Gasification is a promising technology for the effective utilization of low-rank solid fuels such as lignite. Char gasification, a rate-limiting step, has been studied using several kinetic models, one of which is the random pore model (RPM). Although catalytic gasification is an effective method to accelerate the char gasification rate, the RPM is sometimes not applicable to catalytic gasification due to rapid acceleration of the gasification rate with catalysts. Therefore, in our previous study, an extended RPM was applied for the CO
2 gasification for catalyst-loaded char, and the model-predicted results were compared with the experimental results. The model prediction was in good agreement with the experimental results, and the applicability of the extended RPM for CO
2 gasification with catalyst was thus established. In order to analyze the catalytic effect of calcium present in raw coal and the loaded calcium, CO
2 gasification and steam gasification of raw coal char and calcium-loaded coal char were evaluated by dividing the extended RPM into a non-catalytic reaction term and a catalytic reaction term. It was clarified that the first term was constant regardless of the presence or absence of the loaded calcium. The second term successfully described the catalytic effect of calcium. Further unlike in the case of CO
2 gasification, in steam gasification, deactivation of calcium present in raw coal was slower than that of the loaded calcium.
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