Stable mesh-free moving particle semi-implicit method for direct analysis of gas-liquid two-phase flow

被引:25
作者
Natsui, Shungo [1 ]
Takai, Hifumi [1 ]
Kumagai, Takehiko [1 ]
Kikuchi, Tatsuya [1 ]
Suzuki, Ryosuke O. [1 ]
机构
[1] Hokkaido Univ, Fac Engn, Div Engn & Mat Sci, Kita Ku, Sapporo, Hokkaido 0608628, Japan
基金
日本科学技术振兴机构;
关键词
Material processing; Moving particle semi-implicit method; Gas-liquid flow; Incompressible flow; Dispersion; FREE-BOUNDARY PROBLEMS; PACKED-BED; INCOMPRESSIBLE FLUID; NUMERICAL-SIMULATION; MULTIPHASE FLOWS; BLAST-FURNACE; SOLID FLOW; MPS METHOD; HYDRODYNAMICS; BUBBLES;
D O I
10.1016/j.ces.2014.02.038
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In a metallurgical process, gas-liquid flow plays an important role in increasing the efficiency by stirring liquid mechanically or by injecting a gas. Owing to the difficulty of direct observation in a high-temperature system or real furnace experiment, numerical analysis is useful and widely studied. However, flexible treatment of complicated free surface behavior such as fragmentation and coalescence of liquids is still a difficult problem. This paper presents a new particle-based simulation scheme for gas-liquid flow. We improved the numerical stability, which is generally a problem with the particle method, and verified the model's accuracy for fundamental gas-liquid flow analysis. Because all the phases were discretized as particles in Moving Particle Semi-implicit (MPS) method, the proposed model can track the movement of both the gas and liquid phases directly. A large difference in the real density between the gas and liquid phases makes the gas-liquid interface behavior unstable. This study proposed an optimization of the weakly compressible Poisson equation, an initial particle arrangement, and a smoothed interface density in order to stabilize the multi-density Row analysis. This model guarantees conservation of the fluid volume even for a high-density-ratio flow like that at a gas-liquid interface. Therefore, a gas-liquid interface has been represented with high accuracy. We believe that this scheme is also applicable to phenomena in an actual process that includes many dispersal phases. (c) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:286 / 298
页数:13
相关论文
共 50 条
[1]  
[Anonymous], 1978, BUBBLES DROPS PARTIC
[2]  
Bird R.B., 2006, TRANSPORT PHENOMENA, P554
[3]   NUMERICAL COMPUTATION OF FREE BOUNDARY FOR 2-DIMENSIONAL STEFAN PROBLEM BY SPACE-TIME FINITE-ELEMENTS [J].
BONNEROT, R ;
JAMET, P .
JOURNAL OF COMPUTATIONAL PHYSICS, 1977, 25 (02) :163-181
[4]   Numerical simulation of interfacial flows by smoothed particle hydrodynamics [J].
Colagrossi, A ;
Landrini, M .
JOURNAL OF COMPUTATIONAL PHYSICS, 2003, 191 (02) :448-475
[5]   Particle packing algorithm for SPH schemes [J].
Colagrossi, Andrea ;
Bouscasse, B. ;
Antuono, M. ;
Marrone, S. .
COMPUTER PHYSICS COMMUNICATIONS, 2012, 183 (08) :1641-1653
[6]   Incorporation of diffuse interface in smoothed particle hydrodynamics: Implementation of the scheme and case studies [J].
Das, A. K. ;
Das, P. K. .
INTERNATIONAL JOURNAL FOR NUMERICAL METHODS IN FLUIDS, 2011, 67 (06) :671-699
[7]   Bubble Evolution and Necking at a Submerged Orifice for the Complete Range of Orifice Tilt [J].
Das, Arup K. ;
Das, Prasanta K. .
AICHE JOURNAL, 2013, 59 (02) :630-642
[8]   Key issues in the particle method for computation of wave breaking [J].
Gotoh, H ;
Sakai, T .
COASTAL ENGINEERING, 2006, 53 (2-3) :171-179
[9]  
GRACE JR, 1973, T I CHEM ENG-LOND, V51, P116
[10]   Viscous bubbly flows simulation with an interface SPH model [J].
Grenier, N. ;
Le Touze, D. ;
Colagrossi, A. ;
Antuono, M. ;
Colicchio, G. .
OCEAN ENGINEERING, 2013, 69 :88-102