Syntrophy of aerobic and anaerobic ammonia oxidisers

Author:

Wett B.1,Hell M.2,Nyhuis G.3,Puempel T.4,Takacs I.5,Murthy S.6

Affiliation:

1. Department of Environmental Engineering, University of Innsbruck, Technikerstr.13, A-6020 Innsbruck, Austria

2. Achental-Inntal-Zillertal Wastewater Cooperation, HNr.150, A-6261 Strass i.Z, Austria

3. Cyklar-Stulz GmbH, Rietwiesstrasse 39, CH-8737 Gommiswald, Switzerland

4. Department of Microbiology, University of Innsbruck, Technikerstr.23, A-6020 Innsbruck, Austria

5. EnviroSim Europe, 15 Impasse Fauré, 33000 Bordeaux, France

6. DCWASA, DWT, 5000 Overlook Ave., SW Washington, DC 20032, USA

Abstract

Deammonification is known as an efficient and resource saving sidestream process option to remove the nitrogen load from sludge liquors. The transfer of the intermediate product nitrite between both syntrophic groups of organisms – aerobic and anaerobic ammonia oxidizers (AOB) – appears very sensitive to process conditions such as temperature, dissolved oxygen (DO) and operating nitrite level. Growth kinetics for aerobic and anaerobic AOBs differ by one order of magnitude and require an adequate selection of sludge retention time. This paper provides measurement- and model-based results on how selected sludge wasting impacts population dynamics in a suspended growth deammonification system. Anammox enrichment up to a doubled portion in mixed liquor solids can substantially improve process stability in difficult conditions. A case-study on low temperature operations outlines two possible strategies to balance syntrophic consumption of ammonium and nitrite.

Publisher

IWA Publishing

Subject

Water Science and Technology,Environmental Engineering

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