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In this study, the mass transfer accompanied by an instantaneous irreversible   chemical reaction in a slurry bubble column containing sparingly soluble fine   reactant particles has been analyzed theoretically. Based on the penetration   theory, combining the cell model, a one-dimensional mass transfer model was   developed. In the model, the effects of the particle size and the particle   dissolution near the gas-liquid interface on the mass transfer were taken   into account. The mass transfer model was solved and an analytical expression   of the time-mean mass transfer coefficient was attained. The reactive   absorption of SO2from gas mixtures into Mg(OH)2/water slurry was investigated   experimentally in a bubble column reactor to validate the mass transfer   model. The results indicate that the present model has good predicting   performance and could be used to predict mass transfer coefficient for the   complicated gas-liquid-solid three-phase system with an instantaneous   irreversible chemical reaction

Gas-liquid mass transfer with instantaneous chemical reaction in a slurry bubble column containing fine reactant particles