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Aerobic-anaerobic DHS reactor for enhancing denitrification in municipal wastewater treatment. | LitMetric

Aerobic-anaerobic DHS reactor for enhancing denitrification in municipal wastewater treatment.

Sci Total Environ

Department of Civil and Environmental Engineering, Nagaoka University of Technology, Nagaoka 940-2188, Japan; Department of Science of Technology Innovation, Nagaoka University of Technology, Nagaoka 940-2188, Japan. Electronic address:

Published: December 2024

Providing anaerobic environments can enhance the denitrification capacity of wastewater treatment systems. This study developed an aerobic-anaerobic downflow hanging sponge (DHS) reactor to increase denitrification. A siphon tube was integrated with a conventional DHS to create anaerobic conditions by controlling a water column inside the reactor. The siphon heights were set in the middle of the reactor, representing 2/5 of the total volume. Anaerobic conditions were maintained at the bottom (1/5), whereas aerobic conditions were maintained at the top (2/5). The middle part experienced alternating aerobic-anaerobic conditions within a siphon cycle. The hydraulic retention time (HRT) was 3 h, and the temperature was maintained at 30 °C. The study was divided into the low-loading and standard phases based on the influent soluble chemical oxygen demand (sCOD) concentration. During the low-loading phase, the aerobic-anaerobic DHS exhibited a higher sCOD removal rate (53.6 ± 26.6 %) than the control aerobic DHS (35.6 ± 31.9). However, the removal efficiencies for NH₄-N and total nitrogen (TN) were lower, averaging 37.1 ± 24.7 % and 31.5 ± 21 %, respectively. In the standard phase, the aerobic-anaerobic DHS achieved an sCOD removal rate of 69.3 ± 14.8 % and an NH₄-N removal rate of 17.2 ± 11.4 %. The control aerobic DHS showed higher sCOD and NH₄-N removal at 84.7 ± 10.8 % and 54.1 ± 12.8 %, respectively, possibly due to the reduced aerobic zone volume in the aerobic-anaerobic DHS. The TN removal rates were also lower in the aerobic-anaerobic DHS (17.1 ± 11.4 %) than in the control DHS (25 ± 12.3 %). However, based on the ratio of nitrification to TN removal, the aerobic-anaerobic DHS showed a high denitrification rate of 85 %-100 %. The highest number of denitrifiers was in the middle section of the aerobic-anaerobic DHS, with Rhodocyclaceae the most prominent, followed by Comamonadaceae. Maintaining an anaerobic zone improved the denitrification capacity, indicating the potential of the aerobic-anaerobic DHS for efficient municipal wastewater treatment.

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Source
http://dx.doi.org/10.1016/j.scitotenv.2024.177283DOI Listing

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