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Prediction of Barite Sag in Horizontal Annular Flow

机译:水平环形流动中晶体凹陷的预测

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Under certain drilling conditions, the weighting material particles such as barite can settle out of the drilling fluid. This phenomenon, known as barite sag, can lead to a number of drilling problems including lost circulation, well control difficulties, poor cement job, and stuck pipe. This study investigates barite sag, both experimentally and numerically, in the annulus under flow conditions. Experimental work has been conducted on a large flow loop to investigate the effects of major drilling parameters on barite sag by measuring the circulating fluid density. Results of the tests indicate that the highest sag occurs at low annular velocities and rotational speed and also at high inclination angles. It was observed that at inclination angles less than 60°, for any annular velocity, barite sag is not significant. Eccentricity of a non-rotating inner pipe did not have a significant effect on barite sag. However, effects of inner pipe rotation on barite sag for an eccentric annulus are more significant than concentric case. The simulation part of this study is based on a proposed particle tracking method called "Particle Elimination Technique". The traveling path of each solid particle is assumed to be a function of size and shape of the particle, fluid velocity and rheology. Based on the estimated traveling path of particles, density of the fluid is updated considering the number of particles whose paths lead to the bottom of the annulus and become motionless. In order to capture the complexities associated with the solid-liquid flow, a lift force is assigned to the solid particles that enable adjustment of the model with experimental results. Comparing the results of numerical simulation to the experimental study on the effects of annular velocity on barite sag in a horizontal annulus shows a good agreement. The numerical simulation was modified from laboratory scale to real wellbore dimensions for practical drilling applications. Results of the simulation show prediction of the density of the drilling fluid in the horizontal section of a wellbore with various lengths and dimensions under different annular velocities.
机译:在某些钻井条件,加权材料颗粒如重晶石可以解决钻井液进行。这种现象,被称为重晶石下垂,会导致一些钻井问题,包括井漏,井控难点,水泥的工作差,卡钻的。本研究探讨重晶石下垂,实验和数值,在流动条件下的环形空间。实验工作已经在大流动环路已进行调查的主要钻井参数上重晶石沉降通过测量循环流体密度的影响。测试的结果表明,最高的下垂发生在低环形速度和旋转速度,并且还以高倾斜角度。据观察,在倾斜角小于60°,对于任何环速度,重晶石沉降是不显著。非旋转的内管的偏心没有对重晶石下沉一个显著的效果。然而,对于偏心环上重晶石凹陷内管旋转的影响比同心情况下更显著。本研究的模拟部分是基于所谓的“粒子排除法”提出的粒子跟踪方法。各固体颗粒的行进路径被假定为大小和粒子形状,流体速度和流变学的函数。基于粒子的估计行进路径上,流体的密度被更新考虑颗粒其路径导致环,成为一动不动的底部的数目。为了捕获与固液流相关联的复杂性,升力被分配到的固体颗粒,使与实验结果的模型的调整。在水平环显示了重晶石沉降数值模拟的结果相比对环形速度影响的实验研究有很好的一致性。数值模拟,从实验室规模的修改,以实井筒尺寸实际钻井应用。在与根据不同的环形速度不同的长度和尺寸的井眼的水平截面的钻井流体的密度的模拟结果表明预测的结果。

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