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The MBR Book: Principles and Applications of Membrane

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52 <strong>The</strong> <strong>MBR</strong> <strong>Book</strong><br />

(Equation (2.30)). Both these processes dem<strong>and</strong> that specific micro-organisms prevail<br />

(Section 2.2.3). <strong>The</strong> exact micro-organisms responsible for denitrification (nitrate<br />

removal by biochemical reduction) are more varied – it is carried out by many different,<br />

phylogenetically-unrelated heterotrophs (Stewart, 1998; Zumft, 1992).<br />

<strong>The</strong> biological generation <strong>of</strong> nitrate from ammoniacal nitrogen (NH � 4) <strong>and</strong> aerobic<br />

conditions (nitrification), takes place in two distinct stages:<br />

Overall:<br />

2NH � 4 � 3O 2 → 2NO 2 � � 2H � � 2H2O (ammonia → nitrite) (2.26)<br />

2NO � 2 � O 2 → 2NO � 3 (nitrite → nitrate) (2.27)<br />

NH � 4 � 2O 2 → NO � 3 � 2H � � H 2O (2.28)<br />

Since the second step proceeds at a much faster rate than the first, nitrite does not<br />

accumulate in most bioreactors. However, since these micro-organisms are autotrophic<br />

<strong>and</strong> thus rather slow growing, they dem<strong>and</strong> relatively long SRTs to accumulate <strong>and</strong><br />

provide close to complete nitrification (i.e. above 90% ammonia removal). This presents<br />

another advantage <strong>of</strong> <strong>MBR</strong>s where long SRTs are readily attainable.<br />

Denitrification takes place under anoxic conditions when oxidation <strong>of</strong> the organic<br />

carbon takes place using the nitrate ion (NO 3 � ), generating molecular nitrogen (N2)<br />

as the primary end product:<br />

C 10H 19O 3N � 10NO � 3 → 5N 2 � 10CO 2 � 3H 2O � NH 3 � 10OH � (2.29)<br />

where in this equation “C 10H 19O 3N” represents wastewater.<br />

Nitrification relies on sufficient levels <strong>of</strong> carbon dioxide, ammonia <strong>and</strong> oxygen,<br />

the carbon dioxide providing carbon for cell growth <strong>of</strong> the autotrophs. Since nitrifiers<br />

are obligate aerobes, DO concentrations need to be 1.0–1.5 mg/L in suspended<br />

growth systems for their survival. Denitrification takes place when facultative microorganisms,<br />

which normally remove BOD under aerobic conditions, are able to convert<br />

nitrates to nitrogen gas under anoxic conditions. Denitrification requires a<br />

sufficient carbon source for the heterotrophic bacteria. This can be provided by the<br />

raw wastewater, which is why the nitrate-rich waste from the aerobic zone is<br />

recycled to mix with the raw wastewater. Complete nitrification is common in fullscale<br />

<strong>MBR</strong> municipal installations, although, since it is temperature-sensitive,<br />

ammonia removal generally decreases below 10°C. Most full-scale <strong>MBR</strong> sewage<br />

treatment plants are also designed to achieve denitrification.<br />

Most wastewaters treated by biological processes are carbon limited, <strong>and</strong> hence<br />

phosphorus is not significantly removed. This applies as much to <strong>MBR</strong>s as to conventional<br />

plants. It appears that membrane separation <strong>of</strong>fers little or no advantage<br />

regarding phosphorus removal (Yoon et al., 1999). Enhanced biological phosphate<br />

removal can be achieved by the addition <strong>of</strong> an anaerobic zone at the front <strong>of</strong> an activated<br />

sludge plant <strong>and</strong> returning nitrate-free sludge from the aerobic zone (Yeoman<br />

et al., 1986). This has been applied to a some full-scale <strong>MBR</strong> plant where constraints

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