Este trabalho apresenta as avaliações de desempenho, das demandas operacionais e dos fatores intervenientes no aumento da escala da unidade piloto do Reator anaeróbio Horizontal de Leito Fixo (RAHLF) no tratamento de esgoto sanitário após passagem por peneira com malha de 1 mm, durante dois anos de operação. O reator dispunha de volume total de 237,5 1, construídos com tubos comerciais de PVC de 14,5 cm de diâmetro (D), dispostos em cinco módulos horizontais em série de 2,88 m, perfazendo um comprimento total de (L) de 14,4 m e relação de total de L/D de 100. O suporte de imobilização de biomassa, espuma de poliuretano em matrizes cúbicas de 1 cm de aresta, mostrou-se adequado ao desenvolvimento do biofilme. Em partida, sem inoculação prévia, ocorreu a sua consolidação a partir de 70 dias, com predominância de morfologia semelhante a Methanosaeta sp. em relação a da Methanosarcina. Em torno de 90 dias com afluente de 350 mg/l de DQO, observe-se a melhor qualidade do efluente, com valor de 100 mg/l de DQO. Em longa operação ocorreu queda de rendimento e menor reprodutibilidade das previsões do projeto, atribuída aos constantes entupimentos e ineficácia das operações de limpeza, com o comprometimento de volume reacional verificados por estudos de hidrodinâmica. Da investigação das origens dos equipamentos observou-se tratar mais de um efeito local e qualitativamente relacionado à biomassa retida que propriamente quantitativo e extensivo ao longo de todo reator, com produção continuada de polímeros extracelulares, promovendo um efeito sinérgico com os predominantes organismos filamentosos e com os sólidos particulados retidos no leito. Diante das potencialidades desta configuração de reator apontam-se alternativas de mitigação dos entupimentos e o direcionamento dos estudos necessários para novo aumento de escala para o tratamento de esgoto sanitário. / This work evaluated the performance, the operational demands and the intervenient factors in the scale-up of the horizontal flow anaerobic immobilized biomass (HAIB) reactor pilot unit, treating domestic sewage previously screened. The operation was monitored for two years. The five- module (2.88 m length each) reactor volume was 237.5 liters and it was built with commercial PVC pipes of 14.5 cm of diameter (D), resulting in a total length (L) of 14.4 m and in a total ratio L/D of approximately 100. The immobilization support, cubic matrices of polyurethane foam (1 cm edge), showed to be suitable for the anaerobic biofilm development. During the start-up, without previous inoculation, the biofilm seemed to be consolidated after 70 days, and Methanosaeta sp. morphology predominated, in detriment of Methanosarcina. With an affluent of 350 mg COD/L, the best reactor performance was observed in about 90 days of operation (100 mg COD/L in the effluent). However, with the continuous operation, its performance decreased and the project predictions did not seem to fit anymore. These facts were probably due to the frequent cloggings ant the inefficiency of the backwashing procedures, leading to a decreasing of the operational volume. The origin of the clogging seemed to be related to the extracellular polymer production, linked to a synergic effect with the filamentous organisms and the particulate solids in the bed. Despite these operational problems, there were found alternatives to mitigate the clogging, and studies about a new scale-up methodology, in order to treat domestic sewage, were strongly recommended.

O projeto consistiu na concepção e avaliação do desempenho de um sistema anaeróbio-aeróbio para tratamento de esgoto sanitário. O leito do reator foi dividido em quatro compartimentos de igual volume. Foi usada espuma de poliuretano para imobilização da biomassa e, para facilitar a partida do reator, esse material suporte foi previamente inoculado. O projeto teve três fases distintas: na primeira etapa, foi observada a importância da concentração de biomassa anaeróbia no desempenho de reator anaeróbio a princípio operado com metade do leito reacional com espuma e, a seguir, com o leito todo preenchido com espuma. Na segunda etapa, foram testados diferentes tempos de detenção hidráulica no reator que operou apenas em condições anaeróbias. Na última etapa foi operado o reator combinado anaeróbio-aeróbio. Ficou constatada a importância da concentração de microrganismos no desempenho do reator anaeróbio, pois com o aumento da quantidade de espuma, o reator atingiu resultados melhores e maior estabilidade operacional. Foi comprovada a influência do tempo de detenção hidráulica (TDH) no desempenho do reator. Tempos de detenção muito altos acarretam problemas de transferência de massa líquido-sólido, e baixos TDH dificultam adequada ação dos microrganismos. O melhor resultado para o reator em operação exclusivamente anaeróbia foi para o TDH de 10 horas, no qual se conseguiu reduzir a DQO de amostra bruta de 389 +/- 70 mg/L para 137 +/- 16 mg/L, em média. Para o reator operado anaeróbio-aeróbio a DQO de amostra bruta decresceu de 259 +/- 69 mg/L para 93 +/- 31 mg/L, em média. A comparação de todos os resultados obtidos, evidenciou a importância do pós-tratamento aeróbio na remoção de parcela de matéria orgânica não removida em tratamento unicamente anaeróbio. / The project consisted in the design and performance evaluation of an anaerobic-aerobic system for wastewater treatment. Polyurethane foam was used for biomass immobilization and, to smooth the reactor start-up, this supporting material was previously inoculated. The project was divided in three distinct phases. In the first one, the importance of the anaerobic biomass concentration was observed in the performance of the anaerobic reactor in a way to operate the reactor primarily with half of the reaction bed filled with foam and subsequently operate it with the bed completely filled with foam. In the second phase, different times of hydraulic retention were tested with the reactor operating exclusively in anerobic conditions. In the third and last phase, an anaerobic-aerobic combined reactor was operated. It was possible to confirm the importance of microorganism concentration in the performance of the anaerobic reactor, since the increase in the amount of foam allowed the reactor to reach better results and greater operational stability. The influence of the hydraulic retention time in the reactor performance was also proved. Very high retention times cause problems in the liquid-solid mass transference, while low retention times do not allow an adequate action of microorganisms. The best result for the reactor with an exclusive anaerobic operation was the 10 hour retention time, when it was possible to reduce the COD of a 389 +/- 70 mg/L gross sample to a 137 +/- 16 mg/L in average. On the other hand, for the anaerobic-aerobic operating reactor, the COD of a gross sample dropped from 259 +/- 69 mg/ L to 93 +/- 31 mg/L in average. Finally, comparing all the obtained results, it was possible to verify the importance of the anaerobic post treatment in the removal of a part of the organic matter not removed in an exclusively anaerobic treatment.

A atividade industrial diversificada tem sido responsável pelo lançamento, no ambiente, de resíduos que contém materiais tóxicos e/ou de difícil degradação. Benzeno, tolueno, etilbenzeno e xilenos (BTEX) são compostos importantes, por estarem presentes em águas superficiais e subterrâneas, geralmente a partir de contaminações por derivadas de petróleo. Enquanto a degradação aeróbia de BTEX já está amplamente entendida e descrita, a aplicação de processos anaeróbios de tratamento, indicados na década de 80 ainda requer mais estudos. Reatores anaeróbios horizontais de leito fixo de bancada preenchidos com cubos de espuma de poliuretano, contendo lodo anaeróbio proveniente de diversas fontes trataram a água residuária sintética a base de proteínas, carboidratos, lipídios, contendo solução etanólica de BTEX e solução de BTEX em detergente comercial; e solução etanólica de BTEX como únicas fontes de carbono. A influência da adição de nitrato e sulfato como aceptores de elétrons na degradação anaeróbia também é discutida. Os reatores foram capazes de remover BTEX nas concentrações testadas de até 15,0 mg/L de cada composto, com tempos de detenção hidráulica de 11,4 horas e 13,5 horas. Os reatores forneceram condições excelentes para o desenvolvimento de biofilme complexo capaz de degradar BTEX, contendo organismos degradadores de BTEX, acetogênicos, acetoclásticos e hidrogenotróficos. Arqueas metanogênicas representaram menos de 0,5% do total de organismos anaeróbios na biomassa dos reatores. O modelo cinético de primeira ordem com residual foi o que melhor representou os dados experimentais e as velocidades de degradações de BTEX, estimadas neste trabalho, foram cerca de 10 a 94 vezes maiores que as encontradas na literatura, em ensaios realizados em microcosmos. / The diversified industrial activity has been responsible for discharge in the environment of toxic and/or difficult degradation compounds. Benzene, toluene, ethylbenzene and xylenes (BTEX) are important compounds present in surface and ground waters, usually from petroleum products contamination. While BTEX aerobic degradation is extensively understood and described, anaerobic treatment application, started in the eighties, associated to fundamental studies need to be improved. Bench-scale horizontal-flow anaerobic immobilized biomass reactors filled with polyurethane foam matrices, containing immobilized anaerobic biomass from various sources, treated synthetic substrate containing protein, carbohydrates, lipids, BTEX solution in ethanol and BTEX solution in commercial detergent, as well as BTEX solution in ethanol as the sole carbon source. The influence of the addition of nitrate and sulfate as electron acceptors on anaerobic degradation is also discussed. The reactors were able to remove up to 15.0 mg/L of each BTEX compound, with hydraulic detention time of 11.4 hours and 13.5 hours. The reactors provided excellent conditions for developing a complex biofilm with BTEX-degraders, acetogenic, acetoclastic and hydrogenotrophic microorganisms. Methanogenic archaea were found to represent less than 0.5% of the total anaerobic organisms in the biomass inside the reactors. Residual first order kinetic model fitted well the experimental data and the BTEX degradation rates, estimated in this work, were about 10- to 94-fold higher than those found in the literature, in microcosms studies.

O reator anaeróbio em batelada seqüencial é constituído por um frasco de vidro cilíndrico de volume total de cinco litros, envolvido por uma camisa de vidro, por onde escoa a água aquecida, permitindo a operação em temperatura controlada. A biomassa encontra-se imobilizada em partículas cúbicas de espuma de poliuretano (densidade aparente de 23 kg/\'M POT.3\', as quais estão colocadas em um cesto adaptado dentro do frasco cilíndrico. A mistura é promovida por três impelidores de 3,0 cm de diâmetro, distanciados 4,0 cm um do outro, situados ao longo do eixo vertical no centro do reator. O desempenho dessa nova configuração de reator anaeróbio foi avaliado sob diferentes condições os efeitos de transferência de massa nas fases sólida e líquida. Todos os ensaios foram efetuados à temperatura de 30 ± 1 grau Celsius. Cada batelada compreende três etapas: alimentação, reação e descarga. Para avaliar os efeitos da transferência de massa na fase sólida foram feitos quatro ensaios utilizando-se partículas cúbicas de espumas de poliuretano com tamanhos de 0,5 cm; 1,0 cm; 2,0 cm e 3,0 cm de lado, com impelidor tipo hélice e intensidade de agitação de 500 rpm, determinada através de um ensaio preliminar. Para avaliar os efeitos da transferência de massa nas fases sólida e líquida foram feitos experimentos com quatro tipos de impelidores: hélice, turbina plana, turbina inclinada e turbina curva, com intensidades de agitação na faixa de 100 rpm a 1100 rpm. Também foram realizados ensaios hidrodinâmicos para verificar o tempo de mistura e ensaio para verificar a condição de anaerobiose no sistema. A água residuária utilizada em todos os ensaios foi sintética com concentração de 530 ± 37 mg DQO/L. Em todas as condições estudadas o reator apresentou boa eficiência de remoção da matéria orgânica, em torno de 87%. A concentração efluente de ácidos voláteis totais manteve-se em 13 ± 9 mg HAc/L, alcalinidade a bicarbonato de 223 ± 14 mg Ca\'CO IND.3\'/L e pH entre 6,7 e 7,2. A transferência de massa na fase sólida não foi a etapa limitante na conversão da matéria orgânica, quando partículas de 0,5 cm a 2,0 cm de aresta foram usadas no reator anaeróbio em batelada seqüencial. A resistência à transferência de massa na fase sólida somente influenciou a taxa global de reação, quando foram usados tamanhos de partículas cúbicas de 3,0 cm de aresta. A resistência à transferência de massa na fase líquida não foi somente afetada pela intensidade de agitação, mas também pela eficiência da mistura obtida por cada tipo de impelidor. A mistura do líquido dentro do reator obtida pelo impelidor turbina plana foi a mais eficiente. O uso deste tipo de impelidor resultou em menores consumos de energia e ótimo desempenho do reator com baixas taxas de agitação. Os resultados deste estudo permitiram concluir que esta nova configuração não permite a manutenção de condição de anaerobiose estrita no meio, principalmente quando altas intensidades de agitação foram aplicadas e as limitações da eficiência do processo, neste sistema, estão relacionadas principalmente as resistências à transferência de massa do que restrições cinéticas bioquímicas. / The bench-scale anaerobic sequencing batch reactor consisted of a cylindrical glass flask with a total capacity of 5 liters. The reactor was surrounded by a water jacket that allowed the operation to proceed at a constant temperature throughout the experiment. The biomass was immobilized in 5-mm cubic particles of polyurethane foam (apparent density of 23 kg/\'M POT.3\') placed in a basket inside the cylindrical flask. The mixing was provided by three mechanical impellers with diameters of 3 cm, placed 4 cm apart along a vertical axis, at the center of the reactor. All experiments were conducted at the temperature of 30 Celsius degrees. Each batch consisted of three steps: feed, react and liquid withdrawal. The performance of this new reactor configuration was evaluated under different conditions of solid and liquid-phase mass transfer. In order to evaluate the effects of the solid-phase mass transfer, four experiments were carried out with cubical polyurethane foam particles of 0.5 cm, 1.0 cm, 2.0, cm and 3.0 cm side, and with propeller impellers rotating at 500 rpm, achieved by preliminary experiment. The effects of the liquid-phase mass transfer were evaluated through four experiments with four types of impellers: propeller, flat-blade, pitched-blade and curved-blade turbines, at agitation rates from 100 rpm and 1100 rpm. A hydrodynamic test was also carried out in order to verify the mixing time, energy consumption and occurrence of strict anaerobic activity in system. A low-strength synthetic substrate was used in all the experiments with a mean chemical oxygen demand (COD) of 530 ± 37 mg DQO/L. The influence of the solid and liquid-phase mass transfer on the reactor\'s performance was assessed by measuring COD temporal profiles along batch cycles. In all conditions studied the reactor achieved good efficiency, with mean removal of organic matter (COD) of 87%. The effluent mean TVA concentration was 13 ± 9 mg HAc/L, bicarbonate alkalinity was 223 ± 14 mg Ca\'CO IND.3\'/L and the pH values ranged from 6,7 e 7,2. The solid-phase mass transfer was not the limiting step in the organic matter conversion when 0.5 to 2.0-cm side bioparticles were used in the anaerobic sequencing batch reactor. Solid-phase mass transfer resistance only influenced the overall reaction rate when 3.0-cm cubic bioparticles were used. The liquid-phase mass transfer resistance was affected both by agitation and by efficiency of mixture provided by each type of impeller. Among the impellers assayed, the flat-blade one was the most efficient in providing the required mixing conditions. The use of this type impeller resulted in small energy consumption and excellent performance of the reactor with low agitation rate (N = 300 rpm). The results of this study also indicated that this new configuration did not provide conditions for the establishment of strict anaerobic conditions, mainly when high agitation rates were used. Anaerobic process efficiency limitations in this system were mainly related to mass transfer resistances rather than biochemical kinetic restrictions.

Submitted by Renata Lopes (renatasil82@gmail.com) on 2017-05-09T14:17:11Z No. of bitstreams: 1 romuloaugustodeabreufranchini.pdf: 12314039 bytes, checksum: fcf7a0798691ae32d15114b47607205e (MD5) / Approved for entry into archive by Adriana Oliveira (adriana.oliveira@ufjf.edu.br) on 2017-05-17T14:14:58Z (GMT) No. of bitstreams: 1 romuloaugustodeabreufranchini.pdf: 12314039 bytes, checksum: fcf7a0798691ae32d15114b47607205e (MD5) / Made available in DSpace on 2017-05-17T14:14:58Z (GMT). No. of bitstreams: 1 romuloaugustodeabreufranchini.pdf: 12314039 bytes, checksum: fcf7a0798691ae32d15114b47607205e (MD5) Previous issue date: 2010-08-04 / CAPES - Coordenação de Aperfeiçoamento de Pessoal de Nível Superior / CNPq - Conselho Nacional de Desenvolvimento Científico e Tecnológico / FAPEMIG - Fundação de Amparo à Pesquisa do Estado de Minas Gerais / O mel é uma mistura complexa constituída de carboidratos, enzimas, aminoácidos, minerais, ácidos orgânicos e flavonóides. Inúmeros trabalhos evidenciam o potencial terapêutico do mel, o qual suas principais propriedades são a atividade antimicrobiana e ação cicatrizante, sendo estas atribuídas a fatores como acidez, osmolaridade, peróxido de hidrogênio (H2O2), catalase e flavonóides. A primeira pesquisa deste trabalho consistiu na determinação da origem floral das amostras de mel, realizada através da análise microscópica do pólen (melissopalinologia). Os espectros demonstraram a variabilidade polínica das amostras escolhidas. Em outro estudo, dois métodos versáteis, envolvendo a espectrofotometria e amperometria, foi aplicado na determinação dos teores de H2O2 em 17 amostras de mel. O H2O2 foi determinado por análise de injeção em fluxo (FIA) e reatores tubulares contendo a enzima peroxidase imobilizada na resina Amberlite IRA-743. A determinação espectrofotométrica baseouse na oxidação do H2O2 pela enzima na presença de fenol e 4-aminoantipirina e o complexo anti-pirilquinonimina gerado, foi proporcional a concentração de H2O2. Na determinação amperométrica, um eletrodo de ouro eletrodepositado com platina, eletrodo de Ag/AgCl(sat) (+ 0,60V) e uma agulha de aço inoxidável foram utilizados como eletrodos de trabalho, referência e auxiliar, respectivamente. O método baseou-se em três medidas no sistema FIA e a diferença entre os sinais revelou a corrente proporcional de H2O2 no mel. Ambos os métodos apresentaram ampla faixa de linearidade (0,5 a 100 µmol L−1) e baixos limites de quantificação e detecção. As concentrações encontradas ficaram entre 4 e 214 µg g-1. A determinação de H2O2 provou a rapidez, exatidão e sensibilidade dos métodos quando associados aos sistemas FIA. Em outro trabalho, um sensor amperométrico para a determinação da catalase (CAT), acoplado ao sistema FIA e reatores tubulares foi desenvolvido. A quantificação fundamentou-se em 2 etapas de injeção: (1) padrão de H2O2 e (2) padrão de H2O2 tratado com a CAT imobilizada na Amberlite IRA-743. A diferença da corrente entre (1) e (2) mostrou o consumo de H2O2 por unidade de enzima imobilizada O mesmo procedimento foi aplicado para as amostras de mel e a linearidade da curva para a determinação da CAT ficou entre 100 e 5000 UI mL-1. Os níveis de CAT variaram de 9 a 99 UI mg-1. Os resultados demonstraram uma boa relação inversa entre os teores de CAT e H2O2. O último estudo avaliou, in vitro, a atividade antibacteriana contra 18 linhagens de bactérias Gram positivas e negativas. O screening antimicrobiano foi determinado aplicando testes de difusão em ágar e diluição em caldo, exibindo as concentrações inibitórias mínimas, conforme recomendações da CLSI. Concentrações de mel variando entre 1 e 30% (v/v) foram estudadas e 5 amostras apresentaram atividade bacteriostática, especialmente contra S. aureus, S. epidermidis e E. coli. Os resultados reforçaram a idéia da utilização do mel como agente antimicrobiano e enfatizaram que o H2O2 não é o único inibidor de crescimento bacteriano, mas sim um dos constituintes com atividade bacteriostática e bactericida. / Honey is a complex mixture of carbohydrates, amino acids, minerals, organic acids and flavonoids. The therapeutic potential of honey is gradually growing and its scientific evidences of effectiveness. Honey has been reported as antimicrobial agent, to promote healing wound and burns and the antibacterial activity is attributed to factors such as acidity, osmolarity, hydrogen peroxide (H2O2), catalase and flavonoids. The first research of this work involved the determination of the floral origin of honey which was achieved by microscopic analysis of the pollen (melissopalynology). The pollen spectrum showed the pollinic variety corresponding to different taxonomic levels. In the other study, two versatile methods involving spectrophotometry and amperometry were applied for the determination of H2O2 in 17 commercial honey samples. H2O2 was determined by flow-injection analysis (FIA) with a tubular reactor containing peroxidase enzyme immobilized on Amberlite IRA-743 resin. The spectrophotometric determination was based on the oxidation of H2O2 by the enzyme in presence of phenol and 4aminoantipirine. The rate of color generation, due to the formation of the antipyrilquinonimine species was proportional to the concentration of H2O2. In the amperometric determination, a gold electrode modified by electrochemical deposition of platinum, an Ag/AgCl(sat) electrode (+ 0.60V) and a stainless steel tube were employed as working, reference and auxiliary electrodes, respectively. This method was based on three measurements in the FIA system and the difference between peaks showed the proportional current of H2O2 in the honey samples. Both methods showed wide linear dynamic range for H2O2 (0.5 to 100 µmol L−1) and low quantification/detection limits. The concentrations found in the analyzed honeys samples were in the range of 4-214 µg g-1 of H2O2. The determination of H2O2 showed the rapidness, accuracy and sensitivity provided by the two methods, while combined with the FIA system. An amperometric sensor for catalase (CAT) detection in association with FIA system and a tubular reactor containing Amberlite IRA-743 was developed. Catalase quantification was based on two injections: (1) H2O2 standard solution and (2) H2O2 standard solution treated with CAT immobilized on Amberlite IRA-743. The difference between the current obtained from (1) and (2) showed the consumption of H2O2 per unit of enzyme immobilized. The same procedure was used to immobilize CAT in honey samples. The linear dynamic range for CAT extends from 100 to 5000 UI mL-1. The levels of CAT vary from 9 to 99 UI mg-1. Taking into account these results, an inverse correlation was obtained between CAT and H2O2 levels. Finally the antibacterial evaluation of honeys samples against 18 bacterial strains including Gram-negative/positive species was studied. The screening of antimicrobial potential was determined using the drop-test agar diffusion and the broth diluiton methods according to the CLSI recommendations. Increasing honey concentrations, varying from 1 to 30% (v/v) were studied and five samples demonstrated bacteriostatic activity against ATCC® S. aureus, S. epidermidis and E. coli bacterial strains. The results of this preliminary study tend to reinforce the use of honey as antimicrobial agent and emphasize that H2O2 is not the only inhibine present in honey, but it is one of the whole group with bacteriostatic and bactericidal activity.

Les biocapteurs sont des moyens d’analyse en plein essor à la fois rapides, sélectifs et peu coûteux applicables à des domaines extrêmement variés (environnement, santé, agroalimentaire,…). Dans ce type d’outil, un élément sensible de nature biologique (anticorps, enzyme, microorganisme, ADN…) doté d’un pouvoir de reconnaissance pour un analyte ou un groupe d’analytes est associé à un transducteur pouvant être de type électrochimique, optique ou thermique.Dans ce travail, nous nous sommes intéressés au développement de trois biocapteurs pour la détection de substances biologiquement actives. Le premier permet la détermination simultanée de l’adénosine triphosphate (ATP) et du glucose par ampérométrie, le deuxième celle de la créatine kinase, et le troisième est un biocapteur conductimétique pour la quantification de l’ATP. Dans les deux premiers biocapteurs, deux enzymes (l’hexokinase et la glucose oxydase) sont immobilisées à la surface de microélectrodes constituées d’un disque de platine. Le troisième biocapteur est basé sur l’immobilisation de l’hexokinase sur des microélectrodes interdigitées en or. L’immobilisation est réalisée dans tous les cas par co-réticulation des enzymes en présence d’albumine de sérum bovin à l’aide de glutaraldehyde. Les caractéristiques analytiques des biocapteurs ont été déterminées et différentes procédures ont été développées pour l’analyse d’échantillons réels. Les biocapteurs ont pu être appliqués avec succès à la quantification de l’ATP, du glucose et de la créatine kinase dans des préparations pharmaceutiques et du sérum sanguin / Biosensors are rapid, selective and inexpensive devices that combine a biological recognition element, the so-called bioreceptor (e.g. enzymes, antibodies, DNA or microorganisms) to a physical transducer (e.g. electrochemical, optical, thermal or piezoelectrical). They can be used to detect one specific analyte or one family of analytes for a wide range of applications (e.g. environment, food, health). In this work, the detection of biologically active substances was targeted. A biosensor system for simultaneous determination of adenosine triphosphate (ATP) and glucose, a biosensor for creatine kinase analysis, and a novel conductometric biosensor for ATP determination were developed. In the first two biosensors, two enzymes (hexokinase and glucose oxidase) were immobilized at the surface of platinum disc microelectrodes for amperometric detection. The third biosensor was based on hexokinase immobilized onto gold interdigitated microelectrodes for conductometric detection. In all cases, the enzymes were co-immobilized with bovine serum albumin by cross-linking using glutaraldehyde. Analytical characteristics of the biosensors were determined and different procedures were developed for real samples analysis. The biosensors could be successfully applied to the determination of ATP, glucose, and creatine kinase in pharmaceutical samples and blood serum

Este trabalho fundamentou-se na concepção, desenvolvimento tecnológico, ampliação de escala e avaliação do comportamento de sistema combinado anaeróbio-aeróbio de leito fixo e fluxo ascendente, com recirculação da fase líquida, para tratamento de esgoto sanitário. O reator, em escala piloto, foi construído em formato cilíndrico e confeccionado em fibra de vidro com volume total de aproximadamente 2,5 \'M POT.3\', com intuito de desenvolver um sistema capaz de operar como única unidade de tratamento para remoção de matéria orgânica e nitrogênio, reduzindo a geração de lodo e o consumo de energia pela combinação dos processos anaeróbio e aeróbio, possibilitando o aproveitamento das vantagens de cada um e minimizando seus aspectos negativos. Os melhores resultados operacionais foram encontrados para a etapa com tempo de detenção hidráulica total (TDH) de 12 horas e razão de recirculação (r) igual a 3,0, apresentando eficiências médias de remoção de DQO, \'N\'-NTK e SST de 92 ± 3%; 68 ± 11% e 75 ± 7%, respectivamente, com valores médios efluentes de 54 ± 22 mgDQO/L, 14 ± 10 mg \'N\'-NTK/L e 70 ± 42 mgSST/L. Os valores médios de carga orgânica volumétrica (COV) e carga volumétrica de nitrogênio (CVN) removidas foram de 1,08 ± 0,04 kgDQO/\'M POT.3\'.dia e 0,06 ± 0,02 kgNTK/\'M POT.3\'.dia para esta etapa. A estabilidade operacional durante a etapa com TDH de 12 h, a alta remoção de matéria orgânica e nitrogênio, sem a necessidade de adição de fonte exógena de carbono, para promover o processo de desnitrificação, e de suplementação de alcalinidade consumida durante a nitrificação, e a reduzida necessidade de manutenção devido à tecnologia de fabricação adotada, comprovam a viabilidade técnica de utilização do reator combinado de leito fixo como unidade compacta para pequenas comunidades ou vazões afluentes, para tratamento de esgoto sanitário. / This work was based on design, technology development, scale up and performance evaluation of an up-flow combined anaerobic-aerobic fixed bed system, with recycle of the liquid phase, for treatment of domestic sewage. The pilot scale reactor was built in a fiberglass cylindrical shape with a total volume of approximately 2.5 \'M POT.3\', aiming at the development of a system capable of operate as a single treatment unit for organic matter and nitrogen removal, with low sludge production and energy consumption by the advantages of combination of anaerobic and aerobic processes. The improved operating results were found for the condition with overall hydraulic retention time (HRT) of 12 hours and recycle ratio (r) equal to 3.0, with average removal efficiencies of COD, TKN and TSS of 92 ± 3%, 68 ± 11% and 75 ± 7%, respectively, with average effluent values of 54 ± 22 mgCOD/L, 14 ± 10 mgTKN/L and 70 ± 42 mgTSS/L. The average values of removed organic loading rate (OLR) and nitrogen volumetric loading (NVL) reached 1.06 ± 0.04 kgCOD/\'M POT.3.d and 0.06 ± 0.02 kgTKN/\'\'M POT.3\'.d for this phase. The operational stability during the stage with HRT of 12 h, the high organic matter and nitrogen removal, without addition of exogenous carbon source (electron donor) to promote the denitrification process, with no supplementation of alkalinity consumed during nitrification, and the reduced maintenance due to manufacturing technology adopted, proved the technical feasibility of the combined fixed-bed reactor as a compact unit for small communities or low inflow rates, for treatment of domestic sewage.

The photocatalytic degradation of the wastewater dye pollutant methylene blue (MB) at ZnO nanostructured porous thin films, deposited by direct current reactive magnetron sputtering on Si substrates, was studied. It was observed that over 4 photocatalytic cycles (0.3 mg · l−1 MB solution, 540 minUV irradiation), the rate constant k of MB degradation decreased by ∼50%, varying in the range (1.54 ÷ 0.78) · 10–9 (mol·l−1·min−1). For a deeper analysis of the photodegradation mechanism, detailed information on the nanostructured ZnO surface morphology and local surface and subsurface chemistry (nonstoichiometry) were obtained by using scanning electron microscopy (SEM) and x-ray photoelectron spectroscopy (XPS) as complementary analytical methods. The SEM studies revealed that at the surface of the nanostructured ZnO thin films a coral reef structure containing polycrystalline coral dendrites is present, and that, after the photocatalytic experiments, the sizes of individual crystallites increased, varying in the range 43 ÷ 76 nm for the longer axis, and in the range 28 ÷ 58 nm for the shorter axis. In turn, the XPS studies showed a slight non-stoichiometry, mainly defined by the relative [O]/[Zn] concentration of ca. 1.4, whereas [C]/[Zn] was ca. 1.2, both before and after the photocatalytic experiments. This phenomenon was directly related to the presence of superficial ZnO lattice oxygen atoms that can participate in the oxidation of the adsorbed MB molecules, as well as to the presence of surface hydroxyl groups acting as hole-acceptors to produce OH· radicals, which can be responsible for the generation of superoxide ions. In addition, after experiments, the XPS measurements revealed the presence of carboxyl and carbonyl functional groups, ascribable to the oxidation by-products formed during the photodegradation of MB.

<p>Specific and non-specific interactions of solutes with immobilized biomembranes were studied using chromatographic methods. Liposomes, proteoliposomes and red blood cell (RBC) membrane vesicles were immobilized by a freeze-thawing procedure, whereas whole RBCs were adsorbed in the gel beds using electrostatic interaction, binding to wheat germ agglutinin (WGA) or the streptavidin-biotin interaction. </p><p>Superporous agarose gel with coupled WGA was the most promising matrix for RBC adsorption and allowed frontal chromatographic analyses of the cells for about one week. Dissociation constants for the binding of cytochalasin B and glucose to the glucose transporter GLUT1 were determined under equilibrium conditions. The number of cytochalasin B-binding sites per GLUT1 monomer was calculated and compared to corresponding results measured on free and immobilized membrane vesicles and GLUT1 proteoliposomes. This allowed conclusions about the protein´s binding state <i>in vitro</i> and <i>in vivo</i>. </p><p>Partitioning of drugs into biomembranes was quantified and the system was suggested as a screening method to test for possible intestinal absorption of drug candidates. We also studied how membrane partitioning of drugs is affected by the presence of integral membrane proteins or of charged phospholipids.</p><p>An attempt to combine the theory for specific binding and membrane partitioning of solutes in a single equation is briefly presented. </p>

<p>The human glucose transporter GLUT1 is abundant in red blood cells, the blood-brain barrier and epithelial cells, where it mediates the transport of the energy metabolite, glucose. In the present work some properties of GLUT1, including affinity binding of both substrates and inhibitors, transport rates as well as permeabilities of aromatic amino acids and drug-membrane interactions were analyzed by chromatographic methods.</p><p>Reconstitution by size-exclusion chromatography on Superdex 75 from a detergent with a low CMC that provides monomeric GLUT1 was examined regarding D-glucose- and CB binding as well as D-glucose transport. Upon steric immobilization in Superdex 200 gel beads, residual detergent could be washed away and dissociation constants in the same range as reported for binding to GLUT1 reconstituted from other detergents were obtained. The transport rate into the GLUT1 proteoliposomes was low, probably due to residual detergent. Binding to GLUT1 at different pH was analyzed and the affinity of glucose and GLUT1 inhibitors was found to decrease with increasing pH (5–8.7). The average number of cytochalasin B-binding sites per GLUT1 monomers was, in most cases, approximately 0.4. GLUT1 may work as a functional monomer, dimer or oligomer. To determine whether GLUT1 was responsible for the transport of the aromatic amino acids tyrosine and tryptophan, uptake values and permeabilities of these amino acids into liposomes and GLUT1 proteoliposomes were compared to the permeabilities of D- and L- glucose in the same systems. Dihydrocytochalasin B was identified to be a new inhibitor of tyrosine and tryptophan transport into red blood cells. Ethanol turned out to inhibit the specific binding between CB and GLUT1 and also to decrease the partitioning of CB and drugs into lipid bilayers. A capacity factor for drug partitioning into membranes that allows comparison between columns with different amount of immobilized lipids was validated, and turned out to be independent of flow rate, amount of lipids and drug concentration in the ranges tested.</p>