Overview and details of the sessions of this conference. Please select a date or location to show only sessions at that day or location. Please select a single session for detailed view (with abstracts and downloads if available).
8:00am - 8:45am ID: 254 / Session 08A: 1 Main Technical Program Topics: Treatment Innovation and the Future, Wastewater Treatment Process, Recycled Water & Resource Recovery Keywords: deammonification, recycle streams, natural treatment systems
Zeolite-anammox Deammonification Of Biosolids Dewatering Recycle Stream: A Public Domain Technology
David Austin, Mark Madison
Jacobs, United States of America;
The Roseburg Urban Sanitary Authority (RUSA) operates an innovative deammonification wetland capable of treating 5,000 gallons per day, of biosolids filtrate that has an ammonia-N concentration averaging nearly 1,000 mg/L. Liquid from solids dewatering can go either to irrigation or deammonification. The purpose of the wetland is to remove ammonia-nitrogen during periods in the spring when irrigation is not feasible. It is the first commercial zeolite-anammox system.
Biosolids generated at RUSA’s WWTP are dewatered in a center screw press Monday-Friday, year-round. The filtrate from this screw press flows to an off-line clarifier and then is batch-loaded to two wetland cells by siphons. Wetland media is clinoptilolite (a zeolite). Beds drain by siphons to a recirculation basin where a pump transfers wetland effluent to the dosing siphons. Beds flood and drain excess water is pumped back to the plant’s aeration basins.
The wetland started in November 2016 and this presentation will focus on discussing the 4 years of operational experience as well as lessons learned. After a year of complete nitrification, the wetland converted to deammonification (anammox). Since then it has averaged 53 percent deammonification, significantly reduced the ammonia recycle load on the WWTP. Performance has been highly consistent in the past three years. Adding alkalinity to maintain pH above 7.0 while in the nitrification phase was crucial to establish deammonification. Once deammonification started, alkalinity demand stopped. However, recent analysis of performance indicates that maintaining a consistent operational pH of 7.5 to 8.0 – which is ideal - may require occasional alkalinity addition.
This technology is simple and non-proprietary and has potential broad application for small to medium size wastewater systems. Flood and drain contact beds were first used in the 1890s. Anammox was first observed in a contact bed in 1902. Recirculation in flood and drain beds is also public domain technology. With careful attention to design loading criteria, construction detail including the zeolite source, and alkalinity addition during the first nitrification phase; this technology is available to utilities to manage recycle streams with high levels of ammonia-N.
Brief Biography and/or Qualifications David Austin is a Technology Fellow at Jacobs where he is the Global Technology lead for Natural Treatment Systems. He is an environmental P.E. (MN), Certified Senior Ecologist (Ecological Society of America), Certified Lake Manager (North American Lake Management Society), and a past President of the American Ecological Engineering Society. His projects concentrate on reservoir management, treatment wetlands, wastewater reuse, estuarine remediation, and mine water reclamation. Degrees: Mathematics (BA, University of Minnesota-Twin Cities), Water Resources Management (MS, University of Wisconsin-Madison), and Civil & Environmental Engineering (MS, University of California-Davis).
8:45am - 9:30am ID: 103 / Session 08A: 2 Main Technical Program Topics: Treatment Innovation and the Future, Wastewater Treatment Process Keywords: sidestream, nitrogen, anammox, deammonification, MABR
Sidestream Deammonification MABR Development and Performance in Bench-Scale Reactor Treating Anaerobic Digester Dewatering Centrate
A partial nitritation-anammox (deammonification) biofilm was grown in a bench-scale membrane-aerated biofilm reactor (MABR) treating dewatering centrate from a full-scale conventional mesophilic anaerobic digestion process. Anammox activity developed within 165 days of startup in absence of intentional seeding events or strategies such as seeding from an external enrichment or an integrated second-stage process treating partial nitritation effluent.
Average surficial NH3-N and TIN removal rates were 2.6 and 2.3 g N/m2-d for the 77-day operating period ending September 28, 2020 after anammox growth occurred and stabilized. In-situ anammox activity tests confirmed anammox activity and showed an average anaerobic TIN removal rate of 5.3 g N/m2-d under non-limiting substrate conditions, indicating that aerobic rather than anaerobic ammonia oxidation activity was rate-limiting under operational conditions.
These results suggest that MABR may be a viable deammonification alternative with reduced energy, seeding, and startup requirements compared to established commercial approaches.
Ongoing operations are further evaluating fundamental research questions, optimization strategies, and full-scale engineering implications.
Brief Biography and/or Qualifications Bryce Figdore is a senior wastewater process engineer with HDR based in Bellevue, WA. He is enthusiastic about applying his expertise in biological nutrient removal to deliver innovative and robust wastewater treatment and water resource management solutions. Bryce has Bachelor’s, Master’s and Doctorate degrees, respectively, from Penn State, Villanova, and the University of Washington. He enjoys exploring the great Pacific Northwest while fly fishing or hiking with his family.