The supply of precursors from primary metabolism is often overlooked when engineering secondary metabolism for increased product yields. This is because precursor supply may be assumed to be non-limiting, and it is considered difficult to engineer primary metabolism, because control of carbon flow (flux) is generally distributed among most enzymes of the pathway. The aim of this thesis was to increase the production of sterols, part of the isoprenoid class of secondary metabolites, in tobacco (Nicotiana tabacum) Bright Yellow 2 (BY-2) cell cultures. This was achieved by genetically engineering increased activity of mitochondrial citrate synthase, an enzyme of the tricarboxylic acid (TCA) cycle that is involved in the provision of cytosolic acetyl coenzyme A, the primary metabolite precursor to sterols. Metabolic flux analysis revealed that citrate synthase exerts significant control over cyclic TCA cycle flux in BY-2 cells and suggested that increasing the activity of downstream enzymes within secondary metabolism could lead to a further redirection of TCA-cycle-derived precursors into sterol biosynthesis. Attempts were made to achieve this by genetically engineering increased activity of 3-hydroxy-3-methylglutaryl coenzyme A reductase (HMGR), a key enzyme of secondary metabolism involved in sterol biosynthesis. Consistent with previous research, transgenic lines had increased sterol levels. However, the high sterol phenotype was unstable, and attempts to co-express HMGR and citrate synthase genes were unsuccessful. The thesis demonstrates that increasing the provision of precursors to secondary metabolites can result in increased yields of those secondary metabolites but suggests that in most cases the activity of enzymes within secondary metabolism has a greater effect on those yields. It also reveals that single enzymes can exert significant control of flux within primary metabolism, although the control exerted by specific enzymes probably changes with the demands placed on metabolism.

L’accumulation de biopolymère de réserve (PolyHydroxyAlcanoates ou PHA) par la souche Cupriavidus necator, à partir de substrats de type acides gras volatils (acide butyrique, acide propionique et acide acétique) a été étudiée. Elle est induite par une limitation phosphore. Les performances atteintes lors des cultures se situent parmi les meilleures de la littérature pour ce type de substrat : jusqu’à 66 g.L-1 de biomasse totale avec un pourcentage d’accumulation massique de 88% en PHB –PolyHydroxyButyrate- ou en PHB-co-HV -PolyHydroxyButyrate-co-HydroxyValerate- comportant jusqu’à 52% de motifs d’HV.Pour chaque source carbonée, une caractérisation cinétique et stœchiométrique de la souche a été réalisée en l’absence d’effets inhibiteurs dus aux substrats acides grâce à des cultures de type Fed-Batch avec des apports non limitants et non inhibiteurs en carbone. Il a été dégagé :- un taux de croissance maximal de la souche de 0,33 h-1 pour les trois acides étudiés- une relation entre vitesse spécifique de production de PHA et taux de croissance fixée par la disponibilité et les flux de production de NADPH2 avec un découplage inverse pour les taux de croissance supérieurs à 0,05 h-1 et un couplage partiel pour les taux de croissance inférieurs- un optimum de 0,35 Cmole.Cmole-1.h-1, associé à un taux de croissance de l’ordre de 0,05 h-1.- une amélioration de la production de PHB en termes de vitesses spécifiques mais également en termes de rendements si une faible croissance résiduelle est maintenueLa réponse de la souche à un excès de substrat acide a été caractérisée via l’étude de régimes transitoires induits par des pulses sur des cultures continues préalablement stabilisées en régime permanent. Il a été montré qu’en excès de phosphore, face à un brusque excès de substrat, la souche est incapable d’adapter rapidement son taux de croissance. L’excès est donc dirigé vers la production de PHA dont les voies sont plus rapidement mobilisables. En conditions limitantes de phosphore, le substrat excédentaire est utilisé pour la production de PHA. L’inhibition par les acides se traduit par une diminution des capacités de biosynthèse de la biomasse et des PHA entrainant une réduction de l’assimilation du carbone puis une diminution des rendements de conversion. D’autre part la sensibilité d’un système continu à un excès de substrat dépend du point de fonctionnement choisi : plus il est optimal en termes de vitesse, moins le système est robuste. L’acide propionique est très inhibiteur comparé aux autres acides étudiés (dès 3-4 mM contre 30-40 mM). Il n’agit pas simplement via une accumulation excessive dans le cytoplasme mais il exerce également une inhibition spécifique des voies métaboliques.Un antagonisme entre les substrats (acide acétique et butyrique) a été constaté et expliqué grâce à une analyse des flux métaboliques. L’acide acétique est assimilé préférentiellement pour produire la biomasse, l’énergie et les cofacteurs nécessaires à la production de PHA, alors que l’acide butyrique est utilisé pour la synthèse de PHB. La proportion maximale d’acide acétique admise dans l’alimentation en fonction des conditions fixées en régime permanent est calculée et peut être limitée à 40% du carbone.Enfin il a été déterminé que si une croissance résiduelle est assurée grâce à un apport en phosphore, le pourcentage maximal d’HV dans le polymère dépend du taux d’acide propionique dans l’alimentation et ne peux dépasser 33 ± 5% sur acide propionique pur. Par contre, si aucune croissance résiduelle n’est assurée, il est possible de convertir l’acide propionique en motifs d’HV uniquement / Reserve Biopolymer (PolyHydroxyAlkanoates or PHA) accumulation by the strain Cupriavidus necator, from Volatile Fatty Acids (VFA, like butyric acid, propionic acid and acetic acid) was investigated. This production is induced by a phosphorus limitation. For this type of substrates, performances reached during cultures are among the best listed in the literature: up to 66 g.L-1 of total biomass with 88% (w/w) of PHB –PolyHydroxyButyrate- or PHB-co-HV -PolyHydroxyButyrate-co-HydroxyValerate- with a HV content up to 52 Mole%.For each carbon source, kinetic and stoechiometric characterization has been carried out thanks to Fed-Batch cultures with non-limiting and non-inhibitory carbon feed. It has been established:- a maximal growth rate of 0,33 h-1 for the three acid investigated- a relationship between specific PHA production rate and growth rate which is set by the availability and production flux of NADPH2. For growth rate above 0,05 h-1, there is an inverse coupling. For growth rate under 0,05 h-1, there is a partial coupling.- an optimum of 0,35 Cmole.Cmole-1.h-1 is associated with a growth rate of 0,05 h-1.- if a low residual growth rate is maintained, an improvement of PHB production is recorded in terms of specific production rate and yieldsThe response of the strain to an excess of acid substrate was characterized through the investigation of transient state induced by pulsed addition of substrate during continuous cultures stabilized in steady state. It was shown that in excess of phosphorus, when there is a substrate excess, the strain is unable to quickly adapt its growth rate, so the excess is directed to PHA production whose ways seem to be more easily mobilized. Under phosphorus limitation, an excess of substrate is used for PHA production. Acid inhibition results in a decrease in biomass and PHA production capacity which leads to a decrease in carbon assimilation and conversion yields. The sensitivity of a continuous system to an excess of substrate depends on the chosen operating point: the more it is optimal in terms of specific production rate, the less the system is robust. Propionic acid is highly inhibitory compared to the other acids studied (from 3-4 mM versus 30-40 mM). It does not act only via an excessive accumulation in the cytoplasm but also exerts a specific inhibition of metabolic pathways.An antagonism between substrates (acetic and butyric acid) has been established and explained thanks to the Metabolic Flux Analysis. Acetic acid is preferentially used to produce biomass, energy and cofactors for PHA synthesis, whereas butyric acid is used to product PHB. According to the conditions set during steady state, maximal content of acetic acid admitted in the feed can be calculated. It can be limited to 40% of the carbon in the feed.Finally if a growth rate is maintained thanks to a phosphorus supply, the maximal HV content in polymer is function of propionic acid in the feed and cannot exceed 33 ± 5 Mole% on pure propionic acid. Conversely, if there is no residual growth, a total conversion of propionic acid into HV is allowed

O objetivo deste trabalho foi produzir poli-3-hidroxibutirato (P3HB) e poli-3-hidroxibutirato-co-3-hidroxivalerato (PHB-co-3HV), polímeros biodegradáveis, utilizando hidrolisado hemicelulósico, rico em xilose, de bagaço de cana-de-açúcar. O estudo dos fluxos metabólicos de xilose in silico indicou que, através do redirecionamento do metabolismo, é possível aumentar o rendimento P3HB a partir de xilose de 0.25 g g-1 para 0.40 g g-1. Obtiveram-se mutantes no sistema repressão catabólica nos quais se verificaram consumo simultâneo de carboidratos e redução do tempo de consumo dos açúcares. Porém, diferenças de fluxos de carbono resultaram em menores valores de crescimento e produção de PH3B em relação às linhagens parentais. Um programa de bioprospecção destacou Burkholderia sp. F24, em experimentos em biorreator obteve-se 25.04 g l-1 de biomassa, 49.31% de acúmulo de P3HB na massa seca celular, alcançando uma produtividade de 0.28 g l-1 h-1. Além disso, foi possível controlar a fração molar de 3HV na síntese PHB-3HV em F24 utilizando xilose e ácido levulínico. / The aim of this thesis is to produce poly3-hydroxybutyrate (P3HB) and poli-3-hidroxibutirate-co-3-hydroxyvalerate (PHB-co-3HV), biodegradable polymers, using hemicellulosic hydrolysate, rich in xylose, from sugarcane bagasse. Metabolic flux analysis in silico of xylose metabolism indicated that, though metabolism redirection is possible to increase P3HB yield from 0.25 g g-1 to 0.40 g g-1. It was observed simultaneous consumption of sugars and reduction of time necessary to exhaust of all sugars in the media culture in mutants with catabolite repression partially abolished. However, differences in carbon flux resulted in lower growth and P3HB production in comparison to the parental strain. A bioprospecting program selected Burkholderia sp. F24, in experiments in bioreactor it reached 25.04 g l-1, 49.31% of P3HB accumulation of the dry cell mass and 0.28 g l-1 h-1 of productivity. Moreover, it was possible to modulate to molar fraction of 3HV in PHB-co-3HV biosyntheses with Burkholderia sp. F24 using xylose and levulinic acid.

O objetivo deste trabalho foi produzir poli-3-hidroxibutirato (P3HB) e poli-3-hidroxibutirato-co-3-hidroxivalerato (PHB-co-3HV), polímeros biodegradáveis, utilizando hidrolisado hemicelulósico, rico em xilose, de bagaço de cana-de-açúcar. O estudo dos fluxos metabólicos de xilose in silico indicou que, através do redirecionamento do metabolismo, é possível aumentar o rendimento P3HB a partir de xilose de 0.25 g g-1 para 0.40 g g-1. Obtiveram-se mutantes no sistema repressão catabólica nos quais se verificaram consumo simultâneo de carboidratos e redução do tempo de consumo dos açúcares. Porém, diferenças de fluxos de carbono resultaram em menores valores de crescimento e produção de PH3B em relação às linhagens parentais. Um programa de bioprospecção destacou Burkholderia sp. F24, em experimentos em biorreator obteve-se 25.04 g l-1 de biomassa, 49.31% de acúmulo de P3HB na massa seca celular, alcançando uma produtividade de 0.28 g l-1 h-1. Além disso, foi possível controlar a fração molar de 3HV na síntese PHB-3HV em F24 utilizando xilose e ácido levulínico. / The aim of this thesis is to produce poly3-hydroxybutyrate (P3HB) and poli-3-hidroxibutirate-co-3-hydroxyvalerate (PHB-co-3HV), biodegradable polymers, using hemicellulosic hydrolysate, rich in xylose, from sugarcane bagasse. Metabolic flux analysis in silico of xylose metabolism indicated that, though metabolism redirection is possible to increase P3HB yield from 0.25 g g-1 to 0.40 g g-1. It was observed simultaneous consumption of sugars and reduction of time necessary to exhaust of all sugars in the media culture in mutants with catabolite repression partially abolished. However, differences in carbon flux resulted in lower growth and P3HB production in comparison to the parental strain. A bioprospecting program selected Burkholderia sp. F24, in experiments in bioreactor it reached 25.04 g l-1, 49.31% of P3HB accumulation of the dry cell mass and 0.28 g l-1 h-1 of productivity. Moreover, it was possible to modulate to molar fraction of 3HV in PHB-co-3HV biosyntheses with Burkholderia sp. F24 using xylose and levulinic acid.

O copolímero biodegradável poli(3-hidroxibutirato-co-3-hidroxihexanoato) P(3HB-co-3HHx) é um polihidroxialcanoato (PHA) que apresenta várias aplicações. A bactéria Burkholderia sacchari acumula P(3HB-co-2mol%3HHx), a partir de glicose e ácido hexanoico. Com o objetivo de obter P(3HB-co-3HHx) com diferentes teores de 3HHx por B. sacchari, foram construídas linhagens recombinantes, contendo genes do operon phaPCJ de Aeromonas spp. Os recombinantes produziram P(3HB-co-3HHx), a partir de ácidos hexanoico, láurico e linoleico, com teores de 3HHx entre 1,88-18 mol%. Experimentos em biorreator com o recombinante, alimentada na fase de acúmulo por glicose 140 g/L e ácido hexanoico entre 0-45 g/L, resultaram copolímeros com composições variando de 0 a 20 mol% de 3HHx. Os copolímeros assim produzidos foram extraídos e analisados quanto às propriedades físicas. A análise de fluxos metabólicos indicou que a produção de PHA pode ser aumentada com mudanças no metabolismo central e deleção/superexpressão de genes. / The biodegradable copolymer poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) P(3HB-co-3HHx) is a polyhydroxyalkanoate (PHA) presenting various applications. The bacterium Burkholderia sacchari accumulated P(3HB-co-2mol%3HHx) from glucose and hexanoic acid. In order to obtain P(3HB-co-3HHx) with different 3HHx amounts by B. sacchari, recombinant strains containing phaPCJ operon genes from Aeromonas spp were constructed. Recombinant strains produced P(3HB-co-3HHx) from hexanoic, lauric and linoleic acids, with contents of 3HHx ranging from 1.88 to 18 mol%. Experiments with the recombinant in bioreactor, fed in the accumulation phase by glucose 140 g.l-1and hexanoic acid 0-45 g.l-1, resulted in copolymers with compositions ranging from 0 to 20 mol% of 3HHx. The copolymers produced were extracted and analyzed for physical properties. The metabolic flux analysis indicated that PHA production can be increased by modifying the central metabolism and deleting/ overexpressing genes.

Pour des missions spatiales de longue durée, les plantes supérieures doivent faire partie des systèmes de support-vie. Le projet Micro-Ecological Life Support System Alternative (MELiSSA, alternative de système de support-vie micro-écologique) de l’Agence Spatiale Européenne est basé sur un système clos de support vie qui inclut, autour d’un compartiment consommateur, des compartiments microbiens et des plantes supérieures. Les plantes consomment les déchets pouvant être recyclés (les eaux usées et du CO2) et produisent de la nourriture fraîche, de l’eau potable et de l’oxygène pour l’équipage. Un des points clé pour ce type d’étude est le maintien d’un système qui assure le recyclage de tous les éléments C, H, O, N, S, P, … C’est pourquoi la base de l’étude repose sur une modélisation des stœchiométries de conversion qui doit traduire les échanges de matière et d’énergie en fonction des limitations physiques qui sont les paramètres de contrôle du système. L’étape préliminaire a été d’établir un modèle métabolique de feuille (un sous-modèle du modèle biochimique), comprenant le métabolisme central et utilisant les techniques métaboliques d’analyse des modes élémentaires (EFMA) et d’analyse des flux métaboliques (MFA) associé à une vision intégrée de l’énergétique du métabolisme central. En l’absence de données expérimentales suffisantes, le modèle métabolique de feuille a été construit à partir de la composition de la biomasse référencée par le Département Américain de l'Agriculture (USDA) et validé avec les données expérimentales de laitues (Lactuca sativa) cultivées dans l’installation de recherche des systèmes à environnement contrôlé (CESRF) de l’Université de Guelph (Canada). Pour la première approche, le modèle est satisfaisant et prometteur ; il peut prédire la production de biomasse une fois connecté aux facteurs physiques de la croissance de plante (lumière, disponibilité en CO2 et en eau, …) au cours du temps et à la composition de la biomasse. Cependant, nos résultats souffrent d’un manque de données pour vérifier les modèles métaboliques ; ainsi, différents types de mesures pour des prédictions plus précises sont proposés. Le futur modèle doit être en mesure de contrôler la croissance de la plante pour la survie des humains, connaissant les flux provenant des autres compartiments de la boucle MELiSSA. Par ailleurs, l’approche décrite ici peut être utilisée de manière plus générale pour tous types d’études et modélisations du métabolisme, en particulier pour étudier le fonctionnement simultané et/ou consécutif des métabolismes photosynthétique et respiratoire. / For long term space missions, higher plants are necessary to be included in life support systems. The Micro Ecological Life Support System Alternative (MELiSSA) project of European Space Agency (ESA) is based on a closed life support system where microbial and higher plant compartments support the consumer’s compartment. Plants consume the possible recycling wastes (waste water and CO2) and provide fresh food, potable water and oxygen to the crew. One of the key points for this kind of study is to maintain a system which recycles all the elements C, H, O, N, S, P, etc. That is why, the study is based on the modelling of conversion stoichiometries ; they are the results of the control parameters of the system (physical limitations of mass and energy exchanges). As a preliminary step, we have established leaf metabolic model (a sub model of the plant biochemical model) involving central carbon metabolism using metabolic techniques, elementary flux mode analysis (EFMA) and metabolic flux analysis (MFA). It is associated to an integrated approach of energetics and central metabolism. Due to data limitations, the leaf metabolic model was constructed taking the biomass composition of lettuce (Lactuca sativa) from United States Department of Agriculture (USDA) and validated with the experimental data where lettuce grown in controlled Environment Systems Research Facility (CESRF) of University of Guelph (Canada). For the first approach, the model is satisfying and promising ; it can predict the biomass production connecting the physical plant growth factors (light, CO2 and water availability, etc.) along with time course growth and biomass composition. However, our results show the lack of sufficient data ; hence, various kinds of measurements required for more accurate model predictions are proposed. The future model must be able to control and manage the plant growth for human survival knowing the fluxes from other compartments of MELiSSA loop. Further, the approach described here can be used more generically in all kinds of metabolic studies and modeling, especially for studying simultaneous and/or consecutive photosynthetic and respiratory metabolisms.

O copolímero biodegradável poli(3-hidroxibutirato-co-3-hidroxihexanoato) P(3HB-co-3HHx) é um polihidroxialcanoato (PHA) que apresenta várias aplicações. A bactéria Burkholderia sacchari acumula P(3HB-co-2mol%3HHx), a partir de glicose e ácido hexanoico. Com o objetivo de obter P(3HB-co-3HHx) com diferentes teores de 3HHx por B. sacchari, foram construídas linhagens recombinantes, contendo genes do operon phaPCJ de Aeromonas spp. Os recombinantes produziram P(3HB-co-3HHx), a partir de ácidos hexanoico, láurico e linoleico, com teores de 3HHx entre 1,88-18 mol%. Experimentos em biorreator com o recombinante, alimentada na fase de acúmulo por glicose 140 g/L e ácido hexanoico entre 0-45 g/L, resultaram copolímeros com composições variando de 0 a 20 mol% de 3HHx. Os copolímeros assim produzidos foram extraídos e analisados quanto às propriedades físicas. A análise de fluxos metabólicos indicou que a produção de PHA pode ser aumentada com mudanças no metabolismo central e deleção/superexpressão de genes. / The biodegradable copolymer poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) P(3HB-co-3HHx) is a polyhydroxyalkanoate (PHA) presenting various applications. The bacterium Burkholderia sacchari accumulated P(3HB-co-2mol%3HHx) from glucose and hexanoic acid. In order to obtain P(3HB-co-3HHx) with different 3HHx amounts by B. sacchari, recombinant strains containing phaPCJ operon genes from Aeromonas spp were constructed. Recombinant strains produced P(3HB-co-3HHx) from hexanoic, lauric and linoleic acids, with contents of 3HHx ranging from 1.88 to 18 mol%. Experiments with the recombinant in bioreactor, fed in the accumulation phase by glucose 140 g.l-1and hexanoic acid 0-45 g.l-1, resulted in copolymers with compositions ranging from 0 to 20 mol% of 3HHx. The copolymers produced were extracted and analyzed for physical properties. The metabolic flux analysis indicated that PHA production can be increased by modifying the central metabolism and deleting/ overexpressing genes.

pH is a key parameter in the optimization of animal cell processes, and has be linked to specific patterns of consumption and production of extracellular metabolites. However, the effect of extracellular pH on intracellular metabolism has not been fully elucidated. Metabolic flux analysis is a mathematical method that can be used to generate the intracellular flux distributions in cells, e.g. as a function of some environmental parameter. In this work, the overall objective was to develop a culture system and experimental protocol for cultivation of CHO cells, which can be used to generate data for analysis of the relationship between extracellular pH and intracellular fluxes in CHO cells by metabolic flux analysis. First, shake-flask culture of an IgG-producing cell line was performed to select an academic and chemically-defined medium with known composition. This was followed by subsequent adaptation of the cells. It was found that the originally selected medium had to be supplemented with a commercial medium to produce acceptable growth and viability. Shake-flask culture was also performed to evaluate the effect of the biological buffer HEPES on cell growth and viability, and the pH-stability during culture. HEPES-concentrations in the investigated range (7.5-45 mM) did not show an apparent effect on cell growth or viability. The higher concentrations gave slightly better buffering capacity at inoculation, however were not sufficient to keep pH stable during culture. As a result, the idea of using shake flask culture and similar techniques for cultivation of cells at various pH set-points was dismissed. Instead, a culture system and protocol based on a 100 mL Spinner flask with pH-regulation was custom-designed for the project. Features of the final design included continuous monitoring of pH and DO, stable temperature at 37 °C, adjustable agitation rate, as well as the option to incorporate inflow of air, O2 and CO2. In addition, the possibility to disconnect the flask unit to perform medium exchange and sample collection away from the reactor site (i.e. in a laminar flow workbench) was integrated into the design and protocol. The system was demonstrated for pseudo-perfusion culture with the adapted IgG-producing cell line at pH 7.0 during 24 days. Optimized regulation settings were identified. It was shown that the system could support viable cell densities of up to 11 MVC/mL and high viability (> 90 %). During the final phase of culture, stable growth, at specific growth rates of approximately 0.7 Day-1, was achieved. The specific rates of consumption and production of the key metabolites glucose, glutamine, lactate and NH4+, as well as 20 amino acids were analyzed. A majority of the rates were in accordance with CHO cell metabolism. The expected consumption of a majority of the essential amino acids and main carbon sources glucose and glutamine were confirmed, as well as the associated production of by-products lactate and NH4+. The system and protocol developed in this work can be used in future experiments to generate data describing metabolic profiles as a function of various pH-set points. This data may then be used in metabolic flux analysis to further elucidate the metabolism behind pH effects in CHO cells. / pH är en viktig parameter i optimeringen av animalcellsprocesser och har sammankopplats med specifika konsumtions- och produktionsmönster rörande extracellulära metaboliter. Det extracellulära pH-värdets effekt på den intracellulära metabolismen är dock inte fullt klarlagd. Metabolisk flux analys är en matematisk metod som kan användas för att generera intracellulära fluxfördelningar i celler, exempelvis som en funktion av någon yttre parameter. Det övergripande målet i detta arbete var att utveckla ett odlingssystem och experimentellt protokoll för odling av CHO-celler som kan användas för att generera data för metabolisk flux analys där målet är att studera effekten av pH på den intracellulära cellmetabolismen. En IgG-producerande CHO-cellslinje odlades först i skakkolv för att välja ut ett akademiskt kemiskt definierat medium med känd sammansättning. Därefter följde försök att anpassa cellerna till det valda mediet. Det visade sig att ett kommersiellt medium behövde tillsättas för att ge godtagbar tillväxt och viabilitet. Effekten av den biologiska bufferten HEPES på cellernas tillväxt och viabilitet, samt pH-stabiliteten under odling, undersöktes också genom odling i skakkolv. HEPES-koncentrationer i det undersökta intervallet (7.5 – 45 mM) hade ingen större effekt på tillväxt och viabilitet. För de högre koncentrationerna var buffertkapaciteten något bättre precis vid inokulering. Dessa koncentrationer var dock ej tillräckliga för att ge stabilt pH under odlingen. Baserat på dessa resultat övergavs tanken på att använda skakkolvsodling för att odla celler vid olika pH-värden. Ett odlingssystem och ett protokoll baserat på en 100 mL Spinnerflaska med pH-reglering specialdesignades istället för projektet. I det färdiga systemet fanns lösningar för kontinuerlig övervakning av pH och DO, stabil temperatur vid 37 °C, justerbar omrörningshastighet, samt valmöjligheten att flöda in luft, O2 och CO2. Dessutom infördes möjligheten att koppla loss flaskenheten från reglersystemet för byte av medium och provtagning. För att demonstrera systemet genomfördes en odling med den anpassade IgG-producerande cellinjen enligt principen för pseudo-perfusion vid pH 7.0. Odlingen pågick under 24 dagar och optimerade reglerinställningar identifierades. Det visades att systemet kunde understödja cellkoncentrationer upp till 11 miljoner celler per milliliter, samt hög viabilitet (> 90 %). Under den senare delen av odlingen uppnåddes stabil tillväxt, vid specifika tillväxthastigheter omkring 0.7 per dygn. Den specifika konsumtions- och produktionshastigheten för metaboliterna glukos, glutamin, laktat och NH4+, samt 20 aminosyror analyserades. Majoriteten av hastigheterna stämde överens med typisk CHO-cellsmetabolism. Den förväntade konsumtionen av majoriteten av de essentiella aminosyrorna och huvudsakliga kolkällorna glukos och glutamin konfirmerades, såväl som den associerade produktionen av bi-produkterna laktat och NH4+. Odlingssystemet och det experimentella protokollet som utvecklades i detta arbete kan användas i framtida experiment för att generera data som beskriver metaboliska profiler som funktion av extracellulärt pH. Dessa data kan sedan användas i metabolisk flux analys för att dra slutsatser om pH-effekter i CHO-celler.

Background Cancer is one of the leading causes of death in Sweden. In order to develop better treatments against cancer we need to better understand it. One area of special interest is cancer metabolism and the metabolic fluxes. As these fluxes cannot be directly measured, modeling is required to determine them. Due to the complexity of cell metabolism, some limitations in the metabolism model are required. As the TCA-cycle (TriCarboxylic Acid cycle) is one of the most important parts of cell metabolism, it was chosen as a starting point. The primary goal of this project has been to evaluate the previously constructed TCA-cycle model. The first step of the evaluation was to determine the CI (Confidence Interval) of the model parameters, to determine the parameters’ identifiability. The second step was to validate the model to see if the model could predict data for which the model had not been trained for. The last step of the evaluation was to determine the uncertainty of the model simulation. Method The TCA-cycle model was created using Isotopicaly labeled data and EMUs (ElementaryMetabolic Units) in OpenFlux, an open source toolbox. The CIs of the TCA-cycle model parameters were determined using both OpenFlux’s inbuilt functionality for it as well as using amethod called PL (Profile Likelihood). The model validation was done using a leave one out method. In conjunction with using the leave on out method, a method called PPL (Prediction Profile Likelihood) was used to determine the CIs of the TCA-cycle model simulation. Results and Discussion Using PL to determine CIs had mixed success. The failures of PL are most likely caused by poor choice of settings. However, in the cases in which PL succeeded it gave comparable results to those of OpenFLux. However, the settings in OpenFlux are important, and the wrong settings can severely underestimate the confidence intervals. The confidence intervals from OpenFlux suggests that approximately 30% of the model parameters are identifiable. Results from the validation says that the model is able to predict certain parts of the data for which it has not been trained. The results from the PPL yields a small confidence interval of the simulation. These two results regarding the model simulation suggests that even though the identifiability of the parameters could be better, that the model structure as a whole is sound. Conclusion The majority of the model parameters in the TCA-cycle model are not identifiable, which is something future studies needs to address. However, the model is able to to predict data for which it has not been trained and the model has low simulation uncertainty.

L’acétyl-coA occupe une place centrale dans le métabolisme intermédiaire. Il constitue le point de jonction de plusieurs voies métaboliques telles que la .-oxydation, la glycolyse, le catabolisme de certains acides aminés, la cétolyse, la cétogenèse et la synthèse d’acides gras. Il est également impliqué dans d’autres processus tels que l’acétylation des protéines. Au cours de mon travail de thèse, je me suis attachée à étudier différents aspects du métabolisme de l’acétyl-coA. La première partie de mon travail a porté sur la modulation pharmacologique de la .- oxydation dans le but de corriger des déficits de cette voie métabolique. L’intérêt de traitements par 400µM de bézafibrate ou 75µM de resvératrol dans les formes modérées de déficit en VLCAD et en CPT2 avait été montré précédemment. Par des méthodes de référence et grâce à la mise au point de nouvelles techniques, j’ai pu montrer sur des fibroblastes de patients déficitaires en LCHAD que des traitements par une combinaison de 35µM de bézafibrate et 30µM de resvératrol permettent d’augmenter les capacités d’oxydation du palmitate en stimulant la synthèse protéique. L’effet de cette combinaison était comparable à celui d’un traitement par 400µM de bézafibrate. Dans un second temps, je me suis intéressée à deux cofacteurs impliqués dans le métabolisme de l’acétyl-coA : l’acide lipoïque, cofacteur de quatre .-cétoacides déshydrogénases (PDHc, BCKDHc, .- KGDHc et GCS) et la riboflavine, cofacteur d’acyl-coA déshydrogénases de la .-oxydation et de déshydrogénases impliquées dans le catabolisme des acides aminés ramifiés. Ainsi, j’ai participé à la description d’anomalies du métabolisme de l’acide lipoïque, un nouveau groupe de maladies héréditaires du métabolisme caractérisé par un déficit combiné en .-cétoacides déshydrogénases. Par ailleurs, j’ai pu montrer qu’une hyperprolinémie constitue un biomarqueur intéressant pour le diagnostic d’acidurie glutarique de type II primaire ou secondaire, ces dernières pouvant se rencontrer en cas d’anomalie du métabolisme de la riboflavine. J’ai également évalué l’utilisation d’un mélange racémique de L,D-3-hydroxybutyrate afin de corriger les déficits énergétiques induits par un déficit en PDHc ou GLUT1. Via la cétolyse, le L,D-3- hydroxybutyrate génère de l’acétyl-coA. De façon surprenante, l’administration de ce composé s’est traduite par une amélioration de l’état clinique des patients atteints de déficits en PDHc, alors qu’une dégradation a été observée chez les patients atteints de déficits en GLUT1. Cette évolution différente pourrait souligner l’importance de l’anaplérose chez les patients déficitaires en GLUT1. Enfin, la dernière partie de mon travail de thèse porte sur la description d’un patient atteint d’une forme modérée de déficit en pyruvate carboxylase, cette enzyme étant régulée par l’acétyl-coA. Les difficultés diagnostiques rencontrées devant ces formes modérées sont rapportées, ainsi que des essais de traitement par des composés anaplérotiques et par le bézafibrate, malheureusement sans bénéfice net que ce soit in vitro ou in vivo. En conclusion, le métabolisme de l’acétyl-coA est altéré dans de nombreuses maladies héréditaires du métabolisme, dont certaines sont de description récente. Il peut être modulé par différentes approches pharmacologiques. Le développement de nouvelles techniques et notamment les analyses de flux métaboliques fournissent des outils utiles à son exploration et à l’étude de nouveaux traitements. / Acetyl-CoA is crucial for intermediary metabolism. It is at the crossroad of several metabolic pathways such as beta-oxidation, glycolysis, aminoacid catabolism, ketolysis, and fatty acid synthesis. It is also involved in other processes such as protein acetylation. In this document I studied different aspects of acetyl-CoA metabolism. First, I tried to correct fatty acid oxidation defects through pharmacological approach. Thanks to well- known methods and new ones, I showed that a combination of 30µM resveratrol and 35µM bezafibrate increased fatty acid oxidation capacities by increasing protein synthesis, as well as 400µM bezafibrate. Acetyl-CoA metabolism is also altered due to cofactors defects such as lipoic acid or riboflavine deficiency. I was involved in new diseases description and research for new biomarkers in this context. PDHc and GLUT1 deficiency are two different diseases with the same consequence : a defect in acetyl- CoA production from glucose. In order to improve patients’ quality of life, I evaluated the substitution of ketogenic diet with a racemic mix of L,D-3-hydroxybutyrate in PDHc and GLUT1 deficiency. The clinical evolution of patients was strikingly different, with an improvement in PDHc patients, whereas a degradation was noticed in GLUT1 patients. This difference might underline the role of anaplerosis in GLUT1 deficiency. Finally, I evaluated anaplerotic treatment and bezafibrate treatment in pyruvate carboxylase deficiency, an enzyme allosterically regulated by acetyl-CoA. To conclude, acetyl-CoA metabolism is altered in numerous inherited errors of metabolism, some of them being recently described. It can be modulated by pharmacological approaches. The development of new techniques such as metabolic flux analysis are useful for its study and for new treatments evaluation.