Simulation of Particle-laden Turbulent Flow in OpenFOAM

被引:0
作者
Jaiswal, Atul [1 ]
Minh Duc Bui [1 ]
Rutschmann, Peter [1 ]
机构
[1] Tech Univ Munich TUM, Munich, Germany
来源
PROCEEDINGS OF THE 39TH IAHR WORLD CONGRESS | 2022年
关键词
Particle-laden turbulent flow; RANS-DEM; Dispersion model; OpenFOAM;
D O I
10.3850/IAHR-39WC2521716X20221242
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Our work attempts to provide a comprehensive analysis of modelling two-phase flows (fluid-particle) with regard to computational requirements, available models, challenges and limitations. The adopted case (particle-laden backward facing step (BFS) flow) is numerically simulated in the framework of Eulerian-Lanrangian method (RANS-DEM) using OpenFOAM. Firstly, the case was simulated as single-phase (fluid without particles) using solver pimpleFOAM in order to define the simulation parameters and the meshing requirement, giving good agreement with the measured fluid velocity profiles in the experiment. Later on, the case was modified as a two-phase system by including the particles and simulated using two similar yet different solvers namely DPMFoam (standard OpenFOAM solver) and pimpleLPTFoam (self-compiled solver). The simulation results obtained from these two solvers demonstrate almost no difference due to small concentration of particles, indicating that one can save significant computational resources by not considering void fraction in the governing fluid flow equations. Investigation on the coupling regime demonstrates almost no difference in predicted fluid and particle velocity profiles corresponding 1-way and 2-way coupling, as the small number of particles in each CFD cell are unable to modify flow fields significantly. Analysis on different initial velocities of particles shows that by proving zero initial velocity to the particles, they get the opportunity to attain the real velocity depending upon the flow around them and the particle response time (Stokes number). Our study shows that RANS-DEM with simple dispersion models is unable to predict the particle dispersion correctly, thus more sophisticated dispersion models are required.
引用
收藏
页码:4328 / 4335
页数:8
相关论文
共 21 条
[1]  
Brennen ChristopherE., 2005, Fundamentals of Multiphase Flows
[2]   Efficient simulation of particle-laden turbulent flows with high mass loadings using LES [J].
Breuer, Michael ;
Alletto, Michael .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2012, 35 :2-12
[3]   An Euler-Lagrange strategy for simulating particle-laden flows [J].
Capecelatro, Jesse ;
Desjardins, Olivier .
JOURNAL OF COMPUTATIONAL PHYSICS, 2013, 238 :1-31
[4]  
Crowe CT, 2012, MULTIPHASE FLOWS WITH DROPLETS AND PARTICLES, 2ND EDITION, P17
[5]   A novel two-grid formulation for fluid-particle systems using the discrete element method [J].
Deb, Surya ;
Tafti, Danesh K. .
POWDER TECHNOLOGY, 2013, 246 :601-616
[6]   Discrete particle model for sheet flow sediment transport in the nearshore [J].
Drake, TG ;
Calantoni, J .
JOURNAL OF GEOPHYSICAL RESEARCH-OCEANS, 2001, 106 (C9) :19859-19868
[7]  
ELGHOBASHI S, 1994, PREDICTING PARTICLE, V52, P309
[8]   DEM-CFD simulations of fixed bed reactors with small tube to particle diameter ratios [J].
Eppinger, T. ;
Seidler, K. ;
Kraume, M. .
CHEMICAL ENGINEERING JOURNAL, 2011, 166 (01) :324-331
[9]   Turbulence modification by particles in a backward-facing step flow [J].
Fessler, JR ;
Eaton, JK .
JOURNAL OF FLUID MECHANICS, 1999, 394 :97-117
[10]   DEM-CFD modeling of a fluidized bed spray granulator [J].
Fries, L. ;
Antonyuk, S. ;
Heinrich, S. ;
Palzer, S. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (11) :2340-2355