气流条件下电潜泵ESP升压机理建模及实验验证

Jianjun Zhu, Zhihua Wang, Haiwen Zhu, R. Cuamatzi-Meléndez, Jose Alberto Martinez-Farfan, Zhang Jiecheng, Hong-quan Zhang
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引用次数: 4

摘要

作为一种大流量采油的人工举升方法,电潜泵(ESP)的性能受到气体夹带的影响,这是ESP中经常遇到的现象。当发生这种情况时,esp可能会出现中度或严重的封头退化,并伴有产量降低、气锁和流动不稳定。对于基于ESP的生产系统的设计和运行,需要准确的模型来预测含气工况下的ESP增压压力。本文提出了一种简化的旋转电潜泵内气液流动机理模型,该模型不仅能映射电潜泵内的流动模式,还能捕捉到原位气体空隙率、增压压力、气泡大小等多相流动特征。测试ESP气液性能的实验装置由3″不锈钢全封闭液流回路和½″半开放气流回路组成。一个14级串联的径向电潜泵水平安装在测试台上。在每一级钻取压力口,以测量逐级压力增量。气液混合物在卧式分离器中分离,过多的气体被排出,液体继续循环。通过两种类型的试验(映射试验和脉动试验)获取实验数据,全面评估泵在不同工况下的性能。实验中对水/气流量、ESP转速、进气压力等进行了控制。该模型从欧拉方程出发,引入了ESP叶轮出口方向与设计流向相匹配的最佳匹配流量。旋转叶轮中流速三角形的不匹配是由流体流速的变化引起的。模型中考虑了流动方向变化、摩擦、泄漏等因素造成的损失。基于离心流场中稳定气泡的力平衡,可以估算出旋转ESP叶轮内的原位气体空隙率,并由此计算出气液混合密度。预测的ESP增压压力与相应的实验测量结果相匹配,精度可接受。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Mechanistic Modeling of Electrical Submersible Pump ESP Boosting Pressure Under Gassy Flow Conditions and Experimental Validation
As an artificial lift method for high-flow-rate oil production, electrical submersible pumps’ (ESP) performance surfers from gas entrainment, a frequently encountered phenomenon in ESPs. When it occurs, ESPs can experience moderate or severe head degradation accompanied with production rate reduction, gas locking and flow instabilities. For the design and operation of an ESP-based production system, the accurate model is needed to predict ESP boosting pressure under gassy flow conditions. In this paper, a simplified mechanistic model is proposed to model gas-liquid flow inside a rotating ESP. The model not only maps flow patterns in ESPs but also captures the multiphase flow characteristics in terms of in-situ gas void fraction, boosting pressure, bubble size, etc. The experimental facility for testing ESP gas-liquid performance comprises of a 3″ stainless steel fully closed liquid flow loop and ½″ semi-open gas flow loop. A radial-type ESP with 14 stages, assembled in series, was horizontally mounted on the testing rig. Pressure ports were drilled at each stage to measure stage-by-stage pressure increment. The mixture of gas and liquid is separated in a horizontal separator, where excessive gas was vented and the liquid continues circulation. Experimental data were acquired with two types of tests (mapping tests and surging tests) to completely evaluate the pump behaviors at different operational conditions. The water/gas flow rates, ESP rotational speeds, intake pressure etc. were controlled in the experiments. The new model starts form from Euler equations, and introduces a best-match flowrate at which the flow direction at ESP impeller outlet matches the designed flow direction. The mismatch of velocity triangle in a rotating impeller results from the varying liquid flow rates. Losses due to flow direction change, friction, and leakage etc., were incorporated in the model. Based on the force balance on a stable gas bubble in a centrifugal flow field, the in-situ gas void fraction inside a rotating ESP impeller can be estimated, from which the gas-liquid mixture density is calculated. The predicted ESP boosting pressures match the corresponding experimental measurements with acceptable accuracy.
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