Conference Agenda

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).

Session Overview
Session 08A: Wastewater Process: Deammonification
Tuesday, 14/Sept/2021:
8:00am - 9:30am

Location: 110AB

East Building

External Resource:
Show help for 'Increase or decrease the abstract text size'
8:00am - 8:45am

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.

8:45am - 9:30am

Sidestream Deammonification MABR Development and Performance in Bench-Scale Reactor Treating Anaerobic Digester Dewatering Centrate

Bryce Figdore


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.