Theoretical and experimental studies were carried out to quantitativel
y understand the effect of fluid flow on the decarburization reaction
rate in an RH degasser. Hydrodynamic calculations on fluid flow in the
ladle were proved reasonable by a cold model experiment. The decarbur
ization model in conjuction with the fluid flow by hydrodynamic calcul
ations in the ladle made it clear that the decarburization rate obtain
ed from this model was faster than that for perfectly mixed flow, and
slower than that for plug flow when the same parameters were used for
the calculations. The decarburization model enabled us to predict the
concentration distribution of carbon in the ladle during an RH treatme
nt. The maximum carbon content, which was found in the recirculating z
one in the ladle, reached about twice the minimum value obtained in th
e region just below the down-leg. No dead zone existed which would dis
turb the decarburization rate in the process, and it was also made cle
ar that the shape of ladle had little effect on the decarburization ra
te.