Thin-layer convective drying of plantain banana was performed at four different temperatures from 50 to 80 °C, with slice thicknesses from 2 to 8 mm. The drying curves, fitted to seven different semi-empirical mathematical models, were successfully used to fit experimental data ((Formula presented.) 0.72–0.99). The diffusion approach had better applicability in envisaging the moisture ratio at any time during the drying process, with the maximum correlation value ((Formula presented.) 0.99) and minimum value of (Formula presented.) (2 (Formula presented.) and RMSE (5.0 (Formula presented.). The (Formula presented.), (Formula presented.), and (Formula presented.) values were calculated on the basis of the experimental data, and overall ranged from (Formula presented.) to (Formula presented.) m2 s−1, (Formula presented.) to 2.20 (Formula presented.) m s−1 and 13.70 to 18.23 kJ mol−1, respectively. The process energy consumption varied from 23.3 to 121.4 kWh kg−1. The correlation study showed that the drying temperature had a close correlation with (Formula presented.) value and sample hardness. A significant (p < 0.05) increase in hardness of dried plantain banana was observed at 80 °C compared to the other temperatures. Additionally, the sample hardness and process energy consumption were more positively correlated with the thickness of the samples