CFD modeling of multiphase flow in an alkaline water electrolyzer

2020 ◽  
Vol 227 ◽  
pp. 115926 ◽  
Author(s):  
A. Zarghami ◽  
N.G. Deen ◽  
A.W. Vreman
Processes ◽  
2021 ◽  
Vol 9 (6) ◽  
pp. 1048
Author(s):  
Xipeng Guo ◽  
Joel Godinez ◽  
Nicholas J. Walla ◽  
Armin K. Silaen ◽  
Helmut Oltmann ◽  
...  

In a steel-refining ladle, the properties of manufactured steel can be notably degraded due to the presence of excessive inclusions. Stirring via gas injection through a porous plug is often used as part of the steel-refining process to reduce these inclusions. In this paper, 3D computational fluid dynamics (CFD) modeling is used to analyze transient multiphase flow and inclusion removal in a gas-stirred ladle. The effects of gas stirring with bubble-inclusion interaction are analyzed using the Euler–Euler approach for multiphase flow modeling, while the effects of inclusions aggregation and removal are modeled via a population balance model (PBM).


Processes ◽  
2020 ◽  
Vol 8 (12) ◽  
pp. 1634
Author(s):  
Jesús Rodríguez ◽  
Ernesto Amores

Although alkaline water electrolysis (AWE) is the most widespread technology for hydrogen production by electrolysis, its electrochemical and fluid dynamic optimization has rarely been addressed simultaneously using Computational Fluid Dynamics (CFD) simulation. In this regard, a two-dimensional (2D) CFD model of an AWE cell has been developed using COMSOL® software and then experimentally validated. The model involves transport equations for both liquid and gas phases as well as equations for the electric current conservation. This multiphysics approach allows the model to simultaneously analyze the fluid dynamic and electrochemical phenomena involved in an electrolysis cell. The electrical response was evaluated in terms of polarization curve (voltage vs. current density) at different operating conditions: temperature, electrolyte conductivity, and electrode-diaphragm distance. For all cases, the model fits very well with the experimental data with an error of less than 1% for the polarization curves. Moreover, the model successfully simulates the changes on gas profiles along the cell, according to current density, electrolyte flow rate, and electrode-diaphragm distance. The combination of electrochemical and fluid dynamics studies provides comprehensive information and makes the model a promising tool for electrolysis cell design.


2007 ◽  
Author(s):  
Yong Yi ◽  
Madhusudhana Reddy ◽  
Mark Jarrett ◽  
Pin Shyu ◽  
Cletus Kinsey ◽  
...  

2018 ◽  
Vol 8 (3) ◽  
pp. 603-620 ◽  
Author(s):  
Wenxiao Pan ◽  
Janine Galvin ◽  
Wei Ling Huang ◽  
Zhijie Xu ◽  
Xin Sun ◽  
...  

2001 ◽  
Vol 66 (2-4) ◽  
pp. 209-218 ◽  
Author(s):  
Y Jiang ◽  
Mohan R Khadilkar ◽  
Muthanna H Al-Dahhan ◽  
Milorad P Dudukovic

2014 ◽  
Vol 62 ◽  
pp. 43-54 ◽  
Author(s):  
Shibo Kuang ◽  
Z. Qi ◽  
A.B. Yu ◽  
A. Vince ◽  
G.D. Barnett ◽  
...  

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