Microbial interactions and nitrogen removal performance in an intermittently rotating biological contactor treating mature landfill leachate.

Developing efficient landfill leachate treatment is still necessary to reduce environmental risks. However, nitrogen removal in biological treatment systems is often poor or costly. Studying biofilms in anoxic/aerobic zones of rotating biological contactors (RBC) can elucidate how microbial interactions confer resistance to shock loads and toxic substances in leachate treatment. This study assessed the nitritation-anammox performance in an intermittent-rotating bench-scale RBC treating mature leachate (diluted). Despite the leachate toxicity, the system achieved nitritation with an efficiency of up to 34 % under DO values between 0.8 and 1.8 mg.L-1. The highest average ammoniacal nitrogen removal was 45.3 % with 10 h of HRT. The 16S rRNA sequencing confirmed the presence of Nitrosonomas, Aquamicrobium, Gemmata, and Plantomyces. The coexistence of these bacteria corroborated the selective pressure exerted by leachate in the community structure. The microbial interactions found here highlight the potential application of RBC to remove nitrogen in landfill leachate treatment.

Comparative assessment of energy generation from ammonia oxidation by different functional bacterial communities.

Bioelectrochemical ammonia oxidation (BEAO) in a microbial fuel cell (MFC) is a recently discovered process that has the potential to reduce energy consumption in wastewater treatment. However, level of energy and limiting factors of this process in different microbial groups are not fully understood. This study comparatively investigated the BEAO in wastewater treatment by MFCs enriched with different functional groups of bacteria (confirmed by 16S rRNA gene sequencing): electroactive bacteria (EAB), ammonia oxidizing bacteria (AOB), and anammox bacteria (AnAOB). Ammonia oxidation rates of 0.066, 0.083 and 0.082 g NH4+-N L-1 d-1 were achieved by biofilms enriched with EAB, AOB, and AnAOB, respectively. With influent 444 ± 65 mg NH4+-N d-1, nitrite accumulation between 84 and 105 mg N d-1 was observed independently of the biofilm type. The AnAOB-enriched biofilm released electrons at higher potential energy levels (anode potential of 0.253 V vs. SHE) but had high internal resistance (Rint) of 299 Ω, which limits its power density (0.2 W m-3). For AnAOB enriched biofilm, accumulation of nitrite was a limiting factor for power output by allowing conventional anammox activity without current generation. AOB enriched biofilm had Rint of 18 ± 1 Ω and yielded power density of up to 1.4 W m-3. The activity of the AOB-enriched biofilm was not dependent on the accumulation of dissolved oxygen and achieved 1.5 fold higher coulombic efficiency when sulfate was not available. The EAB-enriched biofilm adapted to oxidize ammonia without organic carbon, with Rint of 19 ± 1 Ω and achieved the highest power density of 11 W m-3. Based on lab-scale experiments (scaling-up factors not considered) energy savings of up to 7 % (AnAOB), 44 % (AOB) and 475 % (EAB) (positive energy balance), compared to conventional nitrification, are projected from the applications of BEAO in wastewater treatment plants.

Nitrification in multistage horizontal flow treatment wetlands for landfill leachate treatment.

One of the key challenges in landfill leachate treatment is removing organic matter (OM) and ammonium nitrogen (NH4+-N) at a low cost. To evaluate the feasibility of treatment wetlands for diluted (3:10) landfill leachate treatment with OM and NH4+-N oxidation, a lab-scale shallow subsurface horizontal flow system (HF wetland) comprised of two units operated in series was assessed as post-treatment of partial ammonia stripping system. A HF wetland planted with Heliconia psittacorum (HP) and an unplanted HF wetland (control) were supplemented with micronutrients and monitored under the influence of hydraulic retention time (HRT), pH, and the plant presence on performance. With an HRT above 4 days, mean chemical oxygen demand removal for both HP and the control was less than 20%, without complete mineralization, probably due to the recalcitrance of OM. For NH4+-N, the mean global removal efficiencies with and without influent pH adjustment were, respectively, 74% and 54% for HP and 56% and 43% for the control, resulting in mean concentrations between 36 and 93 mg L-1. The NH4+-N removal was correlated with inorganic carbon consumption followed by NO3- production, which suggests that nitrification was the major route of removal. For both systems, nitrification was significantly higher in one of the units, when biodegradable OM was already consumed and competition between heterotrophic and autotrophic bacteria for dissolved oxygen was likely minimized. By balancing the organic load and availability of dissolved oxygen within each unit in series, a reduced HRT necessary for NH4+-N oxidation was achieved, an essential aspect for the design of high performance constructed wetlands for full scale landfill leachate treatment.

Influence of recirculation over COD and N-NH4 removals from landfill leachate by horizontal flow constructed treatment wetland.

Treatment of landfill leachate is a challenge due to its complex chemical composition and high recalcitrance and because of high costs for conventional wastewater treatment. In our study, leachate from the Quitaúna Landfill, Sao Paulo Metropolitan Region, Brazil, was treated at a laboratory scale with a horizontal subsurface flow constructed treatment wetland (HF-CTW) operating under a recirculation regime. Two units planted with Heliconia psittacorum (HP) and Cyperus papyrus (CP), and one unplanted control unit were assessed. With a recirculation regime over 21 days, the planted units removed 40% of chemical oxygen demand (COD) while the control unit removed only 29%. True color removal efficiencies were 2, 22, and 23% for the control, HP, and CP HF-CTWs, respectively. The ammonium nitrogen removal efficiencies for a 21-day hydraulic retention time (HRT) were 63-81% for planted units and 72% for the control. The increase of the HRT from 7 to 21 days led to the enhancement of ammonium nitrogen removal but did not affect the COD and total nitrogen removals. This phenomenon is a consequence of leachate's low biodegradability. The present study shows the importance of the HRT and plant presence for landfill leachate treatment using HF-CTWs.

Estratégias de tratamento de lixiviado de aterro sanitário com foco na matéria orgânica biodegradável e nitrogênio amoniacal / Strategies of landfill leachate treatment focused on biodegradable organic matter and ammonia nitrogen

Sistemas de tratamento de esgotos, quando aplicados ao tratamento de lixiviado de aterro sanitário, não têm apresentado bons resultados. Por conta disso, faz-se necessário o desenvolvimento de alternativas para o tratamento de lixiviado. Objetivo avaliar o pós-tratamento de lixiviado de aterro sanitário por wetland construído de fluxo subsuperficial horizontal e reator biológico de leito móvel (RBLM). Materiais e métodos foram realizados dois experimentos com tratamento de lixiviado após remoção de amônia por dessorção. No experimento 1 utilizou-se wetlands construídos de fluxo horizontal em escala de bancada (volume total de 30,8 L), plantados com Cyperus papyrus, Heliconia psittacorum e Gynerium sagittatum, e um controle sem vegetação, preenchidos com pedrisco calcário. O sistema foi alimentado com lixiviado diluído em água em diferentes proporções (entre 10 por cento e 30 por cento ) com concentração média de DQO entre 336 e 750 mg.L-1 e nitrogênio amoniacal (N-NH4) entre 47 e 199 mg.L-1. A operação ocorreu em três etapas: (1ª) alimentação contínua e TDH médio entre 2,7 e 5,3 d; (2ª) regime de ciclos de recirculação do efluente, para avaliar o efeito do aumento de TDH para 21 dias; (3ª) alimentação contínua de duas unidades wetlands em série, visando elevar o TDH (entre 8,1 e 9,9 d) sem recirculação. O experimento 2 foi implantado em escala piloto, com uma unidade de dessorção de amônia seguida de um Reator Biológico de Leito Móvel (RBLM) e um biofiltro anóxico. O RBLM (volume efetivo de 380 L) foi preenchido em 50 por cento com anel pall. Resultados e discussão No experimento 1, obteve-se baixa remoção de DQO com médias inferiores a 40 por cento e concentração final entre 270 e 750 mg.L-1...

sewage treatment systems, when applied to the treatment of landfill leachate, have not shown good results. Thus it is necessary to develop alternatives for the treatment of leachate. Objective To assess the post-treatment of landfill leachate by horizontal subsurface flow constructed wetland and moving bed biofilm reactor (MBBR). Materials and methods Two experiments were conducted with treatment of the leachate after removal of ammonia by stripping. In experiment 1, horizontal flow constructed wetlands, at bench scale (total volume of 30.8 L), planted with Cyperus papyrus, Heliconia psittacorum and Gynerium sagittatum, and a control without vegetation, were filled with calcareous gravel. The system was fed with leachate diluted in water with different proportions (between 10 per cent and 30 per cent ) with mean COD concentration of between 336 and 750 mg.L-1 and ammonia nitrogen (NH4-N) between 47 and 199 mg L-1. The operation was divided in three stages: (1st) continuous feeding with mean HRT between 2.7 and 5.3 d; (2nd) regime of effluent recirculation to evaluate the effect of increasing the HRT to 21 days; (3rd) continuous feeding with two wetlands units in series, aimed HRT increasing (between 8.1 and 9.9 d) without recirculation. Experiment 2 was implemented on a pilot scale, with a unit of ammonia stripping followed by MBBR and an anoxic biofilter. The MBBR (380 L working volume) was filled 50 per cent with pall ring. Results and discussion In experiment 1, the COD removal was low, with averages below 40 per cent , with effluent concentration between 270 and 750 mg.L-1...