modelEAU, Département de génie civil et de génie des eaux, Université Laval, Québec City, Québec, Canada.
Hampton Roads Sanitation District, Virginia Beach, Virginia, USA.
Water Environ Res. 2023 Aug;95(8):e10917. doi: 10.1002/wer.10917.
The integration of biological phosphorus removal (bio-P) and shortcut nitrogen removal (SNR) processes is challenging because of the conflicting demands on influent carbon: SNR allows for upstream carbon diversion, but this reduction of influent carbon (especially volatile fatty acids [VFAs]) prevents or limits bio-P. The objective of this study was to achieve SNR, either via partial nitritation/anammox (PNA) or partial denitrification/anammox (PdNA), simultaneously with biological phosphorus removal in a process with upstream carbon capture. This study took place in a pilot scale A/B process with a sidestream bio-P reactor and tertiary anammox polishing. Despite low influent rbCOD concentrations from the A-stage effluent, bio-P occurred in the B-stage thanks to the addition of A-stage WAS fermentate to the sidestream reactor. Nitrite accumulation occurred in the B-stage via partial denitrification and partial nitritation (NOB out-selection), depending on operational conditions, and was removed along with ammonia by the tertiary anammox MBBR, with the ability to achieve effluent TIN less than 2 mg/L. PRACTITIONER POINTS: A sidestream reactor with sufficient fermentate addition enables biological phosphorus removal in a B-stage system with little-to-no influent VFA. Enhanced biological phosphorus removal is not inhibited by intermittent aeration and is stable at a wide range of process SRTs. Partial nitritation and partial denitrification are viable routes to produce nitrite within an A/B process with sidestream bio-P, for downstream anammox in a polishing MBBR.
生物除磷(bio-P)和短程硝化反硝化(SNR)工艺的集成具有挑战性,因为对进水碳源有相互矛盾的需求:SNR 允许上游碳转移,但这种进水碳源的减少(特别是挥发性脂肪酸[VFAs])会阻止或限制生物除磷。本研究的目的是在具有上游碳捕获的工艺中,通过部分硝化/厌氧氨氧化(PNA)或部分反硝化/厌氧氨氧化(PdNA)实现 SNR,同时进行生物除磷。本研究在带有侧流生物除磷反应器和三级厌氧氨氧化抛光的中试规模 A/B 工艺中进行。尽管来自 A 段出水的 rbCOD 浓度较低,但由于将 A 段 WAS 发酵液添加到侧流反应器中,B 段仍发生生物除磷。硝态氮积累通过部分反硝化和部分硝化(NOB 选择)发生在 B 段,这取决于操作条件,并且与氨一起通过三级厌氧氨氧化 MBBR 去除,具有实现低于 2mg/L 的出水 TIN 的能力。
具有足够发酵液添加的侧流反应器可在几乎没有进水 VFA 的 B 段系统中实现生物除磷。
增强的生物除磷不受间歇曝气的抑制,并且在广泛的工艺 SRT 下稳定。
在具有侧流生物除磷的 A/B 工艺中,部分硝化和部分反硝化是在下游厌氧氨氧化 MBBR 中产生亚硝酸盐的可行途径。