Two-Way PBM-Euler Model for Gas and Liquid Flow in the Ladle

被引:3
作者
Zhang, Han [1 ,2 ]
Lei, Hong [1 ,2 ]
Ding, Changyou [1 ,2 ]
Chen, Shifu [1 ,3 ]
Xiao, Yuanyou [1 ,4 ]
Li, Qiang [2 ]
机构
[1] Northeastern Univ, Minist Educ, Key Lab Electromagnet Proc Mat, Shenyang 110004, Peoples R China
[2] Northeastern Univ, Sch Met, Shenyang 110004, Peoples R China
[3] Suzhou Univ, Sch Chem & Chem Engn, Suzhou 234000, Peoples R China
[4] Univ Sci & Technol Liaoning, Sch Mat & Met, Anshan 114000, Peoples R China
基金
中国国家自然科学基金;
关键词
PBM; coalescence model; two-phase flow; bubble behavior; gas-stirred ladle; OpenFOAM; POPULATION BALANCE-EQUATIONS; OXIDE INCLUSIONS; 2-PHASE FLOW; MULTIPHASE FLOW; COUPLED MODEL; SIMULATION; BEHAVIOR; SIZE; CFD; DISCRETIZATION;
D O I
10.3390/ma16103782
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Ladle metallurgy is an important steelmaking technology in high-quality steel production. The blowing of argon at the ladle bottom has been applied in ladle metallurgy for several decades. Until now, the issue of breakage and coalescence among bubbles was still far from being solved. In order to have a deep insight into the complex process of fluid flow in the gas-stirred ladle, the Euler-Euler model and population balance model (PBM) are coupled to investigate the complex fluid flow in the gas-stirred ladle. Here, the Euler-Euler model is applied to predict the two-phase flow, and PBM is applied to predict the bubble and size distribution. The coalescence model, which considers turbulent eddy and bubble wake entrainment, is taken into account to determine the evolution of the bubble size. The numerical results show that if the mathematical model ignores the breakage of bubbles, the mathematical model gives the wrong bubble distribution. For bubble coalescence in the ladle, turbulent eddy coalescence is the main mode, and wake entrainment coalescence is the minor mode. Additionally, the number of the bubble-size group is a key parameter for describing the bubble behavior. The size group number 10 is recommended to predict the bubble-size distribution.
引用
收藏
页数:17
相关论文
共 38 条
[1]   PLUME CHARACTERISTICS AND LIQUID CIRCULATION IN GAS INJECTION THROUGH A POROUS PLUG [J].
ANAGBO, PE ;
BRIMACOMBE, JK .
METALLURGICAL TRANSACTIONS B-PROCESS METALLURGY, 1990, 21 (04) :637-648
[2]   Three-dimensional mathematical modeling of dispersed two-phase flow using class method of population balance in bubble columns [J].
Bannari, Rachid ;
Kerdouss, Fouzi ;
Selma, Brahim ;
Bannari, Abdelfettah ;
Proulx, Pierre .
COMPUTERS & CHEMICAL ENGINEERING, 2008, 32 (12) :3224-3237
[3]   Coupling of CFD and PBE Calculations to Simulate the Behavior of an Inclusion Population in a Gas-Stirring Ladle [J].
Bellot, Jean-Pierre ;
De Felice, Valerio ;
Dussoubs, Bernard ;
Jardy, Alain ;
Hans, Stephane .
METALLURGICAL AND MATERIALS TRANSACTIONS B-PROCESS METALLURGY AND MATERIALS PROCESSING SCIENCE, 2014, 45 (01) :13-21
[4]   Application of Inhomogeneous Discrete Method to the Simulation of Transport, Agglomeration, and Removal of Oxide Inclusions in a Gas-Stirred Ladle [J].
Chen, Gujun ;
He, Shengping .
JOM, 2019, 71 (11) :4206-4214
[5]   Two-way coupling calculation for multiphase flow and decarburization during RH refining [J].
Chen, Shi-Fu ;
Lei, Hong ;
Wang, Meng ;
Yang, Bin ;
Dai, Li-Jun ;
Zhao, Yan .
VACUUM, 2019, 167 :255-262
[6]   Behaviour of Oxide Inclusions in Liquid Steel: Multi-QMOM Simulation [J].
Claudotte, L. ;
Rimbert, N. ;
Gardin, P. ;
Simonnet, M. ;
Lehmann, J. ;
Oesterle, B. .
STEEL RESEARCH INTERNATIONAL, 2010, 81 (08) :630-636
[7]   3D Modeling of the Aggregation of Oxide Inclusions in a Liquid Steel Ladle: Two Numerical Approaches [J].
Daoud, Ismael Lis Alves ;
Rimbert, Nicolas ;
Jardy, Alain ;
Oesterle, Benoit ;
Hans, Stephane ;
Bellot, Jean-Pierre .
ADVANCED ENGINEERING MATERIALS, 2011, 13 (07) :543-549
[8]   Dynamic simulation of dispersed gas-liquid two-phase flow using a discrete bubble model [J].
Delnoij, E ;
Lammers, FA ;
Kuipers, JAM ;
vanSwaaij, WPM .
CHEMICAL ENGINEERING SCIENCE, 1997, 52 (09) :1429-1458
[9]   Validation of CFD models for mono- and polydisperse air-water two-phase flows in pipes [J].
Frank, Th. ;
Zwart, P. J. ;
Krepper, E. ;
Prasser, H. -M. ;
Lucas, D. .
NUCLEAR ENGINEERING AND DESIGN, 2008, 238 (03) :647-659
[10]   Two-group interfacial area transport equations at bubbly-to-slug flow transition [J].
Hibiki, T ;
Ishii, M .
NUCLEAR ENGINEERING AND DESIGN, 2000, 202 (01) :39-76