Use of nitrate, sulphate, and iron (III) as electron acceptors to improve the anaerobic degradation of linear alkylbenzene sulfonate: effects on removal potential and microbiota diversification.

Linear alkylbenzene sulfonate (LAS) is a synthetic anionic surfactant that is found in certain amounts in wastewaters and even in water bodies, despite its known biodegradability. This study aimed to assess the influence of nitrate, sulphate, and iron (III) on LAS anaerobic degradation and biomass microbial diversity. Batch reactors were inoculated with anaerobic biomass, nutrients, LAS (20 mg L-1), one of the three electron acceptors, and ethanol (40 mg L-1) as a co-substrate. The control treatments, with and without co-substrate, showed limited LAS biodegradation efficiencies of 10 ± 2% and 0%, respectively. However, when nitrate and iron (III) were present without co-substrate, biodegradation efficiencies of 53 ± 4% and 75 ± 3% were achieved, respectively, which were the highest levels observed. Clostridium spp. was prominent in all treatments, while Alkaliphilus spp. and Bacillus spp. thrived in the presence of iron, which had the most significant effect on LAS biodegradation. Those microorganisms were identified as crucial in affecting the LAS anaerobic degradation. The experiments revealed that the presence of electron acceptors fostered the development of a more specialised microbiota, especially those involved in the LAS biodegradation. A mutual interaction between the processes of degradation and adsorption was also shown.

Anaerobic co-digestion of microalgal biomass, sugarcane vinasse, and residual glycerol from biodiesel using simplex-centroid mixture design: methane potential, synergic effect, and microbial diversity.

Microalgal biomass (MB) is a promising feedstock for bioenergy production. Nonetheless, the cell recalcitrance and the low C/N ratio limit the methane yield during anaerobic digestion. As an alternative to overcome these challenges, MB co-digestion with different feedstocks has been proposed. Thus, this study evaluated the anaerobic co-digestion (AcoD) of MB cultivated in wastewater with sugarcane vinasse (VIN) and residual glycerol from biodiesel production (GLY). Batch tests were conducted using augmented simplex-centroid mixture design to investigate the impact of AcoD on methane production (SMP), synergistic effects, and the influence on microbial community. When compared to MB digestion, 150 NmL CH4.g-1VS, binary and ternary AcoD achieved SMP increases from 120 to 337%. The combination of 16.7:16.7:66.7 (MB:VIN:GLY) showed the highest SMP for a ternary mixture (631 NmL CH4.g-1VS). Optimal synergies ranged from 1.3 to 1.4 and were primarily found for the MB:GLY AcoD. Acetoclastic Methanosaeta genus was predominant, regardless the combination between substrates. Despite the largest SMP obtained from the MB:GLY AcoD, other ternary mixtures were also highly synergetic and therefore had strong potential as a strategic renewable energy source.

Effect of filtration rates on the performance and head loss development in granular filters during the post-treatment of anaerobic reactor effluent.

This study investigated the performance of a granular filtration system (GFS) composed of a rock filter (RF), a rapid sand filter (RSF), and an activated carbon filter (ACF), applied to the post-treatment of an anaerobic reactor effluent. Four filtration rates (FR) were applied to the GFS (in m3·m-2·d-1): 100-60-60, 100-90-90, 200-120-120, and 200-160-160, for RF-RSF-ACF, respectively. A clarified final effluent with low turbidity (~ 10 NTU), solids (~ 6.5 mg TSS.L-1), and organic matter content (~ 40 mg COD.L-1) was obtained when the GFS worked with FR up to 100-90-90 m3·m-2·d-1. For higher FR, the effluent quality was a little poorer. Principal component analysis showed when the RSF operated at 120 or 160 m3·m-2·d-1, it presented an effluent with higher turbidity which did not affect negatively the ACF performance. The hydraulic load limits in the RSF were reached in periods of 45, 30, and 24.5 h for the FR of 60, 120, and 160 m3·m-2·d-1, respectively, and head loss analysis depicted a more distributed solid retention through the sand depth with the lower FR. Thus, the results revealed that the RF-RSF-ACS system is a promising alternative for effluent polishing of anaerobic reactor, especially when the FR is set at 90 m3·m-2·d-1 or even higher.

Effect of reclaimed water and dehydrated sludge on the morpho-physiology and yield of sorghum.

The effect on the morpho-physiological parameters and yield of sorghum cultivated in a greenhouse with reclaimed water (RW) and (dehydrated sludge (DS) obtained in a sewage treatment plant, was evaluated. Six treatments (T), with five repetitions each, were carried out in entirely randomized blocks. Water (W) was used in T1 (W) (control), T2 (W + NPK), and T3 (W + DS); RW was used in T4 (RW), T5 (RW + P), and T6 (RW + DS). The results showed that irrigation with only RW (T4), or W + DS (T3) was very suitable for the cultivation since an adequate nutritional supply was provided. The positive effects on the morpho-physiological parameters, plant height, stem diameter and stem length (in cm), were: T3 - 148.8, 1.50, and 103, respectively; T4 - 154, 1.70, and 107, respectively; and on the grain production in weight of 1000 seeds (g), and productivity in grains per plant: T3 - 6.97 and 1453, respectively; T4 - 6.81 and 1636, respectively. Both treatments showed for most of the parameters, no significant differences compared with those of T2 or T5 with supplementary fertilizers. A high production of metabolites (mg g-1) like free amino acids was also shown: T3 - 6.45; T4 - 8.43 and proline: T3 - 1.86; T4 - 1.77, known to be a good indication of a plant natural defence against stress conditions, and in soluble protein: T3 - 11.20; T4 - 13.51. Therefore, since the production of such grains with RW or DS can be environmentally and economically beneficial, their use is recommended for small and medium farmers in semiarid regions.

Mesophilic anaerobic digestion of waste activated sludge in an intermittent mixing reactor: Effect of hydraulic retention time and organic loading rate.

An anaerobic digester was operated at mesophilic temperature and with intermittent mixing conditions to treat waste activated sludge. The organic loading rate (OLR) was increased by decreasing the hydraulic retention time (HRT), and the effect on process performance, digestate characteristics and inactivation of pathogens was investigated. The removal efficiency of total volatile solids (TVS) was also measured by biogas formation. The HRT varied from 50 to 7 days, corresponding to OLR from 0.38 to 2.31 kgTVS.m-3.d-1. The acidity/alkalinity ratio remained within stable limits (lower than 0.6) at 50-, 25- and 17-day HRT; due to an imbalance between the production and consumption of volatile fatty acids, the ratio increased to 0.7 ± 0.2 at HRT of 9 days and 7 days. The highest TVS removal efficiencies were 16, 12 and 9%, which were obtained at 50-, 25- and 17 day-HRT, respectively. Intermittent mixing provided solids sedimentation greater than 30% for almost all HRT tested. The highest methane yields (0.10-0.05 m3.kgTVSfed-1.d-1) were obtained when the reactor was operated at a higher HRT (50-17 days). At lower HRT, methanogenic reactions were likely limited. Zinc and copper were the main heavy metals found in the digestate, while the most probable number (MPN) of coliform bacteria remained below 106 MPN.g TVS-1. Neither Salmonella nor viable Ascaris eggs were found in the digestate. In general, increasing the OLR by decreasing the HRT to 17 days under intermittent mixing conditions provided an attractive alternative to treat sewage sludge despite some limitations due to biogas and methane yields.

Biological treatment of real textile wastewater containing sulphate, salinity, and surfactant through an anaerobic-aerobic system.

Real textile wastewater containing high salinity (up to 12.6 g·kg-1) and surfactant (up to 5.9 mg·L-1 of linear alkylbenzene sulfonate - LAS) was submitted to biological treatment for colour (up to 652 mg Pt-Co·L-1) and sulphate (up to 1,568.6 mg SO4-2·L-1) removal. The influence of ethanol and molasses supplementation was firstly evaluated in anaerobic batch reactors for the removal of dyes and sulphate. Subsequently, aiming to remove aromatic amines (dye degradation by-products), an anaerobic-aerobic continuous system supplemented with molasses was applied. Supplementation had no influence on colour removal (maximum efficiencies around 70%), while it improved sulphate reduction (23% without supplementation against 87% with supplementation), and conferred robustness to the reactors, which recovered quickly after higher salinity impact. The aerobic reactor removed aromatic amines when the level of surfactants was lower than 1.0 mg LAS·L-1, but the performance of the system was hindered when the concentration was increased to 5.9 mg LAS·L-1. Findings suggest that the supplementation of an easily biodegradable organic matter might be a strategy to overcome wastewater fluctuation in composition.

Cultivo de melancia no semiárido irrigado com diferentes lâminas de esgoto doméstico tratado / Watermelon cultivation in the semi-arid irrigated with different heights of treated domestic sewage

RESUMO O objetivo deste trabalho foi avaliar a viabilidade agronômica do uso de esgoto doméstico tratado em reator anaeróbio para o cultivo de melancia tipo Crimson Sweet. Em estudo de campo no Sertão Pernambucano, avaliou-se a aplicação de quatro lâminas de irrigação por meio do sistema de gotejamento. Foram avaliadas as lâminas de 50, 75, 100 e 125% baseadas nos resultados da evapotranspiração e nas exigências do sistema de irrigação adotado. A caracterização do efluente tratado indicou conformidade com as recomendações para a aplicação agrícola, entretanto a concentração de sólidos suspensos (114 mg.L-1) demandou maior frequência de limpeza dos gotejadores. Foram observados um aumento da capacidade de troca catiônica e uma redução do pH do solo em todos os tratamentos. O tratamento com lâmina a 125% resultou em frutos de maiores tamanho (20,78 cm) e peso (7,12 kg.un-1), bem como de produtividade média (61,1 t.ha-1). Estes valores são superiores às médias nacional e do Estado de Pernambuco, demonstrando a viabilidade agronômica do reúso nas condições testadas.

ABSTRACT The aim of this paper was to assess the agronomic viability of using anaerobically treated domestic sewage in cultivation of Crimson Sweet watermelon. In a field experiment conducted in the semi-arid region of Pernambuco state, Brazil, four treatments (T) were used to assess the effects of irrigation using dripping system on fruits and soil. Four heights of 50% (T1), 75% (T2), 100% (T3) and 125% (T4), based on the calculated evapotranspiration and irrigation needs, were applied. The treated effluent characteristics indicated compliance with the recommendations for agricultural application, but the concentration of suspended solids (114 mg.L-1) demanded frequent cleansing of the dripper blockages. We observed an increase in the cation exchange capacity and a decrease of the soil pH in all the treatments. The best results were obtained with the treatment T4 (height of 125%), which showed watermelons of bigger size (20.78 cm), as well as the highest productivity (61.1 t.ha-1) and fruit weight (7.12 kg.un-1). These values are higher than those of the country and Pernambuco state, demonstrating the agronomic feasibility of reuse under the studied conditions.

Degradação dos homólogos do alquilbenzeno linear sulfonato em lodo anaeróbio disperso / Degradation of the homologues of linear alkylbenzene sulfonate by dispersed anaerobic sludge

RESUMO: Avaliou-se a degradação anaeróbia do alquilbenzeno linear sulfonato (LAS) e seus homólogos em experimento em escala de laboratório. Foi usado lodo disperso para minimizar o efeito da adsorção. Em primeiro lugar, determinaram-se a maior concentração de LAS (substrato) e a menor concentração de etanol (cossubstrato) que manteriam os micro-organismos ativos, resultando em 25 e 200 mg.L-1, nessa ordem. Posteriormente, o experimento (90 dias) foi realizado em um reator somente com etanol (controle) e outro (reator teste, triplicata) com ambos os substratos nas concentrações anteriores. Os micro-organismos apresentaram crescimento exponencial em 48 h para os 2 reatores; não ocorreu toxicidade pelo LAS no reator teste durante esse período inicial, quando o etanol foi todo consumido. Após então, houve decréscimo de micro-organismos, indicando possível toxicidade por LAS ou intermediários. Observou-se também a diminuição ou ausência da produção de ácidos graxos voláteis e de metano. Portanto, com lodo disperso, a maior parcela da remoção foi por conta da biodegradação, porém, com formação de intermediários que não o acetato nem o metano, apontando a inibição à acidogênese e à metanogênese. Ao final, a remoção do LAS foi de 35% por biodegradação e apenas 0,35% por adsorção ao lodo. A ordem preferencial de biodegradação para os homólogos foi de C13 para C12, C11 e C10, com percentual de degradação em relação à massa inicial de 49, 31, 24 e 17%, respectivamente. A mesma ordem deu-se para a adsorção, da maior para a menor cadeia alquílica, sendo a remoção por adsorção de 0,85; 0,32; 0,13 e 0,01%, respectivamente.

ABSTRACT: The anaerobic degradation of linear alquibenzene sulfonate (LAS) and its homologues was evaluated in batch experiment. Dispersed sludge was used to minimize the effect of adsorption. Initially, the highest concentration of LAS (substrate) and the lowest concentration of ethanol (co-substrate) were determined to maintain the microorganisms active; the results were 25 and 200 mg.L-1, respectively. Afterwards, a 90-day period experiment was conducted with one reactor with only the addition of ethanol (control) and the other (test reactor in triplicate) with both substrates and the previous concentrations found. The microorganisms showed exponential growth in the first 48 h for both reactors; LAS toxicity has not occurred in the test reactor during the first 4 days, during which ethanol was consumed. After that, the microorganisms decreased, indicating possible toxicity due to LAS or intermediates; a decrease or absence of volatile organic acids and methane production was also observed. Therefore, with dispersed sludge the largest removal was due to biodegradation, but with formation of intermediates other than acetate or methane, indicating inhibition of acidogenesis and methanogenesis. At the end, the removal was 35% by biodegradation and only 0.35% by adsorption to the biomass. The preferential order of the biodegradation for the homologues was from C13 to C12, C11 and C10; and the removal in relation to the initial mass of each was 49, 31, 24 and 17%, respectively. The same order occurred to adsorption, from the higher to the lower alkyl chain, with removal of 0.86, 0.32, 0.13 and 0.01%, respectively.

454-Pyrosequencing analysis of highly adapted azo dye-degrading microbial communities in a two-stage anaerobic-aerobic bioreactor treating textile effluent.

Azo dyes, which are widely used in the textile industry, exhibit significant toxic characteristics for the environment and the human population. Sequential anaerobic-aerobic reactor systems are efficient for the degradation of dyes and the mineralization of intermediate compounds; however, little is known about the composition of the microbial communities responsible for dye degradation in these systems. 454-Pyrosequencing of the 16S rRNA gene was employed to assess the bacterial biodiversity and composition of a two-stage (anaerobic-aerobic) pilot-scale reactor that treats effluent from a denim factory. The anaerobic reactor was inoculated with anaerobic sludge from a domestic sewage treatment plant. Due to the selective composition of the textile wastewater, after 210 days of operation, the anaerobic reactor was dominated by the single genus Clostridium, affiliated with the Firmicutes phylum. The aerobic biofilter harbored a diverse bacterial community. The most abundant phylum in the aerobic biofilter was Proteobacteria, which was primarily represented by the Gamma, Delta and Epsilon classes followed by Firmicutes and other phyla. Several bacterial genera were identified that most likely played an essential role in azo dye degradation in the investigated system.

Remoção de alquilbenzeno linear sulfonato em esgoto doméstico tratado em reator UASB e lagoa de polimento / Linear alquilbenzene sulfonate removal from domestic sewage treated in UASB and polishing pond

RESUMO: Avaliou-se a remoção do alquilbenzeno linear sulfonato (LAS) em uma estação de tratamento de esgoto (ETE) com reator tipo UASB e lagoa de polimento durante dois períodos, seco e chuvoso. A remoção de LAS também foi avaliada em uma das 8 células do UASB (810 m3). Nessa célula, a remoção, predominantemente por adsorção, foi de 68±52 e 0% para os períodos seco e chuvoso, respectivamente. A eficiência de remoção global do LAS na ETE foi de 80±15 a 98±3%, considerando os dois períodos sazonais. A concentração de LAS no efluente da lagoa de polimento ficou entre 0,1±0,3 e 0,6±0,3 mg.L-1. Portanto, a qualidade do efluente da ETE, em termos de LAS, foi muito satisfatória, com valores inferiores aos da legislação (<0,5 mg.L-1 de LAS - CONAMA) para as substâncias definidas como aquelas que reagem com o azul de metileno, em águas superficiais de classe 1 a 3.

ABSTRACT: We evaluated the removal of linear alquilbenzene sulfonate (LAS) in a sewage treatment plant (WWTP) with a UASB reactor and a polishing pond during two seasonal periods, dry and rainy. The removal was also evaluated in one of the eight cells of the UASB reactor (810 m3). In this cell, the removal was predominantly by adsorption, of 68±52 and 0% for the dry and rainy seasons, respectively. The total removal efficiency of LAS in the WWTP was between 80±15 and 98±3%, considering the two seasonal periods. The LAS concentration in the polishing pond effluent was between 0.1±0.3 and 0.6±0.3 mg.L-1. Therefore, the quality of the final effluent, in terms of LAS, was very satisfactory, with values lower than those defined by the Brazilian legislation (<0.5 mg L-1 of LAS) of CONAMA, for substances reacting with the methylene blue, when the receiving water body is within the classes 1 to 3.

Cultivo de mudas de eucalipto irrigadas com esgoto doméstico tratado / Cultivation of eucalyptus seedlings irrigated with treated domestic sewage

Avaliou-se o cultivo de mudas de eucalipto da espécie urograndisirrigadas com esgoto doméstico tratado em estação com reator anaeróbio e lagoa de polimento. A irrigação das mudas, em vaso e com base na capacidade de pote (CP) para o solo, foi efetuada em experimento com seis tratamentos (T), com quatro repetições cada. Em T1, T2, T3 e T4, a irrigação com esgoto foi com lâmina a 100, 80, 60 e 40% do índice CP, respectivamente; em T5 e T6, a irrigação foi com água a 80% de CP. Apenas T5 teve adição de fertilizantes (NPK). Uma boa eficiência da estação de tratamento foi obtida durante os 3 meses de experimento, com remoção de demanda bioquímica de oxigênio, demanda química de oxigênio e helmintos de 90, 87 e 100%, respectivamente; portanto, com qualidade de efluente adequada para irrigação de arbóreas. Os desempenhos de T2 e T3 foram os melhores em termos de parâmetros de crescimento da planta (altura, diâmetro do caule, diâmetro da copa, número de folhas e matéria seca); comparativamente, em T2, acumulou-se mais nitrogênio nas folhas e caules. Os resultados obtidos mostram que o cultivo de mudas de eucalipto irrigadas com esgoto tratado, aproveitando os nutrientes e com lâminas adequadas (entre 80 e 60% do índice CP), é viável agronomicamente.

The cultivation of Eucalyptus urograndis seedlings irrigated with domestic sewage effluent of a treatment plant with anaerobic reactor and polishing pond was evaluated. Seedling pots were irrigated based on the soil pot capacity (PC) in six treatments (T) with four repetitions each. The pots in T1, T2, T3 and T4 were irrigated with slide heights at 100, 80, 60 and 40% of the PC index, respectively; in T5 and T6, irrigation was only with water and slide heights at 80% of PC. Only T5 received additional nutrients (NPK). Along the experiment (3 months), the treatment plant showed good removal efficiencies of biochemical oxygen demand (90%), chemical oxygen demand (87%) and helminth eggs (100%); therefore, with adequate effluent quality for tree irrigation. T2 and T3 showed the best results in terms of plant development parameters, like height, stalk diameter, cup diameter, number of leaves and dry matter; comparatively, T2 showed the highest nitrogen accumulation in the leaves and stalks. The results show that cultivation of eucalyptus seedlings irrigated with treated sewage, taking advantage of the nutrients and with adequate slide heights (between 80 and 60% of PC index), is agronomically viable.

Resistencia a la exposición al oxígeno de lodos anaerobios suspendidos / Oxygen exposure resistance in suspended anaerobic sludge

La tolerancia al oxígeno de una biomasa anaerobia suspendida en presencia o ausencia de un sustrato primario (sacarosa) se evaluó en términos de la recuperación de la actividad metanogénica aceticlástica especial (AME) de la biomasa anaerobia y un índice de inhibición 50 por ciento (II50) asociado a la AME. Incubada en presencia de sacarosa. La biomasa anaerobia suspendida mostró resistencia a la exposición al oxígeno; la recuperación de la AME fue >45 por ciento para [O²] iniciales <20 por ciento en el espacio gaseoso, y de 10 a 12 por ciento para [O²] iniciales >20 por ciento en el espacio gaseoso. Cuando fue incubada son fuente, la biomasa suspendida fue mucho más inhibida después de la exposición al oxígeno para [O²] iniciales >20 por ciento. El efecto inhibitorio fue descrito por un II50 elevado /28,6) en contraste con un bajo II50 (5,9) cuando se incubó en presencia de sacarosa. La tolerancia de la biomasa suspendida en este trabajo parece ser del mismo orden de la biomasa anaerobia inmovilizada (gránulos anaerobios) en condiciones de incubación en presencia de sustrato: los II50 fueron 5,9 para todos anaerobios suspendidos (sacarosa) y 5,3 y 2,4 para todos granulares incubados con acetato etanol, respectivamente. La respiración aerobia heterótrofa de los lodos anaerobio floculentos incubados con sacarosa fue cerca de 4 veces mayor que la respiración basal, y la inhibición de la AME descrita por el II50 parece seguir una relación inversa con la respiración aerobia heterótrofa. La relación inversa entre II50 y respiración aerobia heterótrofa se ajustó para datos de todos granulares en la literatura y todos floculentos de este trabajo, y sigue un modelo semi-empírico general, con un coeficiente de correlación de 0,82. Esta relación parece reforzar que uno de los mecanismos principales de protección de los consorcios anaerobios contra la inhibición por oxígeno es la respiración aerobia heterótrofa