where 𝒕 𝒎 (in seconds) is the mixing time where m % of the mixture is homogenised, 𝑅𝑒 is the Reynolds number of the flow, 𝐴 and 𝑏 are the parameters which are dependent on the type and geometry, of the mixer. For turbulent flow (high Reynolds number), 𝑏 = 0 . If so, then the relation between mixing speed and time can be simplified to an inverse relation. Since the dispersion blade rotates at high RPM, turbulent flow can be assumed here. The constant can be estimated using optimised mixing time (where we assume m is close to 100%) and mixing speed data from previous reports . This estimation allows for interpolation to determine minimum mixing time thresholds for specific mixing speeds. Here we assume that there is no maximum time limit for mixing for a speed that is less than the maximum permitted mixing speed. More complex effects that are associated with mixing time and speed in LIB electrode production are ignored for the sake of simplification. For example, prolonged mixing times and elevated speeds can lead to the disruption stable slurry networks, potentially compromising the uniformity and quality of the electrode slurry . There is also the effect of mixing sequence , which is not considered here currently, but that can be considered in the future, given the flexibility of the BMM environment design.