931 resultados para tannery wastewater


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Nanofiltration process for the treatment/valorisation of cork processing wastewaters was studied. A DS-5 DK 20/40 (GE Water Technologies) nanofiltration membrane/module was used, having 2.09 m(2) of surface area. Hydraulic permeability was determined with pure water and the result was 5.2 L.h(-1).m(-2).bar(-1). The membrane presents a rejection of 51% and 99% for NaCl and MgSO4 salts, respectively. Two different types of regimes were used in the wastewaters filtration process, total recycling mode and concentration mode. The first filtration regime showed that the most favourable working transmembrane pressure was 7 bar working at 25 degrees C. For the concentration mode experiments it was observed a 30% decline of the permeate fluxes when a volumetric concentration factor of 5 was reached. The permeate COD, BOD5, colour and TOC rejection values remained well above the 90% value, which allows, therefore, the concentration of organic matter (namely the tannin fraction) in the concentrate stream that can be further used by other industries. The permeate characterization showed that it cannot be directly discharged to the environment as it does not fulfil the values of the Portuguese discharge legislation. However, the permeate stream can be recycled to the process (boiling tanks) as it presents no colour and low TOC (< 60 ppm) or if wastewater discharge is envisaged we have observed that the permeate biodegradability is higher than 0.5, which renders conventional wastewater treatments feasible.

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Wastewater from cork processing industry present high levels of organic and phenolic compounds, such as tannins, with a low biodegradability and a significant toxicity. These compounds are not readily removed by conventional municipal wastewater treatment, which is largely based on primary sedimentation followed by biological treatment. The purpose of this work is to study the biodegradability of different cork wastewater fractions, obtained through membrane separation, in order to assess its potential for biological treatment and having in view its valorisation through tannins recovery, which could be applied in other industries. Various ultrafiltration and nanofiltration membranes where used, with molecular weight cut-offs (MWCO) ranging from 0.125 to 91 kDa. The wastewater and the different permeated fractions were analyzed in terms of Total Organic Carbon (TOC), Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD), Total Phenols (TP), Tannins, Color, pH and Conductivity. Results for the wastewater shown that it is characterized by a high organic content (670.5-1056.8 mg TOC/L, 2285-2604 mg COD/L, 1000-1225 mg BOD/L), a relatively low biodegradability (0.35-0.38 for BODs/COD and 0.44-0.47 for BOD20/COD) and a high content of phenols (360-410 mg tannic acid/L) and tannins (250-270 mg tannic acid/L). The results for the wastewater fractions shown a general decrease on the pollutant content of permeates, and an increase of its biodegradability, with the decrease of the membrane MWCO applied. Particularly, the permeated fraction from the membrane MWCO of 3.8 kDa, presented a favourable index of biodegradability (0.8) and a minimized phenols toxicity that enables it to undergo a biological treatment and so, to be treated in a municipal wastewater treatment plant. Also, within the perspective of valorisation, the rejected fraction obtained through this membrane MWCO may have a significant potential for tannins recovery. Permeated fractions from membranes with MWCO lower than 3.8 kDa, presented a particularly significant decline of organic matter and phenols, enabling this permeates to be reused in the cork processing and so, representing an interesting perspective of zero discharge for the cork industry, with evident environmental and economic advantages. (C) 2010 Elsevier Ltd. All rights reserved.

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Cork processing involves a boiling step to make the cork softer, which consumes a high volume of water and generates a wastewater with a high organic content, rich in tannins. An assessment of the final wastewater characteristics and of the boiling water composition along the boiling process was performed. The parameters studied were pH, color, total organic carbon (TOC), chemical and biochemical oxygen demands (COD, BOD5, BOD20), total suspended solids (TSS), total phenols and tannins (TP, TT). It was observed that the water solutes extraction power is significantly reduced for higher quantities of cork processed. Valid relationships between parameters were established not only envisaging wastewater characterization but also to provide an important tool for wastewater monitoring and for process control/optimization. Boiling water biodegradability presented decreasing values with the increase of cork processed and for the final wastewater its value is always lower than 0.5, indicating that these wastewaters are very difficult to treat by biological processes. The biodegradability was associated with the increase of tannin content that can rise up to 0.7 g/L. These compounds can be used by other industries when concentrated and the clarified wastewater can be reused, which is a potential asset in this wastewater treatment.

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The presence of filamentous fungi was detected in wastewater and air collected at wastewater treatment plants (WWTP) from several European countries. The aim of the present study was to assess fungal contamination in two WWTP operating in Lisbon. In addition, particulate matter (PM) contamination data was analyzed. To apply conventional methods, air samples from the two plants were collected through impaction using an air sampler with a velocity air rate of 140 L/min. Surfaces samples were collected by swabbing the surfaces of the same indoor sites. All collected samples were incubated at 27°C for 5 to 7 d. After lab processing and incubation of collected samples, quantitative and qualitative results were obtained with identification of the isolated fungal species. For molecular methods, air samples of 250 L were also collected using the impinger method at 300 L/min airflow rate. Samples were collected into 10 ml sterile phosphate-buffered saline with 0.05% Triton X-100, and the collection liquid was subsequently used for DNA extraction. Molecular identification of Aspergillus fumigatus and Stachybotrys chartarum was achieved by real-time polymerase chain reaction (RT-PCR) using the Rotor-Gene 6000 qPCR Detection System (Corbett). Assessment of PM was also conducted with portable direct-reading equipment (Lighthouse, model 3016 IAQ). Particles concentration measurement was performed at five different sizes: PM0.5, PM1, PM2.5, PM5, and PM10. Sixteen different fungal species were detected in indoor air in a total of 5400 isolates in both plants. Penicillium sp. was the most frequently isolated fungal genus (58.9%), followed by Aspergillus sp. (21.2%) and Acremonium sp. (8.2%), in the total underground area. In a partially underground plant, Penicillium sp. (39.5%) was also the most frequently isolated, also followed by Aspergillus sp. (38.7%) and Acremonium sp. (9.7%). Using RT-PCR, only A. fumigatus was detected in air samples collected, and only from partial underground plant. Stachybotrys chartarum was not detected in any of the samples analyzed. The distribution of particle sizes showed the same tendency in both plants; however, the partially underground plant presented higher levels of contamination, except for PM2.5. Fungal contamination assessment is crucial to evaluating the potential health risks to exposed workers in these settings. In order to achieve an evaluation of potential health risks to exposed workers, it is essential to combine conventional and molecular methods for fungal detection. Protective measures to minimize worker exposure to fungi need to be adopted since wastewater is the predominant internal fungal source in this setting.

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Filamentous fungi from genus Aspergillus were previously detected in wastewater treatment plants (WWTP) as being Aspergillus flavus (A. flavus), an important toxigenic fungus producing aflatoxins. This study aimed to determine occupational exposure adverse effects due to fungal contamination produced by A. flavus complex in two Portuguese WWTP using conventional and molecular methodologies. Air samples from two WWTP were collected at 1 m height through impaction method. Surface samples were collected by swabbing surfaces of the same indoor sites. After counting A. flavus and identification, detection of aflatoxin production was ensured through inoculation of seven inoculates in coconut-milk agar. Plates were examined under long-wave ultraviolet (UV; 365 nm) illumination to search for the presence of fluorescence in the growing colonies. To apply molecular methods, air samples were also collected using the impinger method. Samples were collected and collection liquid was subsequently used for DNA extraction. Molecular identification of A. flavus was achieved by real-time polymerase chain reaction (RT-PCR) using the Rotor-Gene 6000 qPCR detection system (Corbett). Among the Aspergillus genus, the species that were more abundant in air samples from both WWTP were Aspergillus versicolor (38%), Aspergillus candidus (29.1%), and Aspergillus sydowii (12.7%). However, the most commonly species found on surfaces were A. flavus (47.3%), Aspergillus fumigatus (34.4%), and Aspergillus sydowii (10.8%). Aspergillus flavus isolates that were inoculated in coconut agar medium were not identified as toxigenic strains and were not detected by RT-PCR in any of the analyzed samples from both plants. Data in this study indicate the need for monitoring fungal contamination in this setting. Although toxigenic strains were not detected from A. flavus complex, one cannot disregard the eventual presence and potential toxicity of aflatoxins.

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The tanning industry generates a high quantity of solid wastes. Therefore, there is a need to create valorization [added value] options for these wastes. The main objective of the present work was to study the effect of protein hydrolysates (HP) prepared from fleshings on leather dyeing. During previous studies it was found that the application of HP products, obtained from fleshings, in leather retannage intensified the colour of crust leather. In this work the CIELAB colour system was used to evaluate the effect of HP on retannage processes. The main conclusions of this study were: (i) HP can be used instead of a dicyanodiamide resin (Fortan DC) if the colour parameters of the standard procedure are to be maintained, and (ii) the replacement of an acrylic resin (Fortan A40) by glutaraldehyde-modified HP (GHP) results in a darker skin, and can therefore be interesting for the reduction of the quantity of dye used.

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In this study, the concentration probability distributions of 82 pharmaceutical compounds detected in the effluents of 179 European wastewater treatment plants were computed and inserted into a multimedia fate model. The comparative ecotoxicological impact of the direct emission of these compounds from wastewater treatment plants on freshwater ecosystems, based on a potentially affected fraction (PAF) of species approach, was assessed to rank compounds based on priority. As many pharmaceuticals are acids or bases, the multimedia fate model accounts for regressions to estimate pH-dependent fate parameters. An uncertainty analysis was performed by means of Monte Carlo analysis, which included the uncertainty of fate and ecotoxicity model input variables, as well as the spatial variability of landscape characteristics on the European continental scale. Several pharmaceutical compounds were identified as being of greatest concern, including 7 analgesics/anti-inflammatories, 3 β-blockers, 3 psychiatric drugs, and 1 each of 6 other therapeutic classes. The fate and impact modelling relied extensively on estimated data, given that most of these compounds have little or no experimental fate or ecotoxicity data available, as well as a limited reported occurrence in effluents. The contribution of estimated model input variables to the variance of freshwater ecotoxicity impact, as well as the lack of experimental abiotic degradation data for most compounds, helped in establishing priorities for further testing. Generally, the effluent concentration and the ecotoxicity effect factor were the model input variables with the most significant effect on the uncertainty of output results.

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This article evaluates the sustainability and economic potential of microalgae grown in brewery wastewater for biodiesel and biomass production. Three sustainability and two economic indicators were considered in the evaluation within a life cycle perspective. For the production system the most efficient process units were selected. Results show that harvesting and oil separation are the main process bottlenecks. Microalgae with higher lipid content and productivity are desirable for biodiesel production, although comparable to other biofuel’s feedstock concerning sustainability. However, improvements are still needed to reach the performance level of fossil diesel. Profitability reaches a limit for larger cultivation areas, being higher when extracted biomass is sold together with microalgae oil, in which case the influence of lipid content and areal productivity is smaller. The values of oil and/or biomass prices calculated to ensure that the process is economically sound are still very high compared with other fuel options, especially biodiesel.

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This study performs a sustainability evaluation of biodiesel from microalga Chlamydomonas sp. grown in 20 % (v/v) of brewery’s wastewater, blended with pentose sugars (xylose, arabinose or ribose resulting from the hydrolysis of brewer’s spent grains (BSG). The life cycle steps considered for the study are: microalgae cultivation, biomass processing and lipids extraction at the brewery site, and its conversion to biodiesel at a dedicated external biofuel’s plant. Three sustainability indicators (LCEE, FER and GW) were considered and calculated using experimental data. Literature data was used, whenever necessary, to complement life cycle data, thus allowing a more accurate sustainability evaluation. A comparative analysis of the biodiesel life cycle steps was also conducted, with the main goal of identifying which steps need to be improved. Results show that biomass processing, especially cell harvesting, microalgae cultivation, and lipids extraction are the main process bottlenecks. It is also analysed the influence on the microalgae biodiesel sustainability of adding each pentose sugar to the cultivation media, concluding that it strongly influences the biomass and lipid productivity. In particular, the addition of xylose is preferable in terms of lipid productivity, but from a sustainability point of view, ribose is the best, though the difference from xylose is not significant. Nevertheless, culture without pentose addition presents the best sustainability results.

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The concerns on metals in urban wastewater treatment plants (WWTPs) are mainly related to its contents in discharges to environment, namely in the final effluent and in the sludge produced. In the near future, more restrictive limits will be imposed to final effluents, due to the recent guidelines of the European Water Framework Directive (EUWFD). Concerning the sludge, at least seven metals (Cd, Cr, Cu, Hg, Ni, Pb and Zn) have been regulated in different countries, four of which were classified by EUWFD as priority substances and two of which were also classified as hazardous substances. Although WWTPs are not designed to remove metals, the study of metals behaviour in these systems is a crucial issue to develop predictive models that can help more effectively the regulation of pre-treatment requirements and contribute to optimize the systems to get more acceptable metal concentrations in its discharges. Relevant data have been published in the literature in recent decades concerning the occurrence/fate/behaviour of metals in WWTPs. However, the information is dispersed and not standardized in terms of parameters for comparing results. This work provides a critical review on this issue through a careful systematization, in tables and graphs, of the results reported in the literature, which allows its comparison and so its analysis, in order to conclude about the state of the art in this field. A summary of the main consensus, divergences and constraints found, as well as some recommendations, is presented as conclusions, aiming to contribute to a more concerted action of future research. © 2015, Islamic Azad University (IAU).

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European Journal of Operational Research, nº 73 (1994)

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Dissertação apresentada para obtenção do Grau de Doutor em Engenharia Química e Bioquímica pela Universidade Nova de Lisboa, Faculdade de Ciências e Tecnologia

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Dissertação para obtenção do Grau de Mestre em Engenharia Química e Bioquímica

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Um dos objetivos desta dissertação de mestrado foi avaliar o impacto ambiental do processo de tingimento usado na indústria de curtumes, em termos de volume de efluente produzido e sua carga poluente. Pretendeu-se também encontrar alternativas ao nível do processo de tingimento que levem a uma melhoria na qualidade do efluente produzido. Outro objetivo deste trabalho foi avaliar o funcionamento da ETAR existente na empresa JR Fontes, no que diz respeito aos parâmetros em estudo (carência química de oxigénio - CQO, pH, crómio e teor de sólidos suspensos totais - SST), propondo alterações que permitam respeitar os valores de emissão exigidos na licença de descarga da empresa. Verificou-se que o processo de tingimento aplicado pela empresa JR Fontes é muito poluente, em termos de carga orgânica e matéria em suspensão. Este facto é comprovado pelos resultados obtidos para os três processos estudados: Montana, Galáctico e Navak. Todos os processos apresentam um efluente com pH ácido (aproximado a 3) e valores de CQO superiores a 3550 mg O2/L, sendo o processo Navak aquele que apresenta o valor mais alto para o banho composto, 8362 mg O2/L. Relativamente ao teor de crómio, o banho de recurtume com concentração mais elevada de crómio total é o banho 1 do processo Navak, com 2297 mg/L, sendo que a concentração destes banhos é sempre elevada, igual ou superior a 746 mg/L. No que diz respeito à matéria em suspensão, o processo Navak é novamente o mais poluente, com um valor de 3842 mg SST/L, não sendo obtidos nos outros processos, valores inferiores a 1205 mg SST/L. Na realização de um processo alternativo de tingimento verificou-se que é possível diminuir a carga orgânica do efluente originado. A aplicação de recurtumes sintéticos deu origem a efluentes menos poluentes. O melhor valor obtido para a CQO foi de 1113 mg O2/L, sendo obtidos valores não superiores a 7185 mg O2/L para processos de características semelhantes aos aplicados nesta indústria. Relativamente à ETAR, apesar das restrições ao funcionamento que esta apresenta, no geral pode ser considerada eficiente, embora não consiga atingir o objetivo pretendido de remoção para a CQO, ou seja o valor de 1100 mg O2/L. Nos restantes parâmetros é cumprido o limite de emissão (350 mg SST/L, pH entre 6 e 9 e 2 mg Cr/L para o crómio total): os SST apresentam o valor de 98 mg SST/L, o crómio total de 1,2 mg Cr/L e o pH encontra-se entre 8 e 9. São aqui feitas duas abordagens para solucionar os problemas existentes na ETAR. A primeira considera um ajuste no tratamento e equipamentos existentes, através da reconstrução do tanque de equalização, da substituição do coagulante por sulfato ferroso e da reconstrução do sedimentador, assim como a substituição das tubagens por umas de maior diâmetro, solucionando assim problemas de manutenção de toda a instalação e do incumprimento da legislação. A outra abordagem implica a substituição do sistema de afinação existente, os filtros de areia e carvão ativados, por um sistema de membranas de ultrafiltração ou por dois filtros de carvão ativado. Para tratar um efluente com um valor de CQO de 3000 mg O2/L com o carvão estudado, seriam necessários 132 kg de carvão por coluna, aproveitando-se os equipamentos existentes. No caso das membranas filtrantes, estas são eficazes, reduzindo a CQO em cerca de 70%. Ao contrário do carvão, a aplicação deste sistema implicaria a aquisição de novos equipamentos. Futuramente propõe-se a avaliação dos vários tipos de reagentes usados no tingimento de couro de forma a aplicar no tratamento aqueles que produzam as características desejadas no produto final e a que apresentem um menor resultado de CQO. Propõe-se também o estudo de viabilidade da remoção de crómio dos banhos de recurtume e consequente avaliação da aplicabilidade de um tratamento biológico em substituição ou como complemento do tratamento existente.

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O presente trabalho teve como objectivo a minimização do impacto ambiental do processo de curtume da pele de bovino. A indústria de curtumes transforma a pele, material putrescível, em couro, material nobre, termicamente estável e imputrescível. A transformação da pele em couro origina uma carga poluente apreciável quer quanto a efluentes líquidos quer quanto a resíduos sólidos. O fluxo produtivo da indústria de curtumes pode dividir-se em quatro sectores: ribeira, curtume, tinturaria e acabamento, sendo que os três primeiros geram efluentes líquidos com elevada carga poluente. Neste trabalho, foram avaliadas as fases do processo que geram efluentes líquidos: molho, caleiro, curtume e tinturaria. Na avaliação do processo do molho testou-se uma protease e uma lipase contra um molhante e um desengordurante tradicional, agentes químicos normalmente utilizados no molho mas menos biodegradáveis que as enzimas testadas. Salienta-se o bom resultado obtido quanto à eficiência do molho Na avaliação do processo de caleiro testaram-se várias alternativas no sentido da redução da quantidade de sulfureto de sódio utilizada e da minimização da carga poluente. Entre as alternativas, depilação por oxidação, depilação enzimática com e sem destruição do pêlo, elegeu-se a depilação enzimática sem destruição do pêlo que conduziu a resultados com menor impacto ambiental, nomeadamente a redução da % da quantidade de sulfureto de sódio, sendo a redução da carga poluente de 4,19 % de sulfureto, 32.80% de sólidos suspensos totais (SST),27.09% de sólidos totais (ST) e de 76.90% da carência química de oxigénio (CQO) no efluente de caleiro. No processo do curtume da pele é utilizado crómio como agente de curtume em cerca de 80% das peles tratadas, sendo este metal problemático em termos ambientais. No sentido de reduzir a quantidade de crómio utilizada no processo foi realizado um planeamento factorial onde as variáveis a estudar foram a concentração de crómio e a temperatura, tendo este como objectivo observar qual a quantidade mínima de crómio necessária para termos um produto final nas condições desejadas e gerando um menor impacto ambiental. Concluiu-se desenvolvendo um processo que mostra ser possível reduzir a quantidade de sal de crómio de 7% para 5%, além de ter um impacto ambiental claramente menos agressivo nos efluentes de curtume gerado. Este processo quando comparado com o processo tradicional permite a redução de 27% na CQO, 79% nos SST, 11% nos ST e 38% no teor de crómio Na avaliação do processo de tinturaria foi estudado um processo compacto contra o processo tradicional, tendo-se concluído pelo menor impacto ambiental do processo estudado, nomeadamente ao nível da redução do consumo de água e da carga poluente gerada. A comparação dos dois processos, no que respeita à carga poluente gerada, permitiu concluir por uma redução de 39% da CQO, 50% dos SST, e 12% dos ST quando aplicado o processo compacto Por fim foi feita uma avaliação do impacto ambiental do efluente global gerado pelos processos considerados com menor impacto ambiental contra o processo tradicional, normalmente aplicado na indústria. A aplicação do conjunto dos processos desenvolvidos, quando comparada com a aplicação do conjunto dos processos tradicionais, mostra uma redução de 1% no sulfureto, 40% na CQO, 60 % nos SST, 42 % no crómio e 11% nos ST, mostrando claramente que é possível reduzir a carga poluente da indústria de curtumes atuando no processo. Este trabalho mostrou a importância de atuar no processo para minimizar os custos de tratamento e mesmo de investimento dos efluentes da indústria de curtumes. Importa salientar que os processos desenvolvidos necessitam de validação a uma escala semi-industrial.