Not at all !
Those values are completely unrealistic.
I cannot say what may go wrong because I don't know what your process looks like or the data you are using, I can only speculate.
If you are talking about alternatives for the influent fractionation (the COD to TSS conversion), I assume you are attempting to calibrate a (complex or not) process model only based on influent data. This is a 'dangerous' approach which is bound to result in completely awkward estimates of kinetics parameters - the relation between those and the influent specs is kind on loose ...
You should first calibrate your influent model to make sure that you feed your process with a [b]'correct' influent[/b]; then you should probably look at the steady-state behaviour of your system (sludge age, MLSS, etc.); and only then, if necessary and if you have data to support that, calibrate the kinetic model.
I don't know which data you have for your influent (e.g. COD, TSS, TN, .. ? BOD, TSS, .. ? rbCOD, ..? several combinations are possible), but you need to perform, at least (!) some continuity checks.
For instance: if you have COD and TSS and derive soluble and particulate COD based on F_TSS_COD (the standard fractionation in WEST), you need to make sure that the [b]calculated BOD[/b] (combination of COD components that contribute to BOD) is reasonable, i.e. 2-2.5 or so COD / BOD; or even better, if you have a BOD measurement as well, close enough to your measurement.