Kinetics of biofilm nitrification.
The reaction rates (r(NH(4) (+) ) and r(NO(2) (-) )) in the two-step nitrification reaction were measured in a fluidized-sand-bed biofilm reactor under a range of steady-state conditions with respect to bulk NH(4) (+), NO(2) (-), and O(2) concentrations. It was shown from theory and experiment that under low NH(4) (+) concentration conditions, if the O(2)/NH(4) (+) concentration ratio in the bulk liquid is less than the stoichiometric coefficient (3.4 mg/mg), then oxygen will be rate limiting. In all experiments r(NO(2) (-) ) decreased more than r(NH(4) (+) ) under low oxygen conditions. This resulted in high NO(2) (-) effluent concentrations under low residence time conditions. The influence of the oxygen penetration effects on the relative values of r(NH(4) (+) ) and r(NO(2) (-) ) was experimentally shown to be caused either by the Nitrobacter location in the inner biofilm regions or by a K(m) effect for oxygen. Theoretical support of these findings was provided by a differential diffusion-reaction model which was used to simulate the experimental results.
Tanaka
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Chemical Engineering Laboratory (TCL), Swiss Federal Institute of Technology (ETH), CH-8092 Zürich, Switzerland.
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