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The monitoring of total suspended (TSS) and settleable (SetS) solids in wastewater is essential to maintain the quality parameters for aquatic biota because they can transport pollutants and block light penetration. Determining them by their respective reference methods, however, is laborious, expensive, and time consuming. To overcome this, we developed a new analytical instrument called Solids in Wastewater's Machine Vision-based Automatic Analyzer (SWAMVA), which is equiped with an automatic sampler and a software for real-time digital movie capture to quantify sequentially the TSS and SetS contents in wastewater samples. The machine vision algorithm (MVA) coupled with the Red color plane (derived from color histograms in the Red-Green-Blue (RGB) system) showed the best prediction results with R2 of 0.988 and 0.964, and relative error of prediction (REP) of 6.133 and 9.115% for TSS and SetS, respectively. The constructed models were validated by Analysis of Variance (ANOVA), and the accuracy and precision of the predictions by the t- and F-tests, respectively, at a 0.05 significance level. The elliptical joint confidence region (EJCR) test confirmed the accuracy, while the coefficient of variation (CV) of 6.529 and 10.908% confirmed the good precisions, respectively. Compared with the reference method (Standard Methods For the Examination of Water and Wastewater), the proposed method reduced the analysis volume from 1.5 L to just 15 mL and the analysis time from 12 h to 24 s per sample. Therefore, SWAMVA can be considered an important alternative to the determination of TSS and SetS in wastewater as an automatic, fast, and low-cost analytical tool, following the principles of Green Chemistry and exploiting Industry 4.0 features such as intelligent processing, miniaturization, and machine vision.

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Computational molecular modelling, mass spectrometry and in-vivo tests with Chlorella vulgaris (C. vulgaris) and Daphnia magna (D. magna) were used to investigate the liposolubility and ecotoxicity of MC-LR degradation by-products generated after oxidation by OH• radicals in Fenton process. Exposure of MC-LR (5 µg.L-1) to the most severe oxidation conditions (Fe2+ 20 mM and H2O2 60 mM) resulted in a reduction in the toxin concentration of 96% (0.16 µg.L-1), however, with the formation of many by-products. The by-product of m/z 445 was the most resistant to degradation and retained a toxic structure of diene bonds present in the Adda amino acid. Computational modeling revealed that m/z 445 (tPSA = 132.88 Ų; KOW = 2.02) is more fat-soluble than MC-LR (tPSA = 340.64 Ų; KOW = 0.68), evidencing an easier transport process of this by-product. Given this, toxicity tests using C. vulgaris and D. magna indicated greater toxicity of the by-product m/z 445 compared to MC-LR. When the conversion of MC-LR to by-products was 77%, the growth inhibition of C. vulgaris and the D. magna immobility were, respectively, 6.14 and 0%, with 96% conversion; growth inhibition and the immobility were both 100%  for both species.

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The aim of the present study was to evaluate the biological oxidation of sulphide in two different UASB reactors by assessing the occurrence of oxidized forms of sulphur in the effluents and the amount of S0 that could be recovered in the process. The bioreactors employed were an anaerobic hybrid (AH) reactor employing porous polyurethane foam as support media and a micro-aerated UASB reactor equipped with an aeration device above the digestion zone. The AH reactor produced a final effluent containing low concentrations of S2- (3.87% of total sulphur load). It was achieved due to a complete oxidation of 56.1% of total sulphur. The partial biological oxidation that occurred in the AH reactor allowed the recovery of 30% of the sulphur load as S0. The effluent from the micro-aerated UASB reactor contained 5% of the sulphur load in the form of S2-, while 20.9% was present as dissolved SO42- and 46% was precipitated as S0. It is concluded that the AH reactor or micro-aeration carried out above the digestion zone of the UASB reactor favoured the biological oxidation of S2- and the release of odourless effluents. Both technologies represent feasible and low-cost alternatives for the anaerobic treatment of domestic sewage.

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Considering the high waste generation that comes from agriculture and livestock farming, as well as the demand for natural gas, it is necessary to develop sustainable technologies which can reduce environmental impact. There is no available literature on the use of high-rate horizontal anaerobic reactors with fixed bed (HARFB) and continuous feed for the co-digestion of vegetable wastes (VW) and swine wastewater (SW). The aim of this work was to evaluate the reactor performance in terms of methane production, organic matter consumption, and removal of total and thermotolerant coliforms under different proportions of SW and VW, and organic loading rates (OLR) of 4.0, 5.2 and 11.0g COD (Ld)(-)(1). The mixture of SW and VW in the proportions of 90:10, 80:20 and 70:30 (SW:VW) with those OLRs provided great buffering capacity, with partial alkalinity reaching 3552mgL(-1), thereby avoiding the inhibition of methane production by volatile fatty acids produced during the fermentation process. Higher proportions of VW and higher OLR improved volumetric methane production with a maximum value of 1.08LCH4 (Ld)(-)(1), organic matter removal rates up to 98% and total and thermotolerant coliform removal rates of 99% were also observed.

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The aim of this study was to evaluate the efficiency of two sequencing batch reactors (R1 and R2) at removing nutrient (N and P) and chemical oxygen demand (COD). The two reactors (R1 and R2) were of the same design, operating under identical cycles and had a sludge retention time of 5 d. In R1, the substrate was sewage enriched with cooked and triturated cereals. In R2, the substrate was raw sewage mixed with triturated discarded excess sludge. Respirometry tests were performed to compare the biodegradability of the substrates used during the experimental period. The efficiency of R1 in removing soluble P and N-ammonia was considerably higher (90.4 and 97.2%, respectively) than reactor R2 (60 and 39.2%, respectively). While the effluent generated by R1 contained only minor amounts of N-nitrite and N-nitrate (0.5 +/- 0.4 and 1.7 +/- 0.8 mg L(-1), respectively). The concentrations of nitrite and nitrate in the effluent from R2 were 2 and 7 times higher. The lack of biodegradable COD available for denitrification was responsible for the high concentrations of nitrite and nitrate in the effluent of R2.

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O lodo sanitário, principal subproduto do tratamento de esgotos, constitui um dos maiores problemas ambientais urbanos da atualidade. Em meio a este contexto, objetivou-se nesse estudo avaliar o processo da compostagem conjugada de lodo de tanque séptico (LS) e resíduos sólidos vegetais (RV) e determinar a importância da temperatura para o processo de sanitização do substrato tratado. O experimento, inteiramente casualizado com três tratamentos e três repetições, consistiu de nove reatores aeróbios com 100 litros de capacidade. Os resíduos foram utilizados nas seguintes proporções - T1: 100% RV; T2: 5% LS + 95% RV; T3: 10% LS + 90% RV. A compostagem aeróbia conjugada mostrou ser uma alternativa viável para destruição de ovos de helminto e estabilização dos resíduos, sendo fundamentais para tal, a temperatura, o pH e as relações ecológicas presentes nos reatores.

The sanitary sludge, principal byproduct of sewage treatment, constitutes one of the major municipal environmental problems of the present time. The present study was aimed to evaluate the composting of septic tank sludge (SS) and vegetable solid waste (VW) and to determine the importance of the temperature for the process of sanitization of the treated substrate. The experiment, entirely randomized with three treatments and three repetitions, constituted of nine aerobic reactors with 100 L capacity. The proportions of the wastes utilized were T1: 100%VW; T2: 5%SS + 95%VW; T3: 10%SS + 90%VW. The conjugated composting showed to be a feasible alternative for destruction of helminth eggs and stabilization of the wastes. The temperature, pH and ecological relations present in the reactors were fundamental for this purpose.

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O objetivo deste trabalho foi investigar a viabilidade de se tratar conjuntamente substâncias surfactantes, óleo mineral e lodo de esgoto sanitário. Para todos os tratamentos foram analisadas as concentrações de matéria orgânica (DQO) afluente e efluente. O sistema experimental foi monitorado durante 150 dias e diariamente eram realizadas quantificações do volume e da composição do biogás produzido. Foram constatadas remoções de DQO filtrada média de 82 por cento aos 18 dias, e para DQO bruta em torno de 76 por cento para os seis tratamentos aos 100 dias de operação. A produção de metano observada durante o período experimental demonstrou que as diferentes concentrações de surfactantes presentes no sistema não se mostraram tóxicas o suficiente para inibir as bactérias metanogênicas.

The present work had as objective investigate the viability of treating, through processes anaerobic substances surfactants, mineral oil and sewage sludge. For all the treatments the concentrations of organic matter were analyzed (COD) influent and effluent. The experimental system was monitored for 150 days. The volume and composition of the produced biogas were daily quantificated. Removals of filtered COD average were verified from 82 percent to the 18 days and for raw COD around 76 percent for the six treatments to the 100 dias.de operation. The methane production observed during the experimental period demonstrated that the different concentrations of present surfactants in the system were not shown toxicant enough to inhibit the methanogenic bacterias.

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A poluição de uma bacia hidrográfica pode causar alterações das propriedades físicas, químicas e biológicas da massa de água, comprometendo o seu uso para o consumo humano e para outros tipos de atividades, dependendo do grau de poluição ou contaminação. Os métodos de tratamentos convencionais de efluentes contendo metais pesados produzem quantidades significativas de subprodutos com características recalcitrantes, além de serem técnicas onerosas e de reprodutibilidade baixa. A busca por soluções mais baratas e definitivas levou ao desenvolvimento de tecnologias limpas, dentre estas tecnologias destaca-se o processo de sorção que baseia-se na utilização de substâncias absorventes desses elementos químicos. Este trabalho teve como objetivo avaliar o processo de sorção de metais pesados pelos resíduos sólidos orgânicos utilizando-se das técnicas de termogravimetria. Os resultados obtidos demonstraram que os perfis das curvas da termogravimetria dos resíduos sólidos orgânicos apresentam modificações significativas nas características físicas e químicas, quando submetidas ao processo de sorção dos metais pesados.

Pollution of a hydrographic basin can cause alterations in physical, chemical and biological properties of water mass, committing its use for the human consumption and for other types of activities, depending on the contamination or pollution level. The conventional treatment methods for effluents containing heavy metals produce significant amounts of byproducts with recalcitrant characteristics; besides the techniques being onerous their reproducibility is low. The search for cheaper and definitive solutions led to the development of clean technologies, among these technologies the sorption process based on utilization of absorbent substances for these elements can be pointed out. This work has the objective of evaluating the sorption process of heavy metals by organic solid waste utilizing the thermogravimetric technique. The results obtained demonstrated that the profiles of the thermogravimetric curves of the organic solid waste presented significant modifications in the physical and chemical characteristics when submitted to the heavy metal sorption process.

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O processo de digestão anaeróbia de resíduos sólidos orgânicos com baixa concentração de sólidos é realizado com substrato contendo em média cerca de 5 por cento (percentagem em peso) de sólidos totais. Os problemas de ordem técnica associados a este tipo de tratamento, estão relacionados ao estudo das configurações de reatores que possam viabilizar uma boa eficiência de transformação do material carbonáceo em um período relativamente curto de tempo. Portanto, neste trabalho foi estudado o processo de digestão anaeróbia de resíduos sólidos orgânicos (RSO) com baixa concentração de sólidos em um reator anaeróbio compartimentado (RAC). O reator anaeróbio compartimentado tinha capacidade unitária de 2200 litros e foi operado com tempo de retenção de sólidos de 90 dias. A eficiência de transformação média de STV foi de 75 por cento e o biogás produzido continha em média 60 por cento de gás metano.

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The influence of bovine rumen fluid inoculum during anaerobic treatment of the organic fraction of municipal solid waste (MSW) was studied in this work. The parameters adopted for evaluation were the biostabilization constant of total volatile solids (TVS) and the biostabilization time of the chemical oxygen demand (COD) applied to the reactors. The work was realized in four anaerobic batch reactors of 20 l capacity each, during a period of 365 days. The proportions between MSW/inoculum loaded in the reactors were Reactor A (100%/0%), Reactor B (95%/5%), Reactor C (90%/10%) and Reactor D (85%/15%). The necessary time for biostabilization of half of the applied COD was 459, 347, 302 and 234 days and the average of methane concentration in the biogas produced was 3.6%, 13.0%, 25.0% and 42.6% for Reactors A, B, C and D, respectively. The data obtained affirm that the inoculum used substantially improved the performance of the process.

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