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Title: Simulation of three-phase fluidized bioreactors for denitrification

Technical Report ·
DOI:https://doi.org/10.2172/6795219· OSTI ID:6795219

Fluidized-bed bioreactors were developed and operated at three scales (diameters of 0.1, 0.2, and 0.5 m) by the Chemical Technology Division. The performance of these reactors in denitrification was simulated using the following modified form of Monod kinetics to describe the reaction kinetics: rate = V/sub max/ (NO/sub 3//sup -//K/sub s/ + NO/sub 3//sup -/) (% biomass). In the fluids-movement portion of the simulation the tanks-in-series approximation to backmixing was used. This approach yielded a V/sub max/ of 3.5 g/m/sup 3/-min (% biomass) and a K/sub s/ of 163 g/m/sup 3/ for the 0.5-m bioreactor. Values of V/sub max/ and K/sub s/ were also determined for data derived from the 0.1-m bioreactor, but inadequate RTD data reduced the confidence level in these results. A complication in denitrification is the multi-step nature of the reduction from nitrate to nitrite to hyponitrite and finally to nitrogen. An experimental study of the effect of biomass loading upon denitrification was begun. It is recommended that the experimental work be continued.

Research Organization:
Massachusetts Inst. of Tech., Oak Ridge, TN (USA). School of Chemical Engineering Practice
DOE Contract Number:
W-7405-ENG-26
OSTI ID:
6795219
Report Number(s):
ORNL/MIT-324; TRN: 81-007211
Country of Publication:
United States
Language:
English