2017
DOI: 10.2355/isijinternational.isijint-2016-511
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Numerical Simulation on Bubble Behavior of Disintegration and Dispersion in Stirring-Injection Magnesium Desulfurization Process

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Cited by 17 publications
(16 citation statements)
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“…Various means to improve the fluid flow conditions have been studied using numerical modeling. As for the impeller, the studied aspects include the effect of the impeller geometry, the impeller depth, the impeller rotation rate, the variable impeller rotation rate, and the variable impeller rotation direction …”
Section: Modeling Of Fluid Flow Phenomenamentioning
confidence: 99%
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“…Various means to improve the fluid flow conditions have been studied using numerical modeling. As for the impeller, the studied aspects include the effect of the impeller geometry, the impeller depth, the impeller rotation rate, the variable impeller rotation rate, and the variable impeller rotation direction …”
Section: Modeling Of Fluid Flow Phenomenamentioning
confidence: 99%
“…Their results indicate that the geometry of the impeller has a significant effect on the bubble dispersion and disintegration, gas–liquid mass transfer and power consumption. Ji et al coupled a Euler–Euler model with a bubble population model to study the bubble size distribution and the related break‐up and coalesce effects in a physical model of a KR. The results suggest that increasing the rotation speed of the impeller increased the bubble disintegration and dispersion in clockwise–anticlockwise and clockwise variable‐speed rotation modes .…”
Section: Modeling Of Fluid Flow Phenomenamentioning
confidence: 99%
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