This paper presents experimental studies on the absorption of nitrous gas in microchannels. Liquid and gas phase products have been analysed for a wide range of nominal residence times (0.03-1.4 s), gas compositions (5-10% NO, 5-49% 02, 46-82% H2O, balance argon), system pressures (2.0-10.0 bar), mass fluxes (1.5-30 kg m(-2) s(-1)), and coolant temperatures (23-51 degrees C) in circular tubes with internal diameters of 1.4 and 3.9 mm. Condensation of water vapour is very rapid in the microchannel, thereby enhancing the concentrations of NO and O-2 and leading to highly intensified production of nitric acid. The presence of inerts inhibits the degree of enhancement. A simple model of condensing two-phase annular flow, in which vapour-liquid interface is assumed to be smooth, describes the main features of the observations. The interfacial area between the phases is the single most sensitive parameter in the model. Under the best conditions studied experimentally, an absorption efficiency of 99% was achieved at 2 bar, with an intensification factor relative to a conventional tower absorber of the order of 1000. The NO concentration in the tail gas is of the order of a few percent under these conditions but the tail gas flow is very small. While further work remains to develop a complete process with acceptable emissions, these results indicate that a microstructured system employing passages similar to 1 m long could replace the 70 m absorption tower in a conventional nitric acid plant. (C) 2017 Elsevier Ltd. All rights reserved.