O trabalho é proposto visando melhorar o consumo de xilose na bactéria Burkholderia sacchari utilizando o acúmulo de PHB como modelo de produção Foi desenvolvido um processo de evolução por meio da aplicação de feast and famine e Cultivos sequenciais em fase exponencial. Foi obtida uma linhagem mutante com uma velocidade especifica de crescimento de 0,24 h -1. Foi feita uma análise de fluxos metabólicos da qual foi possível concluir que o metabolismo da xilose acontecia em sua maioria pela VP junto com a ED. Foi feito um ensaio de acumulo com carbono marcado utilizando uma solução de xilose, de 20:80 de xilose marcada 13C em todos os carbonos e xilose não marcado, para determinar quais seriam as possíveis vias metabólicas no uso da xilose por parte de B. sacharia LFM 101 e da linhagem evoluída BSEV11. Foi determinado que houve embaralhamento de carbonos, fato que só acontece quando o metabolismo da xilose e feito pela VP junto com a via ED, assim foi possível conferir a via ED como principal via para o metabolismo da xilose em B. sacchari LFM 101. / To evaluate the possibilities of improving the productivity of PHA production from xylose, evolutionary engineering techniques were applied to B. sacchari to select cells with maximum specific growth rates (max) higher than the wild type. Metabolic flux analysis was also performed to evaluate the fluxes through central pathways and the possibility of further improvements by modifying fluxes rates. The evolved strain reached a max of 0.24 ± 0.01 h-1 at the end of the evolutionary process. Strains were submitted to bioreactor experiments. A metabolic network of the strain was usedn to determine the possible distribution of metabolic fluxes. A total of 19 elementary modes were obtained. It was concluded that the metabolism of xylose occurred mostly by VP along with the ED. The ED pathway has the major activity going on in a cyclic way. It was also performed a 13C labeled xylose assay, in which it was possibly to confirm the obtained results from the metabolic flux analyses.

Indiana University-Purdue University Indianapolis (IUPUI) / Metabolic flux analyses and their more comprehensive forms, genome-scale metabolic networks (GSMNs), have gained tremendous attention in industrial and medical research. Saccharomyces cerevisiae (S. cerevisiae) is one of the organisms that has had its GSMN subjected to multiple frequent updates. The objective of this study is to develop a visualization tool for the GSMN of S. cerevisiae for educational and research purposes. This visualization tool is called the Master Metabolic Map of Saccharomyces cerevisiae (MMMSC). In this study, a metabolic database of S. cerevisiae developed by us was transferred to Cytoscape, a useful and efficient bioinformatics software platform for visualizing molecular networks. After the MMMSC was created, nodes, representing metabolites and enzymes, and edges, representing the chemical reactions that connect the nodes, were curated manually to develop a metabolic visualization map of the whole metabolic system of S. cerevisiae (Figure 4). In the discussion, examples are provided regarding possible applications of MMMSC to predict possible effects of the manipulation of the S. cerevisiae metabolome for industrial and medical purposes. Ultimately, it is concluded that further work is needed to complete the metabolic database of S. cerevisiae and the related MMMSC. In future studies, these tools may be integrated with other omics and other approaches, especially the directed-evolution approach, to increase cost and time efficiency of future research and to find solutions for complex and, thus far, poorly managed environmental and health problems.

Les approches thérapeutiques à base d’anticorps monoclonaux font partie des avenues les plus encourageantes pour le traitement de nombreux cancers. Les cellules ovariennes de hamster chinois (CHO) demeurent la plateforme d’expression d’anticorps la plus couramment utilisée dans l’industrie et est actuellement la plus efficace pour la production à grande échelle. Ces cellules sont capables de produire des anticorps présentant un patron de glycosylation très proche du profil humain et d’atteindre des niveaux de production généralement plus élevés que ceux obtenus avec les autres lignées cellulaires continues existantes. Ces dernières années, les progrès accomplis dans le développement de procédés en cuvée alimentée (fed-batch) ont permis d’augmenter significativement les rendements de production. Néanmoins, les performances des procédés de culture demeurent limitées par les caractéristiques métaboliques des cellules utilisées. Celles-ci présentent en effet une glycolyse et une glutaminolyse dérégulées associées à une forte production de métabolites toxiques tels que le lactate et les ions ammonium. Seule une fraction minime du pyruvate issu de la métabolisation du glucose est incorporée dans le cycle des acides tricarboxyliques (ATC), ce qui explique en partie le métabolisme peu efficace des cellules CHO. Une des enzymes responsables de la connexion entre la glycolyse et le cycle des ATC est la pyruvate carboxylase qui catalyse la conversion du pyruvate en oxaloacétate. Dans les cellules CHO, seulement 5 à 10 % du pyruvate est métabolisé par cette enzyme. Ce projet de recherche s’appuie sur l’hypothèse selon laquelle contrer la déficience de l’activité de la pyruvate carboxylase dans les cellules CHO pourrait pallier en partie au phénomène de dérégulation de la glycolyse, ce qui permettrait d’améliorer la productivité d’anticorps des cellules tout en maintenant une glycosylation adéquate du produit final. Au cours de ces travaux, une lignée cellulaire exprimant de façon stable l’enzyme pyruvate carboxylase de levure, au niveau cytosolique (PYC2) a été générée. Cultivées en mode cuvée alimentée, ces cellules ont montré une croissance et une production d’anticorps améliorées par rapport à la lignée parentale non modifiée. L’analyse des flux métaboliques par marquage isotopique a permis de caractériser en détail le métabolisme de ces cellules. Des différences majeures dans la distribution des flux métaboliques intracellulaires notamment au niveau des flux associés à la lactate déshydrogénase et au cycle de Krebs ont été mises en évidence. L’analyse de la glycosylation a révélé pour sa part, que l’augmentation de la production d’anticorps associée à la modification du métabolisme n’avait pas altéré significativement la qualité du produit final. De façon générale, ce projet de recherche semble corroborer l’existence d’un lien entre la productivité d’anticorps et le métabolisme cellulaire. La caractérisation du métabolisme des cellules CHO et plus précisément du métabolisme du lactate participe à améliorer notre compréhension du métabolisme des cellules CHO et pourrait permettre une amélioration plus rationnelle des fonctions cellulaires d’une part, et des conditions de culture d’autre part. / Antibody-based therapy is a promising approach for cancer treatment. Chinese hamster ovary (CHO) cells represents the most common and efficient antibody expression platform for large scale production. Their abilities to perform human-like glycosylation and produce high antibody titer make them the most suitable system compared to other continuous cell lines. In the past few years, advances in fed-batch process development led to significantly increase production yields. Nevertheless, the metabolic features of continuous cell lines constitute a hurdle to the improvement of process performances. Continuous cell lines typically exhibit a deregulated glycolysis and glutaminolysis causing the accumulation of toxic metabolites such as lactate and ammonia. Thus, only a small percentage of pyruvate, derived from glucose, is incorporated into the tricarboxylic acids (TCA) cycle explaining at least, in part the inefficient CHO cell metabolism. The mitochondrial pyruvate carboxylase, which catalyzes the conversion of pyruvate into oxaloacetate, is one of the key enzymes at the junction of the glycolysis and the TCA cycle. In CHO cells, only 5-10 % of the pyruvate pool is metabolized via this pathway. In this project, we hypothesized that counteracting the pyruvate carboxylase deficiency in CHO cells could alleviate in part, the deregulated glycolysis and consequently improve antibody production yield while maintaining satisfactory antibody glycosylation. In this work, a recombinant CHO cell line producing an antibody was further genetically modified with the insertion of a cytoplasmic yeast pyruvate carboxylase (PYC2) gene. Cultivated in fed-batch mode, PYC2 cells exhibited enhanced cell growth and antibody production yield compared to the parental cell line. Metabolic flux analysis using isotopic tracer led to a detailed characterisation of both cell line metabolism. The metabolic flux distribution obtained highlighted major differences in lactate and TCA fluxes. Comparative glycosylation analysis revealed that the metabolism alteration associated with the increase in antibody production did not significantly alter the product quality. This work seems to corroborate the presumed existence of a link between metabolism and antibody productivity. The cell metabolism characterization and more precisely, lactate production contribute to gain knowledge in CHO cell metabolism and led to rationally improve cellular functions and culture conditions.

L'élucidation des propriétés du réseau métabolique est fondamentale pour la compréhension du fonctionnement cellulaire et pour l'élaboration de stratégies d'ingénierie métabolique. L'objectif de cette thèse était de mieux comprendre la régulation du métabolisme du NADPH, un métabolite "hub" qui joue un rôle central dans de nombreux processus cellulaires, chez Saccharomyces cerevisiae en fermentation. Nous avons utilisé une démarche systématique couplant modélisation et approches multi-“omics” pour étudier de façon quantitative la réponse à une perturbation de la demande en NADPH. Un système expérimental original, basé sur l'expression d'une butanediol déshydrogénase modifiée NADPH-dépendante a été utilisé pour augmenter de façon contrôlée la demande en NADPH. L'utilisation de ce dispositif, le développement et l'utilisation d'un modèle stœchiométrique de la levure dédié à la fermentation ont permis de prédire la répartition des flux pour différents niveaux de perturbation. Ces analyses ont montré, en premier lieu, la très grande capacité de la levure à faire face à des demandes très importantes de NADPH représentant jusqu'à 40 fois la demande anabolique. Pour des demandes modérées (allant jusqu'à 20 fois la demande anabolique), la perturbation est principalement compensée par une augmentation du flux à travers la voie des pentoses phosphate (VPP) et à moindre titre à travers la voie acétate (Ald6p). Pour une forte demande en NADPH, correspondant à 40 fois la demande anabolique, le modèle prédit la saturation de la VPP ainsi que la mise en place du cycle glycérol-DHA, qui permet l'échange du NADH en NADPH. Des analyses fluxomique (13C), métabolomique et transcriptomique, ont permis de valider ces hypothèses et de les compléter. Nous avons mis en évidence différents niveaux de régulation selon l'intensité de la perturbation : pour les demandes modérées, les flux sont réajustés par un contrôle au niveau enzymatique ; pour de fortes demandes, un contrôle transcriptionnel de plusieurs gènes de la VPP ainsi que de certains gènes des voies de biosynthèse des acides aminés est observé, cet effet résultant probablement de la moindre disponibilité en NADPH. Dans l'ensemble, ce travail a apporté un nouvel éclairage sur les mécanismes impliqués dans l'homéostasie du NADPH et plus généralement dans l'équilibre redox intracellulaire. / The elucidation of the properties of metabolic network is essential to increase our understanding of cellular function and to design metabolic engineering strategies. The objective of this thesis was to better understand the regulation of the metabolism of NADPH, a “hub” metabolite which plays a central role in many cellular processes in Saccharomyces cerevisiae during fermentation. We used a systematic approach combining modeling and multi-“omics” analyses to study quantitatively the response to a perturbation of the NADPH demand. An original experimental system, based on the expression of a modified NADPH-dependent butanediol dehydrogenase was used to increase the demand for NADPH in a controlled manner. Through the use of this device and the development and use of a stoichiometric model of yeast dedicated to the fermentation, we predicted the flux distribution for different levels of perturbation. These experiments showed, first, the overwhelming ability of yeast to cope with very high NADPH demand, up to 40 times the anabolic demand. For a moderate level (up to 20 times the anabolic demand), the perturbation is mainly compensated by increased flux through the pentose phosphate pathway (PPP) and to a lesser extent through the acetate pathway (Ald6p). For a high NADPH demand, corresponding to 40 times the anabolic demand, the model predicts the saturation of the PPP as well as the operation of the glycerol-DHA cycle, which allows the exchange of NADH to NADPH. Fluxomics (13C), metabolomics and transcriptomics data were used to validate and to complement these hypotheses. We showed different levels of control depending on the intensity of the perturbation: for moderate demands, flux remodeling is mainly achieved by enzymatic control; for a high demand, a transcriptional control is observed for several genes of the PPP as well as some genes of the amino acids biosynthetic pathways, this latter effect being likely due to the low NADPH availability. Overall, this work has shed new light on the mechanisms governing NADPH homeostasis and more generally the intracellular redox balance.

Résumé confidentiel / No abstract

O 1,3-propanodiol é um composto produzido a partir da fermentação do glicerol por bactérias como a do gênero Klebsiella e que pode ser utilizado para diversas aplicações na indústria, como a produção de PTT (politrimetileno tereftalato). Esse trabalho focou na produção de 1,3-propanodiol utilizando os genes que codificam as enzimas da via retirados de uma cepa de Klebsiella previamente isolada (GLC29). Os genes foram inseridos em um plasmídeo e este em cepa hospedeira de Escherichia coli com alteração na afinidade da enzima isocitrato desidrogenase pelo seu cofator. A enzima foi modificada no genoma da bactéria e utiliza como cofator NAD em vez do NADP original. Ensaios preliminares em agitador rotativo mostraram uma melhoria de produção da cepa mutada em comparação com a Escherichia coli selvagem. Em ensaios em biorreator, variando a concentração de oxigênio dissolvido no meio, a cepa mutante apresentou uma produção 25% maior que a cepa selvagem na condição de maior produção com 5% de oxigênio dissolvido. / The 1,3-propanediol is a compound produced from glycerol fermentation by bacteria such as Klebsiella and which can be used for various applications in industry, such as the production of PTT (polytrimethylene terephthalate). This work focused on the production of 1,3-propanediol using genes encoding the enzymes of the pathway taken from a Klebsiella strain previously isolated (GLC29). The genes were inserted into a plasmid and in the host strain of Escherichia coli with changes in the affinity of the enzyme isocitrate dehydrogenase for its cofactor. The enzyme was modified in the genome of the bacteria using the cofactor NAD instead of the original NADP. Preliminary tests on shaker showed an improvement of production by the mutated strains in comparison to the wild Escherichia coli. In biorreactor cultivation, varying the concentration of dissolved oxygen in the medium, the mutant strain showed a production 25% higher than the wild type strain in the condition with 5% of dissolved oxygen.

The natural ability of filamentous fungi to synthesize, glycosylate, and secrete high levels of protein products has made them potentially attractive hosts for heterologous protein production. Advances in fungal genetics enabled the expression of several high value proteins in filamentous fungi. Particularly the genus, Aspergillus has proven to be potentially useful for the expression of eukaryotic gene products. This thesis pertains to the optimization of recombinant protein production by the fungal host, Aspergillus niger. The target recombinant protein of interest is hen egg white lysozyme (HEWL). This protein encoded in the genome resulting in relatively stable gene construct; however, it is subject to extracellular protease attack. The objective of the proposed research is the development and application of engineering methodology for the analysis and optimization of a fungal bioprocess for recombinant protein production. The underlying hypothesis is that a significant improvement of target protein productivity is achievable by using appropriate optimization techniques. To accomplish this, during the first phase of this study a statistically based experimental method was used to systematically elucidate the effect of medium components (starch, peptone, ammonium sulfate, yeast extract, and CaCl₂.2H₂O) on hen egg white lysozyme production by Aspergillus niger HEWL WT-13-16. A 2⁵⁻¹ fractional factorial design augmented with center points revealed that peptone, starch, and ammonium sulfate were the most significant factors, whereas the other medium components were not important within the levels tested. Then, the method of steepest ascent was employed to approach the proximity of optimum. This task was followed by a central composite design to develop a response surface for medium optimization. The optimum medium composition for lysozyme production was found to be: starch 34 g/L, peptone 34 g/L, ammonium sulfate 11.9 g/L, yeast extract 0.5 g/L, and CaCl₂.2H₂O 0.5 g/L. This medium was projected to produce theoretically 212 mg/L lysozyme. Using this optimized medium, an experimentally observed maximum lysozyme concentration of 209±18 mg/L verified the applied methodology. A second optimization approach was based on metabolic flux analysis (MFA). A comprehensive metabolic network comprising three intracellular compartments (cytoplasm, mitochondrion and peroxisome) was developed for Aspergillus niger. The metabolic flux network included carbohydrate and amino acid metabolism in both anabolic and catabolic reactions. According to experimental observations, the time course of fermentation was divided into five phases, each with unique physiological properties. The network was used to form a set of linear algebraic equations based on the stoichiometry of the reactions by assuming pseudo-steady state for intracellular metabolites. The metabolic flux model consists of 137 metabolites and 287 processes, of which 181 represent biochemical conversions and 106 represent transport processes between the different compartments and the extracellular environment. In addition, due to the physiological evidence some biochemical reactions considered to be active only in one direction. Linear programming was used for optimizing of the specific growth rate as the objective function in combination with 37 measured input and output fluxes of the key metabolites to evaluate corresponding intracellular flux distributions throughout the batch fermentations. The general applicability of the methodology was evaluated by establishing commonality to optimize recombinant HEWL production. The proposed model was able to predict correctly the specific growth rate, oxygen uptake rate, and carbon dioxide evolution rate with good precision. The results of the metabolic flux and sensitivity analysis were employed for medium design. Growth was biphasic; glucose was utilized initially as the carbon source and was followed by its oxidation product, gluconate, later. Logarithmic sensitivity analysis revealed that the addition of proline, alanine and glutamate benefited growth in defined media. The experimental observations and flux analysis showed that tyrosine was a potential candidate for biomass production improvement. The two amino acids, namely proline and tyrosine benefited biomass production during the initial growth phases. Glutamate and alanine were particularly important during the latter stages of the batch process. A series of growth studies were conducted with the identified amino acids added in the medium. In these preliminary nutritional experiments the contribution to growth enhancement was 46% for proline, 23% for glutamate, and 22% for tyrosine. Model predictions were further verified by conducting batch and fed-batch fermentations in a 7- liter bioreactor. The programmed addition of four amino acids (proline, glutamate, alanine, and tyrosine) according to a predetermined schedule resulted in a 44% improvement in biomass and 41% improvement in recombinant protein production. The experiments also confirmed the model prediction that extra amount of amino acids besides the identified ones would not significantly enhance biomass and the recombinant protein production. A computer-based control system was developed for the on-line monitoring and control of the major state variables (e.g., temperature, pH, and DO) during the time course of fermentation. The graphical programming environment, LabVIEW was used to acquire and integrate these variables in a supervisor computer. The temperature of the bioreactor during sterilization and fermentation was controlled using a cascade methodology. The controller parameters of the master and slave loops were determined experimentally to yield a smooth response with minimum overshoot of both the bioreactor and jacket temperatures. The program scheduled various required steps in an established order during the fermentation. This feature of the software guarantees that every necessary operation will be met. The graphical representation of the process is displayed on the screen and helps the user to follow the process and perform the required adjustments. Furthermore, different variables can be observed simultaneously and saved in text or spreadsheet files for further analysis.

The natural ability of filamentous fungi to synthesize, glycosylate, and secrete high levels of protein products has made them potentially attractive hosts for heterologous protein production. Advances in fungal genetics enabled the expression of several high value proteins in filamentous fungi. Particularly the genus, Aspergillus has proven to be potentially useful for the expression of eukaryotic gene products. This thesis pertains to the optimization of recombinant protein production by the fungal host, Aspergillus niger. The target recombinant protein of interest is hen egg white lysozyme (HEWL). This protein encoded in the genome resulting in relatively stable gene construct; however, it is subject to extracellular protease attack. The objective of the proposed research is the development and application of engineering methodology for the analysis and optimization of a fungal bioprocess for recombinant protein production. The underlying hypothesis is that a significant improvement of target protein productivity is achievable by using appropriate optimization techniques. To accomplish this, during the first phase of this study a statistically based experimental method was used to systematically elucidate the effect of medium components (starch, peptone, ammonium sulfate, yeast extract, and CaCl₂.2H₂O) on hen egg white lysozyme production by Aspergillus niger HEWL WT-13-16. A 2⁵⁻¹ fractional factorial design augmented with center points revealed that peptone, starch, and ammonium sulfate were the most significant factors, whereas the other medium components were not important within the levels tested. Then, the method of steepest ascent was employed to approach the proximity of optimum. This task was followed by a central composite design to develop a response surface for medium optimization. The optimum medium composition for lysozyme production was found to be: starch 34 g/L, peptone 34 g/L, ammonium sulfate 11.9 g/L, yeast extract 0.5 g/L, and CaCl₂.2H₂O 0.5 g/L. This medium was projected to produce theoretically 212 mg/L lysozyme. Using this optimized medium, an experimentally observed maximum lysozyme concentration of 209±18 mg/L verified the applied methodology. A second optimization approach was based on metabolic flux analysis (MFA). A comprehensive metabolic network comprising three intracellular compartments (cytoplasm, mitochondrion and peroxisome) was developed for Aspergillus niger. The metabolic flux network included carbohydrate and amino acid metabolism in both anabolic and catabolic reactions. According to experimental observations, the time course of fermentation was divided into five phases, each with unique physiological properties. The network was used to form a set of linear algebraic equations based on the stoichiometry of the reactions by assuming pseudo-steady state for intracellular metabolites. The metabolic flux model consists of 137 metabolites and 287 processes, of which 181 represent biochemical conversions and 106 represent transport processes between the different compartments and the extracellular environment. In addition, due to the physiological evidence some biochemical reactions considered to be active only in one direction. Linear programming was used for optimizing of the specific growth rate as the objective function in combination with 37 measured input and output fluxes of the key metabolites to evaluate corresponding intracellular flux distributions throughout the batch fermentations. The general applicability of the methodology was evaluated by establishing commonality to optimize recombinant HEWL production. The proposed model was able to predict correctly the specific growth rate, oxygen uptake rate, and carbon dioxide evolution rate with good precision. The results of the metabolic flux and sensitivity analysis were employed for medium design. Growth was biphasic; glucose was utilized initially as the carbon source and was followed by its oxidation product, gluconate, later. Logarithmic sensitivity analysis revealed that the addition of proline, alanine and glutamate benefited growth in defined media. The experimental observations and flux analysis showed that tyrosine was a potential candidate for biomass production improvement. The two amino acids, namely proline and tyrosine benefited biomass production during the initial growth phases. Glutamate and alanine were particularly important during the latter stages of the batch process. A series of growth studies were conducted with the identified amino acids added in the medium. In these preliminary nutritional experiments the contribution to growth enhancement was 46% for proline, 23% for glutamate, and 22% for tyrosine. Model predictions were further verified by conducting batch and fed-batch fermentations in a 7- liter bioreactor. The programmed addition of four amino acids (proline, glutamate, alanine, and tyrosine) according to a predetermined schedule resulted in a 44% improvement in biomass and 41% improvement in recombinant protein production. The experiments also confirmed the model prediction that extra amount of amino acids besides the identified ones would not significantly enhance biomass and the recombinant protein production. A computer-based control system was developed for the on-line monitoring and control of the major state variables (e.g., temperature, pH, and DO) during the time course of fermentation. The graphical programming environment, LabVIEW was used to acquire and integrate these variables in a supervisor computer. The temperature of the bioreactor during sterilization and fermentation was controlled using a cascade methodology. The controller parameters of the master and slave loops were determined experimentally to yield a smooth response with minimum overshoot of both the bioreactor and jacket temperatures. The program scheduled various required steps in an established order during the fermentation. This feature of the software guarantees that every necessary operation will be met. The graphical representation of the process is displayed on the screen and helps the user to follow the process and perform the required adjustments. Furthermore, different variables can be observed simultaneously and saved in text or spreadsheet files for further analysis.

In this work an intersection between optimization methods and animal cell culture modeling is considered. We present optimization based methods for analyzing and building models of cell culture; models that could be used when designing the environment cells are cultivated in, i.e., medium. Since both the medium and cell line considered are complex, designing a good medium is not straightforward. Developing a model of cell metabolism is a step in facilitating medium design. In order to develop a model of the metabolism the methods presented in this work make use of an underlying metabolic reaction network and extracellular measurements. External substrates and products are connected via the relevant elementary flux modes (EFMs). Modeling from EFMs is generally limited to small networks, because the number of EFMs explodes when the underlying network size increases. The aim of this work is to enable modeling with more complex networks by presenting methods that dynamically identify a subset of the EFMs. In papers A and B we consider a model consisting of the EFMs along with the flux over each mode. In paper A we present how such a model can be decided by an optimization technique named column generation. In paper B the robustness of such a model with respect to measurement errors is considered. We show that a robust version of the underlying optimization problem in paper A can be formed and column generation applied to identify EFMs dynamically. In papers C and D a kinetic macroscopic model is considered. In paper C we show how a kinetic macroscopic model can be constructed from the EFMs. This macroscopic model is created by assuming that the flux along each EFM behaves according to Michaelis-Menten type kinetics. This modeling method has the ability to capture cell behavior in varied types of media, however the size of the underlying network is a limitation. In paper D this limitation is countered by developing an approximation algorithm, that can dynamically identify EFMs for a kinetic model. / I denna avhandling betraktar vi korsningen mellan optimeringsmetoder och modellering av djurcellodling.Vi presenterar optimeringsbaserade metoder för att analysera och bygga modeller av cellkulturer. Dessa modeller kan användas vid konstruktionen av den miljö som cellerna ska odlas i, dvs, medium.Eftersom både mediet och cellinjen är komplexa är det inte okomplicerat att utforma ett bra medium. Att utveckla en modell av cellernas ämnesomsättning är ett steg för att underlätta designen av mediet. För att utveckla en modell av metabolismen kommer de metoder som används i detta arbete att utnyttja ett underliggande metaboliskt reaktions\-nätverk och extracellulära mätningar. Externa substrat och produkter är sammankopplade via de relevanta elementära metaboliska vägarna (EFM).Modellering med hjälp av EFM är i allmänhet begränsad till små nätverk eftersom antalet EFM exploderar när de underliggande nätverket ökar i storlek. Målet med detta arbete är att möjliggöra modellering med mer komplexa nätverk genom att presentera metoder som dynamiskt identifierar en delmängd av EFM. I artikel A och B betraktar vi en modell som består av EFM och ett flöde över varje EFM.I artikel A presenterar vi hur en sådan modell kan bestämmas med hjälp av en optimeringsteknik som kallas kolumngenerering.I artikel A undersöker vi hur robust en sådan modell är med avseende till mätfel. Vi visar att en robust version av det underliggande optimeringsproblemet i artikel A kan konstrueras samt att kolumngenerering kan appliceras för att identifiera EFM dynamiskt. Artikel C och D behandlar en kinetisk makroskopisk modell. Vi visar i artikel C hur en sådan modell kan konstrueras från EFM.Denna makroskopiska modell är skapad genom att anta att flödet genom varje EFM beter sig enligt Michaelis-Menten-typ av kinetik. Denna modelleringsmetod har förmågan att fånga cellernas beteende i olika typer av media, men storleken på nätverket är en begränsning.I artikel D hanterar vi denna begränsing genom att utveckla en approximationsalgoritm som identifierar EFM dynamiskt för en kinetisk modell. / <p>QC 20150827</p>

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No. of bitstreams: 1 TeseCRS.pdf: 3506039 bytes, checksum: 68f4c5fe1c6ae3672adcedf3450e2f31 (MD5) Previous issue date: 2015-08-27 / Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq) / Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES) / The genus Salmonella spp. has been extensively investigated because these bacteria are important pathogens that frequently cause severe diseases and gastrointestinal infections in humans and animals. Moreover, in recent years, Salmonella has called attention due to the excellent results in the production and in vivo delivery of various substances with potential application in Vaccinology. However, there is still little information available concerning aspects of its metabolism, which hampers both the development of new attenuated strains and the large-scale production of live cells and cellular components. Thus, this work aimed to study the S. typhimurium LT2 metabolism, using traditional and innovative approaches to investigate different carbon sources as well as different bioreactor operation modes and aeration conditions (aerobic and anaerobic). Results obtained in batch and chemostat cultivations indicated that S. typhimurium metabolism differs significantly from E. coli metabolism, closely related bacteria species with regard to the central carbon metabolism. The main difference observed between these bacteria was the high level of acetate production exhibited by S. typhimurium LT2 cells, which, differently from E. coli, occurred even at the lowest dilution rate evaluated. Currently, genome scale metabolic models are important tools for better understanding the phenotypic behavior of many organisms. Therefore the model STM_v1.0 reconstructed for S. typhimurium LT2 was evaluated, comparing experimental data, obtained in chemostat cultivations, with model predictions. Since this model was derived from E. coli model, the simulated results for biomass formation were overestimated and, consequently, predicted acetate fluxes were lower than those obtained experimentally. Therefore, to obtain experimental data useful to improve the model and to reach a better comprehension of S. typhimurium metabolism, the technique of metabolic flux analysis using isotopic labeled substrate was adopted, allowing determination of the fluxes for the main pathways of central carbon metabolism of Salmonella. This analysis revealed different preferred metabolic pathways depending on the specific growth rate. At the lowest dilution rate evaluated, D = 0.24 h-1, glucose was catabolized predominantly by the pentose phosphate and glycolysis pathways, while at the dilution rate of 0.48 h-1, the major pathway of glucose oxidation was Entner-Doudoroff. In addition, a relatively high flux through the citric acid cycle at the higher dilution rate studied was observed. / Bactérias do gênero Salmonella spp. são extensivamente estudadas por serem importantes patógenos, causando frequentemente graves doenças e infecções gastrointestinais em humanos e animais. Além disso, nos últimos anos, estas bactérias vêm ganhando um destaque ainda maior na área da biotecnologia por apresentarem ótimos resultados na produção e veiculação in vivo de diversas substâncias com fins vacinais. No entanto, ainda há poucas informações a respeito de seu metabolismo, dificultando tanto o desenvolvimento de novas linhagens atenuadas, como também a produção em larga escala de células vivas e de componentes celulares. Neste sentido, este trabalho se propôs a estudar o metabolismo de S. typhimurium LT2, utilizando inicialmente abordagens tradicionais para investigar seu comportamento na presença de diferentes fontes de carbono, em diferentes modos de operação de biorreator e de aeração (aeróbias e anaeróbias). Os resultados obtidos em cultivos em batelada e em quimiostatos evidenciaram que o metabolismo da S. typhimurium difere bastante do metabolismo da E. coli, espécies consideradas semelhantes com relação ao metabolismo do carbono central. A principal diferença observada entre essas duas bactérias foi a elevada produção de acetato pelas células de S. typhimurium LT2, mesmo em baixas velocidades de crescimento nas quais este metabólito não é produzido por diversas estirpes de E. coli. Atualmente, modelos metabólicos em escala genômica são ferramentas importantes para que o comportamento do fenótipo de diversos organismos sejam melhor compreendidos. Assim, avaliou-se o modelo STM_v1.0 reconstruído para S. typhimurium LT2, comparando-se dados obtidos experimentalmente, em quimiostatos, e os preditos pelo modelo. No entanto, como este modelo foi baseado no modelo da E. coli, os resultados simulados para produção de biomassa foram superestimados e, consequentemente, os fluxos de acetato foram inferiores aos obtidos experimentalmente. Sendo assim, para se obter dados experimentais úteis para aprimorar o modelo e para uma compreensão maior do metabolismo de S. typhimurium, utilizou-se a técnica de análise dos fluxos metabólicos com substrato isotopicamente marcado, permitindo a determinação dos fluxos das principais vias do metabolismo do carbono central da bactéria em estudo. Essa análise revelou diferenças na utilização das vias metabólicas em função da velocidade específica de crescimento, sendo que na menor taxa de diluição avaliada, D = 0,24 h-1, a glicose foi predominantemente catabolizada pelas vias pentose fosfato e glicólise, enquanto na taxa de diluição de 0,48 h-1, a via principal de oxidação da glicose foi a Entner- Doudoroff. Além disso, também observou-se um fluxo relativamente maior na via do ciclo do ácido cítrico na maior taxa de diluição estudada.