Continuous anaerobic oxidation of methane: Impact of semi-continuous liquid operation and nitrate load on N 2 O production and microbial community.

Autor: Valenzuela EI; Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro, 76230, Mexico., Ortiz-Zúñiga MF; Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro, 76230, Mexico., Carrillo-Reyes J; Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro, 76230, Mexico., Moreno-Andrade I; Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro, 76230, Mexico., Quijano G; Laboratory for Research on Advanced Processes for Water Treatment, Instituto de Ingeniería, Unidad Académica Juriquilla, Universidad Nacional Autónoma de México, Blvd. Juriquilla 3001, Querétaro, 76230, Mexico. Electronic address: GQuijanoG@iingen.unam.mx.
Jazyk: angličtina
Zdroj: Chemosphere [Chemosphere] 2021 Sep; Vol. 278, pp. 130441. Date of Electronic Publication: 2021 Mar 31.
DOI: 10.1016/j.chemosphere.2021.130441
Abstrakt: This work proves the feasibility of employing regular secondary activated sludge for the enrichment of a microbial community able to perform the anaerobic oxidation of methane coupled to nitrate reduction (N-AOM). After 96 days of activated sludge enrichment, a clear N-AOM activity was observed in the resulting microbial community. The methane removal potential of the enriched N-AOM culture was then studied in a stirred tank reactor (STR) operated in continuous mode for methane supply and semi-continuous mode for the liquid phase. The effect of applying nitrate loads of ∼22, 44, 66, and 88 g NO 3 - m -3 h -1 on (i) STR methane and nitrate removal performance, (ii) N 2 O emission, and (iii) microbial composition was investigated. Methane elimination capacities from 21 ± 13.3 to 55 ± 12 g CH 4 m -3 h -1 were recorded, coupled to nitrate removal rates ranging from 6 ± 3.2 to 43 ± 14.9 g NO 3 - m -3 h -1 . N 2 O production was not detected under the three nitrate loading rates applied for the assessment of potential N 2 O emission in the continuous N-AOM process (i.e. ∼22-66 g NO -3 m -3 h -1 ). The lack of N 2 O emissions during the process was attributed to the N 2 O reducing capacity of the bacterial taxa identified and the rigorous control of dissolved O 2 and pH implemented (dissolved O 2 values ≤ 0.07 g m -3 and pH of 7.6 ± 0.4). Microbial characterization showed that the N-AOM process was performed in absence of putative N-AOM archaea and bacteria (ANME-2d, M. oxyfera). Instead, microbial activity was driven by methane-oxidizing bacteria and denitrifying bacteria (Bacteroidetes, α-, and γ-proteobacteria).
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Databáze: MEDLINE