2018
DOI: 10.1016/j.apt.2017.11.001
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Dry grinding in planetary ball mills: Evaluation of a stressing model

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Cited by 55 publications
(58 citation statements)
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“…Figure 3 shows the effect of the polymer feed load on the temporal evolution of the particle size. As expected, a slower reduction of x 50,3 over time is observed with an increase in the feed load [46,47,60]. For prolonged grinding (c.f.…”
Section: Resultssupporting
confidence: 53%
See 1 more Smart Citation
“…Figure 3 shows the effect of the polymer feed load on the temporal evolution of the particle size. As expected, a slower reduction of x 50,3 over time is observed with an increase in the feed load [46,47,60]. For prolonged grinding (c.f.…”
Section: Resultssupporting
confidence: 53%
“…The acceleration, α , is calculated using the effective radius of the revolution, R , which is 70 mm for the used mill, and the angular velocity, ω, to the power of 2. Using the parameters described above, the maximum stress energy, E kin , of a single grinding bead is around 11.8 mJ, however, the effective stress energy a particle experiences typically will be much lower (see e.g., [46,47]). The temperature inside of the grinding vessel was measured every 20 min cycle for 240 min (i.e., 12 grinding cycles); after 60 min, the temperature remained at 40 °C for the rest of the experiment.…”
Section: Methodsmentioning
confidence: 99%
“…The results revealed that, during the milling process, the size of the milling media changed, whereas the material composing the media remained unchanged. Milling media are simulated as discrete elements and the compression and shear forces for each impact are determined by Hertz and Mindlin's contact model, and the resulting velocity is calculated according to Newton's law of motion in the DEM simulation [22]. In order to explore the motion of the balls in a ball milling process, we performed the ball impact energy estimated by a DEM simulation.…”
Section: Resultsmentioning
confidence: 99%
“…However, in-situ observations have not shown signs of balls leaving the vial surface to make clear single collisions; the actual situation is much more complex with multiple types of ball-ball and ball-vial interactions [7, 8, 9]. Nowadays, most of the studies use numerical simulations of the collective three-dimensional ball motion based on the Discrete Element Model (DEM) [10, 11, 12], since it is possible to quantify in a more precise way the effects of successive small collisions between balls, the lack of single ball-wall collisions and the slipping and rolling of balls, situations that occur in real milling conditions [11, 13].…”
Section: Introductionmentioning
confidence: 99%
“…In all these studies, the key role played by the rotational speed of the planetary mill and the number and nature of balls (and indirectly the ball-to-powder ratio, BPR) have always been highlighted since these parameters determine greatly the rate of the energy transfer to the powder material. Nevertheless, the influence of the ratio ( k ) between the rotational speed of the supporting disc ( ω d ) and vials ( ω v ), ( k = -ω v /ω d ), on the milling efficiency has not been frequently addressed [5, 6, 7, 8, 9, 10, 11, 14, 15, 16, 17]. The main reason is that most commercial planetary mills, especially at a laboratory scale, are characterised by a fixed transmission ratio that sets this k parameter to a value of approximately 1.…”
Section: Introductionmentioning
confidence: 99%