A solution containing 130.0lbmKNO3/100lbmH2O at 80.0C is fed to a cooling crystallizer operated at 10.0C. Slurry from the crystallizer ( KNO3 crystals suspended in saturated solution) is fed to a filter, where the crystals are separated from the solution. Use the solubility data in the figure below to determine the production rate of the crystals (lb bm/lbbm feed) and the solid-to-liquid mass ratio (lb mm crystals/ /bm liquid) in the slurry leaving the crystallizer