DEM simulations of the particle flow on a centrifugal fertilizer spreader

被引:63
作者
Van Liedekerke, P. [1 ]
Tijskens, E. [1 ]
Dintwa, E. [1 ]
Rioual, F. [2 ]
Vangeyte, J. [3 ]
Ramon, H. [1 ]
机构
[1] Katholieke Univ Leuven, Dept Biosyst, B-3001 Louvain, Belgium
[2] Irstea, UR TSCF, F-03150 Domaine Des Palaquins, Montoldre, France
[3] ILVO, B-9820 Merelbeke, Belgium
关键词
Discrete element method; Granular fertilizer; Centrifugal spreader; Multi particle; SPINNING DISC; ROLLING FRICTION; MODEL;
D O I
10.1016/j.powtec.2008.08.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Usually, the performance of centrifugal spreaders must be evaluated in large halls by capturing the fertilizer distribution patterns in standardized tests, often Carrying a big cost to the manufacturers. In contrast, this paper proposes a first attempt to model a particle flow subjected to a spinning disc using the Discrete Element Method (DEM) starting from the particle outflow of a bin, using flat as well as inclined discs. The model is validated by experiments in two different ways. The first manner is the measurement of the cylindrical mass distribution along the edge of the disc by a device that collects the fertilizer particles in a tray of baskets around the disc. A second method consists of collecting the particles on the ground after their ballistic flight through the air. Both validation methods are relatively cheap and fit into the present statistical or qualitative interpretation of DEM simulations. Additionally, a number of rotational disc speeds is chosen (300-650 rpm) to incorporate velocity dependent effects of the particle flow. It was found that the DEM simulations show a good qualitative and considerable quantitative agreement with the experiments. The deviations between the simulations and experiments are profound at high disc rotational speeds (500650 rpm) and can be identified as (I) an underestimation of the simulated particle velocities at the edge of the disc and (2) a too low dispersion on the (vertical) simulated particle velocities at the edge of the disc, A parameter study revealed that (I) can be resolved by introducing a velocity dependent friction coefficient, in agreement with literature. The influence of other model parameters such as particle damping and stiffness appears to be small, while the introduction of a rolling friction coefficient to mimic rolling resistance or particle shape does not provide any answer either, and hence reason (2) at this moment Must be addressed to unknown external factors such as disc plane vibrations appearing at higher disc speeds. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:348 / 360
页数:13
相关论文
共 26 条
[1]  
Arnold V. I., 1978, Mathematical methods of classical mechanics
[2]   Model for collisions in granular gases [J].
Brilliantov, NV ;
Spahn, F ;
Hertzsch, JM ;
Poschel, T .
PHYSICAL REVIEW E, 1996, 53 (05) :5382-5392
[3]   Rolling friction of a viscous sphere on a hard plane [J].
Brilliantov, NV ;
Poschel, T .
EUROPHYSICS LETTERS, 1998, 42 (05) :511-516
[4]  
DINTWA E, 2006, THESIS KU LEUVEN BEL
[5]  
GARBEROGLIO G, 2001, THESIS U TRENTO
[6]   Measurement of velocity and diameter of individual fertilizer particles by an optical method [J].
Grift, TE ;
Hofstee, JW .
JOURNAL OF AGRICULTURAL ENGINEERING RESEARCH, 1997, 66 (03) :235-238
[7]  
Haug E.J., 1992, INTERMEDIATE DYNAMIC
[8]   HANDLING AND SPREADING OF FERTILIZERS .5. THE SPINNING DISC TYPE FERTILIZER SPREADER [J].
HOFSTEE, JW .
JOURNAL OF AGRICULTURAL ENGINEERING RESEARCH, 1995, 62 (03) :143-162
[9]  
Inns F.M., 1962, J AGR ENG RES, V7, P345
[10]  
Johnson K.L., 1987, Contact Mechanics