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Experimental Study of DRA for Vertical Two-Phase Annular Flow

机译:垂直两相环状流DRA的实验研究

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摘要

Experimental investigation of drag reduction in vertical two-phase annular flow is presented. The work is a feasibility test for applying drag reducing additives (DRAs) in high production-rate gas-condensate wells where friction in the production tubing limits the production rate. The DRAs are intended to reduce the overall pressure gradient and thereby increase the production rate. Since such wells typically operate in the annular-entrained flow regime, the gas and liquid velocities were chosen such that the experiments were in a vertical two-phase annular flow. The drag reducers had two main effects on the flow. As expected, they reduced the frictional component of the pressure gradient by up to 74%. However, they also resulted in a significant increase in the liquid holdup by up to 27%. This phenomenon is identified as "DRA-induced flooding." Since the flow was vertical, the increase in the liquid holdup increased the hydrostatic component of the pressure gradient by up to 25%, offsetting some of reduction in the frictional component of the pressure gradient. The DRA-induced flooding was most pronounced at the lowest gas velocities. However, the results show that in the annular flow the net effect will generally be a reduction in the overall pressure gradient by up to 82%. The findings here help to establish an envelope of operations for the application of multiphase drag reduction in vertical flows and indicate the conditions where a significant net reduction of the pressure gradient may be expected.
机译:提出了垂直两相环形流减阻的实验研究。这项工作是在高生产率气体冷凝水井中使用减阻添加剂(DRA)的可行性测试,在这种情况下,生产管道中的摩擦会限制生产率。 DRA旨在减小整体压力梯度,从而提高生产率。由于此类井通常在环形夹带流域中运行,因此选择气体和液体的速度,使实验处于垂直两相环形流中。减阻剂对流动有两个主要影响。正如预期的那样,他们将压力梯度的摩擦分量降低了74%。但是,它们也导致液体滞留量显着增加高达27%。这种现象被标识为“ DRA引发的洪水”。由于流动是垂直的,因此液体滞留量的增加使压力梯度的静液压分量最多增加了25%,从而抵消了压力梯度的摩擦分量的减小。在最低气体速度下,DRA引起的洪水最明显。但是,结果表明,在环形流中,净效应通常将使总压力梯度降低多达82%。此处的发现有助于建立在垂直流中应用多相减阻的操作范围,并指出可能期望压力梯度显着净减少的条件。

著录项

  • 来源
    《Journal of Energy Resources Technology》 |2009年第2期|54-58|共5页
  • 作者单位

    WPE/31 Brunei Shell Petroleum Co. Sdn. Bhd., Seria Head Office, Seria KB 3534, Brunei Darussalam;

    Department of Mechanical Engineering, University of Alberta, Edmonton, AL, T6G 2G8, Canada;

    Department of Mechanical Engineering, University of Alberta, Edmonton, AL, T6G 2G8, Canada;

    Department of Mechanical Engineering, University of Alberta, Edmonton, AL, T6G 2G8, Canada;

    Facilities Management, Enbridge Pipelines Inc., Calgary, AL, Canada;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
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  • 入库时间 2022-08-18 00:31:00

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