Comprehensive understanding of evaporation in porous channels is important for the design of modern heat exchangers and thermal systems such as heat pipes. This paper presents a numerical study of evaporation in a vertical porous channel. The volume of the fluid method was applied to capture the interface between phases. The multi-dimensional limiter for explicit solution method, in which there are additional constraints based on the flux-corrected transfer method, was used to solve the interface transfer equation. Pressure drop, Nusselt number, and the drying rate were considered as performance parameters. Comparing simulation results with experimental data showed that this new solver can precisely solve the thermal phase change in a porous medium. The influence of parameters effective on the drying process, such as porosity, permeability, the dynamic contact angle was investigated. Based on the results of the pressure profile in the final state, four different regions are visible. Because of the close fit of the wall temperature to the average cross-sectional temperature, the Nusselt number increases sharply at transition points from the liquid to the vapor phase.By increasing the dynamic contact angle, the average drying rate in the channel is reduced. K E Y W O R D S effective parameters, evaporation, porous medium, vertical channel, VOF method