2021
DOI: 10.1007/s42461-021-00388-w
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Development of a Non-linear Framework for the Prediction of the Particle Size Distribution of the Grinding Products

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Cited by 4 publications
(12 citation statements)
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“…More specifically, it has been proven that the total amount of energy used by the mining and minerals industry is 4-7% of the global energy output [13]. For a typical grinding circuit, the average energy consumption can be as high as 6700 kWh/kt, and represents almost 50% of the total energy consumption in the mining industry [14,15]. This high energy consumption and the associated CO 2 emissions from comminution circuits can be reduced if the grinding behavior of the feed is carefully investigated as a function of the operating parameters of the crusher/mill.…”
Section: Introductionmentioning
confidence: 99%
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“…More specifically, it has been proven that the total amount of energy used by the mining and minerals industry is 4-7% of the global energy output [13]. For a typical grinding circuit, the average energy consumption can be as high as 6700 kWh/kt, and represents almost 50% of the total energy consumption in the mining industry [14,15]. This high energy consumption and the associated CO 2 emissions from comminution circuits can be reduced if the grinding behavior of the feed is carefully investigated as a function of the operating parameters of the crusher/mill.…”
Section: Introductionmentioning
confidence: 99%
“…The PBM, also referred to as the linear time-invariant (LTINV) model, which considers that the breakage rate remains constant during grinding has been adopted by many researchers [22][23][24][25], while in other studies a deviation from the linear kinetic approach has been experimentally observed [26][27][28]. Recently, Petrakis and Komnitsas [15] used the PBM as partial case and developed a non-linear framework for the prediction of the particle size distribution of the grinding products. Nevertheless, the linear kinetic approach has been successfully used for understanding the effect of operating parameters, e.g., ball size, mill speed, media shape, and ball/powder filling, on the grinding efficiency of ball mills [29][30][31][32][33][34][35].…”
Section: Introductionmentioning
confidence: 99%
“…In addition, the same figure reveals that the deviation from the linear theory is more evident for the larger particle sizes which are ground more efficiently than finer particles. The non-linearity of batch grinding systems has been experimentally observed by many researchers [34,35,49]. By comparing the plots of the remaining mass (%) fraction vs. grinding time obtained using different f c values (Figure 3a-c), it appears that for a certain grinding time, lower f c values result in a smaller amount of material which remains in each particle size.…”
Section: Resultsmentioning
confidence: 55%
“…where K is the grinding rate constant and t is the grinding time. Despite the fact that the first-order hypothesis is the most widely used approach to describe the grinding process in a ball mill and many studies have pointed out its advantages [31,32], deviation from the linear kinetics has been experimentally observed in several cases when different materials are used [33][34][35]. Based on the non-linear behavior, Alyavdin proposed that the following formula (Equation ( 3)) can be used in batch milling processes [36,37]:…”
Section: Introductionmentioning
confidence: 99%
“…Recently, Petrakis and Komnitsas [33] developed a nonlinear framework for the prediction of the particle size distribution of the grinding products, where the linear theory of PBM was considered as a partial case. Based on this approach, the fundamental batch grinding mass balance equation was transformed into the well-known (6)…”
mentioning
confidence: 99%