Using a heterogeneous plug flow model for the reactor tubes and a general gas−solid reaction/diffusion
model with intrinsic reaction kinetics for coke combustion and coke gasification, an in-depth study on
the influence of seven operating parameters of the decoking procedure of an ethane cracking furnace is
performed. On the basis of the results of this study, the air and steam flow to the reactor tubes during the
decoking procedure are adapted to propose an optimized decoking procedure that allows reducing the required
decoking time of an industrial ethane cracking furnace by a factor of 3. In the new decoking conditions for
the ethane cracker, the air flow rate is raised by a factor of 3, while the steam dilution is lowered by a factor
of 4.5.