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Theoretical and experimental study of foam for enhanced oil recovery and acid diversion.

机译:用于提高采油率和酸转移的泡沫的理论和实验研究。

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摘要

This dissertation comprises three studies of foam in porous media. The first study is a theoretical model for apparent viscosity of foam in porous media. This represents the first dynamic model for the movement of bubbles through constricted tubes in 2D, accounting for the drag on lamellae (soap films) along pore walls and the capillary forces that govern bubble shape in constricted tubes. At low velocities behavior fits earlier quasi-static and approximate models. At higher velocities, behavior is complex; for instance, pressure gradient can decrease with increasing bubble velocity. This work could provide a component to a fully mechanistic foam simulator.; The second study is an experimental investigation of SAG foam processes for enhanced oil recovery, where gas and surfactant solution are injected in alternating slugs. Experimental fractional-flow curves are presented for two surfactant formulations in Berea sandstone, with no oil present. Results are then scaled-up using fractional-flow theory to a hypothetical 1D field-scale application. In one case the data suggest an abrupt jump from a strong-foam fractional-flow curve to a weaker-foam curve, as has been reported elsewhere. In both cases the data suggest successful mobility control on the field scale.; The third study is an experimental investigation of post-foam liquid injection, which is the key to the success of foam-acid diversion for matrix-acid well stimulation. Results indicate that with high foam quality pressure gradient can be higher during liquid injection than during foam injection; this may require reconsideration of the optimal foam quality for foam-acid diversion. It appears that the water relative-permeability function obtained during foam injection also applies to liquid injection after foam, until trapped gas begins to dissolve into injected liquid. The extent of gas trapping and liquid mobility after foam varied with foam quality here, which means earlier models that exclude this effect may need to be revised.; In both experimental studies, pressure gradient was monitored along the core and liquid saturation was determined by weighing the core continuously during the experiment. Strengths and shortcomings of this technique for determining water saturation are discussed, along with suggestions for improving the technique.
机译:本论文包括对多孔介质中泡沫的三项研究。第一项研究是多孔介质中泡沫表观粘度的理论模型。这代表了气泡在2D中通过缩管的运动的第一个动力学模型,这说明了沿孔壁在薄片(肥皂膜)上的阻力以及控制缩管中气泡形状的毛细管力。在低速下,行为适合较早的准静态模型和近似模型。在较高的速度下,行为很复杂。例如,压力梯度会随着气泡速度的增加而减小。这项工作可以为全机械泡沫模拟器提供一个组成部分。第二项研究是SAG泡沫工艺用于提高采油率的实验研究,其中将气体和表面活性剂溶液注入交替的段塞中。给出了Berea砂岩中两种表面活性剂配方的实验分流曲线,没有油。然后使用分数流理论将结果按比例放大到假设的1D场比例应用中。在一种情况下,数据表明从强泡沫分流曲线突然跳到弱泡沫曲线,正如其他地方报道的那样。在两种情况下,数据都表明在田间规模上成功进行了流动性控制。第三项研究是泡沫后注液的实验研究,这是泡沫酸转移成功刺激基质酸井的关键。结果表明,在泡沫质量较高的情况下,液体注入过程中的压力梯度可能高于泡沫注入过程中的压力梯度。这可能需要重新考虑用于泡沫酸转移的最佳泡沫质量。似乎在泡沫注入期间获得的水相对渗透率函数也适用于泡沫之后的液体注入,直到捕获的气体开始溶解到注入的液体中为止。泡沫后气体的捕集程度和液体流动性随泡沫的质量而变化,这意味着排除这种影响的早期模型可能需要修改。在两个实验研究中,沿岩心监测压力梯度,并在实验过程中通过连续称量岩心来确定液体饱和度。讨论了确定水饱和度的这项技术的优缺点,以及改进该技术的建议。

著录项

  • 作者

    Xu, Qiang.;

  • 作者单位

    The University of Texas at Austin.;

  • 授予单位 The University of Texas at Austin.;
  • 学科 Engineering Petroleum.
  • 学位 Ph.D.
  • 年度 2003
  • 页码 231 p.
  • 总页数 231
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 石油、天然气工业;
  • 关键词

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