首页 | 本学科首页   官方微博 | 高级检索  
     检索      

并联管路气液两相流分流实验与数值模拟
引用本文:马立辉,何利民,米祥冉,罗小明.并联管路气液两相流分流实验与数值模拟[J].科学技术与工程,2021,21(34):14554-14560.
作者姓名:马立辉  何利民  米祥冉  罗小明
作者单位:中国石油大学(华东)储运与建筑工程学院;中国石油国际勘探开发有限公司
基金项目:国家科技重大专项(No.2016ZX05028-004-003)。
摘    要:为了研究气液两相流在并联立管中的分流状况,在实验室中建立了带有并联立管的气液两相流流动回路。建立了气液两相流分流数学模型,通过数值模拟方法对气液两相流分流进行研究。实验过程中发现了并联立管中三种不同的流动状态分别为弹状流-弹状流、搅混流-搅混流以及弹状流-搅混流。实验结果表明当并联立管中的流动状态为弹状流-弹状流时,两根立管中的压降相同,但是并联立管中的液塞排出并不具有同步性,可能产生偏流状况。在气液流速较高的搅混流-搅混流时两相流在并联立管中始终处于均匀分配状态。介于两者之间的弹状流-搅混流,并联立管中的压降产生较大的偏差,气液两相流流量更倾向于搅混流一侧流出,此时并联立管中产生严重的偏流状况。数值模拟过程中,通过对并联立管出口持液率进行监测,在较低的气液速下两相流并不能够均匀分配,但是在较高的气液速下,两相流始终处于均匀分配,可见所建立的数学模型具有良好的准确性。

关 键 词:并联立管,  T形管,  分流特性,  数值模拟
收稿时间:2021/3/25 0:00:00
修稿时间:2021/10/12 0:00:00

Experimental and numerical simulation of gas-liquid two-phase flow splitting in parallel risers
Ma Lihui,He Limin,Mi Xiangran,Luo Xiaoming.Experimental and numerical simulation of gas-liquid two-phase flow splitting in parallel risers[J].Science Technology and Engineering,2021,21(34):14554-14560.
Authors:Ma Lihui  He Limin  Mi Xiangran  Luo Xiaoming
Institution:Provincial Key Laboratory of Oil & Gas Storage and Transportation Safety, College of Pipeline and Civil Engineering, China University of Petroleum
Abstract:In order to study the distribution of gas-liquid two-phase flow in parallel risers, a gas-liquid two-phase flow loop with parallel risers was established in the laboratory. Established a mathematical model of gas-liquid two-phase flow splitting, the splitting characteristics of gas-liquid two-phase flow is studied by numerical simulation method. During the experiment, three different flow states in the parallel riser were found: slug flow-slug flow, churn flow-churn flow and slug flow-churn flow. The experimental results show that when the flow state in the parallel risers are slug-slug flow, the pressure drop in the two risers are the same, but the discharge of the liquid plug in the parallel risers are not synchronized, and the two-phase may be unevenly distributed. When the gas-liquid velocity is high enough to maintain churn-churn flow in the parallel risers, the two-phase flow is always evenly distributed in the parallel risers. The pressure drop of slug-churn flow which between the two flow states in the parallel risers had a large deviation, and the flow of gas-liquid two-phase flow tends to flow out from the side of churn flow, in this case two-phase splitting unevenly in the parallel risers. In the process of numerical simulation, by monitoring the liquid holdup at the outlet of the parallel risers, the two-phase flow can not be evenly distributed at a lower gas-liquid velocity, but at a higher gas-liquid velocity, the two-phase flow were always evenly distributed, which shows that the established mathematical model has good accuracy.
Keywords:Parallel risers    T-junction    Splitting characteristics    Simulation
点击此处可从《科学技术与工程》浏览原始摘要信息
点击此处可从《科学技术与工程》下载免费的PDF全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号