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油水砂多相流中固体颗粒对弯管及T型堵头管的冲蚀
          
Erosion of Pipe Bend and Plugged Tee by Solid Particles in Oil-Water-Sand Multiphase Flow

摘    要
采用计算流体动力学方法在欧拉坐标系下求解连续相运动方程,在拉格朗日坐标系下求解离散相颗粒轨道方程,并利用冲蚀方程研究了管内油、水、砂多相流中固体颗粒运动与管道冲蚀的相互关系,预测最大冲蚀发生位置。结果表明: 弯管冲蚀最严重处位于下游直管段与弯头连接处外侧,T型堵头管冲蚀最严重处位于上下游直管段交接处内侧,T型堵头管的最大冲蚀速率远大于弯管的;T型堵头管中存在明显的颗粒相互碰撞区域以及颗粒滞留区域,在颗粒相互碰撞区域颗粒对管壁的碰撞能降低,在颗粒滞留区域颗粒的滞留减少了新来颗粒对堵头的碰撞,这两个区域都从一定程度上减小了颗粒对管道的冲蚀作用。
标    签 弯管   T型堵头管   油水砂   多相流   冲刷腐蚀   颗粒轨迹   pipe bend   plugged tee   oil-water-sand   multiphase flow   erosion-corrosion   particle trajectory  
 
Abstract
The method of computational fluid dynamics (CFD) was used to solve continuous phase motion equation in the Euler coordinate system, and to solve the discrete phase particle trajectory equation in the Lagrange coordinate system. Then the erosion equation was used to study the relationship between solid particles and pipe erosion in oil-water-sand multiphase flow, and then the maximum erosion position was predicted. The results show that the most serious erosion region in the bend pipe was in the outermost side of the junction of downstream straight pipe and elbow; however for plugged tee, the region was the inner side of the junction of upstream and downstream straight pipe. And the maximum erosion rate of plugged tee was much higher than that of pipe bend. Particle collision region and particle retention region were found in the plugged tee. In the collision region, the collision energy of particles against pipe wall decreased, while in the retention region, the retention of particles impeded the impacts of new particles against the plugged tee. These two regions reduced erosion rate of plugged tee in a certain extent.

中图分类号 TG174   DOI 10.11973/fsyfh-201602009

 
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所属栏目 试验研究

基金项目 国家自然科学基金(51274232); 中央高校基本科研业务费专项资金资助(15CX06070A)

收稿日期 2015/1/29

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备注曹学文(1966-),教授,博士,从事天然气处理与加工、油气水多相流理论及应用、海底管道完整性管理等方面的研究,

引用该论文: PENG Wen-shan,CAO Xue-wen,JI Jun-yi,JIN Xue-tang,WANG Qing. Erosion of Pipe Bend and Plugged Tee by Solid Particles in Oil-Water-Sand Multiphase Flow[J]. Corrosion & Protection, 2016, 37(2): 131


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