The absorption of carbon dioxide into aqueous ammonia solution using packed column was studied experimentally. The overall absorption rate (Phi) and the volumetric overall mass transfer coefficient (K(G)a(v)) were investigated. The overall absorption rate (Phi) varies with the process parameters, including manipulated temperature, gas flow rate, liquid flow rate, aqueous ammonia concentration and CO2 inlet concentration. It is found that the Phi increases with the gas flow rate increasing, although the CO2 removal efficiency demonstrates the opposite trend. The experiment results show that the value of Phi is proportional to the bulk gas partial pressure (P-co2). Besides, the K(G)a(v) value could be determined by calculating the slope of the straight lines of the absorption rate against the bulk gas partial pressure at different ammonia concentrations. It is found that the K(G)a(v) value increases significantly when the aqueous ammonia concentration increases from 1.16 kmol/m(3) to 4.54 kmol/m(3). (C) 2012 Elsevier B.V. All rights reserved.