The enhancement of gas - liquid mass transport by fine adsorbent particles (less then 10μm) and its mechanism were studied. Based on the analysis of enhancement of gas - liquid mass transfer by physical adsorption

and the effect of fine adsorbent particles on fluid viscosity and component diffusion coefficient

the enhancement mechanism model is proposed in this paper with the aid of penetration theory and segmental linearization of adsorption isotherm and is used for performance calculation.