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Critical Sand Deposition Velocity in Horizontal Stratified Flow

机译:水平分层流动中的临界砂沉积速度

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Transport of sand in multiphase pipelines occurs in the petroleum industry as sand is produced co-mingled with crude oil. Stationary sand beds are formed at the pipe bottom when the flow velocity is lower than the critical sand deposition velocity. These sand beds reduce reservoir production and affect the integrity of the pipe system due to pipeline plugging and erosion/corrosion produced by sand particles. Therefore, the production system must be designed to operate at a velocity high enough to enable transport of sand particles along the pipe. For that reason, it is crucial to predict the critical sand deposition velocity in order to maximize reservoir production. Gas-liquid-sand flow hydrodynamics, which is commonly encountered in most reservoirs and also in oil and gas transportation pipelines, is more complex than liquid-sand flow, making the modeling extremely difficult. At present, gas- liquid-sand flow is still not well understood, with limited data available in the literature. In addition, the effect of sand concentration has not been thoroughly studied for two-phase flows transporting sand. Experimental and theoretical investigations have been conducted in this study on gas-liquid-sand stratified flow in horizontal pipes at low sand concentrations. A 4-in experimental facility was designed and constructed and data were acquired utilizing air-water-glass beads flow. The data include measurements of critical sand deposition velocities, namely, the transition between moving and stationary beds. The data reveal that for a constant superficial liquid velocity, the critical mixture and liquid sand deposition velocities increase with increasing sand concentrations. Also, for a given sand concentration, the critical liquid velocity is almost the same for different superficial liquid velocities. The sand deposition correlations of Oroskar and Turian (1980) for single-phase flow and Salama (2000) for two-phase flow are modified and extended in order to develop a new correlation. The developed correlation enables the prediction of critical sand deposition mixture velocity for horizontal stratified flow, as a function of sand concentration along with other parameters. Comparison between the predictions of the developed correlation and the experimental data reveal a very good agreement, whereby the relative errors of mixture and liquid critical sand deposition velocities are ±2.5% and < 5%, respectively.
机译:由于砂与原油共混成,在石油工业中发生砂的运输发生在石油工业中。当流速低于临界砂沉积速度时,在管底形成固定砂床。这些沙床减少了储层生产,并影响管道系统的完整性,由于砂颗粒产生的管道堵塞和腐蚀/腐蚀。因此,生产系统必须设计成以足够高的速度操作以使沿管道运输砂颗粒。因此,预测临界砂沉积速度至关重要以最大限度地提高储层生产。气液砂流动流体动力学,通常遇到在大多数储层和石油和天然气运输管道中,比液体砂流更复杂,使得模型极其困难。目前,气体砂流仍然没有很好地理解,文献中可用的有限数据。此外,对于运输砂的两相流动,砂浓度的作用尚未彻底研究。本研究在低砂浓度下的水液 - 砂分层流动对实验和理论研究。设计并建造了一个4型实验设施,利用空气玻璃珠流量获得数据。数据包括临界砂沉积速度的测量,即移动和固定床之间的过渡。数据显示,对于恒定的浅表液体速度,临界混合物和液体砂沉积速度随着砂浓度的增加而增加。而且,对于给定的砂浓度,对于不同的浅表液体速度,临界液体速度几乎相同。用于两相流的单相流动和沙拉(2000)的奥氏岩和丽安(1980)的砂沉积相关性被修改和扩展,以发展新的相关性。发达的相关性使得能够预测水平分层流动的临界砂沉积混合物速度,作为砂浓度以及其他参数的函数。所发育相关性的预测与实验数据之间的比较揭示了一种非常好的一致性,其中混合物和液态染色沉积速度的相对误差分别为±2.5%和<5%。

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