Os azo corantes atualmente são considerados um assunto preocupante no que se refere à saúde pública e ambiental, pois quando lançados nos efluentes industriais contaminam o meio ambiente. Infelizmente, o método convencional de tratamento de efluentes têxteis, bem como de águas brutas que os recebem não são capazes de remover de maneira eficaz os corantes bem como sua toxicidade. Dentro deste contexto, este trabalho teve como objetivo avaliar a eficiência do tratamento de amostras aquosas por fotoeletrocatálise em comparação com a cloração convencional como método alternativo de degradação de azo corantes, usando os corantes Disperse Orange 1, Disperse Red 1 e Disperse Red 13 como modelo. Adicionalmente, foi avaliada a citotoxicidade dos corantes originais em condrócitos bovinos e células HepG2 em cultura em monocamadas e 3D. Para tanto, soluções desses corantes originais, clorados e fotoeletrocatalisados foram avaliadas utilizando ensaios de genotoxicidade/mutagenicidade, citotoxicidade e ecotoxicidade. Todos os corantes originais e clorados foram genotóxicos para as células HepG2 no ensaio cometa. Para o ensaio com Salmonella, a cloração reduziu a mutagenicidade dos corantes para a linhagem YG1041 e aumentou o efeito para a linhagem TA98, exceto o Disperse Red 13 que teve a mutagenicidade reduzida para as duas linhagens após cloração. A fotoeletrocatálise removeu tanto a genotoxicidade quanto a mutagenicidade. Somente o Disperse Orange 1 induziu apoptose pelo ensaio com anexina V, mas essa citotoxicidade foi removida após os tratamentos. Os corantes Disperse Red 1 e Disperse Red 13 foram tóxicos para D. similis enquanto somente o Disperse Red 1 foi tóxico para V. fischeri, sendo que os tratamentos por cloração e fotoeletrocatálise diminuíram a toxicidade apresentada. Os corantes Disperse Orange 1 e Disperse Red 13 passaram a ser tóxicos para V. fischeri após cloração, sendo que a fotoeletrocatálise do Disperse Red 13 também gerou produtos tóxicos para esse organismo. Assim, embora seja um método de tratamento promissor, atenção deve ser dada na avaliação e aplicação da fotoeletrocatálise como um método alternativo à cloração. Os corantes originais Disperse Orange 1 e Disperse Red 13 diminuíram a atividade mitocondrial dos condrócitos, sendo que o Disperse Red 13 também diminuiu a produção de lactato. Todos os corantes reduziram a atividade mitocondrial das células HepG2 em monocamadas, ao passo que o Disperse Orange 1 deixou de exercer esse efeito no cultivo em 3D. Somente o Disperse Red 13 diminuiu a atividade de desidrogenases das células HepG2 e tal efeito foi observado tanto no cultivo em monocamadas quanto em 3D. / The azo dyes are currently considered as a concern regarding the environmental and public health, since when released in industrial effluents they pollute the environment. Unfortunately, the conventional method of treatment of textile effluents is not able to effectively remove both dyes and their toxicity. Within this context, this study aimed to evaluate the effectiveness of the treatment of aqueous samples by photoelectrocatalysis compared to conventional chlorination as an alternative method of degradation of azo dyes, using the dyes Disperse Orange 1, Disperse Red 1 and Disperse Red 13 as a model. Additionally, we evaluated the cytotoxicity of the original dyes using HepG2 cells and chondrocytes cultured in monolayer and in 3D. To this end, solutions of these original dyes, chlorinated and photoelectrocatalysed were evaluated using tests of genotoxicity / mutagenicity, cytotoxicity and ecotoxicity. All the dyes, original and chlorinated, were genotoxic to HepG2 cells in the comet assay. For the test with Salmonella, chlorination reduced the mutagenicity of the dyes for the YG1041 strain and increased the effect for the TA98 strain, except Disperse Red 13, which had the mutagenic effect reduced for both strains after chlorination. The photoelectrocatalysis removed both genotoxicity and mutagenicity. Only Disperse Orange 1 induced apoptosis by annexin V assay, but this cytotoxicity was removed after treatment. The dye Disperse Red 1 and Disperse Red 13 were toxic to D. similis while only the Disperse Red 1 was toxic to V. fischeri, and the treatment by chlorination and photoelectrocatalysis decreased the toxicity showed. The dyes Disperse Orange 1 and Disperse Red 13 began toxic to V. fischeri after chlorination, and the photoelectrocatalysis of the Disperse Red 13 generated toxic products for this organism. So, while it is a promising treatment method, attention should be given in the evaluation and application of photoelectrocatalysis as an alternative to chlorination. The dyes Disperse Orange 1 and Disperse Red 13 decreased the mitochondrial activity of chondrocytes, and the dye Disperse Red 13 also decreased the production of lactate. All the dyes reduced the mitochondrial activity of the HepG2 cells cultured in monolayer, while the Disperse Orange 1 did no show this effect in 3D. Only Disperse Red 13 decreased the activity of dehydrogenases of HepG2 cells and this effect was observed both in monolayer and in 3D.

VASCONCELOS, Fábio Roger. Bactérias com Potencial Biotecnológico na Descoloração de Corantes Têxteis. 2010. 64 f. : Dissertação (mestrado) - Universidade Federal do Ceará, Centro de Ciências Agrárias, Departamento de Engenharia de Pesca, Fortaleza-CE, 2010 / Submitted by Nádja Goes (nmoraissoares@gmail.com) on 2016-07-14T12:39:39Z No. of bitstreams: 1 2010_dis_frvasconcelos.pdf: 490074 bytes, checksum: c033f812460c47d5fd980f329dc81fa3 (MD5) / Approved for entry into archive by Nádja Goes (nmoraissoares@gmail.com) on 2016-07-14T12:40:02Z (GMT) No. of bitstreams: 1 2010_dis_frvasconcelos.pdf: 490074 bytes, checksum: c033f812460c47d5fd980f329dc81fa3 (MD5) / Made available in DSpace on 2016-07-14T12:40:02Z (GMT). No. of bitstreams: 1 2010_dis_frvasconcelos.pdf: 490074 bytes, checksum: c033f812460c47d5fd980f329dc81fa3 (MD5) Previous issue date: 2010 / The discharge of effluents from textile industries for water bodies is currently a major concern for environmentalists as a function of synthetic dyes used to color fabrics thus polluting the environment. Biological treatments, especially with the use of bacteria, present themselves as the most economically viable and widely used to decolorize colored effluents. Thus, studies were conducted to test the color removal of dyes Remazol Brilliant Blue R, Orange G and Orange II using isolated and in mixed culture strains of Escherichia coli and Aeromonas hydrophila. Firstly, the isolation of bacterial strains from three different environments was made. Then, tests were performed to verify that the dye concentration would limit the growth of each microorganism. In addition to tests of decolorization, other parameters such as pH, biomass, COD removal, total protein and toxicity of metabolites were also monitored. The Escherichia coli strain isolated from the marine environment was able to decolorize concentrations of 2, 5 and 2 mg L-1, respectively, for the RBBR dye, Orange G and Orange II dyes, while the strain E. coli isolated from textile effluent, decolorized in concentrations of 5, 0.5 and 5 mg L-1, respectively. The bacteria Aeromonas hydrophila decolorized, respectively, at 10, 5 and 5 mg L-1, while the consortium of three bacteria decolorized at concentration of 5 mg L-1 for the three dyes tested individually. In these culture conditions the decrease in the rate of COD ranged from 45% to 69% with the lowest rate observed in the assay containing A. hydrophila and dye Orange II (45%) and the highest removal rate in the test containing the dye RBBR and the consortium (69%). Bioassays using Artemia salina showed that during the process of decolorization metabolites were produced with recalcitrant characteristics. The results show that the bacteria Escherichia coli and Aeromonas hydrophila have biotechnological potential in textile dyes, provided that they use low dye concentrations decolorizing / A descarga de efluentes das indústrias têxteis para corpos aquosos é, correntemente, uma das maiores preocupações dos ambientalistas em função dos corantes sintéticos usados para colorir os tecidos poluindo assim o ambiente. A aplicação de tratamentos biológicos, sobretudo com a utilização de bactérias, apresenta-se como um dos mais viáveis economicamente, sendo um dos sistemas mais utilizados para descolorir efluentes coloridos. Neste sentido, estudos foram realizados testes para a remoção de cor dos corantes Remazol Brilliant Blue R, Orange G e Orange II utilizando cepas de Escherichia coli e de Aeromonas hydrophila, isoladas e em cultura mista. Primeiramente foi feito o isolamento das cepas bacterianas de três ambientes diferentes. Em seguida, foram feitos testes para verificar qual concentração do corante seria limite para o crescimento de cada microrganismo. Além dos testes de descoloração também foram monitorados outros parâmetros como o pH, biomassa, remoção de DQO, proteínas totais e toxicidade dos metabólitos formados. A cepa Escherichia coli, isolada do ambiente marinho, foi capaz de descolorir concentrações de 2, 5 e 2 mg L-1, respectivamente, para os corante RBBR, Orange G e Orange II, enquanto que a cepa E. coli, isolada do efluente têxtil, descoloriu nas concentrações de 5, 0,5 e 5 mg L-1, respectivamente. A bactéria Aeromonas hydrophila descoloriu respectivamente nas concentrações de 10, 5 e 5 mg L-1, enquanto que o consórcio das três bactérias descoloriu na concentração de 5 mg L-1 para os três corantes testados individualmente. Nessas condições de cultivo a diminuição na taxa de DQO variou entre 45 e 69%, com a menor taxa observada no ensaio contendo A. hydrophila e o corante Orange II (45%) e a maior taxa de remoção no ensaio contendo o consórcio e o corante RBBR (69%). Bioensaios utilizando o microcrustáceo Artemia salina mostraram que durante o processo de descoloração foram produzidos metabólitos com características recalcitrantes. Os resultados demonstram que as bactérias Escherichia coli e Aeromonas hydrophila apresentam potencial biotecnológico na descoloração de corantes têxteis, desde que sejam utilizadas baixas concentrações dos corantes

Os azo corantes representam o maior grupo de corantes utilizados na indústria, principalmente no ramo têxtil. Sabe-se que grande parte desses produtos resiste aos sistemas de tratamento de efluente e assim, cerca de 10-15% dos corantes perdidos durante o processo de tingimento são lançados no efluente e atingem o meio ambiente. Alguns corantes desse grupo têm mostrado ser cancerígenos e mutagênicos para animais e humanos. Essa toxicidade se deve, em parte, à clivagem da ligação azo formando aminas aromáticas potencialmente cancerígenas. Ainda, a ação de sistema de metabolização nos grupamentos substituintes pode alterar a toxicidade destes compostos. Neste trabalho foram testados os azo corantes Disperse Orange 1 (4-(4--nitrofenilazo)difenilamina); pureza 96%; CAS no 2581-69-3), Disperse Red 1(N-etil-N(2-hidroxietil)-4-(4-nitrofenilazo)anilina; pureza 95%; CAS no. 2872-52-8) e Disperse Red 13 (2-[4-(2-cloro-4-nitrofenilazo)-N-etilfenilamino] etanol; pureza de 95%; CAS no 3180-81-2) usando o ensaio de mutagenicidade com Samonella. Foram utilizadas as linhagens tradicionais, TA98 e TA100 e suas respectivas derivadas com superprodução de nitroredutase e O-acetiltransferase, YG1041 e YG1042. Todos os corantes testados mostraram respostas mais altas com a linhagem TA98 em relação a TA100, o que sugere que esses compostos exercem seu efeito mutagênico principalmente por deslocamento do quadro de leitura do DNA. Para os três corantes, a resposta da linhagem YG1041 em relação a sua parental TA98 foi significativamente aumentada, mostrando a importância da nitroredutase e O-acetiltransferase na mutagenicidade desses corantes. Tal fato foi confirmado com as respostas da TA100 em relação a YG1042. O sistema de metabolização exógeno (S9) diminuiu a mutagenicidade de todos os corantes testados. Considerando os resultados obtidos com a linhagem YG1041, o corante Disperse Red 1 é o mais potente, seguido do Disperse Orange 1 e do Disperse Red 13. / Azo dyes constitute the largest group of colorants used in industry, mainly the textile one, and they pass through industrial wastewater treatment plants nearly unchanged due to their resistance to aerobic treatment. Therefore, it is estimated that 10-15% of the dyes are lost in the effluent during the dyeing process, reaching the environment. Some of these dyes have been shown to be carcinogenic and mutagenic to animals and humans. This toxic effect is, in part due to azo bond cleavage that forms potentially carcinogenic aromatic amines. The toxicity of the dyes can also be altered by the biotransformation of the substitutens. We tested the azo dyes Disperse Orange 1 (4-(4-Nitrophenylazo)diphenylamine); 96% purity; CAS number 2581-69-3), Disperse Red 1(N-Ethyl-N-(2-hydroxyethyl)-4-(4-nitrophenylazo)aniline; 95% purity; CAS number 2872-52-8) and Disperse Red 13 (2-[4-(2-Chloro-4-nitrophenylazo)-N-ethylphenylamino]ethanoll; 95% purity; CAS number 3180-81-2) using Salmonella/microssome mutagenicity assay. We used the traditional strains TA98 and TA100 and the strains with overproducing nitroreductase and O-acetyltransferase, YG1041 and YG1042, derivative of the TA 98 and TA100, respectively. All the dyes tested showed higher responses with the strain TA98 when compared with TA100, suggesting that these compounds induce mainly frameshift mutations. Moreover, we observed an increase in the mutagenicity with the overproducing nitroreductase and O-acetyltransferase strains, showing the importance of these enzymes in the mutagenicity of these dyes. In addition, for all the dyes the mutagenicity decreased after the S9 addition. According to mutagenic response with YG1041, Disperse Red 1 was the most potent, followed by Disperse Orange 1 and Disperse Red 13.

Os azo corantes atualmente são considerados um assunto preocupante no que se refere à saúde pública e ambiental, pois quando lançados nos efluentes industriais contaminam o meio ambiente. Infelizmente, o método convencional de tratamento de efluentes têxteis, bem como de águas brutas que os recebem não são capazes de remover de maneira eficaz os corantes bem como sua toxicidade. Dentro deste contexto, este trabalho teve como objetivo avaliar a eficiência do tratamento de amostras aquosas por fotoeletrocatálise em comparação com a cloração convencional como método alternativo de degradação de azo corantes, usando os corantes Disperse Orange 1, Disperse Red 1 e Disperse Red 13 como modelo. Adicionalmente, foi avaliada a citotoxicidade dos corantes originais em condrócitos bovinos e células HepG2 em cultura em monocamadas e 3D. Para tanto, soluções desses corantes originais, clorados e fotoeletrocatalisados foram avaliadas utilizando ensaios de genotoxicidade/mutagenicidade, citotoxicidade e ecotoxicidade. Todos os corantes originais e clorados foram genotóxicos para as células HepG2 no ensaio cometa. Para o ensaio com Salmonella, a cloração reduziu a mutagenicidade dos corantes para a linhagem YG1041 e aumentou o efeito para a linhagem TA98, exceto o Disperse Red 13 que teve a mutagenicidade reduzida para as duas linhagens após cloração. A fotoeletrocatálise removeu tanto a genotoxicidade quanto a mutagenicidade. Somente o Disperse Orange 1 induziu apoptose pelo ensaio com anexina V, mas essa citotoxicidade foi removida após os tratamentos. Os corantes Disperse Red 1 e Disperse Red 13 foram tóxicos para D. similis enquanto somente o Disperse Red 1 foi tóxico para V. fischeri, sendo que os tratamentos por cloração e fotoeletrocatálise diminuíram a toxicidade apresentada. Os corantes Disperse Orange 1 e Disperse Red 13 passaram a ser tóxicos para V. fischeri após cloração, sendo que a fotoeletrocatálise do Disperse Red 13 também gerou produtos tóxicos para esse organismo. Assim, embora seja um método de tratamento promissor, atenção deve ser dada na avaliação e aplicação da fotoeletrocatálise como um método alternativo à cloração. Os corantes originais Disperse Orange 1 e Disperse Red 13 diminuíram a atividade mitocondrial dos condrócitos, sendo que o Disperse Red 13 também diminuiu a produção de lactato. Todos os corantes reduziram a atividade mitocondrial das células HepG2 em monocamadas, ao passo que o Disperse Orange 1 deixou de exercer esse efeito no cultivo em 3D. Somente o Disperse Red 13 diminuiu a atividade de desidrogenases das células HepG2 e tal efeito foi observado tanto no cultivo em monocamadas quanto em 3D. / The azo dyes are currently considered as a concern regarding the environmental and public health, since when released in industrial effluents they pollute the environment. Unfortunately, the conventional method of treatment of textile effluents is not able to effectively remove both dyes and their toxicity. Within this context, this study aimed to evaluate the effectiveness of the treatment of aqueous samples by photoelectrocatalysis compared to conventional chlorination as an alternative method of degradation of azo dyes, using the dyes Disperse Orange 1, Disperse Red 1 and Disperse Red 13 as a model. Additionally, we evaluated the cytotoxicity of the original dyes using HepG2 cells and chondrocytes cultured in monolayer and in 3D. To this end, solutions of these original dyes, chlorinated and photoelectrocatalysed were evaluated using tests of genotoxicity / mutagenicity, cytotoxicity and ecotoxicity. All the dyes, original and chlorinated, were genotoxic to HepG2 cells in the comet assay. For the test with Salmonella, chlorination reduced the mutagenicity of the dyes for the YG1041 strain and increased the effect for the TA98 strain, except Disperse Red 13, which had the mutagenic effect reduced for both strains after chlorination. The photoelectrocatalysis removed both genotoxicity and mutagenicity. Only Disperse Orange 1 induced apoptosis by annexin V assay, but this cytotoxicity was removed after treatment. The dye Disperse Red 1 and Disperse Red 13 were toxic to D. similis while only the Disperse Red 1 was toxic to V. fischeri, and the treatment by chlorination and photoelectrocatalysis decreased the toxicity showed. The dyes Disperse Orange 1 and Disperse Red 13 began toxic to V. fischeri after chlorination, and the photoelectrocatalysis of the Disperse Red 13 generated toxic products for this organism. So, while it is a promising treatment method, attention should be given in the evaluation and application of photoelectrocatalysis as an alternative to chlorination. The dyes Disperse Orange 1 and Disperse Red 13 decreased the mitochondrial activity of chondrocytes, and the dye Disperse Red 13 also decreased the production of lactate. All the dyes reduced the mitochondrial activity of the HepG2 cells cultured in monolayer, while the Disperse Orange 1 did no show this effect in 3D. Only Disperse Red 13 decreased the activity of dehydrogenases of HepG2 cells and this effect was observed both in monolayer and in 3D.

Le traitement des rejets textiles se fait habituellement via une filière physico-chimique couplée à un traitement biologique. La qualité de l’effluent obtenu obéit difficilement aux normes de recyclage ou de rejet dans le milieu naturel. Dans cet objectif, différentes combinaisons sont proposées: la coagulation floculation (CF) et/ou l’adsorption sur charbon actif (CAP) en poudre couplée aux techniques membranaires (microfiltration (MF) ou ultrafiltration (UF)), la photocatalyse couplée à un traitement aérobie biologique (système membranaire (BRM) ou réacteur discontinu séquentiel (RDS)) ou au traitement anaérobie par voie biologique ou chimique. Une comparaison générale a été réalisée pour optimiser le traitement adéquat. La combinaison CF-CAP-UF est un traitement efficace pour la réduction de la DCO, de la couleur et de la turbidité. La dégradation de deux colorants textiles (azoïque et phthalocyanine) a été étudiée par photocatalyse simple ou combinée à un BRM. Le traitement photocatalytique a été réalisé en présence de dioxyde de titane fixé sur un support en fibres de cellulose dans un réacteur à film tombant en présence d’irradiation UV. Pour les deux types de réacteurs biologiques, bien que la biomasse ait été influencée par la variation de la concentration en colorant et par le mode de fonctionnement continu pour le BRM, elle a pu résister. Après le pré-traitement nous avons obtenu une complète décoloration mais les sous produits photocatalytiques demeurent toxiques et peuvent empêcher l’abattement de la DCO. Dans une dernière partie, nous avons testé le couplage de la photocatalyse à un traitement chimique par hydrogénation catalytique ou biologique par boues granulaires. Cette dernière possibilité s’avère être efficace puisque des taux de décoloration supérieurs à 90% ont été atteints pour différents types de colorants et qu’aucune toxicité des produits obtenus lors du pré-traitement photocatalytique n’a été détectée / The treatment of textile wastewater is usually done by a set of physicochemical processes coupled with a biological treatment. The effluent quality abides with difficulty the norms for reuse or discharge in environment. Various treatment combinations have been tested such as coagulation-flocculation (CF) and adsorption on activated carbon (PAC) coupled with membrane technologies (microfiltration (MF) or ultrafiltration (UF)), photocatalysis coupled with a biological treatment (membrane bioreactor (MBR) or a sequential batch reactor (SBR) or a biological and chemical anaerobic treatment. A general comparison was made to optimise the appropriate treatment. The combination CF-PAC-UF is the most effective of non-biological systems in terms of COD, absorbance and turbidity removal. The degradation of an azoïc and a phthalocyanine textile dyes by simple photocatalysis or combined to a membrane bioreactor has been investigated. Photocatalysis was achieved in a falling film reactor containing titanium dioxide fixed on cellulose fibres under UV irradiation. For both biological systems, although biomass was influenced by the variation of dyes concentration and the continuous operating mode for the MBR, it could resist to the applied conditions. However, even after pre-treatment where full decolouration was achieved, photocatalytic by-products were toxic and could inhibit COD removal. Chemical and biological anaerobic treatment have been applied to textile dyes and combined with a photocatalytic process. Photocatalysis was able to remove more than 90% color from crude as well as autoxidized reduced dye solutions. The photocatalytic end-products were not toxic toward methanogenic bacteria

PhDENV / Department of Ecology and Resource Management / Some industries such as textiles, ceramics, paper and printing are known to use significant amounts of dye to colour their products and during the colouring process, certain quantities of dyes are absorbed by the products, and some of them end up in wastewater. Depending on their application, some synthetic dyes are designed to be chemically or biologically resistant and their presence in the environment can cause severe environmental problems because of their colour impartation to water bodies. Therefore, proper treatment is required to remove these pollutants from wastewater before discharge into the environment. In this thesis, the potential of dye removal from wastewater by calcined magnesite, halloysite nanoclay and calcined magnesite - halloysite nanoclay composite was evaluated. To this end, the study was subdivided to four segments. The first segment of the study focused on evaluating the efficiency of using calcined magnesite to remove Methylene Blue (MB), Direct Red 81 (DR81), Methyl Orange (MO) and Crystal Violet (CV) dyes from aqueous systems using a batch study. To achieve that, several operational factors like residence time, adsorbent dosage, dye concentration and temperature were appraised. The adsorbent was subjected to different kinds of physicochemical characterization to determine the various characteristics that would assist in the dye uptake process. Characterization results showed that the adsorbent material was highly crystalline with magnesite, periclase, dolomite, and quartz as some of the crystalline phases. The batch study proved that calcined magnesite is effective in the treatment of dye contaminated water and moreover it performed well in terms of colour removal, though exceptional results were recorded for CV removal with complete decolourisation occurring in first few minutes of contact. In terms of experimental adsorption capacity, the performance of calcined magnesite was in the order CV (14.99 mg/g) > DR81 (12.56 mg/g) > MO (0.64 mg/g) > MB (0.39 mg/g). Mechanisms of adsorption where explained by fitting the experimental data into adsorption isotherms, kinetics, and thermodynamic parameters. Neither, the Langmuir, nor the Freundlich nor the Dubinin Radushkevich, nor the Temkin model could perfectly describe the adsorption of the four dyes onto calcined magnesite, however adsorption kinetics obeyed the pseudo second order model, implying that, the dye removal process was primarily a chemical process. In accordance with the results of this study, it can be concluded that calcined magnesite can be used effectively for the removal of dyes in aqueous solution and thus can be applied to treat wastewater containing dyes. The second segment of the study focused on the removal of MB, DR81, MO and CV dyes by halloysite nanoclay. Physicochemical characterisation revealed that the nanoclay has a surface area of 42 m²/g and its ABSTRACT iv morphology is predominated by tubular structures, which exhibit some hollow rod like structures. Various important parameters namely contact time, initial concentration of dyes, dosage, solution temperature and solution pH were optimized to achieve maximum adsorption capacity and it was observed that the effect of initial pH and temperature of the aqueous solution was neglibible on removal of the four dyes. The experimental adsorption capacities towards 40 mg/L of MB, DR81, MO and CV dyes were 17.51, 14.11, 0.38, and 4.75 mg/g respectively. The results indicate that natural halloysite nanoclay is an efficient material for the removal of the selected dyes. Due to its low cost and non-toxicity, halloysite nanoclay can be considered a good replacement option of other high cost materials used to treat coloured wastewater especially in developing countries like South Africa. Having observed the performance of calcined magnesite and halloysite nanoclay individually in the removal of selected dyes, a third study was designed with the aim of preparing a nanocomposite adsorbent from the aforementioned adsorbent materials and then evaluating the synergistic influence of the mechanochemical modification by a ball miller on the removal of MB, DR81, MO and CV dyes. Physicochemical characterization was carried out to get an insight of pre- and -post adsorption characteristics of the nanocomposite material and results showed major changes which could be an indication of dye uptake by the nanocomposite material. According to the results, the nanocomposite material outcompeted its component individual constituent materials i.e (calcined magnesite and halloysite nanoclay material) in the removal of DR81, which in turn was the highest removal efficiency observed for the whole batch adsorption study recording a maximum adsorption capacity and percentage removal of 19.89 mg/g and 99.40% respectively. Experimental results fitted the Langmuir and pseudo-second order models perfectly hence demonstrating that adsorption took place on a homogenous adsorbent layer via chemisorption. In overall, the results suggested that the nanocomposite is a suitable adsorbent for decolourising industrial wastewater. Based on the overall performance of the adsorbents in removing the four dyes, it was observed that the nanocomposite material had a high affinity for DR81 dye hence it was chosen as the model dye for further application in column studies. The effect of flow rate, bed height and initial dye concentration on the removal of DR81 was investigated. Maximum bed capacity and equilibrium dye uptake were determined and break through curves were plotted. Percentage dye removal increased with decrease in flow rate and increase in bed height. The maximum capacity of column was found to be about 51.73 mg DR81 per gram of the nanocomposite adsorbent for a flow rate of 3 mL/min, initial concentration of 10 mg/L and 4 cm bed height. Data from column studies was fitted to the Thomas model and Adams-Bohart models. The comparison of the R2 values obtained from both models showed a better fit for the nanocomposite material than the individual halloysite nanoclay and calcined magnesite materials. The study revealed the applicability of calcined magnesite- halloysite nanoclay composite in fixed bed column for the removal of DR81 dye from aqueous solution. v The reuse of an adsorbent is essential in order to make the adsorption process economic and environmentally friendly. To recover the adsorbate and renew the adsorbent for further use, a chemical method of regeneration was applied by using 0.1 M NaOH as the desorbent. Regeneration with 0.1 M NaOH proved very efficient for some dyes and less efficient for others depending on the adsorbent material used at the time. The general observation was that the adsorption capacity of the adsorbent materials decreased with successive adsorption – desorption cycles. Furthermore, regeneration with NaOH, favoured the acidic dyes (DR81 and MO) more than the basic dyes (MB and CV) possibly due to electrostatic interactions between oppositely charged molecules allowing for reversible reactions to take place. The three tested adsorbents namely calcined magnesite, halloysite nanoclay and their nanocomposite thereof were applied for the treatment of real wastewater effluent from a printing and ink industry. The adsorbents performed very well in terms of colour removal as recommended by the South African standards of wastewater discharge, However, in terms of pH, calcined magnesite and the nanocomposite produced a highly alkaline solution hence wastewater neutralisation by an acid is recommended before discharge. These findings show that the two natural clay-based materials (calcined magnesite and halloysite nanoclay) and their nanocomposite thereof have a great potential for application in dye wastewater remediation since the materials used in the process are inexpensive, abundant and require minimal modifications. / NRF

A indústria têxtil gera grandes volumes de efluentes com elevada carga orgânica, forte coloração e toxicidade. Neste trabalho, estuda-se o tratamento de solução aquosa contendo o corante Solophenyl Yellow Arle 154% por meio dos processos O3-H2O2/UV e foto-Fenton, avaliando-se as repostas: remoção de cor em 5 minutos, remoção de cor em 60 minutos, taxa máxima de remoção de cor e remoção de COT em 60 minutos. Os experimentos foram realizados em semibatelada com circulação usando um reator fotoquímico com campo de radiação anular coaxial, constituído de corpo cilíndrico em aço com refletor interno de alumínio para 12 lâmpadas fixadas simetricamente na superfície refletora e um tubo reator em quartzo de 0,7 L, posicionados verticalmente no eixo do refletor. Para o processo O3-H2O2/UV foram utilizadas lâmpadas Phillips TUV (36 W, 254 nm). A corrente gasosa contendo O3 foi introduzida no reator por meio de um difusor. Para o processo foto-Fenton foram utilizadas lâmpadas Sylvania (12 W cada, 300 400 nm) e concentração de Fe(II) de 0,25 mmol/L. Em ambos os processos, solução de peróxido de hidrogênio foi adicionada durante os 30 minutos iniciais de tratamento. As amostras foram analisadas por medidas de carbono orgânico total (COT) e remoção de cor (absorbância medida em 405 nm em espectrofotômetro UV-visível). Em ambos os processos utilizou-se o planejamento experimental Doehlert, definindo os valores mínimo e máximo para cada variável adotada. No caso do processo O3- H2O2/UV (ETAPA I), foram estudados os efeitos da potência elétrica total das lâmpadas (144 432 W), concentração de H2O2 (5 30 mmol/L), concentração inicial de corante (20 100 mg/L), concentração de ozônio (10 40 mg/L) e pH (3 10). No processo foto-Fenton (ETAPA II), estudaram-se os efeitos da potência (160 480 W), concentração de H2O2 (5 30 mmol/L) e concentração inicial de corante (20 100 mg/L). Os resultados da ETAPA I indicaram que o aumento da concentração do corante, em meio ácido, aumenta a remoção de cor em 5 e 60 minutos, sugerindo a eficiência da ação via ozônio molecular sob o grupo cromóforo do corante. Os melhores resultados apresentaram remoção acima de 95% em 5 e 60 minutos de tratamento. Entretanto, para a remoção de COT em 60 minutos o processo não foi eficiente, apresentando resultado máximo de 35,6%. Na ETAPA II obtiveram-se resultados menos satisfatórios para remoção de cor se comparados aos da ETAPA I (56,1% em 5 minutos e 78% em 60 minutos de tratamento), mas melhores em relação à remoção de COT em 60 minutos atigindo 45,1% de remoção. As maiores taxas de remoção de cor foram observadas nos 5 primeiros minutos de tratamento para todos os experimentos. Experimentos complementares realizados em uma terceira etapa (ETAPA III) mostraram que a aplicação do processo O3 seguido do processo foto-Fenton permitiu resultados satisfatórios tanto para remoção de cor (97,2%), quanto para remoção de COT (69,5%). O estudo da ação do processo O3 em modo contínuo e a avaliação econômica preliminar do processo integrado O3 - foto-Fenton sugerem o potencial de aplicação do tratamento integrado a indústrias têxteis. / The textile industry generates large volumes of wastewater with high organic load, strong coloration and toxicity. In this work, the treatment of an aqueous solution containing the dye Solophenyl Yellow Arle 154% was studied by the O3-H2O2/UV and photo-Fenton processes, in order to evaluate the responses color removal after 5 minutes; color removal after 60 minutes; maximum rate of color removal; and TOC removal after 60 minutes. The experiments were carried out in the semi-batch mode with circulation using a photochemical reactor with annular coaxial radiation field, consisting of a cylindrical stainless steel support with an aluminum internal reflector with 12 lamps fixed symmetrically in the internal reflecting surface, and a quartz tube reactor of 0.7 L, positioned vertically along the axis of the reflector. For the O3- H2O2/UV process, Phillips TUV lamps (36 W, 254 nm) were used; the gas stream containing zone was introduced into the reactor through a diffuser. For the photo- Fenton process, Sylvania lamps (12 W each, 300 - 400 nm) and a concentration of Fe (II) of 0.25 mmol/L were used. In both cases, the hydrogen peroxide solution was added in the first 30 minutes of treatment. The samples were analyzed by the measurement of total organic carbon (TOC) and color removal (absorbance measured at 405 nm in a UV-visible spectrophotometer). In both cases the Doehlert experimental design was used, defining the minimum and maximum values of each variable adopted. In the case of O3-H2O2/UV process (PHASE I), the effects of the total electric power of the lamps (144 - 432 W), H2O2 concentration (5 - 30 mmol/L), initial dye concentration (20 - 100 mg/L), ozone concentration (10 - 40 mg/L), and pH (3 - 10) were studied. For the photo-Fenton process, the studied variables were: total electric power of the lamps (160 - 480 W), H2O2 concentration (5 - 30 mmol/L), and initial dye concentration (20 - 100 mg/L). The results of PHASE I indicated that the increase of dye concentration in acidic conditions increases color removal after 5 and 60 minutes, thus suggesting the efficiency of molecular ozone action upon the chromophore group of the dye. The best results showed color removal above 95% after 5 and 60 minutes of treatment. However, for the TOC removal the process was not efficient, with maximum removal after 60 minutes of only 35.6%. In PHASE II less satisfactory results for color removal were obtained in comparison with PHASE I (56.1% after 5 minutes and 78% after 60 minutes of treatment), but with higher TOC removal after 60 minutes, achieving over 45.1%. The highest color removal rates were observed within the first 5 minutes of treatment for all runs. Additional experiments carried out in PHASE III showed that the oxidation by O3 followed by the photo-Fenton process enabled to achieve suitable results for both color (97.2%) and TOC removals (69.5%). The study of the O3 process in the continuous mode and a preliminary economic evaluation suggests a high potential for the use of the integrated O3-photo-Fenton process in textile industries.

A indústria têxtil gera grandes volumes de efluentes com elevada carga orgânica, forte coloração e toxicidade. Neste trabalho, estuda-se o tratamento de solução aquosa contendo o corante Solophenyl Yellow Arle 154% por meio dos processos O3-H2O2/UV e foto-Fenton, avaliando-se as repostas: remoção de cor em 5 minutos, remoção de cor em 60 minutos, taxa máxima de remoção de cor e remoção de COT em 60 minutos. Os experimentos foram realizados em semibatelada com circulação usando um reator fotoquímico com campo de radiação anular coaxial, constituído de corpo cilíndrico em aço com refletor interno de alumínio para 12 lâmpadas fixadas simetricamente na superfície refletora e um tubo reator em quartzo de 0,7 L, posicionados verticalmente no eixo do refletor. Para o processo O3-H2O2/UV foram utilizadas lâmpadas Phillips TUV (36 W, 254 nm). A corrente gasosa contendo O3 foi introduzida no reator por meio de um difusor. Para o processo foto-Fenton foram utilizadas lâmpadas Sylvania (12 W cada, 300 400 nm) e concentração de Fe(II) de 0,25 mmol/L. Em ambos os processos, solução de peróxido de hidrogênio foi adicionada durante os 30 minutos iniciais de tratamento. As amostras foram analisadas por medidas de carbono orgânico total (COT) e remoção de cor (absorbância medida em 405 nm em espectrofotômetro UV-visível). Em ambos os processos utilizou-se o planejamento experimental Doehlert, definindo os valores mínimo e máximo para cada variável adotada. No caso do processo O3- H2O2/UV (ETAPA I), foram estudados os efeitos da potência elétrica total das lâmpadas (144 432 W), concentração de H2O2 (5 30 mmol/L), concentração inicial de corante (20 100 mg/L), concentração de ozônio (10 40 mg/L) e pH (3 10). No processo foto-Fenton (ETAPA II), estudaram-se os efeitos da potência (160 480 W), concentração de H2O2 (5 30 mmol/L) e concentração inicial de corante (20 100 mg/L). Os resultados da ETAPA I indicaram que o aumento da concentração do corante, em meio ácido, aumenta a remoção de cor em 5 e 60 minutos, sugerindo a eficiência da ação via ozônio molecular sob o grupo cromóforo do corante. Os melhores resultados apresentaram remoção acima de 95% em 5 e 60 minutos de tratamento. Entretanto, para a remoção de COT em 60 minutos o processo não foi eficiente, apresentando resultado máximo de 35,6%. Na ETAPA II obtiveram-se resultados menos satisfatórios para remoção de cor se comparados aos da ETAPA I (56,1% em 5 minutos e 78% em 60 minutos de tratamento), mas melhores em relação à remoção de COT em 60 minutos atigindo 45,1% de remoção. As maiores taxas de remoção de cor foram observadas nos 5 primeiros minutos de tratamento para todos os experimentos. Experimentos complementares realizados em uma terceira etapa (ETAPA III) mostraram que a aplicação do processo O3 seguido do processo foto-Fenton permitiu resultados satisfatórios tanto para remoção de cor (97,2%), quanto para remoção de COT (69,5%). O estudo da ação do processo O3 em modo contínuo e a avaliação econômica preliminar do processo integrado O3 - foto-Fenton sugerem o potencial de aplicação do tratamento integrado a indústrias têxteis. / The textile industry generates large volumes of wastewater with high organic load, strong coloration and toxicity. In this work, the treatment of an aqueous solution containing the dye Solophenyl Yellow Arle 154% was studied by the O3-H2O2/UV and photo-Fenton processes, in order to evaluate the responses color removal after 5 minutes; color removal after 60 minutes; maximum rate of color removal; and TOC removal after 60 minutes. The experiments were carried out in the semi-batch mode with circulation using a photochemical reactor with annular coaxial radiation field, consisting of a cylindrical stainless steel support with an aluminum internal reflector with 12 lamps fixed symmetrically in the internal reflecting surface, and a quartz tube reactor of 0.7 L, positioned vertically along the axis of the reflector. For the O3- H2O2/UV process, Phillips TUV lamps (36 W, 254 nm) were used; the gas stream containing zone was introduced into the reactor through a diffuser. For the photo- Fenton process, Sylvania lamps (12 W each, 300 - 400 nm) and a concentration of Fe (II) of 0.25 mmol/L were used. In both cases, the hydrogen peroxide solution was added in the first 30 minutes of treatment. The samples were analyzed by the measurement of total organic carbon (TOC) and color removal (absorbance measured at 405 nm in a UV-visible spectrophotometer). In both cases the Doehlert experimental design was used, defining the minimum and maximum values of each variable adopted. In the case of O3-H2O2/UV process (PHASE I), the effects of the total electric power of the lamps (144 - 432 W), H2O2 concentration (5 - 30 mmol/L), initial dye concentration (20 - 100 mg/L), ozone concentration (10 - 40 mg/L), and pH (3 - 10) were studied. For the photo-Fenton process, the studied variables were: total electric power of the lamps (160 - 480 W), H2O2 concentration (5 - 30 mmol/L), and initial dye concentration (20 - 100 mg/L). The results of PHASE I indicated that the increase of dye concentration in acidic conditions increases color removal after 5 and 60 minutes, thus suggesting the efficiency of molecular ozone action upon the chromophore group of the dye. The best results showed color removal above 95% after 5 and 60 minutes of treatment. However, for the TOC removal the process was not efficient, with maximum removal after 60 minutes of only 35.6%. In PHASE II less satisfactory results for color removal were obtained in comparison with PHASE I (56.1% after 5 minutes and 78% after 60 minutes of treatment), but with higher TOC removal after 60 minutes, achieving over 45.1%. The highest color removal rates were observed within the first 5 minutes of treatment for all runs. Additional experiments carried out in PHASE III showed that the oxidation by O3 followed by the photo-Fenton process enabled to achieve suitable results for both color (97.2%) and TOC removals (69.5%). The study of the O3 process in the continuous mode and a preliminary economic evaluation suggests a high potential for the use of the integrated O3-photo-Fenton process in textile industries.

This diploma thesis is focused on the study of the influence of advanced oxidation processes on degradation of organic dyes. The field of AOP – very effective physically-chemical methods of wastewater treatment – includes application of strong oxidation agents, UV and ionizing radiation and electrical discharges. For this thesis, two of these methods were chosen – the application of oxidation agent (ozone) and UV radiation. Along with electrolysis, which is mentioned rather marginally in this thesis (it is the subject of the previous thesis), these phenomena are products of electrical discharge in water, where they participate in the processes of degradation in a different way. For all measurement series, two direct azo dyes were chosen as model substances – C.I. Direct Blue 106 and C.I. Direct Red 79. The ozonizer, in which either oxygen or synthetic or technical air were loaded as carrier gases, was used for degradation of dyes by ozone. The generated ozone was loaded into the bubbling vessel with dye solution of different initial concentration (10–130 mg.dm-3), which was followed by other bubbling vessel with KI solution for the next analytical determination of the amount of generated ozone. The other parameters changed were the gas flow (1–2 dm3.min-1), ozonizer output (minimal and maximal), type of dye, pH value of the solution (neutral or acid) and additional electrolyte (NaCl, Na2SO4 or any). The reactor for the study of the influence of UV radiation on degradation of dyes was an UV sterilizer into which the equivalent volume of dye solution was added. The possibilities of experimental settings were limited and only the type of dye, an additional electrolyte and pH value of the dye solution were adjusted (as in the case of ozone). Several series of samples were measured with various input conditions which more or less influenced the degradation of investigated dyes in this experiment. It was found that for both used methods the Direct Blue 106 dye was more degradable (with significantly better results for ozone than for UV radiation). The degradation of Direct Red 79 dye proceeded only by ozone treatment, in the case of the application of UV radiation no degradation occurred. By investigation of the influence of initial concentration of dye on its degradation, it was confirmed that with the initial concentration enhancement the final concentration rises as well, whereas in low concentrations (10–50 mg.dm-3) the initial concentration has no effect. The addition of an electrolyte had an accelerating effect on dye degradation in both methods (NaCl and also Na2SO4 showed similar results though the degradation proceeded in different ways). The addition of HCl accelerated the degradation only in the case of UV radiation; during the application of ozone the pH level of the system did not have any influence on the degradation. Oxygen and synthetic air had the strongest effect on ozone degradation (comparable results); in the case of technical air the final dye concentration was higher up to 30 %. The gas flow of 1.5 dm3.min-1 was stated as optimal with the ozonizer output 30 W (maximal). At minimal power the ozonizer produced very low amount of ozone.