ABM Proceedings 2012
DOI: 10.5151/2594-5300-20771
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Distribuição De Gás Inerte Dentro Do Sistema De Refratário Durante O Lingotamento Contínuo De Placas: Modelo Físico E Matemático

Abstract: Distribuição de gás inerte dentro do sistema de refratário durante o lingotamento contínuo de placas [manuscrito] : modelo físico e matemático / Paulo Luiz Santos Junior. -2012.xvii, 83 f. : il. color.; grafs.; tabs.

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“…This in turn demonstrates that the diameter of the bubble in the mold, and the mechanisms that determine this size, rupture and coalescence of the bubbles, is critical in determining the behavior of the continuous phase and dispersed in the mold. This phenomenon was confirmed in a physical model and also been discussed by Banderas et al [13], and Santos et al [9]. Thus the liquid flow rate, for the flow ranges evaluated in this study, influences the process of gas distribution in the mold, besides the direct change of velocity and kinetic energy of the jet at the exit of the nozzle, and also affect the diameter of the bubble in the mold, i.e., higher liquid flows lead to smaller bubble diameters in the mold.…”
Section: A) Comparison Of Results Of Mathematical Modeling and Physicsupporting
confidence: 82%
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“…This in turn demonstrates that the diameter of the bubble in the mold, and the mechanisms that determine this size, rupture and coalescence of the bubbles, is critical in determining the behavior of the continuous phase and dispersed in the mold. This phenomenon was confirmed in a physical model and also been discussed by Banderas et al [13], and Santos et al [9]. Thus the liquid flow rate, for the flow ranges evaluated in this study, influences the process of gas distribution in the mold, besides the direct change of velocity and kinetic energy of the jet at the exit of the nozzle, and also affect the diameter of the bubble in the mold, i.e., higher liquid flows lead to smaller bubble diameters in the mold.…”
Section: A) Comparison Of Results Of Mathematical Modeling and Physicsupporting
confidence: 82%
“…A modification of the central and upper flow was observed at 400l/min, which in turn allowed the formation of a double roll with smaller velocities in the mold and meniscus than in the 336l/min condition. These behaviors were observed in a physical model and discussed by Santos et al [9] and Banderas et al [13]. When comparing the images of Figure 8 of 336 l / min with those of 400 l / min it is seen that the region of the volumetric fraction is much more expanded in the second case.…”
Section: A) Comparison Of Results Of Mathematical Modeling and Physicsupporting
confidence: 66%
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