The precipitation features of calcium phosphate in a fluidized bed reactor in the concentration range between 5 and 100 mg P l(-1) were studied, and the conditions for optimum phosphate removal efficiency were established. The supply of calcium ions should be such that a Ca/P molar ratio of 3 at the inlet of the reactor is achieved. If the water to be treated does not contain magnesium or carbonate ions, the supply of base should suffice to promote a conversion of 50-55% of the incoming phosphate to the solid phase. In the presence of carbonate and magnesium ions, the base supply should provide a conversion of 80-95%. Magnesium and carbonate ions did not have a detrimental effect on the phosphate removal efficiency for inlet concentrations of up to 4.8 x 10(-3) (Mg/P < 2 mol mol(-1)) and 4.8 x 10(-3) kmol m(-3), respectively. The feasibility of a process based on the precipitation of magnesium phosphate instead of calcium phosphate was demonstrated for waters with a low calcium content (Ca/P < 0.8 mol mol(-1)). Finally a method is presented to select process conditions where co-precipitation of unwanted phases can be avoided. Copyright (C) 1996 Elsevier Science Ltd