REDA (REVOLUTIONARY DEGASSING ACTIVATOR)

This is a collaborative work between Prof. S. Kitamura’s research group (Tohoku University, Institute of Multidisciplinary Research for Advanced Materials, Sendai, Japan) and our research group (at IISc).  
 
In recent times the demand of ultra-low carbon steel (ULCS) with improved mechanical properties such as good ductility and good workability has been increased as it is used to produce cold-rolled steel sheets for automobiles. For producing ULCS efficiently, it is necessary to improve the productivity of the vacuum degasser such as RH, DH and tank degasser. Recently, it has been claimed that using a new process, called REDA (Revolutionary Degassing Activator), one can achieve the carbon content below 10ppm in less time. As such, REDA process has not been studied thoroughly. Fluid flow phenomena affect the decarburization rate the most besides the chemical reaction rate. Therefore, in this study, momentum balance equations along with k-eps turbulent model have been solved for gas and liquid phases in two-dimension (2D) for REDA process. Similarly, computational fluid dynamic studies have been made in 2D for tank degasser and RH processes to compare them with REDA process. Computational results have been validated with published experimental and theoretical data (Figure 1). It is found that REDA process is the most efficient among all these processes in terms of mixing efficiency. Fluid flow phenomena have been studied in details for REDA process by varying gas flow rate, depth of immersed snorkel in the steel, diameter of the snorkel and change in vacuum pressure. It is found that design of snorkel affects the melt circulation of the bath significantly. Typical contours of average water velocity in REDA process at air flow rate of 6.1 x 10-4 Nm3/s are shown in Figure 2.

     

Figure 1. Comparison of computed velocity field of lower vessel in RH process with K. Shrirabe and J. Szeleky, Transactions ISIJ 23, (1983), p465-474.



Figure 2. Average velocity contours in REDA process at air flow rate of 6.1 x 10-4 Nm3/s and vacuum pressure 0.032 atm. Position of nozzle is shifted 0.1 m right from the center.

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