2020
DOI: 10.3390/ma13225129
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Effects of Multiple-Hole Baffle Arrangements on Flow Fields in a Five-Strand Asymmetric Tundish

Abstract: This paper reports on the re-engineering of standard five-strand tundish designs into a five-strand asymmetric tundish, which resulted in a non-uniform rate and bias for each strand. We sought to improve the casting conditions by optimizing the liquid steel flow-field in the tundish. Both a water modelling experiment and a numerical simulation were performed to analyze the flow-field according to various diversion hole diameters and injection angles. The results showed that the average residence time decreased… Show more

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Cited by 15 publications
(12 citation statements)
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“…The thickness of the dendritic layer eventually increases, thereby clogging the inner wall of the outlet of the steel nozzle, as is shown in Figure 5 . Titanium and aluminum oxides also form inclusions in slabs when molten steel solidifies [ 17 ]. Owing to the low ductility of titanium and aluminum oxide inclusions, interlayer defects form around these inclusions during hot rolling.…”
Section: Resultsmentioning
confidence: 99%
“…The thickness of the dendritic layer eventually increases, thereby clogging the inner wall of the outlet of the steel nozzle, as is shown in Figure 5 . Titanium and aluminum oxides also form inclusions in slabs when molten steel solidifies [ 17 ]. Owing to the low ductility of titanium and aluminum oxide inclusions, interlayer defects form around these inclusions during hot rolling.…”
Section: Resultsmentioning
confidence: 99%
“…According to related studies, four factors, the height of the stabilizer stopper, whether the stabilizer has a hole, the opening type of the double-layer retaining wall, and the opening diameter, will all have an impact on the flow field of the tundish [29][30][31][32], denoted by A, B, C, and D, respectively. The results of the experimental program combination are shown in Table 2.…”
Section: Orthogonal Experimental Design Resultsmentioning
confidence: 99%
“…Usually, the RTD curve of ideal tracer in the mathematical model is validated by experimental data in the water model. [57][58][59] But in fact, there are huge difference between the ideal tracer and the actual tracer. Figure 5 shows that, with the increase of the tracer mass concentration or the tracer volume, the actual RTD curve (with solute buoyancy) changes from single flat peak to single sharp peak and then to double peaks.…”
Section: Mathematical Modelmentioning
confidence: 99%