L’expérience I.C.E a pour objectif de tester le principe d’équivalence faible (WEP) à la base de la théorie de la relativité générale d’Einstein et postulant l’équivalence entre masse inertielle et masse grave. Si ce principe a toujours été vérifié jusqu’à aujourd’hui, il est d’un intérêt fondamental pour la physique moderne de poursuivre les mesures avec une précision accrue. En effet, de nouvelles théories d’unification de la mécanique quantique et de la relativité générale prévoient une violation de ce principe. Pour réaliser un test du WEP, il suffit de comparer les accélérations de deux objets en chute libre dans un même champ de gravitation, et c’est ce que réalise l’expérience I.C.E à l’échelle quantique (à la différence de la mission spatiale Microscope qui à ce jour a pu vérifier le WEP avec des objets macroscopiques avec une sensibilité sur le paramètre de 2.10−14). Ainsi, l’expérience consiste à réaliser, par une méthode interférométrique, la mesure de l’accélération de deux espèces atomiques (87Rb et 39K) de masses et de compositions différentes, en chute libre dans une enceinte à vide. La sensibilité de la mesure des effets inertiels auxquels les atomes sont sensibles (accélérations et rotations) est d’autant plus grande que la durée de chute libre des atomes est élevée et que la température des nuages est faible. Or, sur Terre au laboratoire, les atomes finissent par tomber au fond de l’enceinte les contenant sous l’effet de la gravité, ce qui limite grandement la sensibilité de la mesure. C’est pourquoi il est intéressant de placer l’expérience dans un environnement de micropesanteur dans lequel les atomes restent au centre de la chambre à vide afin d’atteindre des temps d’interrogation beaucoup plus longs. A ce titre, l’expérience est embarquée jusqu’à plusieurs fois par an, à bord de l’avion Zéro-g de la société Novespace. Les durées de micropesanteur proposées permettent d’atteindre des temps d’interrogation théoriques de l’ordre de la seconde ce qui doit porter le niveau de sensibilité à 10−11. Cependant, nous sommes aujourd’hui très fortement limités par le niveau élevé de vibrations et de rotations de l’avion : la perte de contraste des franges d’interférence engendrée ainsi que le bruit de phase introduit, ne nous permettent pas de dépasser des temps d’interrogation de 5 ms en 0 g. En parallèle, le laboratoire s’est récemment doté d’un simulateur de microgravité sur lequel est montée l’expérience, donnant accès à des temps d’interrogation de plus de 200 ms avec des trajectoires paraboliques d’une très bonne répétabilité (de l’ordre de 3 mg). La cohérence d’une source atomique étant directement reliée à sa température, l’utilisation de nuages ultra-froids est d’un grand intérêt pour améliorer le contraste des franges d’interférence, d’autant plus pour les longs temps d’interrogation visés. Le présent manuscrit synthétise les travaux ayant permis de produire le tout premier condensat de Bose-Einstein (la source atomique ultime) de 87Rb en microgravité par une méthode tout optique, et ce, de manière répétable toutes les 13,5 secondes. Nous démontrons l’efficacité de note méthode de chargement du piège dipolaire basée sur l’association d’un refroidissement par mélasse grise et d’une modulation spatiale des faisceaux dipolaires. Ces résultats ouvrent la voie vers de futures mesures interférométriques très sensibles à grand facteur d’échelle. / The I.C.E experiment aims at testing the weak equivalence principle (WEP) underlying Einstein’s theory of general relativity and which postulates the equivalence between inertial mass and gravitationnal mass. If this principle has always been verified until today, it is of fundamental interest for physics to continue the measurements with greater precision. Indeed, new unifying theories of quantum mechanics and general relativity predict a violation of this principle. To carry out a test of the WEP, it suffices to compare the accelerations of two objects in free fall in the same gravitationnal field. This is what the I.C.E experiment, on the quantum scale, achieves (unlike the spatial Microscope mission, which to date has been able to verify the principle of equivalence with macroscopic objects with a sensitivity on of 2.10−14). Thus, the experiment consists in performing, by an interferometric method, the measurement of the acceleration of two atomic species (87Rb and 39K) of different mass and composition in free fall in a vacuum chamber. The measurement sensitivity of the inertial effects to which the atoms are sensitive (accelerations and rotations) is all the greater as the free fall time of the atoms is high and their temperature is low. But on Earth, in the laboratory, the atoms eventually fall to the bottom of the vacuum chamber containing them under the effect of gravity, which greatly limits the measurement sensitivity achievable. This is why it is interesting to place the experiment in a microgravity environment in which the atoms stay in the center of the vacuum chamber in order to reach much longer interrogation times. As such, several times a year, the experiment is put aboard the aircraft Zero-g of the Novespace company. The available microgravity durations make it possible to reach theoretical interrogation times of the order of one second, which should raise the sensitivity level to 10−11. However, we are today very strongly limited by the high level of vibrations of the aircraft as well as its rotations : the loss of contrast of the interference fringes and the phase noise caused, do not allow us to exceed 5 ms of interrogation times in 0 g. Since the coherence of an atomic source is directly related to its temperature, the use of ultra-cold clouds is of great interest to improve the contrast of the interference fringes, especially for the long interrogation times targeted. In parallel, the laboratory is now equipped with a microgravity simulator on which is mounted the experiment, giving access to interrogation times of more than 250 ms with parabolic trajectories of a very good repeatability (of the order of 3 mg). This manuscript synthesizes the work that produced the very first 87Rb Bose-Einstein condensate in microgravity by all-optical methods, with a repetition rate of 13,5 seconds. We demonstrate the efficiency of our dipole trap loading method based on the association of a grey molasses cooling and a spatial modulation of the dipole beams. These results pave the way for future highly sensitive interferometric measurements with a large scale factor.

A digestão anaeróbia tem se apresentado como um processo de grande interesse sob a ótica da potencial produção de energia renovável (H2 e CH4), considerando-se a ampla variedade de compostos orgânicos que podem ser utilizados. Neste estudo desejou-se avançar na compreensão do sistema de reatores anaeróbios de duas fases (acidogênico seguido de metanogênico) operados em condições termofílicas (55°C), alimentados com melaço da cana-de-açúcar, subproduto da indústria sucroalcooleira. Os experimentos foram conduzidos em reatores anaeróbios de leito fixo estruturado com fluxo ascendente e o melaço foi diluído com água de abastecimento, para adequação da concentração aos processos de tratamento de águas residuárias. Na 1ª Etapa dois reatores acidogênicos foram operados em paralelo para avaliar diferentes formas de inoculação e meios suportes, a fim de manter a produção continua e estável de hidrogênio. Para isso foram aplicadas diferentes cargas orgânicas (2,5, 5 e 10 gDQO.L-1) que resultam em COV de 30, 60 e 120 g.DQO.Lreator1.dia-1, com TDH fixo de 2 horas. A expressão do gene hidrogenase foi detectado em ambos os reatores, mas em maior proporção no reator inoculado com lodo de reator UASB e usando como material suporte a espuma de poliuretano. Sequencialmente a este reator, foi acoplado um reator metanogênico, alimentado com efluente do reator acidogênico, estabilizado nas condições apresentadas, e operado com COV crescentes de 1, 2, 5, 7, 14, 17 e 26,5 gDQO.Lreator-1.dia-1 e consequente diminuição do TDH de 240, 96, 48, 32, 24, 16 e 12 horas. O reator acidogênico na 2ª etapa foi operado por 417 dias consecutivos e COV de 120 g.DQO.Lreator1.dia-1, produzindo hidrogênio continuamente, alcançado valores de produção bruta de H2 de 7,60 LH2.dia-1. O reator metanogênico foi operado por 251 dias consecutivos, produzindo metano e alcançado valores de produção bruta de CH4 de 5,90 LCH4.dia-1. A eficiência de remoção de DQO do sistema de reatores foi de aproximadamente 90%, com contribuição aproximadamente de 10% para o reator acidogênico e contribuição aproximadamente de 80% para o reator metanogênico. O reator acidogênico alcançou rendimento de produção de hidrogênio por kg de melaço aplicado de 392 LH2.kgmelaço-1 e o reator metanogênico de 387 LCH4.kgmelaço-1. Para finalidade de comparações e aplicabilidade, o ganho energético global do sistema de reatores de duas fases foi de aproximadamente 5,7 kWh.kgmelaço-1 (1,4 kWh.kgmelaço-1 para o reator acidogênico e 4,3 kWh.kgmelaço-1 para o reator metanogênico). A produção continua de H2 obtida neste estudo está relacionada à associação das vias dos ácidos produtores de hidrogênio já consolidados pela literatura pertinente (acético e butírico) e pela produção de hidrogênio pela rota do ácido lático, devido a associação entre as comunidades de microrganismos estabelecidas no reator. O sequenciamento massivo MiSeq mostrou a seleção de diversos gêneros de microrganismos com redundância funcional e pertencentes principalmente aos Filos Firmicutes, Proteobacteria e Thermotogae, tais como Clostridium sensu stricto, Thermohydrogenium, Thermoanaerobacterium e Cellulosibacter (Firmicutes); Pseudomonas, Enterobacter, Shewanella e Petrobacter (Proteobacteria) e Fervidobacterium (Thermotogae). Microrganismos produtores de ácido lático também foram selecionados tais como: Lactobacillus, Leuconostoc, Sporolactobacillus e Trichococcus. Dos pontos de vista científico e tecnológico este estudo deu mais um passo para a compreensão dos bioprocessos envolvidos nos sistemas anaeróbios em dois estágios produzindo H2 e CH4 continuamente por longo período de tempo. / Anaerobic digestion has shown as an interesting process for renewable energy production (H2 and CH4), for a wide variety of organic compounds (carbon source). This study aimed to advance the understanding of a two-stage process anaerobic system (acidogenic bioreactor followed by methanogenic bioreactor) under thermophilic condition (55°C) fed with molasses, a sugarcane industry by-product. The experiments were conducted at up-flow structured bed reactors and sugarcane molasses was diluted with tap water, to adjust the concentration to the wastewater treatment. At first stage two acidogenic reactors were operated in parallel to evaluate different source of inocula and support bed, to obtain continuous and stable hydrogen production. It was applied 2.5, 5 and 10 gCOD.L-1 resulting in OLR of 30, 60 and 120 g.COD.Lreactor-1.day-1, with HRT fixed at 2 hours of hydrogenase gene was detected in both reactors but with higher number of copies of the gene in the reactor that showed higher hydrogen production: the reactor sed with sludge of UASB reactor and using polyurethane foam as support material. To this reactor was coupled a methanogenic reactor fed with effluent from acidogenic reactor and operated with increasing OLR (1, 2, 5, 7, 14, 17 e 26,5 gCOD.Lreactor-1.day-1) decreasing the HRT (240, 96, 48, 32, 24, 16 and 12 hours). The acidogenic reactor was operated during 471 days with OLR of 120 g.COD.Lreactor-1.day-1, with HRT fixed at 2 hours, with continuous hydrogen production with a gross production of 7.60 LH2.day-1. The methanogenic reactor was operated for 251 days, with continuous methane production of up to 5.90LCH4.day-1. The COD removal efficiency using the two-stage system was approximately 90% , with 10% contribution by the acidogenic reactor and 80% contribution by the methanogenic reactor. The acidogenic reactor achieved hydrogen yield per kg of applied molasses equal to 392 LH2.kgmolases-1. The methanogenic reactor achieved methane yield per kg of applied molasses equal to 387 LCH4.kgmolasses-1. For comparison and applicability purposes, the overall energy yield using the two stage reactor system was approximately 5.7 kWh.kgmolasses-1 (Acidogenic reactor 1.4 kWh.kgmolasses-1 and Methanogenic reactor 4.3 kWh.kgmolasses-1). The continuous production of H2 obtained in this study is related to the association of the hydrogen producer acids pathway established by the relevant literature (acetic and butyric) and the hydrogen production by the lactic acid pathway due to the microorganisms association established in the reactor. Metagenomic analysis by MiSeq Plataform revealed that hydrogen production was due the selection of microorganisms with functional redundancy mainly of Phyla Firmicutes, Proteobacteria and Thermotogae, such as Clostridium sensu stricto, Thermohydrogenium, Thermoanaerobacterium, Cellulosibacter (Firmicutes); Pseudomonas, Enterobacter, Shewanella and Petrobacter (Proteobacteria) and Fervidobacterium (Thermotogae). Genera of acid latic producers, such as Lactobacillus, Leuconostoc, Sporolactobacillus and Trichococcus, were also selected. From the scientific and technological point of view this study has taken another step towards the understanding of bioprocesses involving two stage anaerobic systems for a long term continuous production of H2 and CH4.

O Brasil é o maior produtor de cana-de-açúcar, e entre os principais subprodutos dessa indústria está o melaço de cana-de-açúcar. Esse substrato é rico em carboidratos, apresentando potencial para ser utilizado na digestão anaeróbia para geração de biogás. Neste estudo, priorizou-se a produção de biogás em condições termofílicas (55°C) com a finalidade de comparação do sistema de duas fases (reator acidogênico seguido de reator metanogênico) e sistema de fase única (acidogênico e metanogênico em uma mesma unidade), utilizando o melaço como substrato. O sistema de duas fases baseou-se na separação da acidogênese e metanogênese. O reator acidogênico (ASTBR – A) foi operado com carga orgânica volumétrica (COV) de 60,0 g L-1d-1 e tempo de detenção hidráulico (TDH) de 4 horas. O reator metanogênico, sequencial ao acidogênico (ASTBR – M II) foi operado em dez fases, com COV variando de 0,6 a 10,0 g L-1d-1 e TDH de 40 e 24 horas. O sistema de fase única foi composto por um reator metanogênico (ASTBR – M I) operado em nove fases com COV entre 2,5 e 10,0 g L-1d-1 e TDH de 28 h. Bicarbonato de sódio (NaHCO3) foi adicionado na proporção de 1,00 g NaHCO3 g-1DQO para todas as fases do ASTBR M II. Para o ASTBR – M I, variou-se a concentração de 1,00 a 0,00 g NaHCO3 g-1 DQO no reator. Para o ASTBR A a porcentagem de hidrogênio (H2) no biogás foi de 51%, a produção volumétrica de hidrogênio (PVH) de 88,0 mL H2 L-1 h-1 e o rendimento de hidrogênio (HY) de 1,18 mol H2 molcarboidratos-1. O microrganismo predominante nesse reator foi o Thermoanaerobacterium, e a principal rota a do ácido lático. O reator ASTBR – M I sofreu acidificação após a retirada completa de alcalinizante, permitindo a detecção de H2 no biogás. Porém, a retomada da adição de NaHCO3 favoreceu o crescimento das arqueias, principalmente metanogênicas hidrogenotróficas. A comparação dos reatores metanogênicos foi realizada para fases com condições semelhantes (COV de 10 g L-1d-1 e 1,00 g NaHCO3 g-1DQO) e permitiu verificar melhor desempenho na produção de CH4 do ASTBR – M II. Em relação ao MY, a eficiência do ASTBR – M II foi 44% superior ao ASTBR M – I. / Brazil is the largest producer of sugarcane and one of the main sub-products of this industry is the molasses, which is rich in carbohydrates and can be used as a substrate for biogas production in anaerobic digestion. In this study, biogas production was evaluated under thermophilic conditions (55 °C) in a two-phases system (acidogenic reactor followed by methanogenic reactor) based on phase separation and a single-phase system (acidogenic and methanogenic microorganisms in a single unit) using molasses as the substrate. The acidogenic reactor (ASTBR-A) was operated under the organic loading rate (OLR) of 60.0 g L-1d-1 and hydraulic retention time (HRT) of 4 hours. The methanogenic reactor (ASTBR M II), which was sequential to acidogenic one, was operated in ten phases with OLR ranging from 0.6 to 10.0 g L-1d-1 and HRT of 40 and 24 hours. The single-phase reactor was composed of a methanogenic reactor (ASTBR -– M I) operated in nine phases with increasing OLR from 2.5 to 10.0 g L-1d-1 and HRT of 28 hours. Sodium bicarbonate (NaHCO3) was added in the ratio of 1.00 g NaHCO3 g-1COD in all phases of ASTBR – M II. For the ASTBR – M I, the concentration varied between 1.00 to 0.00 g NaHCO3 g-1COD. In the ASTBR – A, the percentage of hydrogen (H2) in the biogas was 51%, the volumetric hydrogen production (VHP) was 88.0 mL H2 L-1 h-1 and the hydrogen yield (HY) was 1.18 mol H2 molar-1carbohydrate. The predominant microorganism in this reactor was the Thermoanaerobacterium and the main metabolite route was the lactic acid. The ASTBR – M I suffered acidification after the complete removal of the alkalinizer allowing the detection of hydrogen in the biogas. However, the use of the alkalinizer after its complete removal from the system favored the growth of Archaeas, mainly the hydrogenotrophic methanogens. The comparison of the methanogenic reactors was carried out for phases with similar conditions (OLR of 10 g L-1d-1 and 1.00 g NaHCO3 g-1COD) and allowed to verify a better performance in the methane (CH4) production in the ASTBR – M II. Regarding the methane yield (MY), the efficiency of ASTBR – M II was 44% higher than ASTBR M – I.

Ce travail de thèse rapporte la production tout optique de condensats de Bose-Einstein de 39K. Une étape clé du processus expérimental est l’obtention d’un nuage suffisamment froid permettant le chargement direct d’un piège dipolaire de manière efficace. Notre solution est l’utilisation d’une mélasse fonctionnant dans le bleu de la raie D1 de cet alcalin conduisant à une densité dans l’espace des phases élevée et ainsi au chargement direct d’un grand nombre d’atomes dans un piège à 1550 nm. Le nuage est ensuite polarisé puis comprimé dans un piège dipolaire croisé avant d’entamer un refroidissement évaporatif efficace au voisinage d’une résonance de Feshbach. Ce processus permet la production rapide de condensats de Bose-Einstein toutes les 7 secondes sur notre expérience. Ces nuages dégénérés représentent le point de départ pour la conduite d’expériences visant à étudier les effets du désordre dans les gaz quantiques en dimensions réduites. Nous envisageons l’étude du diagramme de phase du gaz de Bose bidimensionnel désordonné, de la localisation d’Anderson en dimension deux ainsi que l’étude de l’influence du désordre sur un soliton brillant dans une géométrie unidimensionnelle. / This thesis presents the all optical production of 39K Bose-Einstein condensates. A key point in the process is the sub-Doppler cooling that allows for an efficient loading of an optical dipole trap. To this aim we use a gray molasses scheme working on the blue side of the D1 line of this alkali that leads to a high phase space density and a high number of trapped atoms in a 1550 nm optical trap. The cloud is then polarized and compressed in a crossed dipole trap before starting an efficient forced evaporation close to a Feshbach resonance. This process allows us to produce Bose-Einstein condensates every 7 seconds with our experiment. Those degenerate clouds represent the starting point of experiments aiming to study the influence of disorder on quantum gases in low dimensions. We discuss the perspectives to study of the phase diagram of the two-dimensional disordered Bose gas as well as the Anderson localization phenomenon in two dimensions and the behaviour of bright solitons in a disordered potential in a one-dimensional geometry.

Le potassium 39 est l'un des alcalins pour lesquels il est possible de contrôler les interactions entre atomes grâce à l'utilisation de résonances de Feshbach. Cette thèse présente un protocole rapide et performant de production de condensats de Bose-Einstein tout optiques de 39K. Notre technique s'appuie sur l'utilisation de mélasses grises permettant de refroidir suffisamment le nuage atomique pour charger directement un piège optique, ainsi que sur une phase d'évaporation optique réalisée au voisinage d'une résonance de Feshbach afin de contrôler le taux de collisions entre atomes. Des études dans divers mélanges de spins nous ont permis d'observer de nouvelles résonances de Feshbach en onde p ainsi qu'une résonance en onde d. Cette dernière, présentant des caractéristiques peu usuelles, a été étudiée plus en détails afin de comprendre les processus de collisions en jeu. Le modèle développé, faisant intervenir deux étapes de collision à deux corps, permet d'expliquer les résultats expérimentaux obtenus. Dans les gaz de Bose dégénérés de 39K produits, le contrôle des interactions au voisinage de la résonance de Feshbach à 560,7 Gauss pour les atomes de 39K dans l'état |F=1,mF=-1> nous a permis d'adresser différents problèmes physiques. Dans le cas d'interactions répulsives, nous étudions l'expansion d'un condensat de Bose-Einstein dans le crossover dimensionel 1D-3D tandis que pour des interactions attractives, nous formons des solitons brillants dans un piège optique unidimensionnel. Les perspectives d'étude de ces gaz de Bose dégénérés auto-confinés dans des milieux désordonnés sont également discutées. / Potassium 39 is an alkali allowing to control the interactions between atoms thanks to Feshbach resonances. This thesis presents a fast and efficient way to produce all-optical Bose-Einstein condensates of 39K. Our technique is first taking advantage of gray molasses cooling leading to a cold enough sample to directly load an optical trap. Then an optical evaporation is performed near a Feshbach resonance to control the collision rate. Studies in various spin mixtures have allowed us to observe new p-wave Feshbach resonances and a d-wave Feshbach resonance. The later presents unusual properties and has been studied in details to understand the collision processes involved. The model developped is a two stage model, each one of them involving a two body collision. It explains the experimental results obtained. In the produced 39K degenerate Bose gases, tuning interactions near the Feshbach resonance at 560,7 Gauss for the atoms in |F=1,mF=-1> has allowed us to adress different physical problems. For repulsive interactions, we study the expansion of a Bose-Einstein condensate in the 1D-3D dimensional crossover. For attractive interactions we produce bright solitons in a one-dimensional optical trap. Perspectives concerning the study of those degenerate self-confined Bose gases in disordered media are also discussed.

O Brasil é o maior produtor de cana-de-açúcar, e entre os principais subprodutos dessa indústria está o melaço de cana-de-açúcar. Esse substrato é rico em carboidratos, apresentando potencial para ser utilizado na digestão anaeróbia para geração de biogás. Neste estudo, priorizou-se a produção de biogás em condições termofílicas (55°C) com a finalidade de comparação do sistema de duas fases (reator acidogênico seguido de reator metanogênico) e sistema de fase única (acidogênico e metanogênico em uma mesma unidade), utilizando o melaço como substrato. O sistema de duas fases baseou-se na separação da acidogênese e metanogênese. O reator acidogênico (ASTBR – A) foi operado com carga orgânica volumétrica (COV) de 60,0 g L-1d-1 e tempo de detenção hidráulico (TDH) de 4 horas. O reator metanogênico, sequencial ao acidogênico (ASTBR – M II) foi operado em dez fases, com COV variando de 0,6 a 10,0 g L-1d-1 e TDH de 40 e 24 horas. O sistema de fase única foi composto por um reator metanogênico (ASTBR – M I) operado em nove fases com COV entre 2,5 e 10,0 g L-1d-1 e TDH de 28 h. Bicarbonato de sódio (NaHCO3) foi adicionado na proporção de 1,00 g NaHCO3 g-1DQO para todas as fases do ASTBR M II. Para o ASTBR – M I, variou-se a concentração de 1,00 a 0,00 g NaHCO3 g-1 DQO no reator. Para o ASTBR A a porcentagem de hidrogênio (H2) no biogás foi de 51%, a produção volumétrica de hidrogênio (PVH) de 88,0 mL H2 L-1 h-1 e o rendimento de hidrogênio (HY) de 1,18 mol H2 molcarboidratos-1. O microrganismo predominante nesse reator foi o Thermoanaerobacterium, e a principal rota a do ácido lático. O reator ASTBR – M I sofreu acidificação após a retirada completa de alcalinizante, permitindo a detecção de H2 no biogás. Porém, a retomada da adição de NaHCO3 favoreceu o crescimento das arqueias, principalmente metanogênicas hidrogenotróficas. A comparação dos reatores metanogênicos foi realizada para fases com condições semelhantes (COV de 10 g L-1d-1 e 1,00 g NaHCO3 g-1DQO) e permitiu verificar melhor desempenho na produção de CH4 do ASTBR – M II. Em relação ao MY, a eficiência do ASTBR – M II foi 44% superior ao ASTBR M – I. / Brazil is the largest producer of sugarcane and one of the main sub-products of this industry is the molasses, which is rich in carbohydrates and can be used as a substrate for biogas production in anaerobic digestion. In this study, biogas production was evaluated under thermophilic conditions (55 °C) in a two-phases system (acidogenic reactor followed by methanogenic reactor) based on phase separation and a single-phase system (acidogenic and methanogenic microorganisms in a single unit) using molasses as the substrate. The acidogenic reactor (ASTBR-A) was operated under the organic loading rate (OLR) of 60.0 g L-1d-1 and hydraulic retention time (HRT) of 4 hours. The methanogenic reactor (ASTBR M II), which was sequential to acidogenic one, was operated in ten phases with OLR ranging from 0.6 to 10.0 g L-1d-1 and HRT of 40 and 24 hours. The single-phase reactor was composed of a methanogenic reactor (ASTBR -– M I) operated in nine phases with increasing OLR from 2.5 to 10.0 g L-1d-1 and HRT of 28 hours. Sodium bicarbonate (NaHCO3) was added in the ratio of 1.00 g NaHCO3 g-1COD in all phases of ASTBR – M II. For the ASTBR – M I, the concentration varied between 1.00 to 0.00 g NaHCO3 g-1COD. In the ASTBR – A, the percentage of hydrogen (H2) in the biogas was 51%, the volumetric hydrogen production (VHP) was 88.0 mL H2 L-1 h-1 and the hydrogen yield (HY) was 1.18 mol H2 molar-1carbohydrate. The predominant microorganism in this reactor was the Thermoanaerobacterium and the main metabolite route was the lactic acid. The ASTBR – M I suffered acidification after the complete removal of the alkalinizer allowing the detection of hydrogen in the biogas. However, the use of the alkalinizer after its complete removal from the system favored the growth of Archaeas, mainly the hydrogenotrophic methanogens. The comparison of the methanogenic reactors was carried out for phases with similar conditions (OLR of 10 g L-1d-1 and 1.00 g NaHCO3 g-1COD) and allowed to verify a better performance in the methane (CH4) production in the ASTBR – M II. Regarding the methane yield (MY), the efficiency of ASTBR – M II was 44% higher than ASTBR M – I.

Το χρώμιο (Cr) αποτελεί έναν από τους σημαντικότερους ρύπους του φυσικού περιβάλλοντος. Η ευρεία βιομηχανική χρήση του χρωμίου έχει ως αποτέλεσμα την απελευθέρωση μεγάλων ποσοτήτων του μετάλλου στο περιβάλλον κυρίως με τη μορφή του εξασθενούς χρωμίου (Cr(VI)). Το εξασθενές χρώμιο, μία από τις σταθερές μορφές του χρωμίου στο περιβάλλον, είναι ευδιάλυτο, υψηλά τοξικό, καρκινογενές και μεταλλαξιγόνο. Οι σύγχρονες μέθοδοι επεξεργασίας του εξασθενούς χρωμίου χρησιμοποιούν μικροοργανισμούς, στηριζόμενες στη μεταβολική και κυτταρική τους δράση. Πρόκειται για διεργασίες πιο ανταγωνιστικές, αποτελεσματικές και οικονομικές έναντι των συμβατικών φυσικοχημικών μεθόδων (χημική αναγωγή, ανταλλαγή ιόντων, διήθηση, ηλεκτροχημική επεξεργασία, προσρόφηση σε ενεργό άνθρακα, αντίστροφη όσμωση και μεμβράνες) καθώς παρουσιάζουν μικρές ενεργειακές απαιτήσεις, χαμηλό πάγιο και λειτουργικό κόστος και τέλος μικρότερη παραγωγή τοξικής λάσπης. Η βιολογική αναγωγή του εξασθενούς χρωμίου απαιτεί την παρουσία ενός δότη ηλεκτρονίων. Το ρόλο αυτό παίζει ο οργανικός άνθρακας, ο οποίος είναι απαραίτητος για την πραγματοποίηση της διεργασίας αυτής. Στην παρούσα διδακτορική διατριβή μελετήθηκε η επεξεργασία υγρών χρωμικών βιομηχανικών αποβλήτων, με ταυτόχρονη εκμετάλλευση/αξιοποίηση αγροτοβιομηχανικών παραπροϊόντων/αποβλήτων (μελάσα - χαμηλού κόστους και ορρός γάλακτος – μηδενικού κόστους), χρησιμοποιώντας βιολογικές μεθόδους. Αρχικά, πραγματοποιήθηκαν πειράματα για τη βελτιστοποίηση του ρυθμού αναγωγής των μεικτών αερόβιων γηγενών καλλιεργειών σε αντιδραστήρες αιωρούμενης ανάπτυξης. Στη συνέχεια χρησιμοποιήθηκε η μεικτή καλλιέργεια για τη μελέτη της βιολογικής αναγωγής του εξασθενούς χρωμίου σε αντιδραστήρες σταθερής κλίνης πιλοτικής κλίμακας με πλαστικό πληρωτικό υλικό, σε διάφορες λειτουργικές συνθήκες, στοχεύοντας στην μέγιστη απόδοση των συστημάτων και την αποφυγή λειτουργικών προβλημάτων. Το βιολογικό σύστημα που χρησιμοποιήθηκε στην παρούσα διδακτορική διατριβή, αποτελεί μία πολύ αποτελεσματική μέθοδο επεξεργασίας βιομηχανικών αποβλήτων επιβαρυμένων με το τοξικό εξασθενές χρώμιο, χρησιμοποιώντας οικονομικές πηγές άνθρακα όπως η μελάσα και ο ορρός γάλακτος. Η μέθοδος αυτή είναι πολλά υποσχόμενη, συνδυάζοντας υψηλά ποσοστά απομάκρυνσης με εξαιρετικά χαμηλές δαπάνες λειτουργικού κόστους. / Chromium is one of the most serious pollutants of natural environment. The widespread industrial use of chromium leads to the release of large quantities of this metal in the environment, mainly in the form of hexavalent chromium. The hexavalent chromium, one of the most stable forms that we can notice in the environment, is soluble, highly toxic carcinogenic and mutagenic. Contemporary water processing techniques of hexavalent chromium use micro-organisms, based on their metabolic and cellular activity. These procedures are more competitive, more effective and certainly financially affordable over the conventional physicochemical methods (chemical oxidation or reduction, ion exchange, filtration, electrochemical treatment, activated carbon adsorption, reverse osmosis and membrane technologies) as they show low energy demands, low maintenance cost and a smaller production of toxic mud. The biological reduction of hexavalent chromium requires the presence of an electron donor. This part is covered by organic carbon that is essential for carrying out the process. The present thesis studied the treatment of liquid industrial chromate waste and the exploitation/utilization of agroindustrial byproducts/wastewaters (molasses - low cost and cheese whey- zero cost), using biological methods. At the beginning, experiments were conducted to optimize the reduction rate of mixed aerobic indigenous cultures in suspended growth reactors. Subsequently, the mixed culture was used for the biological reduction of the hexavalent chromium, in laboratory pilot scale fixed bed reactors, with plastic media, in various functional conditions targeting to the maximum system performance and the prevention of functional problems. The biological system used in the present thesis constitutes a very effective method of processing industrial wastewater polluted with the toxic hexavalent chromium, by using affordable sources of carbon, such as molasses and cheese whey. This is a quite promising method, combining high removal rates with extremely low operating expenditure.

A digestão anaeróbia tem se apresentado como um processo de grande interesse sob a ótica da potencial produção de energia renovável (H2 e CH4), considerando-se a ampla variedade de compostos orgânicos que podem ser utilizados. Neste estudo desejou-se avançar na compreensão do sistema de reatores anaeróbios de duas fases (acidogênico seguido de metanogênico) operados em condições termofílicas (55°C), alimentados com melaço da cana-de-açúcar, subproduto da indústria sucroalcooleira. Os experimentos foram conduzidos em reatores anaeróbios de leito fixo estruturado com fluxo ascendente e o melaço foi diluído com água de abastecimento, para adequação da concentração aos processos de tratamento de águas residuárias. Na 1ª Etapa dois reatores acidogênicos foram operados em paralelo para avaliar diferentes formas de inoculação e meios suportes, a fim de manter a produção continua e estável de hidrogênio. Para isso foram aplicadas diferentes cargas orgânicas (2,5, 5 e 10 gDQO.L-1) que resultam em COV de 30, 60 e 120 g.DQO.Lreator1.dia-1, com TDH fixo de 2 horas. A expressão do gene hidrogenase foi detectado em ambos os reatores, mas em maior proporção no reator inoculado com lodo de reator UASB e usando como material suporte a espuma de poliuretano. Sequencialmente a este reator, foi acoplado um reator metanogênico, alimentado com efluente do reator acidogênico, estabilizado nas condições apresentadas, e operado com COV crescentes de 1, 2, 5, 7, 14, 17 e 26,5 gDQO.Lreator-1.dia-1 e consequente diminuição do TDH de 240, 96, 48, 32, 24, 16 e 12 horas. O reator acidogênico na 2ª etapa foi operado por 417 dias consecutivos e COV de 120 g.DQO.Lreator1.dia-1, produzindo hidrogênio continuamente, alcançado valores de produção bruta de H2 de 7,60 LH2.dia-1. O reator metanogênico foi operado por 251 dias consecutivos, produzindo metano e alcançado valores de produção bruta de CH4 de 5,90 LCH4.dia-1. A eficiência de remoção de DQO do sistema de reatores foi de aproximadamente 90%, com contribuição aproximadamente de 10% para o reator acidogênico e contribuição aproximadamente de 80% para o reator metanogênico. O reator acidogênico alcançou rendimento de produção de hidrogênio por kg de melaço aplicado de 392 LH2.kgmelaço-1 e o reator metanogênico de 387 LCH4.kgmelaço-1. Para finalidade de comparações e aplicabilidade, o ganho energético global do sistema de reatores de duas fases foi de aproximadamente 5,7 kWh.kgmelaço-1 (1,4 kWh.kgmelaço-1 para o reator acidogênico e 4,3 kWh.kgmelaço-1 para o reator metanogênico). A produção continua de H2 obtida neste estudo está relacionada à associação das vias dos ácidos produtores de hidrogênio já consolidados pela literatura pertinente (acético e butírico) e pela produção de hidrogênio pela rota do ácido lático, devido a associação entre as comunidades de microrganismos estabelecidas no reator. O sequenciamento massivo MiSeq mostrou a seleção de diversos gêneros de microrganismos com redundância funcional e pertencentes principalmente aos Filos Firmicutes, Proteobacteria e Thermotogae, tais como Clostridium sensu stricto, Thermohydrogenium, Thermoanaerobacterium e Cellulosibacter (Firmicutes); Pseudomonas, Enterobacter, Shewanella e Petrobacter (Proteobacteria) e Fervidobacterium (Thermotogae). Microrganismos produtores de ácido lático também foram selecionados tais como: Lactobacillus, Leuconostoc, Sporolactobacillus e Trichococcus. Dos pontos de vista científico e tecnológico este estudo deu mais um passo para a compreensão dos bioprocessos envolvidos nos sistemas anaeróbios em dois estágios produzindo H2 e CH4 continuamente por longo período de tempo. / Anaerobic digestion has shown as an interesting process for renewable energy production (H2 and CH4), for a wide variety of organic compounds (carbon source). This study aimed to advance the understanding of a two-stage process anaerobic system (acidogenic bioreactor followed by methanogenic bioreactor) under thermophilic condition (55°C) fed with molasses, a sugarcane industry by-product. The experiments were conducted at up-flow structured bed reactors and sugarcane molasses was diluted with tap water, to adjust the concentration to the wastewater treatment. At first stage two acidogenic reactors were operated in parallel to evaluate different source of inocula and support bed, to obtain continuous and stable hydrogen production. It was applied 2.5, 5 and 10 gCOD.L-1 resulting in OLR of 30, 60 and 120 g.COD.Lreactor-1.day-1, with HRT fixed at 2 hours of hydrogenase gene was detected in both reactors but with higher number of copies of the gene in the reactor that showed higher hydrogen production: the reactor sed with sludge of UASB reactor and using polyurethane foam as support material. To this reactor was coupled a methanogenic reactor fed with effluent from acidogenic reactor and operated with increasing OLR (1, 2, 5, 7, 14, 17 e 26,5 gCOD.Lreactor-1.day-1) decreasing the HRT (240, 96, 48, 32, 24, 16 and 12 hours). The acidogenic reactor was operated during 471 days with OLR of 120 g.COD.Lreactor-1.day-1, with HRT fixed at 2 hours, with continuous hydrogen production with a gross production of 7.60 LH2.day-1. The methanogenic reactor was operated for 251 days, with continuous methane production of up to 5.90LCH4.day-1. The COD removal efficiency using the two-stage system was approximately 90% , with 10% contribution by the acidogenic reactor and 80% contribution by the methanogenic reactor. The acidogenic reactor achieved hydrogen yield per kg of applied molasses equal to 392 LH2.kgmolases-1. The methanogenic reactor achieved methane yield per kg of applied molasses equal to 387 LCH4.kgmolasses-1. For comparison and applicability purposes, the overall energy yield using the two stage reactor system was approximately 5.7 kWh.kgmolasses-1 (Acidogenic reactor 1.4 kWh.kgmolasses-1 and Methanogenic reactor 4.3 kWh.kgmolasses-1). The continuous production of H2 obtained in this study is related to the association of the hydrogen producer acids pathway established by the relevant literature (acetic and butyric) and the hydrogen production by the lactic acid pathway due to the microorganisms association established in the reactor. Metagenomic analysis by MiSeq Plataform revealed that hydrogen production was due the selection of microorganisms with functional redundancy mainly of Phyla Firmicutes, Proteobacteria and Thermotogae, such as Clostridium sensu stricto, Thermohydrogenium, Thermoanaerobacterium, Cellulosibacter (Firmicutes); Pseudomonas, Enterobacter, Shewanella and Petrobacter (Proteobacteria) and Fervidobacterium (Thermotogae). Genera of acid latic producers, such as Lactobacillus, Leuconostoc, Sporolactobacillus and Trichococcus, were also selected. From the scientific and technological point of view this study has taken another step towards the understanding of bioprocesses involving two stage anaerobic systems for a long term continuous production of H2 and CH4.

Cette thèse présente de nouvelles techniques pour l'étude expérimentale des gaz quantique ultrafroids d'atomes fermioniques de lithium et de potassium. Dans la première partie de cette thèse, nous décrivons la conception et la caractérisation des nouveaux composants de notre dispositif expérimental capable de piéger et refroidir simultanément des atomes de $^6$Li et de $^{40}$K à des températures ultrabasses. Nous rendons compte d'une nouvelle technique de refroidissement sub-Doppler, reposant sur la transition de la raie D$_1$ des atomes alcalins, pour refroidir des atomes de lithium et de potassium par laser. Après cette étape de mélasse, nous avons mesuré une densité dans l'espace des phases de l'ordre de $10^{-4}$ à la fois pour le $^6$Li et le $^{40}$K. Nous présentons le refroidissement par évaporation forcée d'atomes de $^{40}$K qui commence dans un piège magnétique quadripolaire pluggé et continue dans un piège optique dipolaire. Dans ce contexte, nous rendons compte de la production d'un gaz quantique de Fermi dégénéré de $1.5\times10^5$ atomes de $^{40}$K dans un piège dipolaire croisé avec $T/T_{_F} = 0.17$, ce qui ouvre la voie à l'étude des superfluides de $^{40}$K en interaction forte. Dans la deuxième partie de cette thèse, nous présentons une source laser à état solide, de faible largeur spectrale et capable d'émettre 5.2 W de puissance autour de 671 nm, dans la gamme des longueurs d'onde des transitions de la raie D du lithium. La source repose sur un laser en anneau pompé par diode, émettant sur la transition à 1342 nm de Nd:YVO$_4$, capable de produire 6.5 W de lumière dans un faisceau monomode limité par la diffraction. Nous rendons compte de trois différentes approches pour la génération de seconde harmonique du faisceau de sortie, à savoir en utilisant une cavité amplificatrice comprenant un cristal ppKTP, par doublage de fréquence intracavité et par un structure de guide d'onde de ppZnO:LN. / This thesis presents novel techniques for the experimental study of ultracold quantum gases of fermionic lithium and potassium atoms. In the first part of this thesis, we describe the design and characterization of the new components of our experimental apparatus capable of trapping and cooling simultaneously $^6$Li and $^{40}$K atoms to ultracold temperatures. We report on a novel sub-Doppler cooling mechanism, operating on the D$_1$ line transition of alkali atoms, for laser cooling of lithium and potassium. The measured phase space densities after this molasses phase are on the order of $10^{-4}$ for both $^6$Li and $^{40}$K. We present the forced evaporative cooling of $^{40}$K atoms, starting in an optically plugged magnetic quadrupole trap and continuing in an optical dipole trap. In this context, we report on the production of a quantum degenerate Fermi gas of $1.5\times10^5$ atoms $^{40}$K in a crossed dipole trap with $T/T_{_F} = 0.17$, paving the way for the study of strongly interacting superfluids of $^{40}$K. In the second part of this thesis, we present a narrow-linewidth, all-solid-state laser source, emitting 5.2 W in the vicinity of the lithium D-line transitions at 671 nm. The source is based on a diode-end-pumped unidirectional ring laser operating on the 1342 nm transition of Nd:YVO$_4$, capable of producing 6.5 W of single-mode light delivered in a diffraction-limited beam. We report on three different approaches for second-haromonic generation of its output beam, namely by employing an enhancement cavity containing a ppKTP crystal, intracavity frequency doubling and a ppZnO:LN waveguide structure.

On trouve des manifestations de la physique quantique au niveau thermodynamique dansde nombreux systèmes. Un exemple marquant est la superfluidité, découverte au début du20ème siècle, que l’on retrouve de l’hélium aux étoiles à neutrons. Les gaz dilués ultrafroidsoffrent une polyvalence unique pour étudier des systèmes quantiquesmacroscopiques, pouvant directement tester les théories grâce à un environnementcontrôlé. Dans cette thèse, nous présentons plusieurs études expérimentales de gaz froidsde lithium. Le lithium fournit la possibilité de réaliser des ensembles de bosons et defermions, avec des interactions contrôlables entre les constituants. Nous présentons lestechniques utilisées pour préparer et étudier des gaz dégénérés de lithium, et uneamélioration possible des méthodes existantes. Nous décrivons premièrement une étudede la recombinaison à trois bosons avec une interaction à deux corps résonante. Comparésquantitativement à la théorie, ces résultats fournissent une référence pour les étudesfutures du gaz de Bose unitaire. Pour finir, nous présentons la première observationexpérimentale d’un mélange de superfluides de Bose et de Fermi. Nous démontrons queles deux composants sont superfluides et que leur écoulement relatif vérifie les propriétésdes écoulement superfluides, avec une absence de viscosité en dessous d’une vitessecritique puis la présence de dissipation au-delà. En utilisant des excitations collectives dece mélange, nous mesurons l’interaction entre les deux superfluides, en accord avec unmodèle théorique. / Manifestations of Quantum Physics at the thermodynamical level are found in a broadrange of physical systems. A famous example is superfluidity, discovered at the beginningof the 20th century and found in many different situations, from liquid helium to neutronstars. Dilute ultracold gases offer a unique versatility to engineer quantum many-bodysystems, which can be directly compared with theory thanks to the controllability of theirenvironment. In this thesis we present several experimental investigations led on ultracoldlithium gases. Lithium provides the possibility to study ensembles of bosons andfermions, with controllable interactions between the constituents. We present experimentaltechniques for preparation and studies of degenerate gases of lithium, with prospects forimprovement of the existing methods. We first report on an investigation of three-bodyrecombination of bosons under a resonant two-body interaction. This study, quantitativelycompared with theory constitutes a benchmark for further studies of the unitary Bose gas.Finally, we present the first experimental realization of a mixture of a Bose superfluid witha Fermi superfluid. We demon- strate that both components are in the superfluid regime,and that the counter-flow motion between them possesses the characteristics of superfluidflow, with the absence of viscosity below a critical velocity, and an onset of friction above.Using collective oscillations of the mixture, we measure the coupling between the twosuperfluids in close agreement with a theoretical model.