The treatment of synthetic landfill leachate and raw landfill leachate were investigated using two sets of 3 L aerobic sequencing batch reactors (SBR): activated sludge SBR (ASBR) and granular SBR (GSBR). In synthetic young landfill leachate treatment, GSBR was more efficient in nitrogen and carbon removal than ASBR. During the steady period of the experiment, 99% total ammonium nitrogen (TAN) was removed through nitritation and nitrification in GSBR with an average influent TAN concentration of 498 mg/L. On the contrary, complete nitrification was not achieved in ASBR with a nitrification efficiency of 77±10%. GSBR also presented higher efficiency in denitrification and COD removal compared to ASBR. Phosphorus removal efficiency was almost identical in both reactors. Synthetic old landfill leachate treatment using GSBR maintained the stable COD removal efficiency at 66%, when the ammonia nitrogen to the maximum of 465±46 mg/L. The ASBR required a start-up of at least 30 days and removed 59±9% of COD when an influent ammonia nitrogen concentration about 200 mg/L. The GSBR was also more efficient than the ASBR for nitrogen removal. The granular sludge reached a maximum ammonia removal of 95±7%, whereas 96±5% was achieved by ASBR. The phosphorus removal was likely affected by the free nitrous acid (FNA) and the low biodegradability of tannic acid. In raw landfill leachate treatment, the total ammonia nitrogen (TAN) removal efficiency was in GSBR approximately 99.7%. However, the ASBR treatment did not show a consistent performance in TAN removal. TAN removal efficiency decreased with increasing ammonia concentration in the influent. Nitrification in GSBR was partially inhibited at FA concentrations of 48 to 57 mg/L, which was two times more than the FA concentration that inhibited nitrification in ASBR. In terms of chemical oxygen demand (COD) removal, low removal efficiencies of 17% and 26% were observed in ASBR and GSBR, respectively. The low COD removal efficiencies were associated with the refractory organic content of the leachate used in this study, which resulted in a poor phosphorous removal performance as well. Overall, aerobic granular sludge showed a better performance in removing nutrients and organic matter from young or old landfill leachate, being more efficient than the conventional suspended growth activated sludge. Therefore, the use of AGS for leachate treatment should be encouraged. Further investigations should also be addressed, especially with a focus on improving SND and phosphorus removal efficiencies. / May 2017

O objetivo principal desta pesquisa foi comparar o desempenho de dois reatores anaeróbios híbridos de biomassa imobilizada (RAHBI), em escala de laboratório, no processamento da vinhaça de cana-de-açúcar. Um (reator 1) recebendo vinhaça sem tratamento prévio e outro (reator 2) processando vinhaça previamente submetida à coagulação, utilizando-se de um biopolímero experimental a base de cálcio. Os reatores foram construídos em acrílico, com volume de 1,5 litros cada, provido de sistema de recirculação com razão igual a 3. A operação dos reatores foi dividida em duas etapas: a primeira, com duração de 69 dias, teve seu fim caracterizado por um colapso apresentado pelo reator 2. A segunda fase, com duração de 37 dias, onde se observou outro colapso. O principal parâmetro de controle no monitoramento dos reatores foi a quantificação de matéria orgânica, em termos de Demanda Química de Oxigênio (DQO). Durante a Fase I, o reator 1 apresentou eficiência de remoção média de 82,9 ± 4,4% , e o reator 2 de 72,2 ± 18,1%. A carga orgânica volumétrica (COV) média aplicada para o reator 1, durante esta fase, foi de 5,3 ± 1,3 kg DQO/\'M POT.3\'d, e para o reator 2 foi de 5,3 ± 1,6 kg DQO/\'M POT.3\'d. O colapso ocorrido no reator 2 foi evidenciada pelo decréscimo acentuado da eficiência de remoção, chegando a 33,7%. Durante a Fase II, o reator 1 apresentou eficiência de remoção média de 77,5 ± 9,4% , e o reator 2 de 79,2 ± 9,7%. A carga orgânica volumétrica (COV) média aplicada para o reator 1, durante esta fase, foi de 5,1 ± 2,4 kg DQO/\'M POT.3\'d, e para o reator 2 foi de 5,0 ± 2,3 kg DQO/\'M POT.3\'. Ao final desta fase o reator 1 apresentou eficiência de remoção de 80,9%, e o reator 2 65.8%. Foram analisados, também, alcalinidade e produção de metano (\'CH IND.4\'). Durante todas as fases, a alcalinidade dos dois reatores esteve acima de 1000 mg \'CA\'CO IND.3\'/l, indicando estabilidade, em relação a este parâmetro, dos reatores. A produção de \'CH IND.4\' do reator 1 foi de 0,0507 ± 0,0232 l \'CH IND.4\'/h e 0,0838 ± 0,0326 l \'CH IND.4\'/h nas fases I e II, respectivamente. Para o reator 2, esta produção foi de 0,0307 ± 0,0137 l \'CH IND.4\'/h e 0,0800 ± 0,0297 l \'CH IND.4\'/h, para as fases I e II, respectivamente. Foram feitos ensaios de resistência mecânica dos grânulos, análise de microscopia eletrônica de varredura (MEV), Espectrometria de Energia Dispersiva de Raios-X (EDS) e análise da comunidade microbiana, empregando técnicas de biologia molecular. Os testes de resistência mecânica dos grânulos indicam que os grânulos contidos no inóculo, reatores 1 e 2 possuem resistência à desintegração. As análises de MEV e EDS indicam a presença do elemento cálcio com aproximadamente 22% para o inóculo, 39% para o reator 1 e 50% para o reator 2, na massa dos elementos analisados das amostras de grânulos. As análises de biologia molecular indicaram similaridades entre os reatores 1 e 2 de 66,5 e 58%, para os domínios Bacteria e Archea, respectivamente. Desta forma, supõe-se que esta diferença da biota entre os reatores não estaria contribuindo para a falha conferida no reator 2. / This research aimed at compare the performance of two hybrid anaerobic immobilized biomass (HAIB), in laboratory scale, processing vinasse from sugar cane alcohol destilery. Reactor 1 received vinasse without pre-treatment. Reactor 2 processed coagulated vinasse using a calcium-based biopolymer as coagulant. The two reactors were built in acrylic, with a volume of 1,5 liters each. The recirculation flow rate was 3. The operation of the reactors was divided in two phases: first, lasting 69 days, came to an end characterized by a failure (collapse) presented by the reactor 2. The second phase, lasting 37 days, came to an end characterized by another collapse. The main control parameter in the monitoring of the reactors was the quantification of organic matter in terms of COD. During Phase I, the reactor 1 showed average removal efficiency of 82,9 ± 4,4%, and the reactor 2 72,2 ± 18,1%. The organic loading rate (VOC) average applied to reactor 1, during this phase, was 5,3 ± 1,3 kg DQO/\'M POT.3\'d, and 5,3 ± 1,6 kg DQO/\'M POT.3\'d for the reactor 2. The failure occurred in the reactor 2 was evidenced by the sharp decrease of removal efficiency, reaching 33.7%. During Phase II, the reactor 1 showed average removal efficiency of 77,5 ± 9,4%, and the reactor 2 79,2 ± 9,7%. The average VOC applied to reactor 1, during this phase, was 5,1 ± 2,4 kg DQO/\'M POT.3\'d, and 5,0 ± 2,3 kg DQO/\'M POT.3\'d for reactor 2. At the end of this phase, the reactor 1 showed a removal efficiency of 80.9%, and the reactor 2 65.8%. Has also been analyzed, alkalinity and methane (\'CH IND.4\'). During all the phases, the alkalinity of both reactors was above 1000 mg \'CA\'CO IND.3\'/l, indicating stability in the reactors. The production of \'CH IND.4\' was 0.0507 ± 0.0232 l \'CH IND.4\'/h and 0.0326 ± 0.0838 l \'CH IND.4\'/h in phases I and II, respectively. For the reactor 2, the production of \'CH IND.4\' was 0,0307 ± 0,0137 l \'CH IND.4\'/h e 0,0800 ± 0,0297 l \'CH IND.4\'/h for the phases I and II, respectively. Assays were performed in mechanical granules strength, analysis of scanning electron microscopy (SEM), Energy Dispersive Spectroscopy X-ray (EDS) and analysis of the microbial community, using molecular biology techniques. The tests of mechanical of granules strength indicate that the granules contained in the inoculum, reactors 1 and 2 are resistant to disintegration. The SEM and EDS analysis indicated the presence of calcium element with approximately 22% inoculum, 39% for reactor 1 and 50% for reactor 2, in the mass of the elements analyzed samples of granules. The microbial community analyzes indicated molecular similarity between the first and second reactor of 66.5 and 58% for Bacteria and Archea domain, respectively. Thus, it is assumed that the difference between the biota of the reactors would not be contributing to the failure given in the reactor 2.

O objetivo principal desta pesquisa foi comparar o desempenho de dois reatores anaeróbios híbridos de biomassa imobilizada (RAHBI), em escala de laboratório, no processamento da vinhaça de cana-de-açúcar. Um (reator 1) recebendo vinhaça sem tratamento prévio e outro (reator 2) processando vinhaça previamente submetida à coagulação, utilizando-se de um biopolímero experimental a base de cálcio. Os reatores foram construídos em acrílico, com volume de 1,5 litros cada, provido de sistema de recirculação com razão igual a 3. A operação dos reatores foi dividida em duas etapas: a primeira, com duração de 69 dias, teve seu fim caracterizado por um colapso apresentado pelo reator 2. A segunda fase, com duração de 37 dias, onde se observou outro colapso. O principal parâmetro de controle no monitoramento dos reatores foi a quantificação de matéria orgânica, em termos de Demanda Química de Oxigênio (DQO). Durante a Fase I, o reator 1 apresentou eficiência de remoção média de 82,9 ± 4,4% , e o reator 2 de 72,2 ± 18,1%. A carga orgânica volumétrica (COV) média aplicada para o reator 1, durante esta fase, foi de 5,3 ± 1,3 kg DQO/\'M POT.3\'d, e para o reator 2 foi de 5,3 ± 1,6 kg DQO/\'M POT.3\'d. O colapso ocorrido no reator 2 foi evidenciada pelo decréscimo acentuado da eficiência de remoção, chegando a 33,7%. Durante a Fase II, o reator 1 apresentou eficiência de remoção média de 77,5 ± 9,4% , e o reator 2 de 79,2 ± 9,7%. A carga orgânica volumétrica (COV) média aplicada para o reator 1, durante esta fase, foi de 5,1 ± 2,4 kg DQO/\'M POT.3\'d, e para o reator 2 foi de 5,0 ± 2,3 kg DQO/\'M POT.3\'. Ao final desta fase o reator 1 apresentou eficiência de remoção de 80,9%, e o reator 2 65.8%. Foram analisados, também, alcalinidade e produção de metano (\'CH IND.4\'). Durante todas as fases, a alcalinidade dos dois reatores esteve acima de 1000 mg \'CA\'CO IND.3\'/l, indicando estabilidade, em relação a este parâmetro, dos reatores. A produção de \'CH IND.4\' do reator 1 foi de 0,0507 ± 0,0232 l \'CH IND.4\'/h e 0,0838 ± 0,0326 l \'CH IND.4\'/h nas fases I e II, respectivamente. Para o reator 2, esta produção foi de 0,0307 ± 0,0137 l \'CH IND.4\'/h e 0,0800 ± 0,0297 l \'CH IND.4\'/h, para as fases I e II, respectivamente. Foram feitos ensaios de resistência mecânica dos grânulos, análise de microscopia eletrônica de varredura (MEV), Espectrometria de Energia Dispersiva de Raios-X (EDS) e análise da comunidade microbiana, empregando técnicas de biologia molecular. Os testes de resistência mecânica dos grânulos indicam que os grânulos contidos no inóculo, reatores 1 e 2 possuem resistência à desintegração. As análises de MEV e EDS indicam a presença do elemento cálcio com aproximadamente 22% para o inóculo, 39% para o reator 1 e 50% para o reator 2, na massa dos elementos analisados das amostras de grânulos. As análises de biologia molecular indicaram similaridades entre os reatores 1 e 2 de 66,5 e 58%, para os domínios Bacteria e Archea, respectivamente. Desta forma, supõe-se que esta diferença da biota entre os reatores não estaria contribuindo para a falha conferida no reator 2. / This research aimed at compare the performance of two hybrid anaerobic immobilized biomass (HAIB), in laboratory scale, processing vinasse from sugar cane alcohol destilery. Reactor 1 received vinasse without pre-treatment. Reactor 2 processed coagulated vinasse using a calcium-based biopolymer as coagulant. The two reactors were built in acrylic, with a volume of 1,5 liters each. The recirculation flow rate was 3. The operation of the reactors was divided in two phases: first, lasting 69 days, came to an end characterized by a failure (collapse) presented by the reactor 2. The second phase, lasting 37 days, came to an end characterized by another collapse. The main control parameter in the monitoring of the reactors was the quantification of organic matter in terms of COD. During Phase I, the reactor 1 showed average removal efficiency of 82,9 ± 4,4%, and the reactor 2 72,2 ± 18,1%. The organic loading rate (VOC) average applied to reactor 1, during this phase, was 5,3 ± 1,3 kg DQO/\'M POT.3\'d, and 5,3 ± 1,6 kg DQO/\'M POT.3\'d for the reactor 2. The failure occurred in the reactor 2 was evidenced by the sharp decrease of removal efficiency, reaching 33.7%. During Phase II, the reactor 1 showed average removal efficiency of 77,5 ± 9,4%, and the reactor 2 79,2 ± 9,7%. The average VOC applied to reactor 1, during this phase, was 5,1 ± 2,4 kg DQO/\'M POT.3\'d, and 5,0 ± 2,3 kg DQO/\'M POT.3\'d for reactor 2. At the end of this phase, the reactor 1 showed a removal efficiency of 80.9%, and the reactor 2 65.8%. Has also been analyzed, alkalinity and methane (\'CH IND.4\'). During all the phases, the alkalinity of both reactors was above 1000 mg \'CA\'CO IND.3\'/l, indicating stability in the reactors. The production of \'CH IND.4\' was 0.0507 ± 0.0232 l \'CH IND.4\'/h and 0.0326 ± 0.0838 l \'CH IND.4\'/h in phases I and II, respectively. For the reactor 2, the production of \'CH IND.4\' was 0,0307 ± 0,0137 l \'CH IND.4\'/h e 0,0800 ± 0,0297 l \'CH IND.4\'/h for the phases I and II, respectively. Assays were performed in mechanical granules strength, analysis of scanning electron microscopy (SEM), Energy Dispersive Spectroscopy X-ray (EDS) and analysis of the microbial community, using molecular biology techniques. The tests of mechanical of granules strength indicate that the granules contained in the inoculum, reactors 1 and 2 are resistant to disintegration. The SEM and EDS analysis indicated the presence of calcium element with approximately 22% inoculum, 39% for reactor 1 and 50% for reactor 2, in the mass of the elements analyzed samples of granules. The microbial community analyzes indicated molecular similarity between the first and second reactor of 66.5 and 58% for Bacteria and Archea domain, respectively. Thus, it is assumed that the difference between the biota of the reactors would not be contributing to the failure given in the reactor 2.

Ces dernières années ont vu un intérêt croissant pour l'application de nanoparticules de chalcogénure (IP) (par exemple Se, Te) dans divers secteurs industriels, y compris l'énergie, les aciers, le verre et le raffinage du pétrole. Le chalcogénure métallique fluorescent (par exemple CdSe, CdTe) NPs sont utilisés dans les cellules solaires, les capteurs optoélectroniques et aussi dans le domaine de la biologie et de la médecine pour l'imagerie ou de détection comprenant biolabelling. En outre, en raison de la forte toxicité des oxyanions chalcogènes (à savoir, sélénite, séléniate, tellurites et tellurate), leur libération dans l'environnement est très préoccupante. Ainsi, mettre l'accent a été donné dans cette thèse sur le développement d'un nouveau procédé de synthèse microbienne des NPs chalcogénures en combinant le traitement biologique des eaux usées Se / Te contenant avec biorecovery de Se / Te sous la forme de Se / Te chalcogénures NPs.Une attention particulière a été accordée pour étudier l'effet des métaux lourds (par exemple Cd, Zn et Pd) co-contaminants sur bioréduction sélénite par anaérobie granulaire boues. boue anaérobie granulaire capable de réduire sélénite de séléniure de, en présence de Cd a été enrichie pour la synthèse microbienne de CdSe IP. Il était évident que lorsque Cd est présent avec sélénite, soit il forme un complexe de Se-Cd par adsorption sur biogène Se (0) des nanoparticules après EME-oxyanion ou bioréduction il réagit avec le séléniure aqueux (HSe-) pour former CdSe. Les spectres d'absorption et de fluorescence de la phase aqueuse à confirmer la présence de CdSe IP dans la phase aqueuse. spectroscopie Raman et X-ray spectroscopie de photoélectrons (XPS) analyse l'appui de cette constatation. La formation d 'une couche alliée de CdSxSe1-x à l'interface entre le noyau et CdS CdSe shell dans la boue a également été observée. Des études détaillées sur les substances polymères extracellulaires (EPS) révèlent que la teneur en protéines et en polysaccharides comme augmenté dans les EPS extraites de boues enrichi tandis que les substances humiques comme diminué. chromatographie d'exclusion de taille (SEC) des EPS révèle en outre une empreinte distincte pour les protéines et les substances humiques-like, avec une augmentation de haute teneur en protéines comme poids moléculaire et l'apparition de nouveaux pics pour les substances humiques comme dans les EPS après l'enrichissement.Anaérobie des boues lit granulaire (UASB) à courant ascendant a été utilisé pour la première fois pour le retrait continu de tellurite des eaux usées synthétique et la récupération du Te comme biogénique Te (0). La spectroscopie aux rayons X à dispersion d'énergie (EDS), diffraction des rayons X (XRD) et analyse spectroscopique Raman de la biomasse a confirmé le dépôt de Te (0) dans la biomasse. Il était évident que la majorité du Te (0) a été piégé principalement dans l'EPS entourant la biomasse, qui peut être facilement séparé par centrifugation / Recent years have seen a growing interest in the application of chalcogenide nanoparticles (NPs) (e.g. Se, Te) in various industrial sectors including energy, steels, glass and petroleum refining. The fluorescent metal chalcogenide (e.g. CdSe, CdTe) NPs are used in solar cells, optoelectronic sensors and also in the field of biology and medicine for imaging or sensing including biolabelling. Moreover, due to the high toxicity of chalcogen oxyanions (i.e., selenite, selenate, tellurite and tellurate), their release in the environment is of great concern. Thus, emphasize was given in this thesis on the development of a novel microbial synthesis process of chalcogenide NPs by combining biological treatment of Se/Te-containing wastewaters with biorecovery of Se/Te in the form of Se/Te chalcogenides NPs.A special focus was given to study the effect of heavy metal (e.g. Cd, Zn and Pd) co-contaminants on selenite bioreduction by anaerobic granular sludge. Anaerobic granular sludge capable of reducing selenite to selenide in the presence of Cd was enriched for the microbial synthesis of CdSe NPs. It was evident that when Cd is present along with selenite, it either forms a Se-Cd complex by adsorption onto biogenic Se(0) nanoparticles after Se-oxyanion bioreduction or it reacts with aqueous selenide (HSe-) to form CdSe. The absorption and fluorescence spectra of the aqueous phase confirm the presence of CdSe NPs in the aqueous phase. Raman spectroscopy and X-ray photoelectron spectroscopy (XPS) analysis support this finding. The formation of an alloyed layer of CdSxSe1-x at the interface between the CdSe core and CdS shell in the sludge was also observed. Detailed studies on the extracellular polymeric substances (EPS) reveal that the protein and polysaccharide-like content increased in the EPS extracted from enriched sludge while humic-like substances decreased. Size exclusion chromatography (SEC) of EPS further reveals a distinct fingerprint for proteins and humic-like substances, with increase in high molecular weight protein-like and the appearance of new peaks for humic-like substances in the EPS after the enrichment.An upflow anaerobic granular sludge bed (UASB) reactor was used for the first time for continuous removal of tellurite from synthetic wastewater and the recovery of Te as biogenic Te(0). Energy-dispersive X-ray spectroscopy (EDS), X-ray diffraction (XRD) and Raman spectroscopic analysis of biomass confirmed the deposition of Te(0) in the biomass. It was evident that the majority of the Te(0) was trapped predominantly in the EPS surrounding the biomass, which can be easily separated by centrifugation

Ce travail vise à développer une approche originale à micro et à méso-échelle pour étudier divers phénomènes et intensifier les performances du réacteur. A méso-échelle, l'accent est mis sur l'efficacité de la production de biogaz dans un réacteur anaérobie 2D sous différentes conditions hydrodynamiques ainsi qu’à différentes concentrations de substrat. Puis, dans un dispositif microfluidique transparent, une seule granule de différentes tailles a été utilisée sous différentes conditions d'exploitation. Les effets des différentes conditions hydrodynamiques et des concentrations de substrat associés à la taille et la densité des granules de boues sur la production de biogaz ont été étudiés / The present work is focused on developing an original micro to mesoscale approach to investigate various phenomena and then to intensify the performance of a reactor. At mesoscale, the emphasis is given to the interactions between granular sludge particles as well as the biogas production efficiency in a 2D reactor under various hydrodynamic conditions at different concentrations of substrate. Then, within the microdevices, a single sludge particle of various sizes was used under different operating conditions such as superficial liquid velocity and concentration of substrate. The effect of different hydrodynamic conditions and concentration of substrate was studied

Pour faire face à des réglementations de plus en plus contraignantes, des procédés compacts et performants doivent être développés pour assurer un traitement des effluents efficace et pérenne. La technologie des boues granulaires aérobies permet de coupler productivité et compacité pour autant qu’elle soit maîtrisée. La formation des granules implique des conditions opératoires définies principalement dans des réacteurs discontinus. Afin d’améliorer la capacité de traitement, ce travail a pour objectif de proposer des conditions opératoires permettant l’utilisation des boues granulaires aérobies dans un réacteur en régime continu. Pour cela, la technique de granulation de l’écosystème est contrôlée par l’optimisation du fonctionnement d’un réacteur de laboratoire fonctionnant en discontinu (mode transitoire) puis la procédure obtenue est transposée à une taille de réacteur plus importante. Cette étude montre que la charge massique, le cisaillement et la pression de sélection des boues conditionnent la formation des granules et leurs propriétés. Le fonctionnement du réacteur en régime continu a ensuite été étudié. Il est montré que la structure granulaire a pu être maintenue tout en augmentant l’efficacité du procédé, tout paramètre équivalent par ailleurs (capacité de traitement doublée pour le réacteur continu). In fine, le système a été testé avec un effluent industriel. Un logiciel industriel a été utilisé afin de représenter pour l’optimiser le fonctionnement d’un réacteur fluidisé granulaire tel qu’obtenu expérimentalement. Si le module proposé dans ce logiciel a montré ses limites pour simuler un régime SBR, le modèle MBBR , bien que ne considérant pas la granule dans son ensemble, semble être adéquat pour représenter le fonctionnement en continu. L’utilisation des boues granulaires dans un réacteur continu est une technologie prometteuse mais nécessite des investigations sur son fonctionnement à long terme et sa modélisation. / Due to more stringent regulations, wastewater processes need to be more compact and effective. The utilization of aerobic granular sludge conjugates compactness and productivity with the control of the operational. Granulation, which need specific conditions, are mostly operated in batch reactors. To improve the capacity of treatment, this study investigates process conditions for an optimal operation for a continuous reactor working with aerobic granular sludge. First of all, granulation technique is optimized in a laboratory batch reactor (SBR) and results reveal that food to microorganism ratio, shear and selection pressure applied influence pellets’ formation and their properties. Then, this optimized method is successfully scaled-up. After that, the utilization of granules in continuous is studied and this mode increases the reactor capacity while the granular structure is maintained. The utilization of an industrial influent shows reserved results. A commercial software was used to simulate experimental results obtained for a fluidized reactor using pellets. The model, proposed by the software, shows inconsistencies in batch mode. The MBBR model seems more appropriate to simulate continuous mode although the whole pellet is not considered. So, the utilization of aerobic granular sludge in a continuous reactor is a promising technology but further research is needed in the long term operation and its modeling.

O Alquilbenzeno Linear Sulfonado (LAS) é um surfactante aniônico considerado prioridade de risco ambiental entre os contaminantes emergentes atuais. Estudos anteriores reportaram a degradação anaeróbia de LAS por co-digestão da água residuária de lavanderia comercial e co-substratos sintéticos (extrato de levedura e etanol), em reatores em escala de bancada. Todavia, na literatura ainda são limitados os estudos envolvendo co-substratos economicamente viáveis, como o esgoto doméstico. O objetivo deste estudo foi avaliar a eficiência de remoção do LAS, de água residuária de lavanderia comercial em co-digestão com esgoto doméstico. O reator de leito granular expandido (EGSB) escala piloto de 62,0 L foi operado em condição mesofílica, em TDH de 40 h, por 480 dias. O reator foi inoculado com 12,0 L de lodo proveniente de reator UASB usado no tratamento de água residuária de abatedouro de aves. Na primeira etapa, de adaptação, com duração de 60 dias, o reator foi alimentado apenas com esgoto doméstico. Em seguida, o reator foi alimentado com água residuária de lavanderia comercial diluída em esgoto doméstico para obtenção de concentrações de LAS afluente de 5 ± 4; 19 ± 10 e 36 ± 19 mg L-1, nas etapas II, III e IV, respectivamente. Nestas etapas o reator foi monitorado por 60, 270 e 90 dias. Verificou-se diminuição da eficiência de remoção de matéria orgânica de 73 ± 23 % na etapa de adaptação, para 61 ± 25%, 50 ± 15% e 44 ± 15%, respectivamente, para as etapas II, III e IV. Assim como, verificou-se diminuição da eficiência de remoção do LAS de 73 ± 31% para 55 ± 29% e 32 ± 17% nas três últimas etapas. Verificou-se aumento significativo de sulfeto da etapa II para a etapa III e IV, respectivamente de 8 ± 2 mg L-1 para 29 ± 12 mg L-1 e 31 ± 5 mg L-1, respectivamente. Foi realizada a caracterização taxonômica da biomassa do leito do lodo do reator EGSB ao final de cada etapa experimental, sendo identificadas bactérias semelhantes a Bellinea (domínio Bacteria) e Methanosaeta (domínio Archaea), as quais foram as de maior abundância relativa ao longo de toda operação. A tecnologia empregada para remoção do surfactante foi adequada para concentrações afluente de até 20 mgLAS L-1. Aclimatação da biomassa microbiana foi observada, após longo período e exposição aos compostos recalcitrantes da água residuária de lavanderia. / Classified as an emergent contaminant, Alkylbenzene Linear Sulfonate (LAS) is an anionic surfactant of high priority given its environmental risk. Previous studies reported LAS anaerobic degradation from laundry wastewater in co-digestion with synthetic substrates (such as methanol, ethanol and yeast extract). However, studies with more economic viable substrates as domestic sewage still lacking. This study assessed LAS removal from laundry wastewater diluted in domestic sewage, using an Expanded Bed Granular Sludge (EGSB) pilot scale reactor. The reactor was kept in mesophilic temperature, with 62,0 L total volume and it was operated with a hydraulic retention time (HRT) of 40 h. The inoculum was 12,0 L of sludge from an UASB used on a poultry slaughterhouse wastewater treatment plant. On the first stage, of adaptation, the reactor was fed only with domestic sewage for 60 days. Then, commercial laundry wastewater was diluted in domestic sewage to obtain LAS affluent concentrations of 5 ± 4; 19 ± 10 and 36 ± 19 mg L-1, on stages II, III and IV, respectively. These stages lasted for 60, 270 and 90 days. The increase of commercial laundry wastewater proportion on fed resulted in lower organic matter removal efficiencies. These parameter decreased from 73 ± 23% on adaptation, to 61 ± 25%, 50 ± 15% and 39 ± 23% on following stages. As well as LAS removal efficiencies that dropped from 73 ± 31% to 55 ± 29% and 44 ± 15 % on three last stages. Sulphide production enhanced from stage II (8 ± 2 mg L-1) to stage III (29 ± 12 mg L-1) and remained 31 ± 5 mg L-1 on stage IV. Taxonomic characterization of granular sludge biomass in the end of each stage was performed and genders similar to Bellinea (Bacteria domain) and Methanosaeta (Archae domain) were the ones with higher relative abundance in all stages. The technology applied was suitable for anaerobic surfactant removal with LAS affluent concentration of 20 mg L-1. Acclimation of microbial biomass was observed after long exposure of microbial community to recalcitrant compounds from laundry wastewater.

O Alquilbenzeno Linear Sulfonado (LAS) é um surfactante aniônico considerado prioridade de risco ambiental entre os contaminantes emergentes atuais. Estudos anteriores reportaram a degradação anaeróbia de LAS por co-digestão da água residuária de lavanderia comercial e co-substratos sintéticos (extrato de levedura e etanol), em reatores em escala de bancada. Todavia, na literatura ainda são limitados os estudos envolvendo co-substratos economicamente viáveis, como o esgoto doméstico. O objetivo deste estudo foi avaliar a eficiência de remoção do LAS, de água residuária de lavanderia comercial em co-digestão com esgoto doméstico. O reator de leito granular expandido (EGSB) escala piloto de 62,0 L foi operado em condição mesofílica, em TDH de 40 h, por 480 dias. O reator foi inoculado com 12,0 L de lodo proveniente de reator UASB usado no tratamento de água residuária de abatedouro de aves. Na primeira etapa, de adaptação, com duração de 60 dias, o reator foi alimentado apenas com esgoto doméstico. Em seguida, o reator foi alimentado com água residuária de lavanderia comercial diluída em esgoto doméstico para obtenção de concentrações de LAS afluente de 5 ± 4; 19 ± 10 e 36 ± 19 mg L-1, nas etapas II, III e IV, respectivamente. Nestas etapas o reator foi monitorado por 60, 270 e 90 dias. Verificou-se diminuição da eficiência de remoção de matéria orgânica de 73 ± 23 % na etapa de adaptação, para 61 ± 25%, 50 ± 15% e 44 ± 15%, respectivamente, para as etapas II, III e IV. Assim como, verificou-se diminuição da eficiência de remoção do LAS de 73 ± 31% para 55 ± 29% e 32 ± 17% nas três últimas etapas. Verificou-se aumento significativo de sulfeto da etapa II para a etapa III e IV, respectivamente de 8 ± 2 mg L-1 para 29 ± 12 mg L-1 e 31 ± 5 mg L-1, respectivamente. Foi realizada a caracterização taxonômica da biomassa do leito do lodo do reator EGSB ao final de cada etapa experimental, sendo identificadas bactérias semelhantes a Bellinea (domínio Bacteria) e Methanosaeta (domínio Archaea), as quais foram as de maior abundância relativa ao longo de toda operação. A tecnologia empregada para remoção do surfactante foi adequada para concentrações afluente de até 20 mgLAS L-1. Aclimatação da biomassa microbiana foi observada, após longo período e exposição aos compostos recalcitrantes da água residuária de lavanderia. / Classified as an emergent contaminant, Alkylbenzene Linear Sulfonate (LAS) is an anionic surfactant of high priority given its environmental risk. Previous studies reported LAS anaerobic degradation from laundry wastewater in co-digestion with synthetic substrates (such as methanol, ethanol and yeast extract). However, studies with more economic viable substrates as domestic sewage still lacking. This study assessed LAS removal from laundry wastewater diluted in domestic sewage, using an Expanded Bed Granular Sludge (EGSB) pilot scale reactor. The reactor was kept in mesophilic temperature, with 62,0 L total volume and it was operated with a hydraulic retention time (HRT) of 40 h. The inoculum was 12,0 L of sludge from an UASB used on a poultry slaughterhouse wastewater treatment plant. On the first stage, of adaptation, the reactor was fed only with domestic sewage for 60 days. Then, commercial laundry wastewater was diluted in domestic sewage to obtain LAS affluent concentrations of 5 ± 4; 19 ± 10 and 36 ± 19 mg L-1, on stages II, III and IV, respectively. These stages lasted for 60, 270 and 90 days. The increase of commercial laundry wastewater proportion on fed resulted in lower organic matter removal efficiencies. These parameter decreased from 73 ± 23% on adaptation, to 61 ± 25%, 50 ± 15% and 39 ± 23% on following stages. As well as LAS removal efficiencies that dropped from 73 ± 31% to 55 ± 29% and 44 ± 15 % on three last stages. Sulphide production enhanced from stage II (8 ± 2 mg L-1) to stage III (29 ± 12 mg L-1) and remained 31 ± 5 mg L-1 on stage IV. Taxonomic characterization of granular sludge biomass in the end of each stage was performed and genders similar to Bellinea (Bacteria domain) and Methanosaeta (Archae domain) were the ones with higher relative abundance in all stages. The technology applied was suitable for anaerobic surfactant removal with LAS affluent concentration of 20 mg L-1. Acclimation of microbial biomass was observed after long exposure of microbial community to recalcitrant compounds from laundry wastewater.

Les propriétés hydrophobes des polymères extracellulaires (PEC) exercent l’influence profonde sur les propriétés de la surface cellulaire. Cependant, de nombreux facteurs tels que les méthodes d'extractions, le type de substrat influencent les caractéristiques des PEC et les informations concernant des caractéristiques hydrophobes sont rarement documentées. L'objectif principal de cette étude est de développer une méthode appropriée pour étudier l'hydrophobicité des PEC, puis d'étudier les caractéristiques hydrophobes des PEC.Le fractionnement hydrphobe par la résine Supelite™ DAX-8 a d'abord été appliqué sur les PEC extraits de boues granulaires anaérobies, deux conditions de pH d'élution (pH 2 et 5) ont été testées. L'impact de sept méthodes d'extraction sur les caractéristiques hydrophobes des PEC a été évalué. Les résultats ont montré que les méthodes d'extraction et le pH de la solution extraitante ont influencé la composition des PEC et leur hydrophobicité. En outre, les extraitants des PEC, par exempe le formaldéhyde, l'éthanol, le dodécylsulfate de sodium (SDS) et Tween 20, ont non seulement introduit une teneur supplémentaire en carbone pendant la mesure du carbone organique total (COT), mais ils ont également interagit avec la résine DAX-8. En comparant la répartition du poids moléculaire apparent (aMW) des échantillons des PEC non traités et ajustés au pH détectés par chromatographie d'exclusion stérique (en anglais SEC), l’information plus complète d’aMW a été préservée à pH 5. Ainsi, le fractionnement hydrophobe par la résine DAX-8 à pH 5 et les méthodes physiques d'extraction PEC ont été préférés dans cette étude.Une analyse qualitative détaillée des caractéristiques hydrophobes des EPS a été étudiée par la technique de la matrice de fluorescence d’excitation-emission (EEM). Les résultats ont montré que les substances de type humique (HS-like) représentaient la majorité des composés organiques des PEC extraits de la boue granulaire anaérobie, et constituaient également le principal support moléculaire de l'hydrophobicité des extraits. Ces composés hydrophobes de type HS étaient essenciellement des molécules petites tailles de 8 kDa à <1 kDa. L’hydrophobité contributée par les protéines (PN) et les polysaccharides (PS) présentait un moindre rapport.Afin d’explorer les propriétés hydrophobes de PN et de PS, ainsi évaluer l'impact de l'addition de Ni(II) sur l'hydrophobicité des extraits des champignons, fongi Phanerochaete chrysosporium a été choisi. Les résultats ont montré que la teneur de PN et de PS dans les PEC extrait de ce type de fongi variait en fonction de la concentration de Ni(II). Avec une augmentation de la concentration de Ni de 0 mg/L à 25 mg/L, la teneur en PN a diminué alors que celle de PS a été augmentée. L'hydrophobicité des PEC du fongi, déterminée par le traitement de la résine DAX-8, a diminué lors que la concentration de Ni augmentait. Par ailleurs, l'intensité du pic de SEC correspondant aux molécules PN-like (Ex/Em = 225/345 nm) de 1,9 × 103 à 10 kDa a été augmentée par l'addition Ni; en même temps, la distribution d’aMW des composés organiques totaux (UV/210) dans les PEC restait presque stable. Ces résultats ont indiqué que les composés de type PN-like peuvent avoir déterminé l'hydrophobicité des PEC fongique dans des conditions de stress.Dans l’extrait plus hétérogène des PEC de boues granulaires anaérobies, des composés HS-like représentaient le composant organique majeur, ainsi le principal support moléculaire de l'hydrophobicité des PEC. En étudiant les caractéristiques hydrophobes des PEC extrait du champignon Phanerochaete chrysosporium, le PN et le PS des PEC jouaient un rôle actif dans la protection du champignon sous le Ni. La concentration élevée de Ni a diminué l'hydrophobicité des PEC fongique, mais elle a augmenté l'hydrophobicité de la surface cellulaire du champignon. Il semble que la présence de Ni favorise l'apparition d'un champignon plus hydrophobe / The hydrophobic properties of extracellular polymeric substances (EPS) exert a profound influence on the cell surface properties. However, many factors such as EPS extractions methods, substrate type influence EPS characteristics, and limited information regarding to the hydrophobic features of EPS can be found. The main aim of this study is to develop a proper method to study EPS hydrophobicity, and then investigate the hydrophobic features of EPS.The hydrophobic fractionation by Supelite™ DAX-8 resin was first applied on the EPS extracted from anaerobic granular sludge, two elution pH conditions i.e. pH 2 and 5 were tested. The impact of seven EPS extraction methods on the hydrophobic features of EPS was assessed. The results showed that the extraction methods and bulk solution pH dramatically influenced the EPS composition and their hydrophobicity. Besides, the EPS extracting reagents namely formaldehyde, ethanol, sodium dodecyl sulfate (SDS) and Tween 20 not only introduced extra carbon content during total organic carbon (TOC) measurement, but also interacted with the DAX-8 resin. By comparing the apparent molecular weight (aMW) distribution of the untreated and pH-adjusted EPS samples detected by size exclusion chromatography, more complete EPS aMW information was preserved at pH 5. Thus, the hydrophobic fractionation by DAX-8 resin at pH 5 and physical EPS extraction methods were preferred in this study.After identifying the proper conditions for DAX-8 resin fractionation, detailed qualitative analysis of the EPS hydrophobic features was further investigated. The results showed that the humic-like substances (HS-like) were the major organic constituent of the EPS extracted from the anaerobic granular sludge, and they were also the main molecular support of the EPS hydrophobicity. Those hydrophobic HS-like compounds were mainly small molecules ranging from 8 kDa to <1 kDa. Proteins (PN) and polysaccharides (PS) contributed to the EPS hydrophobicity to a lesser extent.The role of PN and PS in the EPS hydrophobicity was difficult to be shown. It is known that the major organic constituents of the EPS extracted from bacteria, algae and fungi are PN and PS. Therefore, to explore the hydrophobic features of PN and PS, as well as to investigate the impact of Ni(II) addition, on the EPS hydrophobicity, the fungus Phanerochaete chrysosporium was chosen. The results showed that the contents of PN and PS in the extracted fungal EPS varied with the Ni(II) concentration. With an increase in the Ni concentration from 0 mg/L to 25 mg/L, the PN content was decreased whereas the PS content was increased. The fungal EPS hydrophobicity, determined by the DAX-8 resin treatment, was decreased as the Ni concentration increased.Besides, the peak intensity on the size exclusion chromatography (SEC) corresponding to the PN-like molecules (Ex/Em = 225/345 nm) ranging from 1.9×103 to 10 kDa were intensified by the Ni addition, while the aMW distribution of the total organics (UV/210) in the EPS remained almost stable. These results indicated that those PN-like compounds may determine the hydrophobicity of fungal EPS under stress conditions.For the more heterogeneous EPS extracted from anaerobic granular sludge, HS-like compounds were identified as the major organic component, as well as the main molecular support of the EPS hydrophobicity. By studying the hydrophobic features of the EPS extracted from the fungus Phanerochaete chrysosporium, it showed that the PN and PS in the EPS played an active role in protecting the fungus under Ni stress. The increased Ni concentration decreased the hydrophobicity of fungal EPS, but it increased the cell surface hydrophobicity of the fungus. It seems that the presence of Ni promoted the fungus becoming more hydrophobic

L'épandage des boues d'épuration est un mode de valorisation à la fois écologique et économique pour autant que l'on maitrise leur qualité et notamment la concentration des métaux lourds mobilisables. Le cuivre est une molécule très répandue, naturelle dans l'environnement, largement utilisée dans l'industrie et l'agriculture. En conséquence, les quantités de cuivre dans l'environnement ont augmenté, de sorte que ce dernier a été choisi dans cette étude comme représentant de la pollution anthropique pour évaluer sa mobilité en fonction de la qualité des boues épandues et des sols. 9 boues classiques et 2 sols (Sol d’herbe (de France) et sol de riz (du Vietnam)) ont été étudiés ainsi que des boues granulaires. Une méthodologie est proposée pour évaluer l'effet de la boue et de l'origine du sol sur la capacité de lessivage du cuivre lors de l'épandage des boues pour les activités agricoles. Les essais de désorption dans les colonnes de sol amendé par des boues ont montré que: a) quelle que soit l'origine du sol amendé, les boues de lit de roseaux (LR), séchées (BCD), centrifugées (BC) ont présenté une libération de Cu inférieure à 2% tandis que les boues de filtre-presse (BFP), digérées (BD), épaissies (BE) et calcaires (BCh) ont amélioré la disponibilité de Cu dans le sol; b) La lixiviation du cuivre dans le sol d’herbe (du France) amendé par des boues granulaires était supérieure à celle mesurée pour les échantillons classiquesde boues; c) Dans le sol de riz (de Vietnam), l'épandage des boues granulaires a limité la désorption de cuivre par rapport aux échantillons de boue (BCh), de filtre-presse (BFP), digérée (BD) ou centrifugée (BC). Quatre mécanismes sont proposés pour expliquer le devenir du Cu dans les sols: 1) le contrôle; 2) le groupe de Cp1, Cp2, BC, LR and BCD; 3) le groupe de BCh, BD, BE, BFP et 4) le groupe de boue granulaire. Il est constaté que pour le sol de riz contenant une faible teneur en matière organique, l'application de boues granulaires ou d'autres types de boue tels que les boues compostées ou séchées peut non seulement augmenter la teneur en éléments nutritifs, mais aussi réduire la capacité de lixiviation du cuivre. / The spreading of sewage sludge is both ecological and economical in sofar as their quality is controlled and in particular the low level of the heavy metals available. Copper is a very common substance, naturally occurring in the environment, widely used in industry and agriculture. As a result, quantities of copper in the environment have increased, so it has been selected in this study as representing human-induced pollution to assess its mobility in relation to the quality of sludge and soil. 9 different sludges and 2 soils (grass soil from France and paddy soil from Vietnam) were studied as well as granular sludge. A methodology was developed to evaluate the effect of sludge and soil origin on copper leaching ability during sludge application for agricultural activities. Desorption tests in soil-amended sludge columns showed that: a) Whateverthe origin of soil, the centri-dried (BCD), centrifuged (BC), reed-bed (LR) sludges presented a Cu release lower than 2% while filter-pressed (BFP), digested (BD), thickened (BE) and limed (BCh) sludge amended soils increased Cu availability in soil; b) the copper leaching of granular sludge amended grass soil was higher than those measured for conventional sludge samples; c) in paddy soil, landspreading of granular sludge limited the Cu desorption compared to limed (BCh), filter-press (BFP), digested (BD) and centrifuged (BC) sludge samples. Four mechanisms groups are proposed to explain the fate of Cu in soils: 1) the control; 2) the group of Cp1, Cp2, BC, LR and BCD; 3) the group of BCh BD BE and BFP, and 4) the group of granular sludge. It is found that paddy soil containing low organic matter, application of granular sludge orother types such as composted or dried sludge can not only increase the nutrient content but also reduce the leaching capacity of copper.