An analysis of high-temperature multiphase processes shows considerable dev
iations from thermodynamic and chemical equilibrium. These can be attribute
d to limited heat and mass transfer, e.g., caused by incomplete mixing. A m
odelling technique is developed to enable the calculation of such complex n
on-equilibrium phenomena. With this technique, a process is simulated using
an appropriate arrangement of simple, local equilibrium reactors coupled b
y defined heat and mass exchange. As an example, the simulation of an LD-co
nverter process was undertaken with focus on non-equilibrium phenomena. In
modelling, great emphasis was placed on a state of the art representation o
f the thermochemistry of the material systems involved. The validation of t
he simulation model shows good agreement between reported and calculated va
lues for species concentration and temperature development over time. Real-
process phenomena can be predicted.