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Model Evaluation of Sand Transport Under Gas-Liquid Stratified Flow

机译:煤气液分层流动砂输送模型评价

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Sand transport in multiphase flow has recently gained particular attention of many companies in oil and gas industry owing to unpleasant circumstances that particle deposition accompanying. The main objective of this study is to evaluate the performance of some existing models for the prediction of the critical sand deposition velocity under gas-liquid stratified flow against acquired experimental data. Experimental data are acquired under stratified flow regime with the air as gas phase, and the water as liquid phase. Spherical glass bead with three particle sizes of 70, 185 and 510 μm with concentrations less than 0.0045 vol/vol are utilized as solid phase. A horizontal 0.1 m ID test facility is designed and constructed in order to investigate the effects of parameters such as phase velocities, particle concentration and particle size on the critical sand deposition velocity. The acquired data are compared with previous models developed by Salama (1998), Stevenson and Thorpe (2002), Hill (2011), Ibarra et al. (2014) and Dabirian et al. (2017) to determine the most reliable model for the prediction of the critical sand deposition velocity. The experimental data show that depending on the particle size and concentration, the critical velocity can change either linearly or exponentially with particle concentration. The evaluation of the previous models with acquired experimental data confirm that Ibarra et al. (2014) and Dabirian et al. (2017) models generally show better performance for the predictions of the critical velocity. Models proposed by Salama (1998) and Hill (2011), respectively, under-predicts and over-predicts the critical velocities under various experimental conditions. Also, the comparison of Stevenson & Thorpe (2002) model and the experimental data corroborates that the model is not an accurate predictive tool for the critical velocity.
机译:由于逐渐沉积的情况随之而来,多相流动的沙子运输最近在石油和天然气行业的许多公司都受到特别关注。本研究的主要目的是评估一些现有模型的性能,以预测煤气液分层流量对获取的实验数据的临界砂沉积速度。在具有空气作为气相的分层流动状态下获得实验数据,以及水作为液相。具有小于0.0045 Vol / VOL的浓度为70,185和510μm的球形玻璃珠,其浓度小于0.0045 Vol / Vol作为固相。设计和构造了水平0.1M ID测试设施,以研究参数如相速度,颗粒浓度和粒度对临界砂沉积速度的影响。将获得的数据与Salama(1998),Stevenson和Thorpe(2002),希尔(2011),Ibarra等人开发的先前模型进行了比较。 (2014)和Dabirian等人。 (2017)确定最可靠的模型,用于预测临界砂沉积速度。实验数据表明,根据粒度和浓度,临界速度可以用颗粒浓度线性或指数呈线性变化。通过获取的实验数据的先前模型的评估证实了IBarra等人。 (2014)和Dabirian等人。 (2017)模型通常对临界速度的预测表现出更好的性能。 Salama(1998)和Hill(2011)提出的模型分别在各种实验条件下预测和过度预测临界速度。此外,Stevenson&Thorpe(2002)模型的比较和实验数据证实的模型不是临界速度的准确预测工具。

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