Treatment of azo dye-containing wastewater in a combined UASB-EMBR system: Performance evaluation and membrane fouling study.

This work investigated the treatment of azo dye-containing wastewater in an upflow anaerobic sludge blanket (UASB) reactor combined with an electro-membrane bioreactor (EMBR). Current densities of 20 A m-2 and electric current exposure mode of 6'ON/30'OFF were applied to compare the performance of the EMBR to a conventional membrane bioreactor (MBR). The results showed that dye (Drimaren Red CL-7B) removal occurred predominantly in the UASB reactor, which accounted for 57% of the total dye removal achieved by the combined system. When the MBR was assisted by electrocoagulation, the overall azo dye removal efficiency increased from 60.5 to 67.1%. Electrocoagulation batch tests revealed that higher decolorization rates could be obtained with a current density of 50 A m-2. Over the entire experimental period, the combined UASB-EMBR system exhibited excellent performance in terms of chemical oxygen demand (COD) and NH4+-N removal, with average efficiencies above 97%, while PO43--P was only consistently removed when the electrocoagulation was used. Likewise, a consistent reduction in the absorption spectrum of aromatic amines was observed when the MBR was electrochemically assisted. In addition to improving the pollutants removal, the use of electrocoagulation reduced the membrane fouling rate by 68% (0.25-0.08 kPa d-1), while requiring additional energy consumption and operational costs of 1.12 kWh m-3 and 0.32 USD m-3, respectively. Based on the results, it can be concluded that the combined UASB-EMBR system emerges as a promising technological approach for textile wastewater treatment.

Microbial fuel cell: Interplay of energy production, wastewater treatment, toxicity assessment with hydraulic retention time.

Microbial fuel cell (MFC) operation under similar conditions to conventional methods will support the use of this technology in large-scale wastewater treatment. The operation of scaled-up air-cathode MFC (2 L) fed with synthetic wastewater (similar to domestic) in a continuous flow was evaluated using three different hydraulic retention times (HRT), 12, 8, and 4 h. We found that electricity generation and wastewater treatment could be enhanced under an HRT of 12 h. Additionally, the longer HRT led to greater coulombic efficiency (5.44%) than MFC operating under 8 h and 4 h, 2.23 and 1.12%, respectively. However, due to the anaerobic condition, the MFC was unable to remove nutrients. Furthermore, an acute toxicity test with Lactuca sativa revealed that MFC could reduce wastewater toxicity. These outcomes demonstrated that scaled-up MFC could be operated as a primary effluent treatment and transform a wastewater treatment plant (WWTP) into a renewable energy producer.

Effects of electrochemical processes application on the modification of mixed liquor characteristics of an electro-membrane bioreactor (e-MBR).

This study evaluated the effects of electrochemical processes on the mixed liquor characteristics of an electro-membrane bioreactor (e-MBR) applied to municipal wastewater treatment. A laboratory-scale e-MBR was assessed under two experimental runs: without the electric field (run I) and with electric field, controlled by the application of an electric current set in 10.0 A m-2 under intermittent exposure mode of 6 minutes ON/18 minutes OFF (run II). The electric field caused approximately 55% removal of both soluble microbial products (SMP) and extracellular polymeric substances (EPS), whereas the proteins/carbohydrates ratio in EPS was increased from 1.9 in the run I to 2.9 in run II, leading to an increment of flocs' hydrophobicity. Additionally, the sludge floc size average value was reduced from 42.2 µm in run I to 24.6 µm in run II, which led to a significant enhancement in the sludge settleability. As a result, the membrane fouling rate was always less than 3.80 mbar d-1 in run II, whereas in run I these values reached up to 34.7 mbar d-1. These results demonstrated that the electrochemical processes enhanced the mixed liquor filterability. Therefore, their implementation represents a great alternative to improve the operational stability of membrane bioreactors.

Simultaneous adsorption of iron and manganese from aqueous solutions employing an adsorbent coal.

In this work, an adsorbent coal was characterized and its sorption properties for the removal of iron and manganese from aqueous solutions were determined. Energy dispersive X-ray (EDX) analysis and X-ray diffraction (XRD) identified the presence of quartz, magnetite and manganese oxide in the adsorbent coal. The results of the adsorption isotherms verified the adsorption of iron and manganese by adsorbent coal showing a linear behaviour and indicated that chemisorption and physisorption occurred. The kinetic results were best adjusted to the pseudo-second order model with a 0.999 correlation coefficient. The results showed that the adsorbent coal could be used efficiently for the removal of iron and manganese from aqueous solutions.

Use of a Waste-Derived Linde Type-A Immobilized in Agarose for the Remediation of Water Impacted by Coal Acid Mine Drainage at Pilot Scale.

A new adsorbent based on an immobilized waste-derived LTA zeolite in agarose (AG) has proven to be an innovative and efficient alternative for removing metallic contaminants from water impacted by acid mine drainage (AMD) because the immobilization prevents the solubilization of the zeolite in acidic media and eases its separation from the adsorbed solution. A pilot device was developed containing slices of the sorbent material [AG (1.5%)-LTA (8%)] to be used in a treatment system under an upward continuous flow. High removals of Fe2+ (93.45%), Mn2+ (91.62%), and Al3+ (96.56%) were achieved, thus transforming river water heavily contaminated by metallic ions into water suitable for non-potable use for these parameters, according to Brazilian and/or FAO standards. Breakthrough curves were constructed and the corresponding maximum adsorption capacities (mg/g) (Fe2+, 17.42; Mn2+, 1.38; Al3+, 15.20) calculated from them. Thomas mathematical model was well fitted to the experimental data, indicating the participation of an ion-exchange mechanism in the removal of the metallic ions. The pilot-scale process studied, in addition to being highly efficient in removing metal ions at toxic levels in AMD-impacted water, is linked to the sustainability and circular economy concepts, due to the use as an adsorbent of a synthetic zeolite derived from a hazardous aluminum waste.

Effects of solid retention time and exposure mode to electric current on Remazol Brilliant Violet removal in an electro-membrane bioreactor.

The performance of an electrochemically assisted anoxic-oxic membrane bioreactor (A/O-eMBR) was assessed as an alternative for azo dye (Remazol Brilhant Violet (RBV)) removal from simulated textile wastewater. The A/O-eMBR was operated under three experimental conditions (runs I, II, and III), in which different solids retention time (SRT) (45 and 20 d) and exposure mode to electric current (6'ON/30'OFF and 6'ON/12'OFF) were assessed. The reactor exhibited excellent decolorization performance for all runs, with average dye removal efficiency ranging from 94.3 to 98.2%. Activity batch assays showed that the dye removal rate (DRR) decreased from 16.8 to 10.2 mg RBV L-1 h-1 when the SRT was reduced from 45 to 20 d, likely attributed to the lower biomass content under lower sludge age. At the electric current exposure mode of 6' ON/12'OFF, a more substantial decrease of DRR to 1.5 mg RBV L-1 h-1 was noticed, suggesting a possible inhibitory effect on dye removal via biodegradation. By reducing the SRT to 20 d, a worse mixed liquor filterability condition was observed, with a membrane fouling rate (MFR) of 0.979 kPa d-1. In contrast, using the electric current exposure mode of 6'ON/12'OFF resulted in lower membrane fouling propensity, with an MFR of 0.333 kPa d-1. A more attractive cost-benefit ratio for dye removal was obtained using the exposure mode of 6'ON/30'OFF, for which the energy demand was estimated at 21.9-22.6 kWh kg dye-1 removed, almost two times lower than that observed for the mode of 6'ON/12'OFF.

Performance of an anaerobic-oxic-anoxic (AOA) system in the simultaneous removal of nutrients and triclosan and bacterial community.

The constant presence of triclosan (TCS) in surface water and wastewater has been verified due to its application in several pharmaceutical and personal care products. Thus, removing this emerging contaminant is essential to minimize the contamination of water bodies. The anaerobic-aerobic-anoxic (AOA) system is an innovative alternative that combines the removal of nutrients and triclosan. This study focuses on the simultaneous removal of carbonaceous matter, nitrogen, phosphorus, and triclosan in a continuous pilot-scale AOA system from synthetic wastewater. The upflow system, in series, was operated at hydraulic retention time (HRT) of 8 h and a flowrate of 2.40 L h-1. Glucose (190 mg L-1) was added to the anoxic reactor as the external carbon source. Besides that, bacterial community structure was investigated using 16S rRNA sequencing in each reactor. The system achieved average removal efficiencies of 96% (14.03 g d-1) for Chemical Oxygen Demand (COD), 85% (2.64 g d-1) for Total Kjeldahl Nitrogen (TKN), 88% (1.40 g d-1) for Total Ammonia Nitrogen (TAN), 20% (0.12 g d-1) for Total Phosphorus (TP), and 93% (1.87 µg d-1) for Triclosan (TCS). The phyla Proteobacteria, Firmicutes, Bacteroidetes, and Chloroflexi were found in greater abundance. The main genera identified were Anaeromusa, Aeromonas, Azospira, Clostridium, and Lactococcus. The organisms related to phylum and genus corroborate the involved processes and the removal performance achieved. In addition, Lactococcus, Thermomonas, Ferruginibacter, and Dechloromonas were involved in triclosan biodegradation. The anaerobic-oxic-anoxic system successfully removed carbonaceous, nitrogenous matter, and triclosan, with glucose increasing the denitrifying activity.

Removal of coloured compounds from textile industry effluents by UV/H2O2 advanced oxidation and toxicity evaluation.

This study has investigated the reduction in coloured substances and toxic compounds present in textile industry effluent by the use of an advanced oxidation process using hydrogen peroxide (H2O2) as oxidant, activated by ultraviolet radiation. The investigation was carried out on industrial effluents, both raw and after biological treatment, using different concentrations of H2O2 in a photochemical reactor equipped with a 250 W high-pressure mercury vapour lamp. The results showed that after 60 minutes of ultraviolet irradiation a H2O2 concentration of 500 mg L(-1) was able to remove approximately 73% of the coloured compounds present in raw effluent and 96% of those present in biologically treated effluent. Additionally, post-treatment toxicity tests performed using the microcrustacean Daphnia magna showed a significant effective reduction in the acute toxicity of the raw effluent. In tests carried out with treatment at a concentration of 750 and 1000 mg L(-1) H2O2, analysis of the frequency ofmicronuclei in erythrocytes of Tilapia cf rendalli exposed to treated effluent samples confirmed that there were no mutagenic effects on the fish. Together, these results indicate that the oxidation process offers a good alternative for the removal of colour and toxicity from textile industry effluent.

Highly efficient removal of aluminum, iron, and manganese ions using Linde type-A zeolite obtained from hazardous waste.

Coal acid mine drainage (AMD) contaminates natural water to form mine-impacted water (MIW), which is characterized by high levels of acidity, sulfate, and metallic ions. This study investigates the use of a Linde Type-A (LTA) zeolite obtained from a hazardous industrial waste for Al3+, Fe2+, and Mn2+ removal from synthetic aqueous solutions. The aim of this study is to stablish a basis for the subsequent treatment of MIW in order to obtain reuse water. In a central composite rotatable design (CCRD) study, 8.25 g L-1 zeolite and 147 rpm were the optimal conditions for treating the multicomponent solution, yielding 99.9, 99.9 and 99.3% removal for Al3+, Fe2+, and Mn2+, respectively. Isothermal studies showed that the affinity of the ions by the zeolite were ranked as Al3+>Mn2+>Fe2+. The best fitting isothermal models for monocomponent solutions were Tóth, Freundlich, and Sips for Al3+, Fe2+, and Mn2+, respectively. In the multicomponent solution, Sips and Freundlich were the better fitting models for Al3+ and Mn2+, respectively, indicating a weakness of the sorbate-sorbent interactions. Kinetic studies revealed that the quantitative removal of Al3+ was achieved in 5 min. The multicomponent solution was transformed into water that was suitable for non-potable use after an optimal time of 60 min. The results demonstrate that LTA zeolite synthetized from hazardous waste has a high potential for remediating contaminated water by metallic ions at low dosages and short times. Using LTA zeolite for remediating contaminated water could make a positive contribution to the circular economy and environmental sustainability.

Comparative study on treatment performance, membrane fouling, and microbial community profile between conventional and hybrid sequencing batch membrane bioreactors for municipal wastewater treatment.

A sequencing batch conventional membrane bioreactor (SB-CMBR) and sequencing batch hybrid membrane bioreactor (SB-HMBR) were operated in parallel under two different hydraulic retention times (HRTs) (namely 12 h and 6 h), and their chemical oxygen demand (COD) and nutrient removal performance, membrane fouling behavior, and microbial community characteristics were compared. Both systems exhibited high organic matter (> 95%) and ammonium (> 98%) removal performance regardless of the HRT applied. As the HRT was reduced from 12 to 6 h, total nitrogen removal slightly increased in both reactors, being higher in the carrier-based MBR, where anoxic zones may have been established within the biofilm. Conversely, total phosphorus removal improved only in the SB-CMBR at the shorter HRT. Moreover, activity batch assays have shown a faster P uptake rate in the SB-CMBR than in the SB-HMBR, a result likely associated with the lower relative abundance of phosphate-accumulating organisms in both adhered and suspended biomass fractions in the hybrid MBR. The results also revealed that more pronounced increases in the transmembrane pressure and, consequently, in the membrane fouling rate at higher COD loading rates were observed in the SB-CMBR, where the soluble microbial products (proteins, polysaccharides, and especially, transparent exopolymer particles), supernatant turbidity, and filamentous bacteria were more significant. Overall, as compared to the conventional MBR, the plastic media-based SB-HMBR showed a lower fouling propensity at all hydraulic conditions tested.

Aplication of the statistical experimental design to optimize mine-impacted water (MIW) remediation using shrimp-shell.

Mine-impacted water (MIW) is one of the most serious mining problems and has a high negative impact on water resources and aquatic life. The main characteristics of MIW are a low pH (between 2 and 4) and high concentrations of SO42- and metal ions (Cd, Cu, Ni, Pb, Zn, Fe, Al, Cr, Mn, Mg, etc.), many of which are toxic to ecosystems and human life. Shrimp shell was selected as a MIW treatment agent because it is a low-cost metal-sorbent biopolymer with a high chitin content and contains calcium carbonate, an acid-neutralizing agent. To determine the best metal-removal conditions, a statistical study using statistical planning was carried out. Thus, the objective of this work was to identify the degree of influence and dependence of the shrimp-shell content for the removal of Fe, Al, Mn, Co, and Ni from MIW. In this study, a central composite rotational experimental design (CCRD) with a quadruplicate at the midpoint (22) was used to evaluate the joint influence of two formulation variables-agitation and the shrimp-shell content. The statistical results showed the significant influence (p < 0.05) of the agitation variable for Fe and Ni removal (linear and quadratic form, respectively) and of the shrimp-shell content variable for Mn (linear form), Al and Co (linear and quadratic form) removal. Analysis of variance (ANOVA) for Al, Co, and Ni removal showed that the model is valid at the 95% confidence interval and that no adjustment needed within the ranges evaluated of agitation (0-251.5 rpm) and shrimp-shell content (1.2-12.8 g L-1). The model required adjustments to the 90% and 75% confidence interval for Fe and Mn removal, respectively. In terms of efficiency in removing pollutants, it was possible to determine the best experimental values of the variables considered as 188 rpm and 9.36 g L-1 of shrimp-shells.

Effect of solids retention time on nitrogen and phosphorus removal from municipal wastewater in a sequencing batch membrane bioreactor.

This study evaluated the removal of organic matter, nitrogen and phosphate from a municipal wastewater in a sequencing batch membrane bioreactor (SBMBR) operated at different solids retention times (SRTs) and subjected to different aeration profiles. The results demonstrated that SRT reduction from 80 to 20 d had a negligible effect on chemical oxygen demand (COD) removal and only a slight negative effect on nitrification. COD removal efficiency remained stable at 97%, whereas ammonium removal decreased from 99% to 97%. The total nitrogen removal efficiency was improved by SRT reduction, increasing from 80% to 86%. Although the total phosphorus (TP) removal was not significantly affected by the SRT reduction, ranging from 40-49%, the P-release and P-uptake processes were observed to increase as the SRT was reduced. The implementation of a pre-aeration phase in the SBMBR operating cycle allowed a higher TP removal performance, which reached up to 76%. Batch tests suggested that the fraction of phosphate removed anoxically from the total (anoxic + aerobic) phosphate removal decreased with the SRT reduction.

Influência da idade do lodo na colmatação das membranas em um biorreator à membrana tratando esgoto sanitário / Effect of solids retention time on membrane fouling in a membrane bioreactor treating municipal wastewater

RESUMO O presente estudo avaliou o efeito da idade do lodo (θc) no potencial incrustante do licor misto em um biorreator à membrana (BRM) tratando esgoto sanitário. Tal avaliação foi conduzida em BRM construído em escala de bancada, com volume útil de 15 L, operado por 420 dias na modalidade de batelada sequencial. Durante o período experimental, foram aplicadas 3 estratégias operacionais, E-1, E-2 e E-3, em que foram testadas as idades de lodo de 80, 40 e 20 dias, respectivamente. Os resultados revelaram que a utilização da idade de lodo de 20 dias resultou em licor misto com maior potencial incrustante, apresentando, neste caso, uma velocidade de colmatação (VC) das membranas de 1,95 mbar dia-1, aproximadamente 2 vezes maior do que a observada nas idades de lodo de 80 e 40 dias. A maior colmatação observada foi atribuída a maior concentração de produtos microbianos solúveis (PMSs) no licor misto e a maior relação proteínas/polissacarídeos (PN/PS) dos flocos biológicos nesse período em questão. Por outro lado, a aplicação da idade de lodo de 80 dias resultou em menor VC das membranas do BRM, com valor de 0,82 mbar dia-1. Contudo, no período final dessa estratégia foi observado crescimento excessivo de bactérias filamentosas, que se refletiu em piora da filtrabilidade do licor misto e aumento da VC das membranas. De maneira geral, os resultados obtidos mostraram que a aplicação da idade de lodo de 40 dias resultou em licor misto com menor potencial incrustante.

ABSTRACT This study evaluated the effect of solids retention time (SRT) on membrane fouling rate in a membrane bioreactor (MBR) treating municipal wastewater. The evaluation was conducted in a membrane bioreactor built in bench scale, with a volume of 15 L, operated for 420 days in the sequential batch regime. During this period, three experimental runs were applied, E-1, E-2 and E-3, in which the solids retention time of 80, 40 and 20 days, respectively, were tested. The results showed that use of 20-days solids retention time resulted in a higher membrane fouling rate (MFR), with value of 1,95 mbar d-1, approximately two times higher than observed in the solids retention time of 80 and 40 days. The higher membrane fouling rate observed was attributed to a higher concentration of soluble microbial products (SMP) in the mixed liquor and to the higher proteins/polysaccharides ratio of the biological flocs in this period. On the other hand, the use of 80-days solids retention time resulted in a lower membrane fouling rate, with a value of 0.82 mbar d-1. However, it was observed in the final period of this experimental run an excessive growth of filamentous bacteria, which was reflected in a deterioration of the mixed liquor filterability and an increase of membrane fouling rate. Overall, the results showed that the 40-days solids retention time resulted in a mixed liquor with lower fouling propensity.

Degradação sazonal de efluentes têxteis por processo foto-Fenton solar mediado por ferrioxalato: descoloração e comportamento dos sólidos / Seasonal degradation of textile effluents through the solar photo-Fenton process mediated by ferrioxalate: discoloration and behavior of solids

RESUMO Neste trabalho foi avaliado o processo foto-Fenton solar mediado por ferrioxalato como tratamento primário de um efluente têxtil bruto (E1) e como um processo de polimento, após processo de lodos ativados (E2). Por um ano, ao menos uma vez por mês, a eficiência de descoloração e o comportamento dos sólidos foram avaliados sob condições naturais de radiação, temperatura e características dos efluentes. As condições operacionais foram as seguintes: 50 mg L-1 de ferro, pH 5, 525 mg L-1 de H2O2, administrados em dosagens decrescentes. O oxalato foi adicionado na razão molar de 1:3 [Fe+3:(C2O4)-2]. A descoloração máxima de E1 foi de 67% para intensidade de radiação de 690 W m-2; já a de E2 foi de 95% para intensidade de 620 W m-2. Houve considerável aumento na turbidez e nos sólidos suspensos em função da precipitação do ferro e de sua ação coagulante. A degradação do complexante durante o processo no E2 em dias ensolarados provocou elevada sedimentabilidade dos sólidos do efluente final, resultando em um sobrenadante clarificado, o que não ocorreu em dias nublados.

ABSTRACT This work evaluates the solar photo-Fenton process mediated by ferrioxalate as a primary treatment of raw textile effluent (E1) and as a polishing step, after active sludge process (E2). For a year, at least once a month, the color removal's efficiency and solids' behavior in the oxidative process treatment were analyze under natural conditions of light, temperature and effluents characteristics. The operational parameters values were: 50 mg L-1 iron, pH 5, 525 mg L-1 H2O2, introduced in decreasing doses. The oxalate was added at the molar ratio of 1:3 [Fe+3:(C2O4)-2]. The color removal of E1 was 60% for 690 W m-2 of radiation intensity and 95% for 620 W m-2 intensity to E2. Considerable increases were observed in turbidity and suspended solids due to the iron precipitation and the consequent coagulant action. In sunny days, the complex degradation in E2 resulted in high settle ability of solids in the final effluent, resulting in a clear supernatant. This has not happened in cloudy days.

Avaliação da nanofiltração e da osmose inversa na remoção de carbofurano em águas de abastecimento / Evaluation of nanofiltration and reverse osmosis membranes on removal of carbofuran in drinking waters

RESUMO: A complexidade físico-química de micropoluentes, como os defensivos agrícolas, exige o uso de tecnologias avançadas de tratamento de água para abastecimento. O objetivo deste estudo foi avaliar a remoção de carbofurano em nível de bancada (batelada) utilizando membranas comerciais de nanofiltração (NF90 - DowFilmtec (r)) e osmose inversa (HR - Koch Membrane Systems(r) ). Nos experimentos foi avaliada a influência da qualidade da matriz de alimentação (água ultrapura, bruta e pré-tratada) contendo carbofurano (50 µgL-1), e da pressão de operação (8 e 15 bar para a NF90 e 15 e 30 bar para a HR). Para a NF90, com a matriz de água ultrapura, as eficiências de remoção foram inferiores (89,8%), porém o fluxo permeado foi superior (132,1 Lm-2h-1) àquelas obtidas com a matriz de água bruta (98,4% - 94,7 Lm-2h-1) e água pré-tratada (95,2% - 95,3 Lm-2h-1) para a pressão de 15 bar. Para a membrana HR, remoções relativamente superiores foram observadas para a pressão de 30 bar para as três matrizes, com a água bruta apresentando os melhores resultados (99,7% - 49,7 Lm-2h-1). Concluiu-se, portanto, que o pré-tratamento da água bruta não acarretou diferença significativa na remoção do carbofurano e não influenciou no fluxo de permeado de acordo com a metodologia adotada (baixo tempo de separação em batelada com recirculação).

ABSTRACT: The physicochemical complexity of micropollutants such as pesticides requires the use of advanced technologies of drinking water treatment. The main objective of this study was to evaluate the removal of carbofuran using commercial nanofiltration (NF90 - DowFilmtec(r)) and reverse osmosis (HR - Koch Membrane Systems(r)) membranes in a bench-scale system (batch operation). The effect of feed matrix quality (ultrapure water, raw water and pretreated water) with carbofuran (50 µgL-1) and the applied pressure (8 and 15 bar for NF90 and 15 and 30 bar for HR) were studied. For NF90, with ultrapure water matrix, the removal efficiencies were lower (89.4%), but the permeate flow was higher (132.1 Lm-2h-1) than those obtained with the raw water (98.4% - 94.7 Lm-2h-1) and pretreated water (95.2% - 95.3 Lm-2h-1) to 15 bar of pressure. For HR membrane relatively higher removals were observed for 30 bar of pressure for the three matrices, with a better behavior for raw water (99.7% - 49.7 Lm-2h-1). In accordance to the methodology adopted (low separation time in batch with recirculation), it can be concluded, therefore, that the pretreatment of raw water did not caused significant difference in carbofuran removal and did not influenced the permeate flux.

Biorreator à membrana em batelada sequencial aplicado ao tratamento de esgoto visando à remoção de nutrientes / Membrane sequencing batch reactor for the wastewater treatment aiming the nutrients removal

Neste trabalho, avaliou-se o desempenho de um biorreator à membrana em batelada sequencial para a remoção de nutrientes (nitrogênio e fósforo) de esgoto sanitário. O reator, construído em escala piloto, foi operado durante 241 dias com tempo total de ciclo de 4 horas, sendo 5 minutos para alimentação, 55 minutos para a fase anóxica e 180 minutos para as fases de aeração e filtração (simultaneamente). Ao longo do monitoramento, foram empregados dois fluxos de filtração: 5,55 e 11,1 L.m-2.h-1, que resultaram nas taxas de troca volumétrica de 5 e 10%, respectivamente. As eficiências médias de remoção de Demanda Química de Oxigênio total, nitrogênio amoniacal e nitrogênio total alcançadas foram de 99, 98 e 96%, respectivamente. Em relação à remoção de fósforo, observou-se inicialmente um baixo rendimento do reator, sendo verificado ao longo do tempo, no entanto, uma tendência de melhora na remoção desse nutriente, atingindo eficiência média de 74% entre os dias 158 e 241. A utilização do fluxo de filtração de 5,55 L.m-2.h-1 proporcionou uma operação estável ao biorreator à membrana em batelada sequencial no que se refere à pressão transmembrana, tendo sido atingido o valor limite de 0,7 bar apenas uma vez em 181 dias de operação, ao passo que, com fluxo de 11,1 L.m-2.h-1, esse limite foi atingido 3 vezes em 55 dias.

This study evaluated the performance of a membrane bioreactor sequencing batch, in pilot scale, to remove nutrients (nitrogen and phosphorus) from domestic wastewater. The reactor was operated for 241 days with a total cycle time of 4 hours, with 5 minutes for feeding, 55 minutes for the anoxic phase and 180 minutes for the aeration and filtration phases (simultaneously). Throughout the monitoring, two filtration flows were employed: 5.5 and 11.1 (critical flux) L.m-2.h-1, which resulted in the volume exchange rates of 5 and 10%, respectively. The removal efficiencies of total Chemical Oxygen Demand, ammonia nitrogen and total nitrogen were achieved by 99, 98 and 96%, respectively. Regarding phosphorus removal, a poor performance was observed in the beginning of the experiment; however, a tendency of improvement in the removal of this nutrient was further verified, reaching an efficiency average of 74% between the operational days 158 and 241. The flux filtration at 5.55 L.m-2.h-1 has provided a membrane bioreactor sequencing batch stable operation in relation to transmembrane pressure since it reached the limit value of 0.7 bar only once in 181 operational days, while for 11.1 L.m-2.h-1 it was observed 3 times in 55 days.

Desinfecção de efluentes sanitários através de dióxido de cloro / Disinfection of domestic wastewater using chlorine dioxide

A desinfecção dos esgotos deve ser considerada quando se pretende reduzir os riscos de transmissão de doenças infecto-contagiosas. Nesse sentido, os requisitos de qualidade de uma água devem ser avaliados em função dos usos previstos para a mesma. O dióxido de cloro (ClO2) possui excelentes propriedades bactericidas, virucidas, esporocidas e algicidas e, devido a isso, é usado como desinfetante de água de abastecimento e efluente doméstico, bem como inibidor de crescimento de algas. O objetivo do trabalho foi estudar a melhor dosagem para uma boa desinfecção de efluentes sanitários previamente tratados mediante lodos ativados por aeração prolongada, avaliar a inativação de coliformes e o residual de dióxido de cloro remanescente. Foram realizados ensaios para diferentes dosagens de dióxido de cloro e diferentes tempos de contato. Os resultados obtidos mostraram que a dosagem mais indicada para desinfecção do efluente estudado foi 2,0 mg ClO2/L com um tempo de contato de 20 minutos, condições sob as quais é atingido 100 por cento de remoção de coliformes fecais e oxidada parcialmente a matéria orgânica remanescente, em tanto que os valores de pH e residual de ClO2 do efluente mantêm-se dentro dos admitidos pelas normativas brasileira e estadunidense em vigor. O estudo econômico levado a cabo permitiu concluir que a desinfecção de efluente doméstico mediante dióxido de cloro pode ser economicamente viável.

Caracterização da microfauna em estação de tratamento de esgotos do tipo lodos ativados: um instrumento de avaliação e controle do processo / Microfauna characterization in activated sludge wastewater treatment plant: an instrument of assessment and control of process

A microfauna presente em uma ETE por lodos ativados foi caracterizada, correlacionada com parâmetros físico-químicos e utilizada em modelos existentes de avaliação de sistemas. Durante 351 dias o lodo ativado manteve-se estável com flocos compactos, pequenos e com poucos filamentos. Os protozoários predominantes no lodo foram as tecamebas e os ciliados predadores de flocos, indicando estabilidade do sistema. Os métodos propostos em literatura, baseados no IBL, na densidade total da microfauna e na relação entre ciliados predadores de flocos e ciliados fixos, mostraram-se eficientes para o diagnóstico das condições depurativas do sistema. A análise qualitativa do lodo, englobando o tamanho, quantidade de filamentos, compactação e a identificação das espécies dominantes, foi suficiente para uma caracterização imediata das condições depurativas do sistema de tratamento.