then fed to a cooling crystallizer operating at 50F. an evaporation system, where 70% of the water in solution is removed. The concentrated solutions 10,000 kg of a dilute magnesium sulfate solution containing 10% MgSO4 in water is passed through During cooling, 10% of the water led to the crystallizer is removed by evaporation. The resulting mass of the crystal crop. The phase diagram for MgSO4-water system is shown in Fig. 3 - clearly mixture in the crystallizer generates heptahydrate crystals and mother liquor at 50F . Calculate the mark any information read from the chart. then fed to a cooling crystallizer operating at 50F. an evaporation system, where 70% of the water in solution is removed. The concentrated solutions 10,000 kg of a dilute magnesium sulfate solution containing 10% MgSO4 in water is passed through During cooling, 10% of the water led to the crystallizer is removed by evaporation. The resulting mass of the crystal crop. The phase diagram for MgSO4-water system is shown in Fig. 3 - clearly mixture in the crystallizer generates heptahydrate crystals and mother liquor at 50F . Calculate the mark any information read from the chart