The chemical bath deposition (CBD) process is currently favored for the pre
paration of CdS thin films of commercial interest. A chemical engineering t
ype analysis of the CBD process is carried out in this paper to aid its des
ign and optimization. Model equations are developed (based on a population
balance formulation) for the temporal variation of reactant concentrations
as well as of the solid phase, both in the bulk and on the substrate. A pos
sible sequence of elementary mechanisms (i.e., nucleation, surface reaction
, etc.) is suggested, and the resulting comprehensive model is solved numer
ically. Computational results show that the model is consistent with availa
ble experimental data on film thickness evolution. Furthermore, the influen
ce of the process parameters on the results is studied theoretically and di
scussed extensively for several cases. The model may prove very useful for
optimization of the CBD process with respect to its design variables (react
ant concentrations, process time, etc.) as well as for efficient experiment
al determination of presently uncertain or missing parameter values.