A series of experiments on the facilitated transport of CO2 through supported liquid membranes impregnated with aqueous solutions of various amines as carriers was performed, and the effects of the reaction rate and the chemical equilibrium of the reaction between CO2 and amine on the permeability of CO2 were investigated. Four primary amines (monoethanolamine (MEA), ethylenediamine (EDA), monoprotonated ethylenediamine (EDAH(+)), 2-amino-2-methyl-1-propanol (AMP)), one secondary amine (diethanolamine (DEA)) and two tertiary amines (triethanolamine (TEA), methyldiethanolamine (MDEA)) were used as the carrier. The feed gas was a mixture of CO2 and CH4. High CO2 permeabilities were obtained with the EDAN(+) membrane due to its moderate chemical equilibrium constant Kc, which is favorable for both fast absorption of CO2 at the feed side of the membrane and fast stripping at the sweep side. Low CO2 permeabilities were obtained with the tertiary amine and AMP membranes due to their low reactivity. The CO2 permeability through the MEA membrane, which has too large a K-eq value at low temperature, increased with increasing temperature due to the decrease in K-eq and also due to the increase in the reaction rate. The experimental results obtained with the MEA, DEA and EDAH(+) membranes were simulated on the basis of the theory of facilitated transport.