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Modeling of Nitrous Oxide Production from Nitritation Reactors Treating Real Anaerobic Digestion Liquor

In this work, a mathematical model including both ammonium oxidizing bacteria (AOB) and heterotrophic bacteria (HB) is constructed to predict N(2)O production from the nitritation systems receiving the real anaerobic digestion liquor. This is for the first time that N(2)O production from such system...

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Detalles Bibliográficos
Autores principales: Wang, Qilin, Ni, Bing-Jie, Lemaire, Romain, Hao, Xiaodi, Yuan, Zhiguo
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Nature Publishing Group 2016
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4850461/
https://www.ncbi.nlm.nih.gov/pubmed/27125491
http://dx.doi.org/10.1038/srep25336
Descripción
Sumario:In this work, a mathematical model including both ammonium oxidizing bacteria (AOB) and heterotrophic bacteria (HB) is constructed to predict N(2)O production from the nitritation systems receiving the real anaerobic digestion liquor. This is for the first time that N(2)O production from such systems was modeled considering both AOB and HB. The model was calibrated and validated using experimental data from both lab- and pilot-scale nitritation reactors. The model predictions matched the dynamic N(2)O, ammonium, nitrite and chemical oxygen demand data well, supporting the capability of the model. Modeling results indicated that HB are the dominant contributor to N(2)O production in the above systems with the dissolved oxygen (DO) concentration of 0.5–1.0 mg O(2)/L, accounting for approximately 75% of N(2)O production. The modeling results also suggested that the contribution of HB to N(2)O production decreased with the increasing DO concentrations, from 75% at DO = 0.5 mg O(2)/L to 25% at DO = 7.0 mg O(2)/L, with a corresponding increase of the AOB contribution (from 25% to 75%). Similar to HB, the total N(2)O production rate also decreased dramatically from 0.65 to 0.25 mg N/L/h when DO concentration increased from 0.5 to 7.0 mg O(2)/L.