Waste Water Treatment Plants are known to have significant emissions of several pollutants from the different treatment phases. Among such pollutants, volatile organic and inorganic compounds, often having low odour detection thresholds, cause odour nuisance to the population. One of the purposes of the present work is to determine which are the more suitable methodologies to assess the odour emissions from liquid passive area sources, by means of a thorough study of the models capable of describing the volatilization phenomena of the odoriferous compounds from such sources. Several different models were evaluated for the open field emission, selecting the most appropriate one. Moreover, the models describing volatilization under a forced convection regime inside a wind tunnel device have been investigated, in order to describe the situation inside this sampling device, typically used for sampling on liquid sources. By means of experimental tests involving pure liquid acetone and pure liquid butanone, it was verified that the model more suitable to describe precisely the volatilization inside the sampling hood is the model for the emission from a single flat plate in forced convection and laminar regime, with a fluid dynamic boundary layer fully developed and a developing mass transfer boundary layer. The proportionality coefficient for the model was re-evaluated in order to account for the specific characteristics of the adopted wind tunnel device. Due to the differences between the fluid dynamic conditions in the open field and inside the hood, it was deemed useful to devise a correlation that-according to the flush rate adopted inside the chamber-is capable of computing the wind velocity at a 10 m height that would cause the same emission flux that is estimated from the analysis of the sample collected with the wind tunnel. Finally, the field of application was clearly defined for the considered models during the project, discussing the two different kinds of compounds commonly found in emissive liquid pools or liquid spills, i.e. gas phase controlled and liquid phase controlled compounds.