2020
DOI: 10.1002/srin.202000022
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Numerical Simulation of Tracers Transport Process in Water Model of a Vacuum Refining Unit: Single Snorkel Refining Furnace

Abstract: The improvement of mixing conditions in vacuum refining unit plays an important role in enhancing the purity and decarburization of molten steel. A numerical simulation is established to calculate the transport and mixing process of tracers in a water model of Single‐Snorkel Refining Furnace. The results show that the transport process of tracer in water model consists of one main circulation stream (inside the ladle and the vacuum chamber) and two side circulation streams (inside the ladle). The injection of … Show more

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Cited by 19 publications
(23 citation statements)
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“…Drag force coefficient ( C D ) is determined by the Schiller–Naumann drag model (Kim et al , 2007; Ling and Zhang, 2019): with bubble Reynolds number (Re) (Kishan and Dash, 2006; Zhang et al , 2020): …”
Section: Numerical Simulationmentioning
confidence: 99%
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“…Drag force coefficient ( C D ) is determined by the Schiller–Naumann drag model (Kim et al , 2007; Ling and Zhang, 2019): with bubble Reynolds number (Re) (Kishan and Dash, 2006; Zhang et al , 2020): …”
Section: Numerical Simulationmentioning
confidence: 99%
“…2.1 Co-Ar-molten steel flow Due to the complicated metallurgical phenomena, several assumptions in Table 1 are introduced to reduce the exceedingly heavy computational load (Thomas and Zhang, 2001;Ajmani et al, 2004;Wei and Hu, 2005;Yang et al, 2012;Dai et al, 2020;Zhang et al, 2020). The CO-Ar-molten steel flow can be described by following governing equations: Mixture density (r m ):…”
Section: Numerical Simulationmentioning
confidence: 99%
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“…The Realizable Two-Layer k-ε model, which combines the realizable k-ε model [20] with the two-layer approach proposed by Rodi [21] , is applied to calculate the turbulent flow in tundish. The formula are not reproduced here and can be found in reference [22] . The volume mesh is generated in STAR CCM+, utilizing the trimmer and prism layer meshing options.…”
Section: Cfd Model Descriptionmentioning
confidence: 99%
“…The tracer was added from the feed inlet port on the vacuum chamber sidewall, and the mixing time was defined as the first time when the conductivity stabilized at AE5%, [21,36] AE3%, [37] or AE1%. [38] As the mixing time is related to the location of monitors and the fluid flow field distribution in the ladle, [6] many researchers have given out the mixing time of several points for different positions and various operation conditions. [23,39,40] However, it is difficult to figure out the mixing time distribution on the whole vertical center section in the ladle.…”
mentioning
confidence: 99%