Mechanism of Fine Bubbles Entrapment beneath the Surface of Continuously Cast Slabs

Kasai, Norifumi; Watanabe, Yoshio; Kajiwara, Takaharu; Toyoda, Mamoru

doi:10.2355/tetsutohagane1955.83.1_24

Cited by 14 publications

(8 citation statements)

References 2 publications

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“…Such a temperature difference hardly affects the flow patterns in the pipe. The flow rate of water ranges from 5 to 70 cm 3 /s and that of air ranges from 0.75 to 70 cm 3 /s. (4) The water-air two-phase flow was discharged into the reservoir, and the water was circulated with the pump.…”

Section: Methodsmentioning

confidence: 99%

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Model Experiment on the Behavior of Argon Gas in Immersion Nozzle

Ishiguro

Iguchi

2003

ISIJ International

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Section: Methodsmentioning

confidence: 99%

“…[1][2][3] This is because the adhesion causes a change in the shape and size of the cross section of the nozzle and leads to an uneven discharging flow at the two ports of the nozzle. In the worst case the nozzle clogging takes place.…”

Section: Introductionmentioning

confidence: 99%

Model Experiment on the Behavior of Argon Gas in Immersion Nozzle

Ishiguro

Iguchi

2003

ISIJ International

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“…[7,8] Smaller bubbles are easily captured by the solidified shell, causing segregation, [9] pencil blister, and sliver defects. [10][11][12] Therefore, it is necessary to better understand and optimize the bubble size and distribution in the CC mold to avoid bubble-related defects.The gas injection method, casting parameters, [13,14] nozzle design, [15] physical properties of the gas and liquid phases, [16] and temperature have a great effect on the bubble size and distribution inside the SEN and the CC mold. Water model measurements have shown that bubble diameters decrease with a higher casting speed and submergence depth of the SEN, as well as with a lower gas flow rate.…”

mentioning

confidence: 99%

“…[14,[17][18][19][20] However, the effect of temperature on the bubble size has been rarely studied in the water model of a continuous steel caster. The gas injection method in the water model experiment included the gas channel of the stopper rod, [21][22][23][24][25] small holes or porous refractory in the upper tundish nozzle (UTN), [16,[26][27][28] and the slide gate of the SEN. [11,29] Bai and Thomas [16] investigated the effects of the liquid velocity, gas-injection flow rate, injection hole diameter, and gas composition on the initial bubble-formation behavior. The gas was injected through a square tube below the tundish tank outlet.…”

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Effect of Temperature and Multichannel Stopper Rod on Bubbles in Water Model of a Steel Continuous Caster

Liu

Zhou

Zhang

et al. 2021

steel research int.

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Argon gas has been widely injected into submerged entry nozzles (SENs) to prevent nozzle clogging during the slab continuous casting (CC) process. Meanwhile, argon bubbles also reduce the negative pressure and air aspiration, [1,2] promoting the mixing and flotation of inclusions from the molten steel in the CC mold. [3][4][5][6] Abnormal larger bubbles float up close to the outer wall of the SEN and escape from the top surface quickly, which causes slag entrainment into the molten steel. [7,8] Smaller bubbles are easily captured by the solidified shell, causing segregation, [9] pencil blister, and sliver defects. [10][11][12] Therefore, it is necessary to better understand and optimize the bubble size and distribution in the CC mold to avoid bubble-related defects.The gas injection method, casting parameters, [13,14] nozzle design, [15] physical properties of the gas and liquid phases, [16] and temperature have a great effect on the bubble size and distribution inside the SEN and the CC mold. Water model measurements have shown that bubble diameters decrease with a higher casting speed and submergence depth of the SEN, as well as with a lower gas flow rate. [14,[17][18][19][20] However, the effect of temperature on the bubble size has been rarely studied in the water model of a continuous steel caster. The gas injection method in the water model experiment included the gas channel of the stopper rod, [21][22][23][24][25] small holes or porous refractory in the upper tundish nozzle (UTN), [16,[26][27][28] and the slide gate of the SEN. [11,29] Bai and Thomas [16] investigated the effects of the liquid velocity, gas-injection flow rate, injection hole diameter, and gas composition on the initial bubble-formation behavior. The gas was injected through a square tube below the tundish tank outlet. Kasai and Iguchi [29] obtained the critical value of the water flow rate to carry the gas injected through the slide gate into the mold. The variation of the bubble size inside the SEN and the mold was also studied. [30] Lee et al. [31] investigated the effect of refractory properties on the initial stages of bubble formation. Air was injected through the porous refractory in the center of the UTN wall. For gas injection from the stopper rod tip, single [21,23,31] and multichannel [32,33] blowing methods have been studied in recent years. Gas injection from a single channel created abnormal large bubbles or gas pockets, and produced slug or annular flows inside the SEN, resulting in unstable flow and violent level fluctuations, whereas gas injection from multiple channels produced a more stable surface level in the mold and retarded the clogging on the stopper rod tip. [24] However, studies on the effect of the hole diameter of the gas channel of the stopper rod on the bubble size distribution are little reported.In this study, the bubble size and distribution in the CC mold were investigated and measured using a 0.5-scale water model. First, the effect of the water temperature on the bubble size and

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