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Multiphase flow separation in liquid-liquid cylindrical cyclone and gas-liquid-liquid cylindrical cyclone compact separators.

机译:液-液圆柱旋风分离器和气-液-液圆柱旋风紧凑型分离器中的多相流分离。

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摘要

The hydrodynamics of multiphase flow in Liquid-Liquid Cylindrical Cyclone (LLCC©1) and Gas-Liquid-Liquid Cylindrical Cyclone (GLLCC ©2) compact separators have been studied experimentally and theoretically for evaluation of their performance as free water knockout devices. In both GLLCC and the LLCC configurations, no complete oil-water separation occurs. Rather, both separators perform as free water knockouts, delivering a clean water stream and an oil rich stream.; A new state-of-the-art, two-inch, three-phase, fully instrumented flow loop has been designed and constructed. Experimental data on oil-water separation efficiency in the LLCC and the GLLCC have been acquired.; A total of 260 runs have been conducted for the LLCC for water-dominated flow conditions. Four different flow patterns in the inlet have been identified, namely, Stratified flow, Oil-in-Water Dispersion - Water Layer flow, Double Oil-in-Water Dispersion flow and Oil-in-Water Dispersion flow. For all runs, an optimal split ratio exists, where the flow rate in the water stream is maximum with 100% water cut. The value of the optimal (maximum) split ratio depends upon the existing flow pattern. For the Stratified and Oil-in-Water Dispersion - Water Layer flow patterns, this maximum split ratio is about 60%. For the Double Oil-in-Water Dispersion and Oil-in-Water Dispersion flow patterns, the maximum split ratio ranges from 50% to 20%, decreasing with the increase of oil content in the inlet stream.; Experimental data on oil-water separation efficiency in the GLLCC have been acquired. A total of 220 experimental runs have been conducted, including the oil-water separation efficiency for different combinations of oil and water superficial velocities, and varying the split ratio for each combination. The GLLCC separation efficiency data reveal that it performs, in addition to the separation of the gas phase, also as a free water knockout. This occurs only for very low oil concentrations at the inlet, below 10%. Also, lower separation efficiencies are observed, as compared to the LLCC configuration.; Novel mechanistic models have been developed for the prediction of the complex flow behavior and the separation efficiency in the LLCC and GLLCC. The models consist of several sub-models, including inlet analysis, nozzle analysis, droplet size distribution model, and separation model based on droplet trajectories in swirling flow.; Comparisons between the experimental data and the LLCC and GLLCC model predictions show excellent agreement. The models are capable of predicting both the trend of the experimental data as well as the absolute measured values. The developed models can be utilized for the design and performance analysis of the LLCC and GLLCC.; 1LLCC - Liquid-Liquid Cylindrical Cyclone - Copyright, The University of Tulsa, 1998. 2GLLCC - Gas-Liquid-Liquid Cylindrical Cyclone - Copyright, The University of Tulsa, 2000.
机译:对液-液圆柱旋流器(LLCC ©1 )和气-液-液圆柱旋流器(GLLCC ©2 )紧凑型分离器中的多相流动进行了流体动力学研究。从理论上评估其作为游离水敲除装置的性能。在GLLCC和LLCC配置中,都不会发生油水分离。相反,两个分离器都可以作为自由水分离器,提供清洁的水流和富含油的流。设计并构造了一种新的,最新的,两英寸,三相,仪器齐全的流量回路。获得了LLCC和GLLCC中油水分离效率的实验数据。对于LLCC,在以水为主的流动条件下,总共进行了260次运行。确定了进样口中的四种不同流型,即分层流,水包油中的水-水层流,水包油中的双重水流和水包油中的流。对于所有运行,都存在最佳分流比,其中在100%含水率的情况下,水流中的流速最大。最佳(最大)分配比的值取决于现有的流型。对于分层型和水包油型-水层流型,此最大分流比约为60%。对于水包油双分散和水包油双分散流型,最大分流比范围为50%至20%,随着进料流中含油量的增加而减小。已经获得了GLLCC中油水分离效率的实验数据。总共进行了220次实验,包括油和水表观速度的不同组合的油水分离效率,以及每种组合的分流比。 GLLCC分离效率数据表明,除气相分离外,它还可以作为游离水分离出。仅在进口处的油浓度非常低(低于10%)时才会发生这种情况。而且,与LLCC配置相比,观察到较低的分离效率。已经开发了新颖的力学模型来预测LLCC和GLLCC中的复杂流动行为和分离效率。这些模型包括几个子模型,包括入口分析,喷嘴分析,液滴尺寸分布模型和基于旋流中液滴轨迹的分离模型。实验数据与LLCC和GLLCC模型预测之间的比较显示出极好的一致性。该模型能够预测实验数据的趋势以及绝对测量值。开发的模型可用于LLCC和GLLCC的设计和性能分析。 1 LLCC-液-液圆柱形旋风分离器-版权所有,塔尔萨大学,1998年。 2 GLLCC-气-液-液圆柱形旋风分离器-版权所有,塔尔萨大学, 2000。

著录项

  • 作者

    Oropeza-Vazquez, Carlos.;

  • 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 2001
  • 页码 120 p.
  • 总页数 120
  • 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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