2015
DOI: 10.1016/j.apm.2015.02.054
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Mathematical modeling of blast furnace burden distribution with non-uniform descending speed

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Cited by 48 publications
(41 citation statements)
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“…First, the smaller coal particles are at the bottom of the chute flow, and then distribute to the inner side of the burden stream. [9,17] Second, after hit the pile, the small particles get trapped in the voids among the large coal particles on the surface and thus percolate toward the center instead of the wall. [11] Third, the larger ones have a larger rolling momentum after colliding with the burden pile and can roll to the outer side of the burden pile.…”
Section: Effect Of the Chute Angle On The Size Segregationmentioning
confidence: 99%
“…First, the smaller coal particles are at the bottom of the chute flow, and then distribute to the inner side of the burden stream. [9,17] Second, after hit the pile, the small particles get trapped in the voids among the large coal particles on the surface and thus percolate toward the center instead of the wall. [11] Third, the larger ones have a larger rolling momentum after colliding with the burden pile and can roll to the outer side of the burden pile.…”
Section: Effect Of the Chute Angle On The Size Segregationmentioning
confidence: 99%
“…Upgrades and modifications have also been made to the BF shaft model, including the implementation of non‐uniform burden descent speed, variable coke and ore layer porosity in the radial and vertical directions, and the mixing layer between coke and iron ore layers in the furnace. Using some of these upgrades, analyses of the impacts of coke layer porosity, coke particle size, and relative burden descent speed on furnace operation were conducted, indicating that decreasing coke particle size could result in a ≈2% reduction in furnace coke consumption for a given operating scenario…”
Section: Cfd Blast Furnace Model Applicationsmentioning
confidence: 99%
“…Therefore, controlling a void fraction in the stacked layer, i.e., the burden distribution at the top of the blast furnace, is the most effective operation for stabilizing the gas flow. Much research has been experimentally conducted and some mathematical models have been proposed to estimate and control the burden distribution [1][2][3][4][5]. These models can give useful information in the daily operation.…”
Section: Introductionmentioning
confidence: 99%