The drying of electrodes is a crucial and often limiting process step in the manufacturing chain of lithium-ion batteries. [1] While the coating step can be carried out at high coating speeds, as shown by Diehm et al., the application of high drying rates still challenges the throughput in electrode production. [2] High energy demand on the one hand and drying condition-dependent electrode properties on the other demand the necessity of an optimally conducted drying process. [3,4] The negative influence on the product properties thereby primarily occurs at high drying rates. [5] The application of high drying rates can lead to a migration of additives like binder and carbon black to the surface of the electrode layer, resulting in low adhesion between active material and current collector foil. [6][7][8][9][10] Furthermore, the electrochemical performance deteriorates compared with gently dried electrodes due to the accumulation of insulating binder and carbon black at the surface, resulting in an increased electrical resistance. [6,11] Binder migration is attributed to the capillary pressure-driven induction of concentration differences during the emptying of the porous electrode structure, leading to an inhomogeneous distribution of components over the electrode height. [5] Nevertheless, it has been shown that these effects can be compensated for by selecting suitable process parameters. Isothermal drying tests indicate that a high film temperature and a low heat transfer coefficient can have a positive effect on adhesion, therefore indicating a more homogeneous distribution of electrode components. [9] The authors reasoned that binder diffusion processes could take place to compensate for concentration differences caused by capillary pore emptying to some extent. Due to the proportionality of diffusion coefficient and temperature, as well as the antiproportionality of viscosity and temperature, higher electrode temperatures increase binder mobility and therefore adhesion. [6,9,11] In addition, the authors illustrate the influences and limitations regarding electrode temperature and drying rate in the convective drying process, which are determined by air temperature, convective heat transfer coefficient, and humidity. Based on an enthalpy balance for double-sided heat input, a maximum electrode temperature of about 50 °C is determined during the evaporation process, while the air temperature was set to 150 °C, the dew point to 15 °C, and the convective heat transfer coefficient to 80 W m À2 K À1 , resulting in a drying rate of 6.15 g m À2 s À1 . [9] These limitations in terms of electrode film temperature are due to the enthalpy transferred with the evaporation flow, which cools the electrode layer below the temperature of the supplied air.