This paper describes an experimental investigation on the flow characteristics within a rotating cylinder containing a rolling bed of sand. The axis of the cylinder was horizontal and there was no axial bulk flow of particles. The velocity field of the gas flowing through the cylinder was measured b
Avalanche Time of Granular Flows in Rotary Kilns
β Scribed by X. Liu; S. Zhou; E. Specht
- Publisher
- John Wiley and Sons
- Year
- 2010
- Tongue
- English
- Weight
- 245 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0930-7516
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β¦ Synopsis
Abstract
Discrete avalanching is the dominant motion of granular beds in industrial rotary kilns. The avalanche time is an important parameter influencing the heatβ and material transfer inside the kiln. Experiments are conducted on a rotating cylinder to measure the time evolution of avalanches. Nonspherical particles (rice) and low filling degrees are used in order to simulate the operating conditions in industrial kilns. The difference between the average critical angle and stop angle of the avalanche is found to be in the range of 7Β°β9Β°, i.e., much higher values than ever reported in literature. As the filling degree is three times increased, the average critical angle is found to be approximately constant, whereas the average stop angle is slightly increased and the avalanche time is increased by 20β%. For all experimental configurations, the average avalanche time occupies about 35β%β38β% of the total circle time (elevation time plus avalanche time). Experimental data are used to test theoretical models from different authors. Comparison demonstrates that the models proposed by Mellmann and Davidson et al. can predict well the increasing tendency of average avalanche time with filling degrees. The former has higher accuracy with errors less than 5β% for all experiments. Results of this work are useful for kiln design and further theoretical studies on dynamics of granular avalanches.
π SIMILAR VOLUMES
A non linear model proposed by Perron and Bui (1994), which focuses on the dynamics of slow mode to predict the transient response induced by step changes in operating variables in the motion of the granular bed in a rotary kiln, was validated for different experimental conditions. The variables inc
Starting from a simple mechanism of the movement of granular solids in a rotating cylinder, as first indicated by VBIIL, formulae are derived for the hold-up of an inclined rotary kiln, with and without end constrictions. A good agreement is found between the theoretical values and the experimental
The two-dimenslonal flow of a mass of cohesionless granular materiaI down a rough bed is studied by the use of the method of strMned coordinates. The work is relevant to the motion of rockfalls, ice avalanches and dense flowing snow avalanches. By appropriate non-dimensionalization, a small paramete