Dimensionamento de um reactor de leito fluidizado para gasificação de biomassa

Na actualidade, quando se procura a diversificação energética, em especial de fontes renováveis, a gasificação surge como uma forma promissora de aproveitamento da biomassa, nomeadamente dos resíduos florestais, para a geração de energia eléctrica. Neste contexto, passou-se em revista as diversas formas de gasificação, a sua evolução histórica e os diversos tipos de reactores com as suas vantagens e desvantagens. De igual forma, foram analisadas as disponibilidades e características da biomassa no mundo e em Portugal, destacando-se as suas potencialidades e as dificuldades no seu aproveitamento. Fez-se o dimensionamento de um reactor-gasificador de leito fluidizado borbulhante à escala piloto, bem como dos equipamentos complementares, sistema de alimentação, ventilador, ciclone, filtro para o gás produzido e gerador eléctrico. As dimensões dum reactor para trabalhos laboratoriais foram determinadas por cálculo das condições hidrodinâmicas, que, também, permitiram calcular o caudal de ar a utilizar. Por balanços materiais, considerando-se uma composição experimental do gás de síntese citada na literatura, determinou-se uma possível composição da alimentação e um caudal de alimentação.

Biofiltration of Air/Styrene and Air/Styrene/Acetone mixtures in a bubble column reactor

The goal of this work was the treatment of polluted waste gases in a bubble column reactor (BCR), in order to determinate the maximum value of reactor’s efficiency (RE), varying the inlet concentration (C in) of the pollutants. The gaseous mixtures studied were: (i) air with styrene and (ii) air with styrene and acetone. The liquid phase used to contain the biomass in the reactor was a basal salt medium (BSM), fundamental for the microorganisms’ development. The reactor used in this project consists of a glass column of 620mm height and inside diameter 75mm. In all essays there were continually measured: pH, dissolved oxygen and liquid’s temperature. Temperature and pH were controlled (T=24ºC, 7.0 ≤ pH ≤ 7.7). In all experiments the liquid volume (including the biomass) used in the reactor was kept constant (1.5L) as well as the total gas flowrate (1 L/min). Concerning the goal of the work, some parameters were calculated: the organic load (OL), removal efficiency (RE), elimination capacity (EC), biomass concentration (xf) and dry biomass concentration (Xdw). In a first series of experiments, the gas mixture used was air with styrene, varying its concentration from 191 mg.m-3 to 6500 mg.m-3.It was concluded that the RE maximum value (97%) was obtained for C in Sty = 4200 mg.m-3. For the maximum tested value of C in Sty, RE obtained was 20%. In a second step, the gaseous mixture included acetone, varying C in Sty between 225 mg.m-3 and 2659 mg.m-3 and C in Ac between 153mg.m-3 and 1389 mg.m-3. The aim of these tests was the determination of C in Ac for which RE was maximum, obtaining C in Ac = 750 mg.m-3. A third series of experiments was performed, in which C in Ac was maintained equal to that value and C in Sty was varied until higher values (5422 mg.m-3). RE maximum values obtained in this last series were 100% for styrene and 40% for acetone. One important conclusion is the fact that the microorganisms available degrade better styrene than acetone. On the ambit of this study, it was possible to identify the species available in biomass: Xanthobacter antotrophicus py2, Enterobacter aerogenes, Nocardia, Corynebacterium Spp., Rhodococcus rhodochrous e Pseudomonas Sp.

Contribuição para o estudo da influência do dióxido de carbono no processo de biodegradação (reactor fed-batch proporcional)

O reactor “Fed-batch” Proporcional utiliza o aumento de pressão que se verifica no interior do reactor, provocado pela acumulação do dióxido de carbono produzido no decurso da degradação aeróbia de um composto orgânico, para adicionar substrato ao reactor, sendo a alimentação proporcional à velocidade ou taxa de degradação de substrato. Nestas circunstâncias, e pretendendo-se avaliar da fiabilidade daquele tipo de reactor, era necessário verificar se a reacção biológica era perturbada pela acumulação de dióxido de carbono. Assim, o presente trabalho teve por objectivo estudar a influência do dióxido de carbono, dissolvido na solução de fermentação, no crescimento microbiano e no consumo de substrato, através da comparação do funcionamento, em paralelo, de dois reactores “fed-batch”, sendo um proporcional e outro aberto. Constatou-se que os valores das constantes cinéticas, taxa específica de consumo de substrato (qobs) e coeficiente de rendimento celular (Y(X/S)), determinados no reactor “Fed-batch” Proporcional e num reactor “Fed-batch” Aberto, operados em condições equivalentes, eram semelhantes. Os valores da taxa de crescimento específica (μobs) apresentam diferenças mais significativas, no entanto a maioria dos testes estatísticos não-paramétricos aplicados demonstraram que o conjunto de valores de cada reactor pertencem à mesma distribuição. A taxa de consumo de oxigénio (OUR), que reflecte a viabilidade da biomassa, é normalmente superior no reactor “Fed-batch” Aberto. Os resultados obtidos no presente estudo não evidenciaram efeitos inibidores, para a reacção biológica, provocados pelo dióxido de carbono dissolvido, ou pelos iões bicarbonato que se acumulam no reactor “Fed-batch” Proporcional.

Inhibition of Aspergillus fumigatus and its biofilm by Pseudomonas aeruginosa is dependent on the source, phenotype and growth conditions of the bacterium

Aspergillus fumigatus (Af) and Pseudomonas aeruginosa (Pa) are leading fungal and bacterial pathogens, respectively, in many clinical situations. Relevant to this, their interface and co-existence has been studied. In some experiments in vitro, Pa products have been defined that are inhibitory to Af. In some clinical situations, both can be biofilm producers, and biofilm could alter their physiology and affect their interaction. That may be most relevant to airways in cystic fibrosis (CF), where both are often prominent residents. We have studied clinical Pa isolates from several sources for their effects on Af, including testing involving their biofilms. We show that the described inhibition of Af is related to the source and phenotype of the Pa isolate. Pa cells inhibited the growth and formation of Af biofilm from conidia, with CF isolates more inhibitory than non-CF isolates, and non-mucoid CF isolates most inhibitory. Inhibition did not require live Pa contact, as culture filtrates were also inhibitory, and again non-mucoid>mucoid CF>non-CF. Preformed Af biofilm was more resistant to Pa, and inhibition that occurred could be reproduced with filtrates. Inhibition of Af biofilm appears also dependent on bacterial growth conditions; filtrates from Pa grown as biofilm were more inhibitory than from Pa grown planktonically. The differences in Pa shown from these different sources are consistent with the extensive evolutionary Pa changes that have been described in association with chronic residence in CF airways, and may reflect adaptive changes to life in a polymicrobial environment.

Mapping and characterization of a green biofilm inside of Vilar de Frades Church (Portugal)

Vilar de Frades church is integrated in the Vilar de Frades Monastery, located in the North part of Portugal (Barcelos). The monastery, founded in 566, suffered several architectural modifications and restoration works, the most relevant was in the XVI century. The church, in granite, has one nave and six bays,holding ten chapels with vaults of crossed ribbings. Nowadays, the chapels present a severe biological colonization characterised by an intense green biofilm, which becoming apparent in other locations inside the church. In the course of a general survey concerning the conservation state of the church, an accurate campaign was planned in order to assess the main biodeterioration agents, map biological colonization and determine the environmental conditions. Laboratory analyses were accomplished with optical microscopy and spectrofluorometry. This study presents the results of this campaign. Details on conservation or preservation works that need to be implemented are also presented.

Monitoring the ex-vivo expansion of human mesenchymal stem/stromal cells in xeno-free microcarrier-based reactor systems by MIR spectroscopy

Human mesenchymal stem/stromal cells (MSCs) have received considerable attention in the field of cell-based therapies due to their high differentiation potential and ability to modulate immune responses. However, since these cells can only be isolated in very low quantities, successful realization of these therapies requires MSCs ex-vivo expansion to achieve relevant cell doses. The metabolic activity is one of the parameters often monitored during MSCs cultivation by using expensive multi-analytical methods, some of them time-consuming. The present work evaluates the use of mid-infrared (MIR) spectroscopy, through rapid and economic high-throughput analyses associated to multivariate data analysis, to monitor three different MSCs cultivation runs conducted in spinner flasks, under xeno-free culture conditions, which differ in the type of microcarriers used and the culture feeding strategy applied. After evaluating diverse spectral preprocessing techniques, the optimized partial least square (PLS) regression models based on the MIR spectra to estimate the glucose, lactate and ammonia concentrations yielded high coefficients of determination (R2 ≥ 0.98, ≥0.98, and ≥0.94, respectively) and low prediction errors (RMSECV ≤ 4.7%, ≤4.4% and ≤5.7%, respectively). Besides PLS models valid for specific expansion protocols, a robust model simultaneously valid for the three processes was also built for predicting glucose, lactate and ammonia, yielding a R2 of 0.95, 0.97 and 0.86, and a RMSECV of 0.33, 0.57, and 0.09 mM, respectively. Therefore, MIR spectroscopy combined with multivariate data analysis represents a promising tool for both optimization and control of MSCs expansion processes.

INVESTIGATION OF BIOFILM FORMATION IN COAGULASE-NEGATIVE STAPHYLOCOCCI ISOLATED FROM PLATELET CONCENTRATE BAGS

Platelet Concentrates (PCs) are the blood components with the highest rate of bacterial contamination, and coagulase-negative staphylococci (CoNS) are the most frequently isolated contaminants. This study investigated the biofilm formation of 16 contaminated units out of 691 PCs tested by phenotypic and genotypic methods. Adhesion in Borosilicate Tube (ABT) and Congo Red Agar (CRA) tests were used to assess the presence of biofilm. The presence of icaADC genes was assessed by means of the Polymerase Chain Reaction (PCR) technique. With Vitek(r)2, Staphylococcus haemolyticus was considered the most prevalent CoNS (31.25%). The CRA characterized 43.8% as probable biofilm producers, and for the ABT test, 37.5%. The icaADC genes were identified in seven samples by the PCR. The ABT technique showed 85.7% sensitivity and 100% specificity when compared to the reference method (PCR), and presented strong agreement (k = 0.8). This study shows that species identified as PCs contaminants are considered inhabitants of the normal skin flora and they might become important pathogens. The results also lead to the recommendation of ABT use in laboratory routine for detecting biofilm in CoNS contaminants of PCs.

BIOFILM FORMATION OF Vibrio cholerae ON STAINLESS STEEL USED IN FOOD PROCESSING

Vibrio cholerae represents a significant threat to human health in developing countries. This pathogen forms biofilms which favors its attachment to surfaces and its survival and transmission by water or food. This work evaluated the in vitro biofilm formation of V. cholerae isolated from clinical and environmental sources on stainless steel of the type used in food processing by using the environmental scanning electron microscopy (ESEM). Results showed no cell adhesion at 4 h and scarce surface colonization at 24 h. Biofilms from the environmental strain were observed at 48 h with high cellular aggregations embedded in Vibrio exopolysaccharide (VPS), while less confluence and VPS production with microcolonies of elongated cells were observed in biofilms produced by the clinical strain. At 96 h the biofilms of the environmental strain were released from the surface leaving coccoid cells and residual structures, whereas biofilms of the clinical strain formed highly organized structures such as channels, mushroom-like and pillars. This is the first study that has shown the in vitro ability of V. cholerae to colonize and form biofilms on stainless steel used in food processing.

Acidogenic digestion of effluents of the cheese industry in packed bed biofilm reactors

Dissertation for the Master degree in Biotechnology

Acetalização de glicerol e fenilacetaldeído assistida por pervaporação em reactor de membrana catalítica

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

Contribuição para o estudo da modelação da digestão anaeróbia de resíduos sólidos, estudo da influência da geometria do reactor na cinética do processo

O presente trabalho tem como objectivo contribuir para o estudo do desenvolvimento de um modelo matemático aplicado à digestão anaeróbia de resíduos sólidos, que incorpore os condicionamentos da geometria dos reactores e a sua influência na cinética do processo biológico. Nesse sentido, o trabalho propõe-se avaliar o comportamento cinético de três reactores, com o mesmo volume mas com diferentes relações tridimensionais, utilizando o mesmo substrato, e idênticos parâmetros ambientais e operacionais de funcionamento. Pretendeu-se estudar em que medida a relação do comprimento, largura e altura de um reactor pode interferir nas taxas de remoção de substrato, condicionando a respectiva difusão na biomassa e crescimento dos microrganismos. Considera-se que este aspecto é do maior interesse para o desenvolvimento de um modelo cinético, podendo minimizar desvios inerentes à própria modelação de processos biológicos complexos. A geometria do reactor, que se correlaciona com uma determinada relação tridimensional, pode constituir um parâmetro importante, que se designou por Kcig (Constante de Inibição Geométrica), dada a influência que poderá exercer na cinética do processo biológico. A sua avaliação, parametrização e consequente modelação, deverá facilitar a escolha da relação comprimento/largura/altura mais adequada, de forma a optimizar o funcionamento operacional do reactor. O plano experimental desenvolveu-se em duas fases, utilizando-se dois substratos com graus distintos de dificuldade de utilização pelos microrganismos, nomeadamente: Fase 1 (glucose), Fase 2 (FORSU e relva). Concluiu-se que a cinética do processo é influenciada pela relação entre as áreas de separação de biogás/biomassa (As) e de contacto biomassa/reactor (Ac), que interferem na geometria do reactor. Assim, através dos resultados das fases 1 e 2 pode observar-se que a variação da taxa de remoção de substrato se aproxima de uma função de saturação, pelo que se propõe uma adaptação do modelo de Monod, através de um formalismo que incorpora uma grandeza adimensional, Kcig, para reflectir o efeito da geometria do reactor. Verificou-se que a equação adoptada para Kcig se mostrou adequada, o que permitiu, através do modelo de Monod ajustado, estimar os valores de rx máx e Ks que se admite estarem mais próximos dos verdadeiros, embora se considere que apenas se pretende corrigi-los em função do efeito da geometria do reactor. Por outro lado, o estudo permitiu identificar um valor de Kcig para o reactor de 2,5 L, a partir do qual poderá não ser interessante a relação entre a taxa de remoção de substrato e a área de construção do reactor.

Metanólise de óleo de soja em biodiesel através de um reactor de membrana

Com o aumento das necessidades energéticas, bem como dos cada vez mais conhecidos efeitos nocivos dos combustíveis fósseis, tornou-se imperativo pesquisar e desenvolver alternativas sustentáveis e verdes a esses recursos. O biodiesel é considerado como o melhor substituto para o combustível diesel convencional de base petroquímica. A transesterificação de óleos vegetais revela-se como uma importante via de obtenção do biodiesel. Na produção de biodiesel com catalisadores básicos homogéneos, como o hidróxido de sódio, deparamo-nos com um problema na hidrólise de triglicéridos, levando à formação de sabões e emulsões. Mesmo quando são usados reagentes secos, há formação de água devido à reacção do hidróxido com o álcool. Estes problemas podem ser solucionados com a utilização de catalisadores heterogéneos. Este estudo incidiu na preparação de membranas catalíticas de álcool polivinílico (PVA) incorporadas com um catalisador heterogéneo sólido básico (óxido de cálcio) obtido de resíduos industriais (casca de ovo). Caracterizaram-se as membranas catalíticas através da determinação da espessura, ângulos de contacto, grau de inchamento e espectroscopia de infravermelho. As membranas de PVA foram testadas na metanólise de óleo de soja em reactor batch e reactor de membrana catalítica. Estudou-se o efeito da reticulação química e por irradiação gama, nas propriedades das membranas e na actividade catalítica.

Projecto de um bio-reactor para cultura celular em membranas tubulares

O Grupo de Engenharia de Tecidos da FCT/UNL desenvolve e produz membranas poliméricas tubulares biodegradáveis que servem de substrato a culturas celulares e que se destinam a substituir temporariamente vasos sanguíneos danificados. O objectivo desta dissertação foi o desenvolvimento de um bio-reactor com a capacidade de bombeamento controlado de um fluido adequado à manutenção de uma cultura celular, que simula a passagem do fluxo sanguíneo pelo interior das membranas tubulares, permitindo que as células nelas semeadas recebam os estímulos adequados ao seu desenvolvimento. Foi construído um bio-reactor de perfusão pulsátil para cultura celular em membranas tubulares que é instalável numa incubadora, beneficiando assim de condições ambientais — pH, temperatura e humidade — semelhantes às fisiológicas. O bio-reactor é capaz de gerar estímulos mecânicos pulsáteis favoráveis ao alinhamento de células endoteliais e de músculo liso. O sistema foi desenvolvido de modo a que a pressão e o caudal aplicados às membranas pudessem ser monitorizados e controlados. Foram semeadas células endoteliais em matrizes planas de policaprolactona, tendo-se confirmado a sua adesão e proliferação por microscopia de fluorescência. Após enrolamento, obtiveram-se duas membranas tubulares com células endoteliais semeadas no lúmen. Uma delas foi submetida a cultura estática, e outra a cultura dinâmica no bio-reactor. Após 10 dias de condicionamento in vitro, as membranas foram novamente observadas por microscopia de fluorescência. Os resultados obtidos não foram conclusivos, pelo que serão necessários novos estudos para concluir se o bio-reactor construído é capaz de garantir o condicionamento mecânico das células semeadas nas matrizes.

Rifampicin fails to eradicate mature biofilm formed by methicillin-resistant Staphylococcus aureus

INTRODUCTION: Antimicrobial activity on biofilms depends on their molecular size, positive charges, permeability coefficient, and bactericidal activity. Vancomycin is the primary choice for methicillin-resistant Staphylococcus aureus (MRSA) infection treatment; rifampicin has interesting antibiofilm properties, but its effectivity remains poorly defined. METHODS: Rifampicin activity alone and in combination with vancomycin against biofilm-forming MRSA was investigated, using a twofold serial broth microtiter method, biofilm challenge, and bacterial count recovery. RESULTS: Minimal inhibitory concentration (MIC) and minimal bactericidal concentration for vancomycin and rifampicin ranged from 0.5 to 1mg/l and 0.008 to 4mg/l, and from 1 to 4mg/l and 0.06 to 32mg/l, respectively. Mature biofilms were submitted to rifampicin and vancomycin exposure, and minimum biofilm eradication concentration ranged from 64 to 32,000 folds and from 32 to 512 folds higher than those for planktonic cells, respectively. Vancomycin (15mg/l) in combination with rifampicin at 6 dilutions higher each isolate MIC did not reach in vitro biofilm eradication but showed biofilm inhibitory capacity (1.43 and 0.56log10 CFU/ml reduction for weak and strong biofilm producers, respectively; p<0.05). CONCLUSIONS: In our setting, rifampicin alone failed to effectively kill biofilm-forming MRSA, demonstrating stronger inability to eradicate mature biofilm compared with vancomycin.

Antibacterial, anti-swarming and anti-biofilm formation activities of Chamaemelum nobile against Pseudomonas aeruginosa

AbstractINTRODUCTION:Chamomile ( Chamaemelum nobile ) is widely used throughout the world, and has anti-inflammatory, deodorant, bacteriostatic, antimicrobial, carminative, sedative, antiseptic, anti-catarrhal, and spasmolytic properties. Because of the increasing incidence of drug-resistant bacteria, the development of natural antibacterial sources such as medical herbs for the treatment of infectious diseases is necessary. Extracts from different plant parts such as the leaves, flowers, fruit, and bark of Combretum albiflorum, Laurus nobilis , and Sonchus oleraceus were found to possess anti-quorum sensing (QS) activities. In this study, we evaluated the effect of C. nobile against Pseudomonas aeruginosa biofilm formationMETHODS:The P. aeruginosa samples were isolated from patients with different types of infection, including wound infection, septicemia, and urinary tract infection. The flowers of C. nobile were dried and the extract was removed using a rotary device and then dissolved in dimethyl sulfoxide at pH 7.4. The microdilution method was used to evaluate the minimum inhibitory concentration (MIC) of this extract on P. aeruginosa , and biofilm inhibition was assayed.RESULTS:Eighty percent of the isolated samples (16/20) could form a biofilm, and most of these were isolated from wound infections. The biofilm inhibitory concentration of the C. nobile extract was 6.25-25mg/ml, whereas the MIC was 12.5-50mg/ml.CONCLUSIONS:The anti-QS property of C. nobile may play an important role in its antibacterial activity, thus offering an additional strategy in the fight against bacterial infections. However, molecular investigation is required to explore the exact mechanisms of the antibacterial action and functions of this phytocompound.