技术 Q3 ENGINEERING, CHEMICAL
Xinfeng Jia, Kangkang Wang, Jian Xiong, Binhai Jiao, Dong Liu, Zhangxin Chen, Liangliang Jiang, Zhanxi Pang
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引用次数: 0

摘要

作为蒸汽辅助重力泄油(SAGD)最重要的采油机制之一,重力泄油在很大程度上取决于蒸汽室边缘的倾角。溶液气的存在会造成底部倾角较小的椭圆形汽室,从而导致重力泄油效率低下,减慢产油速度。针对这一问题,本研究提出了一种新方案--变压 SAGD(VP-SAGD)。它基本上是一种 SAGD 工艺,在某些阶段,通过控制操作条件诱发压力激增,从而改变蒸汽腔的形状。这将导致蒸汽室底部的滑移角增大,热蒸汽和原油之间的热传输效率提高。结果表明,VP-SAGD 能够将采油率提高 20%,将累积汽油比(cSOR)降低 7%。其特殊的采油机理包括拭油效应、底部蒸汽室边界倾斜角增大以及传热增强。其中,倾斜角最大可增加 40%。此外,在压力下降期间,生产者井底压力(BHP)较低,因此后期增产效果较好。压力激增的最佳时机是汽室增长的中期阶段。生产者井底压力下降越低,增产效果越好。此外,VP-SAGD 策略在渗透率为 k = 0.5-10 达西或溶解气体含量大于 2% 的重油储层中效果更好。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A new pressure control scheme on steam-assisted gravity drainage for heavy oil production

As one the most important recovery mechanisms of steam-assisted gravity drainage (SAGD), gravity drainage is largely dependent on the inclination angle of the steam chamber edge. The existence of solution-gas causes an ellipsoid-shaped chamber that has small inclination angle at the bottom, which leads to inefficient gravity drainage and slows down oil production. To address this problem, this study proposes a new scheme, variable-pressure SAGD (VP-SAGD). It is basically a SAGD process, at certain stages of which pressure surge is induced by controlling the operating conditions so that the shape of steam chamber can be altered. This leads to a larger slip angle in the steam chamber at the bottom and more efficient heat transport between hot steam and crude oil. Results show that VP-SAGD is able to increase oil recovery by up to 20% and decrease cumulative steam–oil ratio (cSOR) by up to 7%. Its special oil extraction mechanisms include swabbing effect, enlarged inclination angle of steam chamber boundary at the bottom, and enhanced heat transfer. Particularly, the inclination angle is increased by up to 40%. In addition, a lower producer bottom-hole pressure (BHP) during pressure drawdown leads to a better production incremental in later stages. The optimal timing for pressure surge is the middle stage of steam chamber growth. The lower the producer BHP decrease, the better the yield increase. Moreover, The VP-SAGD strategy works better in heavy oil reservoirs with a permeability of k = 0.5–10 Darcy or solution gas content of greater than 2%.

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来源期刊
Canadian Journal of Chemical Engineering
Canadian Journal of Chemical Engineering 工程技术-工程:化工
CiteScore
3.60
自引率
14.30%
发文量
448
审稿时长
3.2 months
期刊介绍: The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.
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