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A study of oil-water flows in large diameter horizontal pipelines.

机译:大直径水平管道中油水流动的研究。

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This study involves an experimental and theoretical investigation of oil-water flows. Oil with a viscosity of 3 cP and a density of 820 kg/m 3 and ASTM substitute seawater were used. The oil-water flow characteristics including pressure gradient, water holdup, phase distribution, velocity profile, phase inversion, mixture viscosity and droplet size in a 10 cm I. D. and 40 m long acrylic pipeline were studied. Input water fractions between 0 to 100% are examined at mixture velocities ranging from 0.4 m/s to 3.0 m/s. The temperature is maintained at 25°C and the system pressure is kept at 0.136 MPa. The effect of surfactant on oil-water flows is also examined.; The results show that the pressure gradient does not change much with the increasing in input water cut until 20%. It then increases and peaks around the phase inversion point, and gradually decreases to the pure water's value at 100% input water. Water holdup and phase distribution are strongly affected by input water cut, and mixture velocity. Above 2.0 m/s, the composition of oil-water mixture across the cross section of the pipe is no longer conspicuous. Velocity profiles show that the mixed layer moves approximately 1.2 times of the input mixture velocity. Phase inversion point is determined at around 45% input water. Minimum droplet size is observed at low mixture velocities.; The pressure gradient is affected at high surfactant concentrations, especially at high velocities. With the surfactant, homogenous flow can be obtained at lower mixture velocities especially for the water cut of 40% and higher. Surfactant does not affect the velocity distribution significantly for the flow conditions investigated. The phase inversion point is lowed to be around 40% when 10 ppm surfactant is added.; A correlation for oil-water mixture apparent viscosity was developed. The three-phase segregated flow model was completed and a four-phase segregated flow model was developed to estimate the flow characteristics in pipeline. Agreement with experimental data is good. A multi-layer model is also proposed and constructed for predicting the water dropout/onset of corrosion, and it can be applied to any complex geometry.
机译:这项研究涉及油水流的实验和理论研究。使用粘度为3 cP,密度为820 kg / m 3 的油和ASTM替代海水。研究了在10 cm I. D.和40 m长丙烯酸管道中的油水流动特性,包括压力梯度,持水率,相分布,速度分布,相转化,混合物粘度和液滴尺寸。在0.4 m / s至3.0 m / s的混合速度下检查0至100%之间的输入水馏分。温度保持在25℃,系统压力保持在0.136MPa。还检查了表面活性剂对油水流量的影响。结果表明,压力梯度不会随着输入含水率的增加而变化很大,直到20%。然后在相变点附近增加并达到峰值,然后在100%输入水处逐渐降低至纯水的值。含水率和相分布受输入含水率和混合速度的强烈影响。高于2.0 m / s时,管道横截面上的油水混合物的成分不再明显。速度曲线显示混合层的运动速度约为输入混合速度的1.2倍。相转化点被确定为约45%的输入水。在低混合速度下观察到最小的液滴尺寸。在高表面活性剂浓度下,尤其是在高速下,压力梯度会受到影响。使用表面活性剂,可以在较低的混合速度下获得均匀的流动,特别是对于含水率达到40%或更高的情况。在所研究的流动条件下,表面活性剂不会显着影响速度分布。当添加10ppm表面活性剂时,相变点降低到约40%。建立了油水混合物表观粘度的相关性。完成了三相隔离流模型,并开发了四相隔离流模型来估计管道中的流动特性。与实验数据吻合很好。还提出并构建了一个多层模型来预测水的滴落/腐蚀的开始,它可以应用于任何复杂的几何形状。

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