This study examines the mass transfer characteristics of a rotating bed that is equipped with static baffles. The volumetric liquid-side mass transfer coefficient (k(L)a) and the effective gas-liquid interfacial area were determined using a deoxygenation system and a chemisorption of CO2 in NaOH solution, respectively; the local liquid-side mass transfer coefficient (k(L)) was thus calculated. The effects of liquid flow rate, rotational speed, baffles and type of packing on these mass transfer parameters were investigated. Experimental results show that the bed with baffles had a higher interfacial area and lower k(L) than that without baffles. Adding baffles to the bed did not significantly affect the k(L)a values. Additionally, the packing with a larger specific interfacial area yielded higher values of k(L)a mainly because the effective interfacial area was higher. (c) 2015 Elsevier B.V. All rights reserved.