Thanks to the replacement of the condensation kinetics equation of a vapor in a gas stationary flow in a two-dimensional configuration by four differential equations describing the particle size distribution in the condensed phase, the system of hyperbolic differential equations for the evolutions of the two phases may be solved numerically by a Lax-Wendroff finite difference scheme. The theoretical results show how the evolutions of the physical flow quantities along the two-phase fluid streamlines, the properties of the nucleation and growth zones of the condensed nuclei, and the shape of the line of onset of condensation, are influenced by the two-dimensional effect due to the nozzle geometry.