The workflow of the evaporation model proposed in this Article is schematized in Figure . This section will discuss the critical aspects of our modelling procedure, i.e.: (i) the slurry phase, The slurry phase has been previously validated by comparing the experimental and simulated slurry shear-viscosity curve, where the AM particle size distribution arises from devoted in house experimental measurements, while the CBDs are effective particles accounting for carbon, binder and solvent. Both AM and CBD particles are considered to be spherical. In the case study reported here, the slurry was composed of LiNi0.33Mn0.33Co0.33O2 (NMC), Carbon black (C65), polyvinylidene difluoride (PVdF) and N-Methyl-2-pyrrolidone (NMP). The weight ratio considered is 94:3:3 (NMC:C65:PVdF), with a SC of 65%. The SC is defined here as the mass of the solid components (NMC+C65+PVdF) divided to the total mass of the slurry (solid components + solvent). The validation of the simulated slurry structure utilized along this work is reported in section S1 of the Supplementary information.