2021
DOI: 10.1007/s11661-021-06428-w
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Determining Drag Coefficient of Simplified Dendritic Particles in Metallurgical Systems

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Cited by 2 publications
(1 citation statement)
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“…[5][6][7][8] Acid leaching for removing the P-rich phase [9][10][11] requires energy intensive conditions such as crushing/grinding and low cooling rate presenting economical restrictions to its industrial application. Separation due to gravity by floating of the C 2 S-C 3 P crystals was shown possible under a low cooling rate of below 2 °C/m [8,[12][13][14] which could only be implemented under controlled cooling. Ideally separation should be undertaken whilst the slag is in the liquid state so that crushing or grinding are not be required.…”
Section: Introductionmentioning
confidence: 99%
“…[5][6][7][8] Acid leaching for removing the P-rich phase [9][10][11] requires energy intensive conditions such as crushing/grinding and low cooling rate presenting economical restrictions to its industrial application. Separation due to gravity by floating of the C 2 S-C 3 P crystals was shown possible under a low cooling rate of below 2 °C/m [8,[12][13][14] which could only be implemented under controlled cooling. Ideally separation should be undertaken whilst the slag is in the liquid state so that crushing or grinding are not be required.…”
Section: Introductionmentioning
confidence: 99%