The kinetics of reoxidation of Al killed steel with slag and air were inves
tigated in laboratory experiments using tammann furnace and in plant experi
ments using commercial 85 x 10(3) kg tundish. Experimental results were dis
cussed by the coupled reaction model.
Observed apparent rate constants of [sol.Al] decreased with increasing (CaO
)/(SiO2) ratio in laboratory experiments and showed a good agreement with c
alculated ones.
Flow rate of air leak at steady state was evaluated to be 3.0 x 10(-5) and
4.0 x 10(-4) m(3)/s inside and outside of immersion tube in commercial tund
ish, respectively and was estimated to have little influence on reoxidation
.
Mass transfer coefficient in metal was estimated to be 6.0 x 10(-5) m/s bas
ed on the tundish mixing model and the coupled reaction model.
Observed [sol.Al] in tundish decreased with increasing (%FeO)+(%MnO) value
in ladle slag and showed a good agreement with calculated one by considerin
g reoxidation in ladle and air leak at unsteady state.