The
present work focuses on the gasification of a single carbon-anode
particle with CO2, using a detailed reaction-transport
model based on the reaction intrinsic kinetics and transport of gaseous
species. The model includes the mass conservation equations for the
gas components and solid carbon particles, resulting in a set of nonlinear
partial differential equations, being solved using numerical techniques.
The model may predict the gas generation rate, the gas compositions,
and the carbon consumption rate during the gasification of a carbon
particle. Five kinetic models were compared to describe the gasification
behavior of carbon particles. It was found that the random pore model
(RPM) provided the best description of the reactivity of anode particles.
The model also predicted the particle shrinkage during the gasification
process. The model was validated using experimental results obtained
with different particle size ranges, being gasified with CO2 at 1233 K. The experiments were performed in a thermogravimetric
analyzer (TGA). Good agreement between the model results and the experimental
data showed that this approach could quantify with success the gasification
kinetics and the gas distribution within the anode particle. In addition,
the Langmuir–Hinshelwood (L–H) model is used in order
to capture the inhibition effect of carbon monoxide on the gasification
reaction. The effectiveness factor and Thiele modulus simulated for
various particle sizes helped assess the evolution of the relative
dominance of diffusion and chemical reactions during the gasification
process.