Typical correlations to calculate an impellerâs just suspended speed are based upon experiments with slurries with narrow particle size distributions and concentrations smaller than 20-30%v/v in which suspension is due to turbulent eddies in the inertial subrange. In the minerals processing industry, however, particles are often widely graded with a significant portion of them (â>50%) being smaller than 75 µm. While at elevated concentrations (>20-30% v/v), these types of slurries can become viscous and even non-Newtonian, we do not have an applicable correlation. New suspension experiments are presented for three model widely graded slurries over concentrations of 1 < xv < 50%v/v. As the concentration increases, the suspension mechanism changes from inertial subrange turbulence to the viscous regime. We present a preliminary correlation for the viscous suspension regime, for which one is not currently available. This correlation exploits a suspension viscosity due to the presence of the fines.