Lg. Gordeeva et al., THE KINETICS OF GASIFICATION OF MICROPOROUS CARBON WITH OXYGEN - A FRACTAL APPROACH, Kinetics and catalysis, 38(6), 1997, pp. 840-847
The kinetics of gasification of Sibunit synthetic carbon with oxygen i
s studied at T = 480-550 degrees C. The apparent activation energy of
the process is E-a = 155 +/- 15 kJ/mol at a degree of gasification x b
elow 0.7. The classical and fractal analyses of the data obtained by t
he transmission electron microscopy, small-angle X-ray scattering, and
low-temperature nitrogen adsorption techniques are used to study vari
ations in the structure of Sibunit carbon during its gasification. The
kinetics of gasification is controlled by two competing factors: a sm
oothing of the carbon surface during gasification, which is accompanie
d by a decrease in the gasification rate, and an increase in the surfa
ce area of the pores accessible to the reactant, which, in contrast, c
auses an increase in the gasification rate. A Monte Carlo simulation o
f gasification of Sibunit carbon by reactive consumption of a determin
istic fractal cluster shows that the assumptions on the chemical unifo
rmity of the cluster surface and on the existence of a fractal system
of pores make it possible to adequately model the kinetics of gasifica
tion and variations in the structure of this carbon material at x > 0.
2.