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An investigation of low liquid loading gas-liquid stratified flow in near-horizontal pipes.

机译:近水平管道中低液体负荷气液分层流的研究。

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摘要

Low liquid loading gas-liquid two-phase flow was studied both experimentally and theoretically. Two sets of facilities with different diameters were used to conduct experiments with air and water as working fluids. On the 50.8-mm ID flow loop, the superficial gas velocity changed from 5 to 25 m/s, and the superficial liquid velocity changed from 0.00025 to 0.03 m/s. The pipe inclination angle varied from -2° to 2° from horizontal with an increment of 1°. Stratified-smooth flow, stratified-wavy flow and annular flow were encountered. On the 149.6-mm ID flow loop, the superficial gas velocity ranged from 7.5 to 21 m/s, and the superficial liquid velocity ranged from 0.005 to 0.05 m/s. The pipe inclination angle was -2°, 0°, and 2° from horizontal. Stratified-smooth flow and stratified-wavy flow were covered. The measured parameters included gas flow rate, liquid flow rate, pressure, temperature, pressure gradient, liquid holdup, wetted wall perimeter, liquid entrainment fraction, liquid film thickness, and interfacial velocity. A total of 351 data points was collected in the present study.; A mechanistic two-fluid model with new closure relationships was developed to better predict low liquid loading gas-liquid two-phase flow characteristics. New correlations for wetted wall fraction, liquid-wall friction factor and interfacial friction factor are proposed. An iterative calculation procedure is given to solve for pressure gradient and liquid holdup for given operation conditions, pipe geometry and fluid properties. A calculation program was written in FORTRAN language.; The TUFFP databank, the Espedal (1998) data, and the present study data were used to evaluate the proposed model and existing models and correlations, including the Hart et al. (1989) model, the Zhang et al. (2003) unified model, and the Beggs and Brill (1973) correlation. A screening process was applied to the TUFFP databank before it was used to do the evaluation. The evaluation showed that the proposed model gave the best predictions for both liquid holdup and pressure gradient.
机译:对低液载气液两相流进行了实验和理论研究。使用两组具有不同直径的设备以空气和水作为工作流体进行实验。在50.8 mm内径流动环路上,表观气体速度从5变为25 m / s,表层液体速度从0.00025变为0.03 m / s。管道倾斜角度从水平方向在-2°到2°之间变化,增量为1°。遇到了分层平稳流动,分层波浪流动和环形流动。在149.6毫米内径流回路上,表观气体速度范围为7.5至21 m / s,表层液体速度范围为0.005至0.05 m / s。管道倾斜角度与水平面成-2°,0°和2°。覆盖了层流和层流。测量的参数包括气体流速,液体流速,压力,温度,压力梯度,液体滞留率,湿壁周长,液体夹带率,液体膜厚度和界面速度。本研究共收集了351个数据点。建立了具有新的闭合关系的机械两流体模型,以更好地预测低液载气液两相流动特性。提出了湿壁比,液壁摩擦系数和界面摩擦系数的新的相关性。给出了迭代计算程序,以解决给定操作条件,管道几何形状和流体特性的压力梯度和液体滞留率。计算程序是用FORTRAN语言编写的。 TUFFP数据库,Espedal(1998)数据和本研究数据用于评估提出的模型和现有模型及相关性,包括Hart等。 (1989)模型,Zhang等。 (2003年)统一模型,与Beggs和Brill(1973年)相关。在对其进行评估之前,对TUFFP数据库进行了筛选过程。评估表明,所提出的模型对液体滞留量和压力梯度均给出了最佳预测。

著录项

  • 作者

    Fan, Yongqian.;

  • 作者单位

    The University of Tulsa.;

  • 授予单位 The University of Tulsa.;
  • 学科 Engineering Petroleum.
  • 学位 Ph.D.
  • 年度 2005
  • 页码 178 p.
  • 总页数 178
  • 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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