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Results highlighted that N2O concentrations decreased when the biofilm concentrations increased within the aerobic reactor.
Bulking material mixed in FF in one aerobic reactor had no effect on the stability of FF.
Analysis of an anoxic selector coupled with an aerobic reactor showed that good selection can be obtained with small selectors and a sufficiently large recycle ratio.
The control purpose is to maintain the dissolved oxygen concentration in an aerobic reactor of the wastewater treatment plant at the set-point.
The process involves feeding the ammonium-containing effluent from the carbon-utilising anode to an external biofilm-based aerobic reactor for nitrification, and then feeding the nitrified liquor to the MFC cathode for nitrate reduction.
The control objectives are to robustly achieve a prescribed quality of the effluent from the wastewater treatment plant at a least energy cost due to oxygen pumping into an aerobic reactor.
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The operation time is 600 days for anaerobic reactors and 250 days for aerobic reactors.
The reason for this difference is that the aerobic reactors generated much more microbial products.
The analysis of two mixed aerobic reactors suggests that the selector volume should be comparable or larger than that of the reactor.
Because of this condition, it can be concluded that total inert COD/total COD ratios of the aerobic reactors were 60%, whereas those of anaerobic reactors were 50%.
To achieve high conversions in aerobic reactors a substrate concentration gradient should be established implying that the recycle ratio and the sludge-age should be sufficiently small while the dissolved oxygen concentration should be sufficiently large.
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