To date, only two modelling approaches, considering both AM and CBD particles, were published for 3D LIB slurry evaporation: the one reported by us and Forouzan et al. and the one reported by Srivastava et al. Both these approaches have been developed through the open-source molecular dynamics software LAMMPS. Srivastava et al. considered the solvent implicitly by applying a Langevin 47 force field (FF) to the particles, while the evaporation was performed by simply shrinking the slurry structure until reaching the desired electrode thickness. Along our 3D manufacturing computational workflow, the solvent at the slurry phase is accounted by expanding the CBD particles and decreasing their density. The latter makes the CBD at the slurry phase an effective particle enabling to account for carbon, binder and solvent, as extensively discussed by us in a previous work. The evaporation is performed by shrinking the CBD diameter to remove all the solvent, leading to a particles rearrangement and to the dried electrode mesostructure. An advantage of such approach, respect the one of Srivastava et al., is that the electrode macroproprierties (porosity, density, thickness) arises from the particles' interactions, rather than being imposed shrinking the simulation box. The latter allows comparing such macroscopic observables with their experimental counterpart in order to to parametrize the model, as previously showed. However, none of the procedures discussed above could lead to heterogeneous electrode mesostructures. Bearing in mind the critical importance of additives migration and the economic interest of increasing the drying speed, it is of interest the development of 3D physics-based models able to simulate CBD migration during solvent evaporation.