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This paper examines the design and implementation of a full-scale integrated fixed-film activated sludge (IFAS) partial denitrification-anammox (PdNA) process at the Hampton Roads Sanitation District (HRSD) James River Treatment Plant (JRTP) in Newport News, VA, USA. The study assesses the operational outcomes of PdNA in the postanoxic zone of two full-scale demonstration treatment trains. Over 650 days, the first implementation, IFAS 1, underwent three supplemental carbon combinations for partial denitrification (PdN): step-fed primary clarifier effluent (PCE), methanol and PCE, and glycerol and PCE. Anammox bacteria were established in IFAS 1 144 days post-startup, during the second phase of carbon addition, marking the first successful full-scale deliberate application of an integrated PdNA process. Once IFAS 1's maximum anammox activity reached steady state during the final phase of carbon addition, IFAS 1 achieved an average in situ total inorganic nitrogen (TIN) removal rate of 0.93 ± 0.52 g/m/day (0.35 ± 0.24 g/m/day due to anammox). The second reactor, IFAS 2, was implemented a year later, using only step-fed PCE as an external carbon source. Anammox bacteria were confirmed in IFAS 2 192 days post-startup, demonstrating the potential for establishing anammox without an external carbon source and highlighting anammox bacteria's ability to establish and persist under limited nitrite (NO ) conditions. Although IFAS 2 demonstrated that PCE was sufficient for anammox establishment, the more limited carbon available for maintaining anoxic conditions and promoting PdN resulted in minimal in situ anammox activity and a lower maximum anammox activity (0.18 ± 0.05 g-N/m/day). However, IFAS 1 demonstrated that supplementing external carbon with PCE can result in substantial carbon savings. At steady state, supplementing glycerol addition with PCE in IFAS 1 increased carbon savings from 43% to 75% compared to full denitrification. This study offers valuable insights into the operational dynamics, challenges, and benefits of implementing full-scale mainstream PdNA, thereby contributing to the intensification of wastewater treatment processes. PRACTITIONER POINTS: For the first time, a deliberate design and implementation of a full-scale mainstream IFAS PdNA process was successfully completed. Anammox activity was established without biomass seeding, and it was not prevented by using carbons with lower PdN efficiencies. Significant carbon cost savings were achieved by supplementing external carbon with carbon provided via step feed to the PdNA zone. Anammox's ability to remove ammonia coming with step feed to the second anoxic zone is a unique benefit of PdNA.
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http://dx.doi.org/10.1002/wer.70093 | DOI Listing |
J Environ Manage
September 2025
National and Local Joint Engineering Laboratory of Municipal Sewage Resource Utilization Technology, Jiangsu Collaborative Innovation Center of Technology and Material of Water Treatment, School of Environmental Science and Engineering, Suzhou University of Science and Technology, Suzhou, 215009, Ch
The anaerobic ammonia oxidation (anammox) process has attracted considerable interest for its advantages in low energy requirements, reduced sludge output, and eliminating the need for external carbon sources. However, its application is constrained by the long generation time, slow growth, and challenges in enriching anammox bacteria. Studies indicate that carbon material addition significantly accelerates anammox bacteria proliferation, enhances nitrogen removal efficiency, and improves anammox microbial activity.
View Article and Find Full Text PDFJ Environ Manage
September 2025
State Environmental Protection Engineering Center for Pollution Treatment and Control in Textile Industry, College of Environmental Science and Engineering, Donghua University, Shanghai, 201620, China. Electronic address:
Multivalent cations are commonly employed to accelerate sludge aggregation and granulation, yet they often compromise intragranular mass transfer and diminish microbial activity. Here, the effect of Fe(III) dosing on granule formation and anammox-driven nitrogen removal over a 110-day continuous operation was investigated. Fe(III) supplementation enhanced interactions with extracellular polymeric substances (EPS), transforming flocculent biomass into highly porous granules and yielding a 67.
View Article and Find Full Text PDFEnviron Res
September 2025
National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Beijing University of Technology, Beijing 100124, PR China.
Partial denitrification coupled with anammox (PD/A) has emerged as a promising low-carbon strategy for energy-efficient nitrogen removal from municipal wastewater. However, the reactivation of PD/A systems following operational disturbances remains challenging, particularly under continuous-flow conditions, where microbial interactions and process stability are more complex than in sequencing batch reactors. This study systematically and first evaluated the recovery dynamics of a continuous-flow PD/A process seeded with low-activity granular sludge stored at 4 °C for three months.
View Article and Find Full Text PDFBiotechnol Bioeng
September 2025
Department of Environmental Engineering, School of Chemistry and Chemical Engineering, Henan University of Science and Technology, Luoyang, China.
Chloroacetonitrile poses significant challenges to anaerobic ammonium oxidation (anammox) process due to its toxicity. This study evaluated the effects of chloroacetonitrile on anammox and further explored the potential of a 1.5 V and 1000 Hz pulsed electric field (PEF) in mitigating prolonged chloroacetonitrile stress.
View Article and Find Full Text PDFWater Res
August 2025
College of Bio-systems Engineering and Food Science, Zhejiang University, Hangzhou 310058, China; Ocean Academy, Zhejiang University, Zhoushan, 316021, China. Electronic address:
Salinity-driven nitrogen removal mechanisms in iron-carbon CWs (Fe-C-CWs) remain poorly understood for aquaculture tailwater management. Through a 155-day trial under four salinities (designated as S0, S10, S20, and S30), result showed that S20 achieved optimal removals of total nitrogen (84.9 ± 3.
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