Flow regime identification in gas-liquid flow and three-phase fluidized beds

1997 ◽  
Vol 52 (21-22) ◽  
pp. 3979-3992 ◽  
Author(s):  
J.-P. Zhang ◽  
J.R. Grace ◽  
N. Epstein ◽  
K.S. Lim
2020 ◽  
Vol 143 (2) ◽  
Author(s):  
Kwame Sarkodie ◽  
Andrew Fergusson-Rees

Abstract The accurate identification of gas–liquid flow regimes in pipes remains a challenge for the chemical process industries. This paper proposes a method for flow regime identification that combines responses from a nonintrusive optical sensor with linear discriminant analysis (LDA) and quadratic discriminant analysis (QDA) for vertical upward gas–liquid flow of air and water. A total of 165 flow conditions make up the dataset, collected from an experimental air–water flow loop with a transparent test section (TS) of 27.3 mm inner diameter and 5 m length. Selected features extracted from the sensor response are categorized into feature group 1, average sensor response and standard deviation, and feature group 2 that also includes percentage counts of the calibrated responses for water and air. The selected features are used to train, cross validate, and test four model cases (LDA1, LDA2, QDA1, and QDA2). The LDA models produce higher average test classification accuracies (both 95%) than the QDA models (80% QDA1 and 45% QDA2) due to misclassification associated with the slug and churn flow regimes. Results suggest that the LDA1 model case is the most stable with the lowest average performance loss and is therefore considered superior for flow regime identification. In future studies, a larger dataset may improve stability and accuracy of the QDA models, and an extension of the conditions and parameters would be a useful test of applicability.


Author(s):  
Jiarong Zhang ◽  
Li Liu ◽  
Shuai Liu ◽  
Hanyang Gu

Abstract Vertical swirling gas-liquid flow is a kind of complex two-phase flow containing a nonzero tangential velocity component in engineering applications. The accurate flow regime characterization, phase distribution information and pressure drop data about vertical swirling flow are the basis for the optimization of steam generator (SG), which can greatly reduce the cost and improve the safety of nuclear plants. To get these key parameters of swirling vertical flow, we have made a comprehensive visualization experiment in a vertical pipe with 30mm diameter and 5m length by high-speed camera. The experimental pipe is separated into swirling part and non-swirling part. We have set three observation section with different vertical heights in the swirling part. Changing the flow rate of water and gas, different swirling flow pattern photos can be captured by high-speed camera. Based on the photos of different positions and image-processing MATLAB code, we can get three flow regime maps and figure out the decaying law of swirling gas-liquid flow. The pressure drop can be recorded by rotameter at each position. The decaying law of pressrure drop can be concluded from it. These data can be a guide for designing gas-liquid separator in SG to improve the efficiency of nuclear plant.


Author(s):  
K. Ashok Kumar ◽  
S. Lokesh ◽  
K.T.V. Nagendra ◽  
K.V. Ramesh

2012 ◽  
Vol 69 (1) ◽  
pp. 578-586 ◽  
Author(s):  
Xi Wang ◽  
Yumei Yong ◽  
Ping Fan ◽  
Gengzhi Yu ◽  
Chao Yang ◽  
...  

1999 ◽  
Vol 103 (3) ◽  
pp. 243-259 ◽  
Author(s):  
E. Maucci ◽  
C.L. Briens ◽  
R.J. Martinuzzi ◽  
G. Wild

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