用伽马射线法评价高粘度液体对两相流段塞流平动速度的影响

Y. Baba, A. Aliyu, N. E. Okeke, A. S. Girei, H. Yeung
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摘要

段塞流的平移速度,即段塞流单元的速度,是段塞流体内最大混合速度和漂移速度的总和。该参数的准确估计对油气管道的节能设计具有重要意义。查阅文献发现,现有的该参数预测模型是基于低粘度液体(1pa)的观测建立的。S或更少)。然而,在输送高粘度油品的管道中,其行为有明显不同。本文报道了高黏度油气流动中段塞流平动速度的新数据。用粘度为0.7 ~ 6.0 Pa的空气和矿物油的混合物进行了规模实验。在直径0.0762 m、长度为17 m的水平管道中。油的粘度随温度的变化关系式为μ=−0.0043T3+0.0389T2−1.4174T+18.141。采用两对采样频率为250 Hz的快速采样伽马密度计测量段塞流的平移速度。在所研究的实验流动条件范围内,观察到液体油粘度的增加对段塞流的平移速度有很大影响。利用现有数据集,并结合文献中获得的石油粘度范围为0.189-6.0 Pa的数据,推导出了一个包含粘度对段塞流平移速度影响的新的预测相关性。S为水平流量。通过统计分析和验证与新的封闭关系的比较显示,与现有的相关性相比,性能显着提高。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Evaluating the Effects of High Viscosity Liquid on Two Phase Flow Slug Translational Velocity using Gamma Radiation Methods
Slug translational velocity, described as the velocity of slug units, is the summation of the maximum mixture velocity in the slug body and the drift velocity. Accurate estimation of this parameter is important for energy-efficient design of oil and gas pipelines. A survey of the literature revealed that existing prediction models of this parameter were developed based on observation from low viscosity liquids (of 1 Pa.s or less). However, its behaviour in pipes transporting higher viscosity oils is significantly different. In this research work, new data for slug translational velocity in high-viscosity oil-gas flows are reported. Scaled experiments were carried out using a mixture of air and Mineral oil of viscosity ranging from 0.7 to 6.0 Pa.s in a 17-m long horizontal pipe of 0.0762 m ID. Temperature dependence of the oil's viscosity is given as μ=−0.0043T3+0.0389T2−1.4174T+18.141. The slug translational velocity was measured by means two pairs of two fast-sampling Gamma Densitometers with a sampling frequency of 250 Hz. For the range of experimental flow conditions investigated, increase in liquid oil viscosity was observed to strongly influence slug translational velocity. A new predictive correlation incorporating the effect of viscosity on slug translational velocity was derived using the current dataset and incorporating those obtained in literature with oil viscosity ranging from 0.189–6.0 Pa.s for horizontal flow. A comparison by statistical analysis and validation and of the new closure relationship showed a remarkably improved performance over existing correlations.
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