A laboratory scale semi-batch fed anaerobic ammonia oxidation (ANAMMOX) reactor was operated in the lab under two different feeding operations. In the first scenario, termed as phase I, the reactor was seeded and operated with NO(2) -N added externally with the filtrate to the reactor in the ratio needed for the successful ANAMMOX. A second reactor was also initiated shortly after the start-up of the ANAMMOX to accomplish partial nitrification (nitritation reactor) to generate NO(2) -N. In phase II, the operation of the ANAMMOX reactor was switched to the mode in which case the partially nitrified effluent from the nitritation reactor was fed to the ANAMMOX reactor. In both phases, real filtrate from a local wastewater treatment plant was used as the feed. The ANAMMOX reactor sustained a loading rate (average 0.33 ± 0.03 with a max of 0.4 g N (L day)(-1) ) which is comparable with many other fed-batch reactors in the literature. Consistent total N removal (average of 82 ± 4%) could be sustained in the ANAMMOX reactor during both phases. The nitritation reactor also consistently enabled a NO(2) -N to NH(3) -N ratio of 1.2:1 which was needed for the successful operation of the ANAMMOX reactor in phase II. Sequence analysis and FISH showed that Kuenenia stuttgartiensis dominated the enriched ANAMMOX community along with several unidentified, but seemingly enriched, potential ANAMMOX strains. Microbial ecology analysis for nitritation reactor showed the dominance of Nitrosomonas europaea. In summary, this manuscript provides important information on the start-up and operation of anammox reactor with detailed investigation on microbial ecology in this reactor.
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http://dx.doi.org/10.1002/bit.24767 | DOI Listing |
Water Res X
January 2025
Qinhuangdao Huaheng Biological Limited Company, Qinhuangdao, 066000, China.
A full-scale simultaneous partial nitrification, anaerobic ammonia oxidation (anammox), and denitrification (SNAD) reactor was initiated to address the problem of high energy consumption for the treatment of low C/N wastewater. The SNAD system achieved a nitrogen removal rate of 0.9 kg/(m·d) at an influent NH₄-N concentration of 500 mg/L after 450 days of stable operation.
View Article and Find Full Text PDFWater Res
December 2024
State Key Joint Laboratory of Environment Simulation and Pollution Control, School of Environment, Tsinghua University, Beijing, China; Research and Application Centre for Membrane Technology, School of Environment, Tsinghua University, Beijing, 100084, China. Electronic address:
The integration of partial nitrification-anammox (PN/A) into membrane-aerated biofilm reactor (MABR) is a promisingly energy-efficient and high-efficiency technology for nitrogen removal. The inhibition of nitrite oxidizing bacteria (NOB) remains as the most significant challenge for its development. In our investigation, we proposed a novel process to integrate carriers to MABR (CMABR), which combined the carriers enriched with anaerobic ammonium-oxidizing bacteria (AnAOB) and partial nitrifying MABR system.
View Article and Find Full Text PDFBioresour Technol
December 2024
Centre for Environmental Health and Engineering (CEHE), Department of Civil and Environmental Engineering, University of Surrey, Guildford GU2 7XH, UK. Electronic address:
Nitrogen removal via anammox is efficient but challenged by their slow growth. Adding granular activated carbon (GAC) increased the total nitrogen removal rate to 66.99 g-N/m/day, compared to 50.
View Article and Find Full Text PDFJ Environ Manage
December 2024
Institute of Pollution Control and Environmental Health, School of Energy and Environmental Engineering, Hebei University of Technology, Tianjin, 300401, China.
The new-type submerged granular sludge membrane bioreactor (S-GSMBR) was constructed by installing a membrane module inside an upflow anaerobic sludge blanket. S-GSMBR achieved the fast start-up (47 d) and long-term stable operation (133 d) of mainstream Anammox process as well as the effective control of membrane fouling. The maximum nitrogen removal rate and efficiency were 0.
View Article and Find Full Text PDFJ Environ Manage
December 2024
Key Laboratory of Urban Storm Water System and Water Environment Ministry of Education, Beijing University of Civil Engineering and Architecture, Beijing, 100044, China; Sino-Dutch R&D Centre for Future Wastewater Treatment Technologies/Key Laboratory of Urban Stormwater System and Water Environment, Beijing University of Civil Engineering and Architecture, Beijing, 100044, China.
Excessive organic matter in the anaerobic ammonia oxidation (Anammox) leads to the growth of a large number of heterotrophic bacteria, which disrupts the anaerobic ammonia oxidation. The adsorption-anaerobic ammonia oxidation process can effectively reduce excessive organic matter, capturing it instead of consuming it, which is a sustainable development technology. In this study, utilizing the excellent adsorption performance of aerobic granular sludge (AGS), an adsorption-regeneration process was employed to remove organic matter at the front end of the Anammox process through bio-adsorption in an artificial simulated domestic sewage environment, and it was successfully used for denitrification.
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