“…This fact is due to the high buffer capacity of the anaerobic digester effluent caused by NH 3 /NH + 4 and H 2 CO 3 /HCO − 3 /CO 2− 3 equilibria. In this sense, the use of biological processes, which involve reactions with HCO − 3 and/or ammonium consumption or pH changes, could be considered an attractive pretreatment to reduce the consumption of reagents during phosphorus recovery (Mañas et al, 2011;Johansson et al, 2017;Simoes et al, 2018). For example, the previous application of nitrification Equation 3or partial nitrification-anammox processes (Equation 4) would decrease the amount of NaOH required up to 50 and 89%, respectively, and, in the last case, struvite recovery would be economically profitable (Campos et al, 2017).…”