HPAM溶液在管道湍流输送过程中的降解(或缺乏)和减阻

S. Jouenne, J. Anfray, P. Cordelier, K. Mateen, D. Levitt, I. Souilem, P. Marchal, C. Lemaitre, L. Choplin, Jonathon Nesvik, T. Waldman
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引用次数: 14

摘要

在聚合物驱项目中使用的经验法则往往会限制水解聚丙烯酰胺聚合物在管道中运输的距离,而不会发生明显的降解。然而,在敏感环境中,如海上设施,需要最大限度地减少足迹,聚合物水化过程的集中和长途运输可能是可取的。需要更可靠的规则来设计管网,并估计聚合物在湍流条件下运输过程中的机械降解。在这项工作中,我们以经验大规模管道实验和理论发展的形式提出证据,反驳了聚合物管道运输受到机械降解限制的说法。我们的工作得出结论,机械退化发生在临界速度下,该速度随管道直径的增加而增加。如果在给定的管道中没有达到临界速度,那么聚合物溶液可以输送的距离就没有限制。此外,还测量了粘性聚合物溶液的减阻效果,并将其作为管道长度、管径、流体流速和聚合物浓度的函数。在较大的管道中,对于给定的速度,定义了一个包线来确定预期的最小和最大阻力降低。对于直径在14和22英寸之间变化的管道。当速度大于1m /s时,预计减阻率在55%至80%之间。开发了一个更精细的模型,以更小的不确定性预测减阻。综上所述,适用于水运的经典设计规则(流体速度< 3 m/s)可以应用于聚合物网络的设计。因此,对于三级聚合物项目,现有注水网络应与聚合物输运的力学要求相适应。对于二次聚合物项目,改变设计规则,考虑到高水平的减阻,应该会给管道设计和安装带来一定的经济效益
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Degradation (or Lack Thereof) and Drag Reduction of HPAM Solutions During Transport in Turbulent Flow in Pipelines
Rules of thumb that are used in the industry for polymer-flooding projects tend to limit the distance over which hydrolyzed poly-acrylamide polymers can be transported in pipelines without under-going significant degradation. However, in sensitive environments, such as offshore facilities where footprint minimization is required, centralization of the polymer-hydration process and long-distance transport may be desirable. More-reliable rules are required to de-sign the pipe network and to estimate mechanical degradation of polymers during transport in turbulent conditions.In this work, we present evidence in the form of empirical large-scale pipeline experiments and theoretical development refuting the claim that polymer pipeline transport is limited by mechanical degradation. Our work concludes that mechanical degradation oc-curs at a critical velocity, which increases as a function of pipe di-ameter. Provided the critical velocity is not reached in a given pipe, there is no limit to the distance over which polymer solution can be transported. In addition, the drag reduction of viscous polymer solutions was measured as a function of pipe length, pipe diameter, fluid ve-locity, and polymer concentration. An envelope was defined to fix the minimum and maximum drag reductions expected for a given velocity in larger pipes. For pipes with diameters varying between 14 and 22 in. at a velocity greater than 1 m/s, the drag-reduction percentage is anticipated to be between 55 and 80%. A more- refined model was developed to predict drag reduction with less uncertainty. In conclusion, classical design rules applied for water transport (fluid velocity < 3 m/s) can be applied to the design of a polymer network. Therefore, for tertiary polymer projects, the existing water-injection network should be compatible with the mechanical requirements of polymer transportation. For secondary polymer projects, changing the rules of design by taking into account the high level of drag reduction should bring some economy to the pipe design and installation
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