Stefan
flow that is caused by non-equimolar diffusion in the boundary layer
is often neglected in studies of the coke gasification reaction (Ccoke + CO2 = 2CO). An inaccurate and incomplete
understanding of the metallurgical coke gasification reaction mechanism
has had a major influence on the coke-making industry. Meanwhile,
it is adverse to the reasonable use of the resources of coking coal
as well as energy savings. Therefore, this paper has treated the external
diffusion coefficient, mass transfer coefficient, concentration of
carbon dioxide (CO2) on the outside and inside of coke,
and kinetic parameters as objects to study the effect of Stefan flow.
Isothermal experiments of metallurgical coke gasification with CO2 were carried out for 1100–1300 °C and at atmospheric
pressure. After modification, the coefficients of external diffusion
and mass transfer decreased and the deviation of corrections were
45 and 35%, respectively. Under the different temperatures, the concentration
of CO2 on the outer surface of coke together with its distribution
inside coke all decreased. Meanwhile, the region of the coke gasification
reaction was reduced as well as close to the outer surface area of
coke because of Stefan flow. Kinetic parameters were affected by Stefan
flow, and they increased to a certain degree.