Coke formed on the internal skin of the reactor tube, limits the on-stream time of
cracking furnaces. On the basis of the plant output information and insight in the mechanisms
for coke formation in pyrolysis reactors, a mathematical model describing the coke formation
has been derived. It consists of four reactions for coke production, assuming that the sources
of coke formation are ethylene, propylene, butadiene and aromatics. The coking model was
combined with two other models, the kinetic model for the pyrolysis of naphtha and a reactor
model. The combination of these models allows accurate prediction of the run length of the
reactor with a limitation value of 1100 °C for tube wall temperature. In this model, ethylene,
propylene, butadiene and aromatics have been postulated as the coke precursors, 30,10,10 and
50 percent, respectively.