In a case where lime, Ca(OH)2, is used to control pH, do I still have to use Cl- in initial system constraints in X1t? In this scenario, a fixed amount of lime is added to the medium initially and more is added if pH falls lower than a target value. For example, initial lime amount = 0.5 g/kg, in a volume of 40 liters of the medium (column) and the target pH = 10.5. The target pH is not always strictly met.
Can I directly model the use of lime as pH control in this case? If not, then how would I determine the equivalent Cl- to use in the model?