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N2O production in a single stage nitritation/anammox MBBR process

N2O production in a single stage nitritation/anammox MBBR process

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stricter it might lead to elevated emissions of nitrous oxide from the biological removal<br />

<strong>process</strong>es. It is therefore of great importance to design and operate these <strong>process</strong>es to<br />

m<strong>in</strong>imise the emissions of nitrous oxide to the atmosphere.<br />

Wastewater treatment plants us<strong>in</strong>g biologic treatment <strong>process</strong>es for nutrient removal<br />

are produc<strong>in</strong>g excessive sludge giv<strong>in</strong>g rise to ammonium rich effluent from the<br />

anaerobic sludge digestion. This <strong>in</strong>ternal wastewater stream is recomb<strong>in</strong>ed with the<br />

<strong>in</strong>fluent of the treatment plant and corresponds to 15-20% of the total nitrogen load of<br />

the wastewater treatment plant (Fux et al., 2003). In the early 1990s a new biological<br />

treatment <strong>process</strong> for nitrogen removal through anaerobic ammonium oxidation<br />

(<strong>anammox</strong>) was discovered by research teams <strong>in</strong> Holland, Germany and Switzerland<br />

(Mulder et al., 1995, Hippen et al., 1997, Siegrist et al., 1998). The technology has turned<br />

out to be suitable for treatment of reject waters and other problematic wastewaters<br />

with a low COD/N ratio and high ammonium concentrations. The bacteria perform<strong>in</strong>g<br />

the microbial conversion of nitrite <strong>in</strong>to d<strong>in</strong>itrogen gas are strict anaerobe autotrophs<br />

and the <strong>process</strong> has the potential to replace conventional nitrification/denitrification of<br />

recirculated high strength ammonium streams with<strong>in</strong> the wastewater treatment plant<br />

(Strous et al., 1997). No additional carbon source is needed, the oxygen demand is<br />

reduced by 50% <strong>in</strong> the nitrify<strong>in</strong>g step and the aeration can thereby be strongly reduced<br />

(Jetten et al., 2001, Fux et al., 2002). This means that the <strong>process</strong> offers an opportunity to<br />

decrease the carbon footpr<strong>in</strong>t of the wastewater treatment plant <strong>in</strong> terms of sav<strong>in</strong>g<br />

possibilities of both additional carbon source and power consumption (Jetten et al.,<br />

2004). Further advantages with the <strong>anammox</strong> <strong>process</strong> is that the <strong>production</strong> of surplus<br />

sludge is m<strong>in</strong>imized and that high volumetric load<strong>in</strong>g rates can be obta<strong>in</strong>ed result<strong>in</strong>g <strong>in</strong><br />

reduced operational and <strong>in</strong>vestment costs (Abma et al., 2007). However there are<br />

doubts that the <strong>process</strong> could produce significant amounts of <strong>N2O</strong> gas with negative<br />

environmental impacts detract<strong>in</strong>g the <strong>process</strong> advantages.<br />

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