A 13.4 L dry tubular biofilm reactor (DTB), with ceramics rings as carrier, was used to treat a polluted air stream using methanol as a model pollutant. The design of this reactor was based on the creation of a mist by contacting the waste gas and a liquid nutrient solution inside an atomizing nozzle. The liquid was supplied intermittently (16 s every 3 min) in order to minimize water addition (91% of reactor operational time corresponded to ''dry'' conditions). The reactor was operated at empty bed residence times (EBRT) of 42 s and volumetric loading rates of 1.5-3.0 kg/m 3 /d. Biofilm growth was observed first on the walls of the reactor, and subsequently growth developed on the surface of the rings. Methanol was completely removed from the gas phase at low loading rates and the removal efficiency was around 83-93% at a loading of 3.0 kg/m 3 /d. Organic carbon mass balances showed that, in the presence of the carrier, up to 73% methanol was biodegraded; nondegraded methanol and other metabolites constituted the remaining fraction in the liquid and gas effluent.