Condensation is a significant topic in engineering areas. For example, during the expansion processwithin a steam turbine, condensing steam may form droplets which can reduce the machine’s efficiencyor even damage the blades. Hence, understanding this phenomenon is a hard requirement to minimisesuch damage or, in turn, to utilise the phenomenon under certain conditions.Nucleation or droplet formation, normally regarded as the first step of condensation, may determinewhether condensation occurs. Thus, numerous studies have been conducted to build the first understand-ing of nucleation, namely the nucleation theory. Amount this, the so-called classical nucleation theory(CNT) is popular which describes the homogeneous nucleation process and is widely used in engineer-ing calculations. The CNT partly considers the ideal gas law and is normally applied for steam at lowpressures exhibiting semi-ideal states. However, it was found later that the CNT might not reflect thenucleation process of real gases correctly, because real gases do not follow the ideal gas law. To predictthe nucleation process of real gases, modifications to the classical nucleation model have been made.However, from the author’s knowledge, none of them has been widely proven. The reason could be thatthe modifications did not include a review of the CNT from the perspective of real gases. This mayalso prevent an individual discussion on nucleation models because they normally have to be applied inconjunction with a droplet growth model.Hence, the presented work intends to check the validity of CNT from the perspective of real gasesand to develop a nucleation model for real gases, by following the classical derivation process from thethermodynamic-kinetical aspect. To achieve this goal, the assumptions made in the CNT regarding theideal gas law are identified and appropriately modified by considering the real gas equation of state.Firstly, models of the elevation in Gibbs free energy based on various approaches of the equationof state are concretely derived and compared, to analyse the impact of real gases on a simple vapour-droplet system. Secondly, an inconsistency is identified in the classical equilibrium droplet distributionwithin a supersaturated vapour against one of its significant assumptions as the fluid state exhibits a lowcompressibility factor. To eliminate this inconsistency, a method is presented by which the equilibriumdroplet distribution of a real gas is calculated. It shows plausible results at relatively low reduced tem-peratures and has limitation at relatively high reduced temperatures due to uncertainty in solving real gasequation of state. Furthermore, the presented work assumes an additional nucleation of small droplets tothe CNT, increasing the evaluated nucleation rate in principle.Finally, different nucleation models are applied to calculate the condensation process with constantexpansion rates. To focus on the nucleation process, the supercooling at the Wilson point is considered thekey parameter. The comparison between calculation results exhibits a quasi-linear correlation betweenthe supercooling at Wilson point and the logarithm of expansion rate. An extension of the “peak” ofnucleation rate can be detected at Wilson points very close to the critical point, leading to an evidentdeviation between the Wilson supercooling and the maximal supercooling. Furthermore, the calculationresults are compared with experiments regarding CO2, R12, R22, and water in Laval nozzles. It is foundin general that the classical model overpredicts the nucleation rate. In contrast, the presented models withthe additional nucleation agree with the test results regarding the supercooling at Wilson points.