917 resultados para RUMEN FERMENTATION


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Dietary sources of methylamines such as choline, trimethylamine (TMA), trimethylamine N-oxide (TMAO), phosphatidylcholine (PC) and carnitine are present in a number of foodstuffs, including meat, fish, nuts and eggs. It is recognized that the gut microbiota is able to convert choline to TMA in a fermentation-like process. Similarly, PC and carnitine are converted to TMA by the gut microbiota. It has been suggested that TMAO is subject to ‘metabolic retroversion’ in the gut (i.e. it is reduced to TMA by the gut microbiota, with this TMA being oxidized to produce TMAO in the liver). Sixty-six strains of human faecal and caecal bacteria were screened on solid and liquid media for their ability to utilize trimethylamine N-oxide (TMAO), with metabolites in spent media profiled by Proton Nuclear Magnetic Resonance (1H NMR) spectroscopy. Enterobacteriaceae produced mostly TMA from TMAO, with caecal/small intestinal isolates of Escherichia coli producing more TMA than their faecal counterparts. Lactic acid bacteria (enterococci, streptococci, bifidobacteria) produced increased amounts of lactate when grown in the presence of TMAO, but did not produce large amounts of TMA from TMAO. The presence of TMAO in media increased the growth rate of Enterobacteriaceae; while it did not affect the growth rate of lactic acid bacteria, TMAO increased the biomass of these bacteria. The positive influence of TMAO on Enterobacteriaceae was confirmed in anaerobic, stirred, pH-controlled batch culture fermentation systems inoculated with human faeces, where this was the only bacterial population whose growth was significantly stimulated by the presence of TMAO in the medium. We hypothesize that dietary TMAO is used as an alternative electron acceptor by the gut microbiota in the small intestine/proximal colon, and contributes to microbial population dynamics upon its utilization and retroversion to TMA, prior to absorption and secondary conversion to TMAO by hepatic flavin-containing monooxygenases. Our findings support the idea that oral TMAO supplementation is a physiologically-stable microbiota-mediated strategy to deliver TMA at the gut barrier.

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Acetate is a short chain fatty acid produced as a result of fermentation of ingested fibers by the gut microbiota. While it has been shown to reduce cell proliferation in some cancer cell lines1,2, more recent studies on liver3 and brain4 tumours suggest that acetate may actually promote tumour growth. Acetate in the cell is normally converted into acetyl-coA by two enzymes and metabolized; mitochondrial (ACSS1) and cytosolic (ACSS2) acetyl-coA synthetase. In the mitochondria acetyl-coA is utilized in the TCA cycle. In the cytosol it is utilized in lipid synthesis. In this study, the effect of acetate treatment on the growth of HT29 colon cancer cell line and its mechanism of action was assessed. HT29 human colorectal adenocarcinoma cells were treated with 10mM NaAc and cell viability, cellular bioenergetics and gene expression were investigated. Cell viability was assessed 24 hours after treatment using an MTT assay (Sigma, UK, n=8). Cellular oxygen consumption rate (OCR) and extracellular acidification rate (ECAR) was measured by XFe Analyzer (Seahorse Bioscience, USA). After a baseline reading cells were treated and OCR and ECAR measurements were observed for 18 hours (n=4). Total mRNA was isolated 24 hours after treatment using RNeasy kit (Qiagen, USA). Quantitative PCR reactions were performed using Taqman gene expression assays and Taqman Universal PCR Master Mix (ThermoFisher Scientific, UK) on Applied Biosystems 7500 Fast Real-Time PCR System (Life Technologies, USA) and analysed using ΔΔCt method (n=3). Acetate treatment led to a significant reduction in cell viability (15.9%, Figure 1). OCR, an indicator of oxidative phosphorylation, was significantly increased (p<0.0001) while ECAR, an indicator of glycolysis, was significantly reduced (p<0.0001, Figure 2). Gene expression of ACSS1 was increased by 1.7 fold of control (p=0.07) and ACSS2 expression was reduced to 0.6 fold of control (p=0.06, Figure 3). In conclusion, in colon cancer cells acetate supplementation induces cell death and increases oxidative capacity. These changes together with the trending decrease in ACSS2 expression suggest suppression of lipid synthesis pathways. We hypothesize that the reduced tumor growth by acetate is a consequence of the suppression of ACSS2 and lipid synthesis, both effects reported previously to reduce tumor growth3–5. These effects clearly warrant further investigation.

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O presente trabalho tem como objectivo o diagnóstico ambiental da empresa Lacticinios do Paiva, S.A, a avaliação da água do processo e da ETARI e o estudo da fermentação do soro de queijo com o intuito de produção de bioetanol. No diagnóstico ambiental da empresa, observou-se que 18.227.731 litros de leite usados anualmente geram 5.031 ton/ano de queijo, 7.204 ton/ano de soro de queijo, 74.201 m3/ano de efluente liquido, 14 ton/ano de plástico e 20 ton/ano de cartão. Os principais problemas com necessidade de optimização são a recuperação de água das lavagens, avaliação da produção de biogás no digestor anaeróbio, recuperação do volume de leite que é desperdiçado na produção de queijo fresco de longa duração, avaliação da eficiência energética da empresa, valorização das natas e do soro de queijo. Decidiu-se neste trabalho avaliar a possibilidade de reciclagem das águas de lavagem, avaliar o funcionamento da ETARI face à legislação existente e estudar a possibilidade de valorização do soro de queijo. Na avaliação das águas de processo das lavagens para posterior reciclagem, verifica-se que relativamente ao pH e aos sólidos suspensos não existe problema, podendo encarar-se a hipótese de reciclagem directa. No entanto, no que respeita à carga orgânica das águas de lavagem do sistema de ultrafiltração do queijo fresco de longa duração, constata-se que esta não poderia ser utilizada novamente, uma vez que apresenta valores elevados de CQO. Para a sua reutilização, será necessário remover a CQO, hipótese que se estudou com resultados positivos. Verificou-se que, um tratamento por adsorção em carvão activado precedido de microfiltração, reduz a CQO de forma significativa permitindo admitir a hipótese de reciclagem da água, nomeadamente para as 1ª e 3ª águas de lavagem. As outras águas teriam necessidade de mais tempo de contacto com o carvão activado. No sentido de avaliar o funcionamento da ETARI, foram analisadas várias correntes da mesma, em particular a do efluente final, no que respeita a parâmetros como: pH, Sólidos Suspensos Totais, Carência Química de Oxigénio, Carência Bioquímica de Oxigénio, Turvação, Nitratos, Fósforo Total, Azoto Kjeldalh, Azoto Amoniacal e Cloretos. Observou-se que os valores para o efluente final da ETARI são os seguintes: pH compreendido entre [7,21 – 8,69], SST entre [65,3 – 3110] mg/L, CQO entre [92,5 – 711,5] mg/L, CBO5 entre [58 – 161] mg/L, NO3- entre [10,8 – 106,7] mg/L, fósforo total entre [8,3 – 64,3] mg/L, turvação entre [67,7 – 733,3] FTU e cloretos entre [459,9 – 619,81] mg/L; pode-se dizer que os parâmetros analisados se encontram quase sempre dentro da gama de valores impostos pela Câmara Municipal de Lamego pelo que o efluente pode ser lançado no Colector Municipal de Cambres. Relativamente à fermentação alcoólica do soro de queijo, verifica-se que a levedura Kluyveromyces Marxianus consegue degradar praticamente todo o açúcar presente no permeado produzindo assim uma quantidade razoável de etanol. Quando se utilizou a levedura Saccharomyces Cerevisiae, a produção de etanol foi muito reduzida, como esperado, dado que esta levedura apresenta dificuldades na metabolização da lactose. Constatou-se assim que a melhor levedura para a fermentação do permeado do soro de queijo é a Kluyveromyces Marxianus, estimando-se em 150 mg a produção de etanol por L de soro.

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Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Química e Biológica

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Trabalho Final de Mestrado para obtenção do grau de Mestre em Engenharia Mecânica

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Dissertation presented to obtain the Ph.D degree in Biochemistry

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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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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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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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The maximum amount of ethyl carbamate (EC), a known animal carcinogen produced by the reaction of urea and ethanol, allowed in alcoholic beverages is regulated by legislation in many countries. Wine yeast produce urea by the metabolism of arginine, the predominant assimilable amino acid in must. This action is due to arginase (encoded by CARl). Regulation of CARl, and other genes in this pathway, is often attributed to a well-documented phenomenon known as nitrogen catabolite repression. The effect of the timing of di-ammonium phosphate (DAP) additions on the nitrogen utilization, regulation of CARl, and EC production was investigated. A correlation was found between the timing of DAP addition and the utilization of nitrogen. When DAP was added earlier in the fermentations, less amino nitrogen and more ammonia nitrogen was sequestered from the media by the cells. It was also seen that early DAP addition led to more total nitrogen being used, with a maximal difference of ~25% between fermentations where no DAP was added versus addition at the start of the fermentation. The effect of the timing ofDAP addition on the expression of CARJ during fermentation was analyzed via northern transfer and the relative levels of CARl expression were determined. The trends in expression can be correlated to the nitrogen data and be used to partially explain differences in EC formation between the treatments. EC was quantified at the end of fermentation by GC/MS. In Montrachet yeast, a significant positive correlation was found between the timing of DAP addition, from early to late, and the final EC concentration m the wine (r = 0.9226). In one of the fermentations, EC levels of 30.5 ppb was foimd when DAP was added at the onset of fermentation. A twofold increase (69.5 ppb) was observed when DAP was added after 75% of the sugars were metabolized. When no DAP was added, the ethyl carbamate levels are comparable at a value of 38 ppb. In contrast, the timing of DAP additions do not affect the level EC produced by the yeast ECU 18 in this manner. The study of additional yeast strains shows that the effect of DAP addition to fermentations is strain dependent. Our results reveal the potential importance of the timing of DAP addition to grape must with respect to EC production, and the regulatory effect of DAP additions on the expression of genes in the pathway for arginine metabolism in certain wine yeast strains.

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The high sugar concentration in Icewine juice exerts hyperosmotic stress in the wine yeast causing water loss and cell shrinkage. To counteract the dehydration, yeast synthesize and accumulate glycerol as an internal osmolyte. In a laboratory strain of S. cerevisiae, STLl encodes for Stllp, an H+ /glycerol symporter that is glucose inactivated, but induced upon hyperosmotic stress. STLl, was found to be a highly upregulated gene in Icewine fermenting cells and its expression was 25-fold greater than in yeast cells fermenting diluted Icewine juice, making it one of the most differentially expressed genes between the two fermentation conditions. In addition, Icewine fermenting cells showed a two-fold higher glycerol production in the wine compared to yeast fermenting diluted Icewine juice. We proposed that Stllp is (1) active during Icewine fermentation and is not glucose inactivated and (2) its activity contributes to the limited cell growth observed during Icewine fermentation as a result of the dissipation of the plasma membrane proton gradient. To measure the contribution ofStl1p in active glycerol transport (energy dependent) during Icewine fermentation, we first developed an Stllp-dependent (14C]glycerol uptake assay using a laboratory strain of S. cerevisiae (BY 4742 and LiSTLl) that was dependent on the plasma membrane proton gradient and therefore energy-dependent. Wine yeast K1-Vll16 was also shown to have this energy dependent glycerol uptake induced under salt stress. The expression of STLl and Stllp activity were compared between yeast cells harvested from Icewine and diluted Icewine fermentations. Northern blot analysis revealed that STLl was expressed in cells fermenting Icewine juice but not expressed under the diluted juice conditions. Glycerol uptake by cells fermenting Icewine juice was not significantly different than cells fermenting diluted Icewine juice on day 4 and day 7 of Vidal and Riesling fermentations respectively, despite encountering greater hyperosmotic stress. Furthermore, energy- dependent glycerol uptake was not detected under either fermentation conditions. Because our findings show that active glycerol uptake was not detected in yeast cells harvested from Icewine fermentation, it is likely that Stllp was glucose inactivated despite the hyperosmotic stress induced by the Icewine juice and therefore did not play a role in active glycerol uptake during Icewine fermentation.

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Icewine is a sweet dessert wine fermented from the juice of grapes naturally frozen on the vine. The production of Icewine faces many challenges such as sluggish fermentation, which often yields wines with low ethanol, and an accumulation of high concentration of volatile acidity, mainly in the form of acetic acid. This project investigated three new yeast strains as novel starter cultures for Icewine fermentation with particular emphasis on reducing acetic acid production: a naturally occurring strain of S. bayanus/S. pastorianus isolated from Icewine grapes, and two hybrids between S. cerevisiae and S. bayanus, AWRI 1571 and AWRI 1572. These strains were evaluated for sugar consumption patterns and metabolic production of ethanol, glycerol and acetic acid, and were compared to the performance of a standard commercial wine yeast KI-VI116. The ITS rONA region of the two A WRI crosses was also analyzed during fermentations to assess their genomic stability. Icewine fermentations were performed in sterile filtered juice, in the absence of indigenous microflora, and also in unfiltered juice in order to mirror commercial wine making practices. The hybrid A WRI 1572 was found to be a promising candidate as a novel starter culture for Icewine production. I t produced 10.3 % v/v of ethanol in sterile Riesling Icewine fermentations and 11.2 % v/v in the unfiltered ones within a reasonable fermentation time (39 days). Its acetic acid production per gram sugar consumed was approximately 30% lower in comparison with commercial wine yeast K I -V 1116 under both sterile filtered and unfiltered fermentations. The natural isolate S. bayanus/S. pastorianus and AWRI 1571 did not appear to be suitable for commercial Icewine production. They reached the target ethanol concentration of approximately 10 % v/v in 39 day fermentations and also produced less acetic acid as a function of both time and sugar consumed in sterile fermentations compared to KI-V1116. However, in unfiltered fermentations, both of them failed to produce the target concentration of ethanol and accumulated high concentration of acetic acid. Both A WRI crosses displayed higher loss of or reduced copies in ITS rDNA region from the S. bayanus parent compared to the S. cerevisiae parent; however, these genomic losses could not be related to the metabolic profile.

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The relationships between vine water status, soil texture, and vine size were observed in four Niagara, Ontario Pinot noir vineyards in 2008 and 2009. The vineyards were divided into water status zones using geographic information systems (GIS) software to map the seasonal mean midday leaf water potential (,P), and dormant pruning shoot weights following the 2008 season. Fruit was harvested from all sentinel vines, bulked by water status zones and made into wine. Sensory analysis included a multidimensional sorting (MDS) task and descriptive analysis (DA) of the 2008 wines. Airborne multispectral images, with a spatial resolution of 38 cm, were captured four times in 2008 and three times in 2009, with the final flights around veraison. A semi-automatic process was developed to extract NDVI from the images, and a masking procedure was identified to create a vine-only NDVI image. 2008 and 2009 were cooler and wetter than mean years, and the range of water status zones was narrow. Yield per vine, vine size, anthocyanins and phenols were the least consistent variables. Divided by water status or vine size, there were no variables with differences between zones in all four vineyards in either year. Wines were not different between water status zones in any chemical analysis, and HPLC revealed that there were no differences in individual anthocyanins or phenolic compounds between water status zones within the vineyard sites. There were some notable correlations between vineyard and grape composition variables, and spatial trends were observed to be qualitatively related for many of the variables. The MDS task revealed that wines from each vineyard were more affected by random fermentation effects than water status effects. This was confirmed by the DA; there were no differences between wines from the water status zones within vineyard sites for any attribute. Remotely sensed NDVI (normalized difference vegetation index) correlated reasonably well with a number of grape composition variables, as well as soil type. Resampling to a lower spatial resolution did not appreciably affect the strength of correlations, and corresponded to the information contained in the masked images, while maintaining the range of values of NDVI. This study showed that in cool climates, there is the potential for using precision viticulture techniques to understand the variability in vineyards, but the variable weather presents a challenge for understanding the driving forces of that variability.