Residential subsurface flow treatment wetlands in northern Minnesota

2001 ◽  
Vol 44 (11-12) ◽  
pp. 345-352 ◽  
Author(s):  
R. Axler ◽  
J. Henneck ◽  
B. McCarthy

Approximately 30% of Minnesotans use on-site systems (~500,000 residences) and >50% are failing or non-compliant with regulations due to restrictive soils and site conditions. Many sites occur near lakes and streams creating health hazards and deteriorating water quality. SSF CWs have been evaluated year-round at two northern sites since 1995. The NERCC CWs simulate single homes and the Grand Lake demonstration CW treats STE from a cluster of 9 lakeshore homes. Systems were generally able to achieve design criteria of 25 mgTSS/L and 30 mgBOD5/L and the NERCC CWs required only 0.3m of unsaturated soil to achieve consistent disinfection to <200 fecals/100 mL year round. Seeding experiments with Salmonella indicated removal efficiencies of 99.8% in summer and 95% in winter. High strength (∼300 mgBOD/L, 95 mgTN/L) influent at NERCC probably limited system performance, particularly N-removal (mass) which was ∼42% in summer and 20% in winter. The data indicate CW's are a viable, year-round treatment option for homeowners in terms of performance, ease of operation, and cost but require additional maintenance related to inconsistent vegetation growth, winter insulation, and meeting concentration-based regulatory standards since they were seasonally and annually variable due to rain events, partial freezing, spring snowmelt, and summer evapotranspiration.

2015 ◽  
Vol 72 (12) ◽  
pp. 2236-2242 ◽  
Author(s):  
L. I. Borges ◽  
C. M. López-Vazquez ◽  
H. García ◽  
J. B. van Lier

In this study, nitrite reduction and methanogenesis in a single-stage upflow anaerobic sludge blanket (UASB) reactor was investigated, using high-strength synthetic domestic wastewater as substrate. To assess long-term effects and evaluate the mechanisms that allow successful nitrite reduction and methanogenesis in a single-stage UASB, sludge was exposed to relatively high nitrite loading rates (315 ± 13 mgNO2−-N/(l.d)), using a chemical oxygen demand (COD) to nitrogen ratio of 18 gCOD/gNO2−-N, and an organic loading rate of 5.4 ± 0.2 gCOD/(l.d). In parallel, the effects of sludge morphology on methanogenesis inhibition were studied by performing short-term batch activity tests at different COD/NO2−-N ratios with anaerobic sludge samples. In long-term tests, denitrification was practically complete and COD removal efficiency did not change significantly after nitrite addition. Furthermore, methane production only decreased by 13%, agreeing with the reducing equivalents requirement for complete NO2− reduction to N2. Apparently, the spatial separation of denitrification and methanogenesis zones inside the UASB reactor allowed nitrite reduction and methanogenesis to occur at the same moment. Batch tests showed that granules seem to protect methanogens from nitrite inhibition, probably due to transport limitations. Combined COD and N removal via nitrite in a single-stage UASB reactor could be a feasible technology to treat high-strength domestic wastewater.


2021 ◽  
Author(s):  
Kuno Kasak ◽  
Keit Kill ◽  
Evelyn Uuemaa ◽  
Ülo Mander

<p>Treatment wetlands are widespread measures to reduce agricultural diffuse pollution. Systems that are often planted with emergent macrophytes such as Typha spp. and Phragmites spp. are efficient to reduce nutrients, particularly nitrogen and phosphorus compounds. While many experiments have been conducted to study the emission of carbon dioxide (CO<sub>2</sub>) and methane (CH<sub>4</sub>), little attention has been paid for the emission of nitrous oxide (N<sub>2</sub>O). Few studies have been shown that usually N<sub>2</sub>O emission from water saturated ecosystems such as wetlands is low to negligible. In Vända in-stream treatment wetland that was built in 2015 and located in southern Estonia, we carried out first long term N<sub>2</sub>O measurements using floating chambers. The total area of the wetland is roughly .5 ha; 12 boardwalks, each equipped with two sampling spots, were created. Samples were collected biweekly from March 2019 through January 2021. In each sampling campaign water table depth, water and air temperature, O<sub>2</sub> concentration, oxygen reduction potential, pH and electrical conductivity were registered. Water samples for TN, NO<sub>3</sub>-N, NO<sub>2</sub>-N, TOC, TIC and TC were collected from inflow and outflow of the system in each sampling session and the average concentrations were 5.1 mg/L, 3.68 mg/L, <0.1 mg/L, 41.2 mg/L and 28.7, respectively. Our results showed a very high variability of N<sub>2</sub>O emission: the fluxes ranged from -4.5 ug m<sup>-2</sup> h<sup>-1</sup> to 2674.2 ug m<sup>-2</sup> h<sup>-1</sup> with mean emission of 97.3 ug m<sup>-2</sup> h<sup>-1</sup>. Based on gas samples (n=687) we saw a strong correlation (R<sup>2</sup> = -0.38, p<0.0001) between N<sub>2</sub>O emission and water depth. The average N<sub>2</sub>O emission from sections with the water table depth >15 cm was 45.9 ug m<sup>-2</sup> h<sup>-1</sup> while sections with water table depth <15 cm showed average emission of 648.3 ug m<sup>-2</sup> h<sup>-1</sup>. The difference between these areas was more than 10 times. Water temperature that is often considered as the main driver had less effect to the N<sub>2</sub>O emission. For instance, at lower temperatures, when the emissions from deeper zones decreased, there was no temperature effect on emissions from shallow zones. We also saw that over the years the overall N<sub>2</sub>O emission followed clear seasonal dynamics and has a slight trend towards lower emissions. This can be related to the more intensive vegetation growth that has been increased from ~40% in 2019 to approximately 90% in 2020. Our study demonstrates that the design of the wetland is not only important for the water treatment, but it can also determine the magnitude of greenhouse gas emissions. We saw that even slight changes in water table depth can have a significant effect on the annual N<sub>2</sub>O emission. Thus, in-stream treatment wetlands that have water table depth at least 15 cm likely have remarkably lower N<sub>2</sub>O emissions without losing water treatment efficiency.</p><p> </p>


2018 ◽  
Vol 642 ◽  
pp. 208-215 ◽  
Author(s):  
R. Lombard-Latune ◽  
L. Pelus ◽  
N. Fina ◽  
F. L'Etang ◽  
B. Le Guennec ◽  
...  

2020 ◽  
Vol 713 ◽  
pp. 136510 ◽  
Author(s):  
German Dario Martinez-Carvajal ◽  
Laurent Oxarango ◽  
Rémi Clément ◽  
Pascal Molle ◽  
Nicolas Forquet

2020 ◽  
Vol 742 ◽  
pp. 140608
Author(s):  
Camila Maria Trein ◽  
Camille Banc ◽  
Kevin Maciejewski ◽  
Amanda de Moraes Motta ◽  
Rémy Gourdon ◽  
...  

Author(s):  
Tong Wang ◽  
Tong Wu ◽  
Haiyan Wang ◽  
Weiyang Dong ◽  
Yaqian Zhao ◽  
...  

Nitrogen (N) remains a great challenge in wastewater treatment while attempts to remove N has continuously been a research point for decades. In this study, the long-term performance of four identical-shape denitrification MBBRs (moving bed biofilm reactors) with four different configurations of cylindrical polyethylene as carriers (Φ25 × 12, Φ25 × 4, Φ15 × 15, and Φ10 × 7 mm) for advanced N removal of real reverse osmosis concentrate was investigated in great detail. The N of the real concentrate can be effectively removed by denitrification MBBRs when the pH, temperature, hydraulic retention time (HRT), C/N ratio, and filling rate are 7.50–8.10, 24~26 °C, 12 hours, 6.6, and 50%, respectively. The results showed that the MBBR with the Φ15 × 15 poly-carrier had the best removal efficiency on NO3-–N (78.0 ± 15.8%), NO2-–N (43.79 ± 9.30%), NH4+–N (55.56 ± 22.28%), and TN (68.9 ± 12.4%). The highest biomass of 2.13 mg/g-carrier was in the Φ15 × 15 poly-carrier was compared with the other three carriers, while the genes of the Φ15 × 15 poly-carrier reactor were also the most abundant. Proteobacteria was the most abundant phylum in the system followed by Bacteroidetes and then Firmicutes. The entire experiment with various parameter examination supported that Φ15 × 15 poly-carrier MBBR was a promising system for N removal in high strength concentrate. Despite the lab-scale trial, the successful treatment of high strength real reverse osmosis concentrate demonstrated the reality of the treated effluent as possible reclaimed water, thus providing a good showcase of N-rich reverse osmosis concentrate purification in practical application.


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