981 resultados para RUMINAL FERMENTATION


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To compare two yeast identification methods, i. e, the manual and the VITEK mechanical methods, 62 clinical samples from hemocultures and animal sources were analyzed. After identification as Candida yeasts by the VITEK method, the strains were recharacterized using manual assimilation methods and sugar fermentation tests. Our findings reveal 58% concurrent identification between the two methods for animal strains, and 51% for human hemoculture strains.

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The fecal contamination of raw seafood by indicators and opportunistic pathogenic microorganisms represents a public health concern. The objective of this study was to investigate the presence of enteric bacteria colonizing oysters collected from a Venezuelan touristic area. Oyster samples were collected at the northwestern coast of Venezuela and local salinity, pH, temperature, and dissolved oxygen of seawater were recorded. Total and fecal coliforms were measured for the assessment of the microbiological quality of water and oysters, using the Multiple Tube Fermentation technique. Analyses were made using cultures and 16S rRNA gene sequencing. Diverse enrichment and selective culture methods were used to isolate enteric bacteria. We obtained pure cultures of Gram-negative straight rods with fimbriae from Isognomon alatus and Crassostrea rhizophorae. Our results show that P. mirabilis was predominant under our culture conditions. We confirmed the identity of the cultures by biochemical tests, 16S rRNA gene sequencing, and data analysis. Other enterobacteria such as Escherichia coli, Morganella morganii and Klebsiella pneumoniae were also isolated from seawater and oysters. The presence of pathogenic bacteria in oysters could have serious epidemiological implications and a potential human health risk associated with consumption of raw seafood.

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O presente trabalho tem como objetivo a otimização da etapa de fermentação dos açúcares obtidos a partir da drêche cervejeira para produção do bioetanol através da utilização das leveduras Pichia stipitis NCYC 1541 e Kluyveromyces marxianus NCYC 2791 como agentes fermentativos. O meio de cultura usado para manter as culturas destas leveduras foi Yeast Extract Peptone Dextrose (YEPD). O principal propósito deste trabalho foi o de encontrar alternativas aos combustíveis fósseis, pautando-se por soluções inofensivas para o meio ambiente e sustentáveis. Assim, o trabalho está dividido em quatro etapas: 1) caraterização química e biológica da drêche; 2) pré-tratamento ácido e hidrólise enzimática para primeiramente quebrar as moléculas de lenhina que envolvem os polímeros de celulose e hemicelulose e em seguida romper as ligações poliméricas destas macromoléculas por ação enzimática e transforma-las em açúcares simples, respetivamente, obtendo-se então a glucose, a maltose, a xilose e a arabinose; e, por último, 3) otimização da etapa de fermentação da glucose, maltose e das pentoses que constitui a condição essencial para se chegar à síntese do bioetanol de um modo eficiente e sustentável e 4) a recuperação do bioetanol produzido por destilação fracionada. A quantificação dos açúcares libertados no processo foi feita recorrendo a análises por cromatografia líquida de alta eficiência (HPLC). Neste estudo foram identificados e quantificados cinco açúcares: Arabinose, Glucose, Maltose, Ribose e Xilose. Na etapa de pré-tratamento e hidrólise enzimática foram usados os ácidos clorídrico (HCl) e nítrico (HNO3) com a concentração de 1% (m/m), e as enzimas Glucanex 100g e Ultraflo L. Foram testadas seis condições de pré-tratamento e hidrólise enzimática, alterando os parâmetros tempo de contacto e razão enzimas/massa de drêche, respetivamente, e mantendo a temperatura (50 ºC), velocidade de agitação (75 rpm) e concentração dos ácidos (1% (m/m)). No processamento de 25 g de drêche seca com 0,5 g de Glucanex, 0,5 mL de Ultraflo e um tempo de reação de 60 minutos para as enzimas foi obtida uma eficiência de 15%, em hidrolisado com 6% da celulose. Realizou-se a fermentação do hidrolisado resultante do pré-tratamento ácido e hidrólise enzimática de drêche cervejeira e de meios sintéticos preparados com os açúcares puros, usando as duas estirpes selecionadas para este estudo: Pichia stipitis NCYC 1541 e Kluyveromyces marxianus NYCY 2791. As eficiências de fermentação dos açúcares nos meios sintéticos foram superiores a 80% para ambas as leveduras. No entanto, as eficiências de fermentação do hidrolisado da drêche foram de 45,10% pela Pichia stipitis e de 36,58 para Kluyveromyces marxianus, para um tempo de fermentação de 72 horas e à temperatura de 30 °C. O rendimento teórico em álcool no hidrolisado da drêche é de 0,27 g/g, três vezes maior do que o real (0,0856 g/g), para Pichia stipitis e de 0,19 g/g seis vezes maior do que o real (0,0308 g/g), para a Kluyveromyces marxianus.

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Este trabalho teve como objetivo avaliar e comparar os impactes ambientais da produção do butanol considerando três processos produtivos: um que usa fontes fósseis e dois que usam fontes renováveis, nomeadamente palha de trigo e milho. Para o primeiro caso considerouse o processo oxo e os restantes usaram o processo de produção ABE (acetona, butanol e etanol). Na primeira etapa estudaram-se e descreveram-se os diferentes processos referidos. A análise do ciclo de vida foi depois aplicada efetuando as quatro fases nomeadamente definição do âmbito e objetivo, inventário, avaliação de impactes e interpretação dos resultados obtidos. O inventário foi efetuado tendo em conta a bibliografia existente sobre estes processos e com o auxílio da base de dados Ecoinvent Versão3 Database™. Na avaliação de impactes utilizou-se o método Impact 2002 + (Endpoint). Concluiu-se que a produção do butanol pelo processo ABE utilizando o milho é a que apresenta maior impacte ambiental e a que produção do butanol pelo processo ABE usando a palha de trigo é a que apresenta um menor impacte ambiental, quando o processo de alocação foi efetuado tendo em conta as massas de todos os produtos produzidos em cada processo. Foi efetuada uma análise de sensibilidade para a produção de butanol usando palha de trigo e milho relativa aos dados de menor qualidade. No processo da palha de trigo fez-se variar a quantidade de material enviado para a digestão anaeróbia e a quantidade de efluente produzida. No processo relativo ao milho apenas se fez variar a quantidade de efluente produzida. As variações tiveram um efeito pouco significativo (<1,3%) no impacte global. Por fim, efetuou-se o cálculo dos impactes considerando uma alocação económica que foi executada tendo em conta os preços de venda para o ano 2013 na Europa, para os produtos produzidos pelos diferentes processos. Considerando o valor económico verificou-se um aumento do peso relativo ao butanol, o que fez aumentar significativamente o impacte ambiental. Isto deve-se em grande parte ao baixo valor económico dos gases formados nos processos de fermentação. Se na alocação por massa for retirada a massa destes gases os resultados obtidos são similares nos dois tipos de alocação.

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Dissertation presented to obtain the Ph.D degree in Biology

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

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Dissertação para obtenção do Grau de Mestre em Biotecnologia

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Resumo: Objetivou-se avaliar a degradação in situ da Jurema preta. Foram estimados os valores da degradação potencial e efetiva da matéria seca, proteína bruta e fibra em detergente neutro. A jurema preta apresenta bom potencial de degradação para matéria seca e fibra em detergente neutro, já para a proteína bruta, parece haver necessidade de ação enzimática pós rúmen para que seja melhor aproveitada. [In situ degradability of jurema preta (Mimosa tenuiflora) in thinned and enriched caatinga rangelands]. Abstract: We aimed with this manuscript to present the evaluation of in situ degradability of Jurema preta in thinned and enriched caatinga. Were estimated the potential and effective degradation of dry matter, crude protein and neutral detergent fiber. The jurema preta shrubs have good potential to dry matter and neutral detergent fiber degradation, but to crude protein, to maximize their harnessing the post rumen digestion is needed.

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

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Succinic acid (SA) is a highly versatile building block that is used in a wide range of industrial applications. The biological production of succinic acid has emerged in the last years as an efficient alternative to the chemical production based on fossil fuels. However, in order to fully replace the competing petro-based chemical process from which it has been produced so far, some challenges remain to be surpassed. In particular, one main obstacle would be to reduce its production costs, mostly associated to the use of refined sugars. The present work is focused on the development of a sustainable and cost-e↵ective microbial production process based on cheap and renewable resources, such as agroindustrial wastes. Hence, glycerol and carob pods were identified as promising feedstocks and used as inexpensive carbon sources for the bioproduction of succinic acid by Actinobacillus succinogenes 130Z, one of the best naturally producing strains. Even though glycerol is a highly available carbon source, as by-product of biodiesel production, its consumption by A. succinogenes is impaired due to a redox imbalance during cell growth. However, the use of an external electron acceptor such as dimethylsulfoxide (DMSO) may improve glycerol metabolism and succinic acid production by this strain. As such, DMSO was tested as a co-substrate for glycerol consumption and concentrations of DMSO between 1 and 4% (v/v) greatly promoted glycerol consumption and SA production by this biocatalyst. Aiming at obtaining higher succinic acid yield and production rate, batch and fed-batch experiments were performed under controlled cultivation conditions. Batch experiments resulted in a succinic acid yield on glycerol of 0.95 g SA/g GLY and a production rate of 2.13 g/L.h, with residual production of acetic and formic acids. In fed-batch experiment, the SA production rate reached 2.31 g/L.h, the highest value reported in the literature for A. succinogenes using glycerol as carbon source. DMSO dramatically improved the conversion of glycerol by A. succinogenes and may be used as a co-substrate, opening new perspectives for the use of glycerol by this biocatalyst. Carob pods, highly available in Portugal as a residue from the locust bean gum industry, contain a significant amount of fermentable sugars such as sucrose, glucose and fructose and were also used as substrate for succinic acid production. Sugar extraction from raw and roasted carobs was optimized varying solid/water ratio and extraction time, maximizing sugar recovery while minimizing the extraction of polyphenols. Kinetic studies of glucose, fructose and sucrose consumption by A. succinogenes as individual carbon sources till 30 g/L were first determined to assess possible metabolic diferences. Results showed no significant diferences related to sugar consumption and SA production between the diferent sugars. Carob pods water extracts were then used as carbon source during controlled batch cultivations. (...)

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Polysaccharides are gaining increasing attention as potential environmental friendly and sustainable building blocks in many fields of the (bio)chemical industry. The microbial production of polysaccharides is envisioned as a promising path, since higher biomass growth rates are possible and therefore higher productivities may be achieved compared to vegetable or animal polysaccharides sources. This Ph.D. thesis focuses on the modeling and optimization of a particular microbial polysaccharide, namely the production of extracellular polysaccharides (EPS) by the bacterial strain Enterobacter A47. Enterobacter A47 was found to be a metabolically versatile organism in terms of its adaptability to complex media, notably capable of achieving high growth rates in media containing glycerol byproduct from the biodiesel industry. However, the industrial implementation of this production process is still hampered due to a largely unoptimized process. Kinetic rates from the bioreactor operation are heavily dependent on operational parameters such as temperature, pH, stirring and aeration rate. The increase of culture broth viscosity is a common feature of this culture and has a major impact on the overall performance. This fact complicates the mathematical modeling of the process, limiting the possibility to understand, control and optimize productivity. In order to tackle this difficulty, data-driven mathematical methodologies such as Artificial Neural Networks can be employed to incorporate additional process data to complement the known mathematical description of the fermentation kinetics. In this Ph.D. thesis, we have adopted such an hybrid modeling framework that enabled the incorporation of temperature, pH and viscosity effects on the fermentation kinetics in order to improve the dynamical modeling and optimization of the process. A model-based optimization method was implemented that enabled to design bioreactor optimal control strategies in the sense of EPS productivity maximization. It is also critical to understand EPS synthesis at the level of the bacterial metabolism, since the production of EPS is a tightly regulated process. Methods of pathway analysis provide a means to unravel the fundamental pathways and their controls in bioprocesses. In the present Ph.D. thesis, a novel methodology called Principal Elementary Mode Analysis (PEMA) was developed and implemented that enabled to identify which cellular fluxes are activated under different conditions of temperature and pH. It is shown that differences in these two parameters affect the chemical composition of EPS, hence they are critical for the regulation of the product synthesis. In future studies, the knowledge provided by PEMA could foster the development of metabolically meaningful control strategies that target the EPS sugar content and oder product quality parameters.

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Marine ecosystem can be considered a rather exploited source of natural substances with enormous bioactive potential. In Mexico macro-algae study remain forgotten for research and economic purposes besides the high amount of this resource along the west and east coast. For that reason the Bioferinery Group of the Autonomous University of Coahuila, have been studying the biorefinery concept in order to recover high value byproducts of Mexican brown macro-algae including polysaccharides and enzymes to be applied in food, pharmaceutical and energy industry. Brown macroalgae are an important source of fucoidan, alginate and laminarin which comprise a complex group of macromolecules with a wide range of important biological properties such as anticoagulant, antioxidant, antitumoral and antiviral and also as rich source of fermentable sugars for enzymes production. Additionally, specific enzymes able to degrade algae matrix (fucosidases, sulfatases, aliginases, etc) are important tools to establish structural characteristics and biological functions of these polysaccharides. The aims of the present work were the integral study of bioprocess for macroalgae biomass exploitation by the use of green technologies as hydrothermal extraction and solid state fermentation in order to produce polysaccharides and enzymes (fucoidan and fucoidan hydrolytic enzymes). This work comprises the use of the different bioprocess phases in order to produce high value products with lower time and wastes.

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Thermal degradation upon melting is one of the major drawbacks reported for polyhydroxyalkanoates (PHA). However, the role of residues originating from the fermentation and the extraction steps on the thermal stability of this class of biopolymers still needs to be clarified. In the particular case of PHA produced from mixed microbial cultures (MMC), this topic is even less documented in the literature. Here, two polyhydroxy(butyrate-co-valerate) (PHBV) produced from MMC enriched in PHA accumulating organisms and fed with cheese whey were studied. A micro extrusion line is used to produce filaments and assess the processability and the degradation of processed PHBV. The prototype micro extrusion line allows for studying grams of materials. The two PHBV contain 18 mol% HV. PHBV was recovered with 11 wt% residues, and further submitted to a purification procedure resulting in a second biopolyester containing less than 2 wt% impurities. The thermorheological characterization of the two PHBV is first presented, together with their semicrystalline properties. Then the processing windows of the two biopolyesters are presented. Finally, the properties of extruded filaments are reported and the thermomechanical degradation of PHBV is extensively studied. The structure was assessed by wide angle X-ray diffraction, mechanical and rheological properties are reported, thermal properties are studied with differential scanning calorimetry and thermogravimetric analysis, whereas Fourier Transform Infrared spectroscopy was used to assess the impact of the extrusion on PHBV chemical structure. All results obtained with the two PHBV are compared to assess the effects of residues on both PHBV processability and degradation.

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This study focuses on the optimization of cheese whey formulated media for the production of hyaluronic acid HA by Streptococcus zooepidemicus. Culture media containing whey (W; 2.1 g/L) or whey hydrolysate (WH; 2.4 g/L) gave the highest HA productions. Both W and WH produced high yields on protein consumed, suggesting cheese whey is a good nitrogen source for S. zooepidemicus production of HA. Polysaccharide concentrations of 4.0 g/L and 3.2 g/L were produced in W and WH in a further scale-up to 5 L bioreactors, confirming the suitability of the low-cost nitrogen source. Cheese whey culture media provided high molecular weight (> 3000 kDa) HA products. This study revealed replacing the commercial peptone by the low-cost alternative could reduce HA production costs by up to a 70%compared to synthetic media.

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Tese de Doutoramento em Biologia Ambiental e Molecular