Effect of size distribution on mixing of a polydisperse wet granular material in a belt-driven enclosure

被引:11
作者
Mahapatra, Pallab Sinha [1 ,2 ]
Mathew, Sam [1 ]
Panchagnula, Mahesh V. [1 ]
Vedantam, Srikanth [3 ]
机构
[1] Indian Inst Technol, Dept Appl Mech, Madras 600036, Tamil Nadu, India
[2] Univ Illinois, Dept Mech & Ind Engn, Chicago, IL 60607 USA
[3] Indian Inst Technol, Dept Engn Design, Madras 600036, Tamil Nadu, India
关键词
Wet granular mixing; Polydisperse flow; Belt driven enclosure; QUASI 2D PILES; ROTATING DRUM; SEGREGATION; SIMULATION; PARTICLES; DYNAMICS; FLOW; SYSTEMS; DEM;
D O I
10.1007/s10035-016-0633-1
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
We use a recently developed coupled fluid-particle discrete element model to study mixing of a wet granular material in a two dimensional setting. The particles are modeled as linearly elastic disks and are considered to be immersed in a Newtonian fluid. The fluid-particle interaction is modeled using a linear drag model under the assumption that the fluid inertia is small compared to particle inertia. The granular slurry is driven by a belt moving at constant velocity in a square cavity. In the simulations, we consider three types of size distributions: monodisperse, bidisperse with several particle size ratios, and polydisperse Gaussian distributions with several different standard deviations. Mixing is characterized using both strong and weak measures. Size segregation is observed only in the bidisperse simulations. The energy required for mixing polydisperse slurries decreases with increasing standard deviation of the particle sizes. Finally, we show the benefits of engineering certain polydisperse particle size distributions towards minimizing energy consumption.
引用
收藏
页数:12
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共 37 条
[31]  
Qingqing Y., 2015, GEOENVIRON DISASTERS, V2, P1
[32]   Polydisperse granular flows in a bladed mixer: Experiments and simulations of cohesionless spheres [J].
Remy, Brenda ;
Khinast, Johannes G. ;
Glasser, Benjamin J. .
CHEMICAL ENGINEERING SCIENCE, 2011, 66 (09) :1811-1824
[33]   Dynamical effects in the segregation of granular mixtures in quasi 2D piles [J].
Rodriguez, D. ;
Benito, J. G. ;
Ippolito, I. ;
Hulin, J. -P. ;
Vidales, A. M. ;
Unac, R. O. .
POWDER TECHNOLOGY, 2015, 269 :101-109
[34]   Experimental and numerical investigation into the residence time distribution of granular particles on forward and reverse acting grates [J].
Samiei, K. ;
Peters, B. .
CHEMICAL ENGINEERING SCIENCE, 2013, 87 :234-245
[35]   A COMPUTER-SIMULATION METHOD FOR THE CALCULATION OF EQUILIBRIUM-CONSTANTS FOR THE FORMATION OF PHYSICAL CLUSTERS OF MOLECULES - APPLICATION TO SMALL WATER CLUSTERS [J].
SWOPE, WC ;
ANDERSEN, HC ;
BERENS, PH ;
WILSON, KR .
JOURNAL OF CHEMICAL PHYSICS, 1982, 76 (01) :637-649
[36]   Behaviour of macroscopic rigid spheres in lid-driven cavity flow [J].
Tsorng, S. J. ;
Capart, H. ;
Lo, D. C. ;
Lai, J. S. ;
Young, D. L. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2008, 34 (01) :76-101
[37]   Numerical simulation of three-dimensional unsteady granular flows in rotary kiln [J].
Yin, Hongchao ;
Zhang, Ming ;
Liu, Hong .
POWDER TECHNOLOGY, 2014, 253 :138-145