Mathematical Model for Three-Phase Compressible Dual Porosity Streamline Simulation

Author(s):  
A. Myasnikov ◽  
A. Kozlova ◽  
F. Bratvedt ◽  
K. Bratvedt
2006 ◽  
Author(s):  
Antonina Kozlova ◽  
Frode Bratvedt ◽  
Kyrre Bratvedt ◽  
Artem Myasnikov

2016 ◽  
Vol 22 (98) ◽  
pp. 56-61
Author(s):  
Vladislav A. Kosenko ◽  
◽  
Valeriy O. Kvashnin ◽  

2014 ◽  
Vol 651-653 ◽  
pp. 428-431
Author(s):  
Xia Zhao

Taking Model DK-52 (Grade 0.05) multi-function three-phase electrical measuring instrument calibration device as an example, the paper describes how to evaluate the uncertainty in measurement result of indication errors in mathematical model.


2016 ◽  
Author(s):  
Boonruang Wangsilabatra ◽  
Satean Tunyasrirut ◽  
Wachirapond Permpoonsinsup

2020 ◽  
Vol 13 (1) ◽  
pp. 234-239
Author(s):  
Clemence Raïssa Tchatchouang Simo ◽  
Odette Ngano Samba ◽  
Pierre Kisito Talla ◽  
Lukong Cornelius Fai

2016 ◽  
Vol 1812 ◽  
pp. 29-34
Author(s):  
Juan A. López ◽  
Marco A. Ramírez-Argáez ◽  
Adrián M. Amaro-Villeda ◽  
Carlos González

ABSTRACTA very realistic 1:17 scale physical model of a 140-ton gas-stirred industrial steel ladle was used to evaluate flow patterns measured by Particle Image Velocimetry (PIV), considering a three-phase system (air-water-oil) to simulate the argon-steel-slag system and to quantify the effect of the slag layer on the flow patterns. The flow patterns were evaluated for a single injector located at the center of the ladle bottom with a gas flow rate of 2.85 l/min, with the presence of a slag phase with a thickness of 0.0066 m. The experimental results obtained in this work are in excellent agreement with the trends reported in the literature for these gas-stirred ladles. Additionally, a mathematical model was developed in a 2D gas-stirred ladle considering the three-phase system built in the physical model. The model was based on the Eulerian approach in which the continuity and the Navier Stokes equations are solved for each phase. Therefore, there were three continuity and six Navier-Stokes equations in the system. Additionally, turbulence in the ladle was computed by using the standard k-epsilon turbulent model. The agreement between numerical simulations and experiments was excellent with respect to velocity fields and turbulent structure, which sets the basis for future works on process analysis with the developed mathematical model, since there are only a few three-phase models reported so far in the literature to predict fluid dynamics in gas-stirred steel ladles.


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