An Experimental Analysis of Gas-Liquid Flow Breakdown in a T-Junction

被引:0
|
作者
Ma, Lihui [1 ]
Han, Zhuo [1 ]
Li, Wei [1 ]
Qi, Guangfeng [1 ]
Cheng, Ran [2 ]
Wang, Yuanyuan [1 ]
Mi, Xiangran [3 ]
Zhang, Xiaohan [1 ]
Li, Yunfei [1 ]
机构
[1] Sinopec Shengli Oilfield Co, Tech Inspect Ctr, Dongying 257000, Peoples R China
[2] Sinopec Shengli Oilfield Co, New Energy Dev Ctr, Dongying 257000, Peoples R China
[3] China Natl Oil & Gas Explorat & Dev Co Ltd, Beijing 100034, Peoples R China
来源
FDMP-FLUID DYNAMICS & MATERIALS PROCESSING | 2024年 / 20卷 / 06期
关键词
Two-phase fl ow; T-junction; split model; entrance effect mechanism model; improved model; 2-PHASE FLOW; PIPES; PRESSURE;
D O I
10.32604/fdmp.2024.046405
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
When a gas-liquid two-phase flow (GLTPF) enters a parallel separator through a T-junction, it generally splits unevenly. This phenomenon can seriously affect the operation efficiency and safety of the equipment located downstream. In order to investigate these aspects and, more specifically, the so-called bias phenomenon (all gas and liquid flowing to one pipe, while the other pipe is a liquid column that fluctuates up and down), laboratory experiments were carried out by using a T-junction connected to two parallel vertical pipes. Moreover, a GLTPF prediction model based on the principle of minimum potential energy was introduced. The research results indicate that this model can accurately predict the GLTPF state in parallel risers. The boundary of the slug flow and the churn flow in the opposite pipe can be predicted. Overall, according to the results, the pressure drop curves of the two-phase flow in the parallel risers are basically the same when there is no bias phenomenon, but the pressure drop in the parallel riser displays a large deviation when there is a slug flow-churn flow. Only when the parallel riser is in a state of asymmetric flow and one of the risers produces churn flow, the two-phase flow is prone to produce the bias phenomenon.
引用
收藏
页码:1381 / 1392
页数:12
相关论文
共 50 条
  • [1] Numerical Simulation and Analysis of Gas-Liquid Flow in a T-Junction Microchannel
    Hongtruong Pham
    Wen, Lu
    Zhang, Hongbo
    ADVANCES IN MECHANICAL ENGINEERING, 2012,
  • [2] Gas-liquid flow splitting in T-junction with inclined lateral arm
    Le-le Yang
    Shuo Liu
    Hua Li
    Jian Zhang
    Ying-xiang Wu
    Jing-yu Xu
    Journal of Hydrodynamics, 2018, 30 : 173 - 176
  • [3] Gas-liquid flow splitting in T-junction with inclined lateral arm
    杨乐乐
    刘硕
    李华
    张健
    吴应湘
    许晶禹
    Journal of Hydrodynamics, 2018, 30 (01) : 173 - 176
  • [4] The split of stratified gas-liquid flow at a small diameter T-junction
    Das, G
    Das, PK
    Azzopardi, BJ
    INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2005, 31 (04) : 514 - 528
  • [5] Gas-liquid flow splitting in T-junction with inclined lateral arm
    Yang, Le-le
    Liu, Shuo
    Li, Hua
    Zhang, Jian
    Wu, Ying-xiang
    Xu, Jing-yu
    JOURNAL OF HYDRODYNAMICS, 2018, 30 (01) : 173 - 176
  • [6] Comparative analysis of gas-liquid flow in T-junction microchannels with different inlet orientations
    Liu, Dongren
    Ling, Xiang
    Peng, Hao
    ADVANCES IN MECHANICAL ENGINEERING, 2016, 8 (03) : 1 - 14
  • [7] Numerical Study on Bubble Formation of a Gas-Liquid Flow in a T-Junction Microchannel
    Dai, Li
    Cai, Wangfeng
    Xin, Feng
    CHEMICAL ENGINEERING & TECHNOLOGY, 2009, 32 (12) : 1984 - 1991
  • [8] T-junction separation modelling in gas-liquid two-phase flow
    Margaris, Dionissios P.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2007, 46 (02) : 150 - 158
  • [9] A general design procedure for gas-liquid Taylor flow T-junction microreactors
    Chang, Yu
    Sheng, Lin
    Deng, Jian
    Luo, Guangsheng
    REACTION CHEMISTRY & ENGINEERING, 2023, 8 (05) : 1192 - 1203
  • [10] Gas-liquid flow in T-junction microfluidic devices with a new perpendicular rupturing flow route
    Tan, J.
    Li, S. W.
    Wang, K.
    Luo, G. S.
    CHEMICAL ENGINEERING JOURNAL, 2009, 146 (03) : 428 - 433