A pure culture of Pseudomonas putida was grown ns a film on carbon par
ticles in a differential fluidized bed biofilm reactor a new experimen
tal system for the application of diffusion-reaction models. In the ac
tive biofilm, effective diffusion coefficients of the essential substr
ates-phenol and oxygen-were simultaneously calculated The multisubstra
te biokinetic expression used in the model solution was derived by non
linear regression analysis of the data of continuous system fermenter
experiments. The determined biokinetic equations were utilized to solv
e the diffusion-reaction model for effective diffusion coefficients in
the active biofilm. The ratio of the evaluated effective diffusion co
efficient through active biofilm to that of water varied between 17-44
% and 9-24% for phenol and oxygen, respectively for different biofilm
densities. Results of the study showed a fair agreement with the liter
ature at low biofilm densities.