Degradability in the rumen of several protein sources was determined by suspending from 12 to 13 g of feedstuff in dacron bags into the rumen for 0, 2, 6, 12, 24, 36, 48, and 72 h. Rumen cannulated lactating Holstein cows consuming a diet of corn silage, alfalfa, soybean, and high moisture corn were used. Degradability of protein varied from 18.6% for corn gluten meal to 72.3% for soybean meal. Gel electrophoresis was used to monitor rates of degradation in the rumen of fractions of corn gluten (CGM), CORN, cottonseed (CSM), peanut (PM), and soybean meal (SBM) protein fractions. Fractional degradation rates in the rumen were determined from densitometric analysis of stained polypeptides bands on SDS-PAGE gels. Acidic subunits of soybean glycinin were degraded at a faster rate than basic subunits (.144 vs .104 h⁻¹). Rates of degradation of zein in corn and corn gluten meal were .026 and .015 h⁻¹, respectively. Protein degradability estimated by using B subfractional components did not differ from degradability measured using total B fractions. Lag phase associated with dacron bags suspension technique did not change effective degradability. Protein solubility in SDS-PAGE sample buffer was highly correlated (R²=.958) with in situ protein degradability of CORN, CSM, DBG, FM, PM, and SBM. Different rates of degradation of each fraction may directly influence protein and amino acid contribution to the animal. / Master of Science

Eicosapentaenoic acid (EPA, C20:5, n-3) is a long chain crucial unsaturated fatty acid, essential for the regulation of critical biological functions in humans. Its benefits include the therapeutic treatment of cardiovascular disease, schizophrenia and Alzheimer's disease. The fungus Pythium irregulare (ATCC 10951) has great potential as a natural EPA producer. In this study, the electroporation conditions for P. irregulare were determined. The auxotrophic selectable genes ura, trp and his were respectively cloned into the plasmid pESC to construct shuttle vectors. Electroporation with 2.0kV and a 0.2cm cuvette was applied as the most effective condition for heterogeneous genes transformation. The yield and content of EPA and other components of total fatty acids (TFA) were further determined by the FAME approach with GC, as well as the analysis of biomass. The EPA content in P. irregulare with heterologous pESC-TRP vector reached 16.68 mg/g if cultured in auxotrophic medium, which showed a 52.33% increase compared to the wild-type P. irregulare. The maximum of EPA yield was 98.52 mg/L from P. irregulare containing the pESC-URA plasmid, a 32.28% increase over the wild-type. However, the maximum cell dried weight of these two organisms were respectively 6.13g/L and 5.3g/L, significantly less than the 6.80g/L of the wild-type. Not only was a feasible approach detected to electro-transform and increase the EPA yield of P. irregulare, this study also inferred that Ï -6 route was mainly involved in the EPA biosynthesis in this organism. An antisense RNA (asRNA) thermodynamic model was developed to design new asRNA constructs capable of fine-tuning gene expression knockdown. The asRNA technology is now identified as an effective and specific method for regulating microbial gene expression at the posttranscriptional level. This is done by targeting mRNA molecules. Although the study of regulation by small RNAs is advanced in eukaryotes, the regulation of expression through artificially introducing antisense oligodeoxynucleotides into host is still being developed in prokaryotes. To study the thermodynamics of asRNA and mRNA binding, (i) the fluorescence protein genes GFP and mCherry were separately cloned into the common pUC19 vector and (ii) antisense GFP and antisense mCherry DNA fragments were randomly amplified and inserted into the constructed plasmid under the control of an additional plac promoter and terminator. The expression level of fluorescence reporter proteins was determined by plate reader in this combinatorial study. A thermodynamic model to describe the relationship between asRNA binding and observed expression level was created. The study indicates two factors that minimum binding energy of the asRNA-mRNA complex and the percentage of asRNA binding mRNA were crucial for regulating the expression level. The correlation relationship between gene expression level and binding percentage multiplied by the minimum binding energy was found to show a good correlation between the thermodynamic parameters and the observed level of gene expression. The model has the potential to predict the sequence of asRNA and the approach will ultimately be applied to cyanobacteria to increase lipids production. Here, the long-term approach is to build metabolic switches from asRNA that can turn "on/off" various cellular programs and metabolic pathways at will in a fine-tuned manner. This will allow engineers to control metabolic activity in response to reactor conditions. / Master of Science

The high cell density fermentation of recombinant Pichia pastoris for human serum albumin (HSA) production is a high oxygen demand process. The oxygen demand is usually met by increased agitation rate and use of oxygen-enriched air. Microbubble fermentation however can supply adequate oxygen to the microorganisms at relatively low agitation rates because of improved mass transfer of the microbubbles used for the sparging. Conventionally sparged fermentations were conducted for the production of HSA using P. pastoris at agitation rates of 350, 500, and 750 rpm, and were compared to MBD sparged fermentation at 150, 350, and 500 rpm agitation rates. The MBD improved the volumetric oxygen transfer coefficient (kLa) and subsequently increased the cell mass and protein production compared to conventional fermentation. Cell production in MBD fermentation at 350 rpm was 4.6 times higher than that in conventional fermentation at 350 rpm, but similar to that in the conventional 750 rpm. Maximum cell mass productivity in the conventional 350 rpm was only 0.37 g / (L·h), while the maximum value in MBD 350 rpm was 2.0 g / (L·h), which was similar to 2.2 g / (L·h) in the conventional 750 rpm. Biomass yield on glycerol Ys (g cell/ g glycerol) was 0.334 g / g in the conventional 350 rpm, 0.431 g / g in MBD 350 rpm and 0.438 g / g in the conventional 750 rpm. Protein production in MBD 350 rpm was 7.3 times higher than that in the conventional 350 rpm, but similar to the conventional 750 rpm. Maximum protein productivity in the conventional 350 rpm was 0.37 mg / (L·h), 2.8 mg / (L·h) in MBD 350 rpm, and 3.3 mg / (L·h) in the conventional 750 rpm. Protein yield on methanol Yp (mg protein / g methanol) was 1.57 mg /g in the conventional 350 rpm, 5.02 in MBD 350 rpm, and 5.21 in the conventional 750 rpm. The volumetric oxygen transfer coefficient kLa was 1011.9 h-1 in MBD 350 rpm, which was 6.1 times higher than that in the conventional 350 rpm (164.9 h-1) but was similar to the conventional 750 rpm (1098 h-1). Therefore, MBD fermentation results at low agitation of 350 rpm were similar to those in the conventional fermentation at high agitation of 750 rpm. There was considerable improvement in oxygen transfer to the microorganism using MBD sparging relative to the conventional sparging. Conventional fermentations were conducted both in a Biostat Q fermenter (small) at 500 rpm, 750 rpm, and 1000 rpm, and in a Bioflo III fermenter (large) at 350 rpm, 500 rpm, and 750 rpm. At the same agitation rate of 500 rpm, cell production in the large reactor was 3.8 times higher than that in the small one, and no detectable protein was produced in the small reactor at 500 rpm. At the same agitation rate of 750 rpm, both cell production and protein production in the large reactor were 4.6 times higher than the small reactor. Thus, the Bioflo III fermenter showed higher oxygen transfer efficiency than the Biostat Q fermenter, because of the more efficient aeration design of the Bioflo III fermenter. / Master of Science

The acetone-butanol fermentation by Clostridium acetobutylicum is receiving renewed interest as a process for large scale solvent production. The fermentation kinetics have been modeled as functions of substrate, butyrate, and butanol concentrations and pH. These models have been applied to simulate batch, single stage stirred continuous, and two stage stirred continuous fermentations. The batch simulation results accurately reproduced trends of cell growth, acid production, and solvent production reported in experimental studies. The performance of the two stage, continuous process was shown to be vastly superior to that of the single stage process on the basis of outlet butanol concentration, volumetric productivity, and substrate utilization. The ratio of the two reactor volumes which will yield the maximum productivity was found to depend upon the feed substrate concentration and the desired effluent butanol concentration. The dilution rate necessary to achieve this optimum operating state was dependent upon the ratio of the reactor volumes. / M.S.

Thesis (PhDAgric (Viticulture and Oenology. Wine Biotechnology))--University of Stellenbosch, 2010. / ENGLISH ABSTRACT: Stuck alcoholic fermentations are a major enological problem for the international winemaking industry. Incomplete wine fermentations are frequently characterized by high residual fructose concentrations and the near-absence of residual glucose, a fact that is due to the glucophilic character of the wine yeast Saccharomyces cerevisiae. Wines with high contents of post fermentation sugar are very susceptible for microbial spoilage since residual fructose and/or glucose can be metabolized by bacteria and yeast to undesired by-products such as volatile acid and off-flavours, resulting in wine spoilage and considerable economic losses. It has been reported that stuck fermentations are usually caused by several synergistically acting inhibition factors, and the glucose to fructose ratio (GFR) is thought to play an important role in this context. This study is aimed at contributing towards a better understanding of this industrial problem, and at finding industrially applicable solutions. In a first part, this study describes the isolation of two appropriate strains of the fructophilic yeast Zygosaccharomyces bailii from the natural microflora of grapevine, followed by trials in small scale test fermentations using stuck industrial fermentations as model media. These experiments were expanded to also investigate large scale industrial fermentations. As a result, a strategy for the treatment of stuck fermentations was developed and successfully applied in several wineries with fermentation problems. This methodology represents an entirely novel and industrially applicable solution to high residual fructose levels. In a second part, the data contributes to elucidating the molecular nature of the fructophilic phenotype of Z. bailii by characterizing some of the genes and proteins that may be responsible for the fructophilic character. In particular, the investigation focused on the first two steps of hexose metabolism, the transport of sugar into the cell by permeases and sugar phosphorylation by hexokinases, which combined are thought to be primarily responsible for sugar preference. One result of this study was Fructoferm W3©, a dry yeast product which is commercially available. Fructoferm W3 was awarded with the innovation medal for enological products at Intervitis/Interfructa, Stuttgart, Germany in 2007. / AFRIKAANSE OPSOMMING: Die voorkoms van steek alkoholiese fermentasies is ‘n ernstige problem in die internasionale wyn industrie. Onvolledige fermentasies word dikwels gekenmerk deur hoë residuele fruktose konsentrasies en die veitlike afwesigheid van residuele glukose. Die kenmerke kan meestal toegeskryf word aan die glukofilliese kakakter van die wyngis Saccharomyces cerevisiae. Wyne met ‘n hoë suiker inhoud na die afloop van fermentasie is vatbaar vir mikrobiese bederf aangesien residuele fruktose en/of glukose gemetaboliseer kan word deur bakterië en gis om ongewenste byprodukte soos vlugtige sure en bygeure te vorm wat kan lei tot wyn bederf en aansienlike ekonomies verlies. Dit is vasgestel dat steek fermentasies gewoonlik veroorsaak word deur verskeie sinergisties werkende inhibisie faktore, waartoe die glukose/fruktose verhouding ‘n noemenswaardiege bydrae lewer. Die mikpunt van hierdie studie was om ‘n bydrae te lewer tot die begrip van steek fermentasies en die daarstelling van moontlike industriële oplossings. Die eerste deel van die werk beskryf die isolasie van twee rasse van die gis Zygosaccharomyces baillie uit die natuurlike wingerd mikroflora, gevolg deur steekproewe in die vorm van kelinskaalse fermentasies met steek industriële fermentasies gebruik as model media. Hierdie ekserimente is vervolgens uitgebrei om grootskaalse industriële steek fermentasies te bestudeer. Die uitkoms van hierdie werk het gelei tot die ontwikkeling van ‘n strategie vir die behandeling van steek fermentasies wat susksesvol toegepas is in verskeie wynmakerye. Die metodiek bring ‘n nuwe en industrieel toepasbare oplossing vir hoë residuele fruktose vlakke. Die data aangebied in die tweede afdeling dra by tot die verheldering van die molekulêre natuur van die fruktofilliese fenotipe van Z. baillie deur die tipering van gene en protiëne wat moontlik verantwoordelik is vir die fruktofilliese karakter van die gis. Die ondersoek het spesifiek op die eerste twee stappe van heksose metabolisme, naamlik die invoer van suiker in die sel deur permeases en suiker fosforilering deur heksokinases, gekonsentreer. Die kombinasie van die twee prosesse is vermoedelik verantwoordelik vir die regulering van suiker voorkeur. ‘n Gevolg van die studie was die ontwikkeling van ‘n droë gisproduk, Fructferm W3©, wat kommersieel beskikbaar gestel is. Fructoferm W3 is in 2007 toegeken met die innovasie medalje vir wynkundige produkte by Intervittis/Interfructa in Stuttgart, Duitsland.

Nous avons mis au point un fermenteur continu multi-étagé (MSCF) dans le but de reproduire les conditions de la fermentation alcoolique en conditions œnologiques. Ce bioréacteur permet de maintenir les levures dans un milieu stable et contrôlé tout en découplant la croissance et la phase stationnaire. Le système offre donc la possibilité d'obtenir des levures non croissantes dans un milieu de composition stable. Dans un premier temps, nous avons validé la pertinence du MSCF pour reproduire les conditions de fermentation du batch, par approche intégrée (des paramètres cinétiques, des métabolites intra et exo cellulaire et de l'expression génique). Nous avons ensuite utilisé ce bioréacteur pour étudier les mécanismes d'adaptation métabolique des microorganismes suite à un ajout d'azote, pratique largement répandue en œnologie. Plusieurs résultats originaux ont été obtenus concernant, notamment, la réorganisation du cycle TCA, le transport des sources azotées et la synthèse des alcools supérieurs et esters. La fiabilité de l'outil mis au point et l'originalité des données obtenues ouvrent des perspectives à l'utilisation du MSCF pour la compréhension du métabolisme et des mécanismes d'adaptation des levures. / We set up a multi-stage continuous fermentor (MSCF) to mimic the conditions of alcoholic fermentation. In this bioreactor, the yeasts are in a steady and well controlled state representative of the growth and stationary phases of the batch. The ability of the MSCF to reproduce batch fermentation was assessed using an integrated approach (measurement of kinetic parameters, intra and exo-cellular metabolites and gene expression). We then used the MSCF to study the impact of nitrogen supplementation performed during the stationary phase, on yeasts metabolism. Several original results were obtained, concerning the TCA cycle, the transport of nitrogenous sources and the synthesis of higher alcohols and esters. This work points out the interest of using the MSCF to assess the effect of medium perturbations during alcoholic fermentation, especially during the stationary phase. More generally, the accuracy of the MSCF and the originality of the data obtained open new prospects for a better understanding of yeasts metabolism and regulation mechanisms.

L'achèvement de la fermentation alcoolique est corrélé au niveau de formation de biomasse, qui varie selon les souches de levure S. cerevisiae. La maîtrise de cette fermentation passe par une meilleure compréhension des liens entre métabolisme azoté et formation de biomasse ainsi que des mécanismes contribuant aux variations de formation de biomasse entre souches. L'analyse des cinétiques de consommation de 18 composés azotés a montré que l'ordre de consommation des sources d'azote est similaire pour 14 souches et s'explique principalement par les caractéristiques cinétiques et le mode de régulation des perméases impliquées dans leur transport. Par contre, des variations sont observées dans les profils de consommation de l'azote, qui mettent en jeu des mécanismes différents suivant la disponibilité en azote du milieu. En présence d'un excès d'azote, les souches « faibles productrices » présentent une capacité limitée d'assimilation de l'ammonium ; lorsque l'azote est présent en faible quantité, elles métabolisent plus efficacement l'arginine stockée dans la vacuole pendant la phase de croissance. Afin de déterminer la distribution des flux d'azote dans la cellule, nous avons développé une approche quantitative basée sur la filiation isotopique de sources d'azote marquées 13C ou 15N. Cette étude a révélé une incorporation limitée des acides aminés exogènes dans la biomasse au profit de la synthèse de novo, à l'exception de la leucine majoritairement intégrée dans la biomasse et de l'arginine stockée dans la vacuole. Enfin, cette étude a confirmé expérimentalement que les capacités d'assimilation de l'ammonium et de remobilisation de l'arginine sont des éléments clés des différences de production de biomasse entre souches. Cette étude apporte un nouvel éclairage sur l'efficacité d'utilisation et l'allocation de sources complexes d'azote pendant la fermentation œnologique et sur les mécanismes impliqués dans la variabilité de production de biomasse chez S. cerevisiae. / The completion of alcoholic fermentation is correlated with the level of biomass formation, which varies depending on the S. cerevisiae yeast strain. Achieving a better control of the fermentation requires a better understanding of the relationship between nitrogen metabolism and biomass formation and of the mechanisms contributing to variation in biomass formation between strains. The analysis of the kinetics of consumption of 18 nitrogen compounds showed that the order of consumption of nitrogen sources is similar for 14 strains and is mainly due to the kinetic characteristics and mode of regulation of permeases involved in their transport. By cons, variations are observed in the patterns of nitrogen consumption, which involve different mechanisms depending on the availability of nitrogen in the medium. In the presence of excess nitrogen, "low producing" strains have a limited capacity for assimilation of ammonium; when nitrogen is present in small quantities, they metabolize more efficiently arginine stored in the vacuole during the growth phase. To determine the intracellular distribution of nitrogen fluxes, we developed a quantitative approach based on isotopic filiation of 13C or 15N labeled nitrogen sources. This study revealed a limited incorporation of exogenous amino acids in biomass in favor of de novo synthesis, with the exception of leucine mostly integrated in the biomass and arginine stored in the vacuole. Finally, this study confirmed experimentally that the capacity of ammonium assimilation and remobilization of arginine are key determinant governing the differences of biomass production between strains. This study sheds new light on the efficient use and allocation of complex nitrogen sources during wine fermentation and on the mechanisms involved in the differences in biomass production within the S. cerevisiae species.

Les souches Saccharomyces cerevisiae présentent une forte diversité phénotypique, notamment au niveau des propriétés fermentaires parmi les souches œnologiques. Les bases moléculaires de ces différences de comportements ainsi que les mécanismes d'adaptation à l'environnement œnologique sont encore mal connues. Les variations d'expression génique contribuent à cette diversité phénotypique, cependant les réseaux et les gènes concernés sont peu décrits. Afin d'aborder ces questions, nous avons développé une approche intégrée « génétique-génomique » qui combine la cartographie de QTL en fermentation alcoolique et les profils d'expression d'une population recombinée. La recherche de QTL d'expression nous a permis de détecter 1465 eQTL correspondant à des régulations locales ou distantes dont certaines regroupées en hotspots. Nous avons déterminé qu'une duplication d'un segment chromosomique est impliquée dans le contrôle de la cinétique de fermentation. Nos données ont révélé que les perturbations d'expression concernent de nombreux réseaux métaboliques. Nous avons caractérisé plus finement les sources de variations d'expression qui affectent les systèmes de détoxification, et avons montré que les modifications de régulation de plusieurs exporteurs membranaires sont liées à des mutations dans des facteurs de transcription. Nous avons également décrypté les variations contrôlant les gènes du métabolisme de la thiamine. Nous montrons qu'une altération du senseur Thi3p, conduit à privilégier l'expression des gènes de biosynthèse de la thiamine chez la souche œnologique aux dépens d'un gène de pyruvate décarboxylase. Ces travaux nous ont ainsi permis d'accéder à une partie des bases moléculaires responsables de la diversité et de l'adaptation des souches aux conditions œnologiques. / Saccharomyces cerevisiae strains have a high phenotypic diversity, particularly in terms of fermentation properties among wine strains. The molecular bases underlying these behavior differences and the mechanisms of adaptation to the wine environment are still poorly known. Changes in gene expressions contribute to this phenotypic diversity. However, the regulatory networks and the genes involved are badly described. To address these questions, we developed an integrated “genetics-genomics” approach that combines QTL mapping in alcoholic fermentation and expression analysis of a recombinant population. The search for expression QTL allowed us to detect 1465 eQTL corresponding to local or distant regulations, several of them being grouped into hotspots. We highlighted that a duplication of a chromosomal segment is involved in the control of the fermentation kinetics. Our data showed that the expression disturbances are involved in many metabolic networks. We characterized more precisely the sources of expression variations affecting the detoxification systems, and showed that the changes in regulation of several membrane exporters are linked to mutations in transcription factors. We have also deciphered the variations controlling genes of the thiamine metabolism. We showed that an alteration of the sensor Thi3p tends to favor the expression of genes for the thiamine biosynthesis in wine strain at the expense of a gene encoding a pyruvate decarboxylase. This work allowed us to access some of the molecular bases responsible of the diversity and the strains adaptation to oenological conditions.

Au Mexique l’état de Tamaulipas est susceptible de devenir l'un des plus grands producteurs de mezcal. Contrairement à d’autres boissons alcoolisées, la mycoflore responsable de la fermentation alcoolique du mezcal n'a pas été pleinement identifiée ou caractérisée métaboliquement. Il est d'un grand intérêt industriel de savoir si les levures indigènes impliquées dans la fermentation de moûts d’agave ont une forte nature fructophilique qui serait induite par la composition naturelle riche en fructose du moût. De plus, la caractérisation cinétique des levures et au niveau moléculaire des transporteurs impliqués dans la consommation de fructose par cette flore est pertinente étant donné que des études sur l'utilisation des hexoses par Saccharomyces cerevisiae n’ont pas montré que les transporteurs de glucose et de fructose étaient différents. Dans ce travail, la population levurienne étudiée était de 17 isolats, à partir de 103 initialement isolés de la mezcaleria "El Palmar" Emilio Lozoya, situé à San Carlos (Tamaulipas, Mexique) au niveau de différentes étapes. Seules les levures de l’espèce Saccharomyces cerevisiae ont été retenues et étudiées. En particulier de polymorphismes des 2 gènes des transporteurs principaux de sucres associes au fructose consume HXT1 et HXT3, a été évalué en comparaison à une souche de référence. Les résultats obtenus dans cette étude suggèrent la nécessité d'une analyse approfondie afin de préciser les liens entre la fructophilie et l'expression et / ou la structure des gènes des transporteurs de sucres lors de la fermentation alcoolique. / The Mexican state of Tamaulipas has the potential to become one of the main producers of mezcal. But contrary to what is known about other alcoholic beverages, the mycoflora involved in this alcoholic fermentation has not been completely identified nor characterised from the metabolic point of view. There is an increasing industrial interest on knowing if the native yeasts associated to agave must fermentations possess a fructophilic behaviour, favoured by the natural high fructose composition of the agave musts. Moreover, the kinetic characterisation of these yeasts and the molecular analysis carried out on the hexose transporters genes reported to be involved in the glucose and fructose consumption is pertinent, and several studies on Saccharomyces cerevisiae have demonstrated a differential preference for each hexose. In this study, a set of 17 yeast isolates were chosen from an original collection of 103 yeast isolated at the mezcalería El Palmar Emilio Lozoya, which is located at San Carlos (Tamaulipas, Mexico) from different stages of the fermentation. Only those belonging to S. cerevisiae specie were studied, mainly concerning the polymorphisms found on their two main hexose transporter genes associated to a preferential consumption of fructose, HXT1 and HXT3, and results compared to a control strain. The results obtained showed that there is no a direct link between the fructophilic phenotype and/or the structure of these genes and that more studies are needed to establish such relationships

L'hydrogène, qui constitue une solution alternative et durable à l’usage d’énergies fossiles, est produit essentiellement par reformage de combustibles fossiles (95%). Des filières de production plus soucieuses de l'environnement sont envisagées. Deux familles de technologies sont explorées: 1) par décomposition thermochimique ou électrochimique de l'eau et 2) à partir de différentes sources de biomasse. Parmi celles-ci, les cellules d'électrolyse microbienne ou «Microbial electrolysis cell (MEC)» permettent de produire de l'hydrogène par électrolyse de la matière organique. Une MEC consiste en une cathode classique qui assure la production d'hydrogène par la réduction électrochimique de l'eau, associée à une bioanode qui oxyde des substrats organiques en dioxyde de carbone. Ce processus d'oxydation n'est possible que grâce au développement sur l'anode d'un biofilm microbien électroactif qui joue le rôle d'électro-catalyseur. Par rapport aux procédés courants d'électrolyse de l'eau, une MEC requière un apport énergétique 5 à 10 fois plus faibles. En outre, les procédés « classiques » de production de bio-hydrogène par voie fermentaire en cultures mixtes convertissent des sucres avec des rendements limités à 2-3 moles d'hydrogène par mole d'hexose tout en coproduisant des acides organiques. Alimenté par de l'acétate, une MEC produit au maximum 3 moles d'hydrogène/mole d'acétate. Le couplage de la fermentation à un procédé d'électrolyse microbienne pourrait donc produire de 8 à 9 moles d'hydrogène/mole d'hexose, soit un grand pas vers la limite théorique de 12 moles d'hydrogène/mole d'hexose. L'objectif de cette thèse est d'analyser les liens entre la structure des communautés microbiennes dans les biofilms électroactifs et en fermentation, les individus qui les composent et les fonctions macroscopiques (électroactivité du biofilm, production d'hydrogène) qui leur sont associées dans des conditions permettant de réaliser le couplage des deux procédés. L'originalité de cette étude a été de travailler en milieu salin (30-35 gNaCl/L), favorable au transport de charges dans l'électrolyte de la MEC. Dans un premier temps, la faisabilité de la fermentation en conditions salines (3-75 gNaCl/L) a été démontrée en lien avec l'inhibition de la consommation de l'hydrogène produit et une forte prédominance d'une nouvelle souche de Vibrionaceae à des concentrations en sel supérieures à 58 gNaCl/L. D'autre part, la mise en œuvre de biofilms électroactifs dans des conditions compatibles avec la fermentation sombre a permis la sélection d'espèces dominantes dans les biofilms anodiques et présentant des propriétés électroactives très prometteuses (Geoalkalibacter subterraneus et Desulfuromonas acetoxidans) jusqu'à 8,5 A/m². En parallèle, la sélection microbienne opérée lors d'une méthode d'enrichissement utilisée pour sélectionner ces espèces à partir d'une source d'inoculum naturelle sur leur capacité à transférer leurs électrons à des oxydes de Fer(III) a été étudiée. Une baisse des performances électroactives du biofilm liée à une divergence de sélection microbienne dans ces deux techniques de sélection mène à limiter le nombre de cycle d'enrichissement sur Fer(III). Cependant, l'enrichissement sur Fer(III) reste une alternative efficace de pré-selection d'espèces électroactives qui permet une augmentation de rendement faradique de 30±4% à 99±8% par rapport au biofilm obtenu avec un inoculum non pré-acclimaté. Enfin, l'ajout d'espèces exogènes issues de la fermentation sombre sur le biofilm électroactif a révélé une baisse de l'électroactivité du biofilm se traduisant par une diminution de la densité de courant maximale produite. Cette baisse pourrait s'expliquer par à une diminution de la vitesse de transfert du substrat due à un épaississement apparent du biofilm. Cependant, un maintien de sa composition microbienne et de la quantité de biomasse laisse supposer une production d'exopolymères (EPS) dans le biofilm en situation de couplage. / Nowadays, alternative and sustainable solutions are proposed to avoid the use of fossil fuel. Hydrogen, which constitutes a promising energy vector, is essentially produced by fossil fuel reforming (95%). Environmentally friendly production systems have to be studied. Two main families of technologies are explored to produce hydrogen: 1) by thermochemical and electrochemical decomposition of water and 2) from different biomass sources. Among those last ones, microbial electrolysis cells (MEC) allow to produce hydrogen by electrolysis of organic matter. A MEC consists in a classical cathode, which provides hydrogen production by electrochemical reduction of water, associated to a bio-anode that oxidizes organic substrates into carbon dioxide. This process is only possible because of the anodic development of an electroactive microbial biofilm which constitutes an electrocatalyst. In comparison to classical water electrolysis process, a MEC requires 5 to 10 times less electrical energy and therefore reduces the energetic cost of produced hydrogen. Furthermore, classical process of dark fermentation in mixed cultures converts sugars (saccharose, glucose) to hydrogen with a limited yield of 2-3 moles of hydrogen per mole of hexose because of the coproduction of organic acids (mainly acetic and butyric acids). Fed with acetate, a MEC can produce up-to 3 moles of hydrogen per mole of acetate. Therefore, the association of these two processes could permit to produce 8 to 9 moles of hydrogen per mole of hexose, which represents a major step toward the theoretical limit of 12 moles of hydrogen per mole of hexose.Therefore, this work aims at analyzing the relationship between microbial community structures and compositions and the associated macroscopic functions (biofilm electroactive properties, hydrogen production potential) in electroactive biofilms and in dark fermentation in conditions allowing the coupling of the two processes. The originality of this study is to work in saline conditions (30-35 gNaCl/L), which favors the charges transfer in the MEC electrolyte.First of all, feasibility of dark fermentation in saline conditions (3-75 gNaCl/L) has been shown. This was linked to an inhibition of produced hydrogen consumption and the predominance of a new Vibrionaceae species at salt concentrations higher than 58 gNaCl/L. Secondly, electroactive biofilm growth in conditions compatibles to dark fermentation (pH 5.5-7 and fed with different organic acids) allowed to select dominant microbial species in anodic biofilms that present promising electroactive properties (Geoalkalibacter subterraneus and Desulfuromonas acetoxidans) with maximum current densities up to 8.5 A/m². In parallel, the microbial selection occurring during iron-reducing enrichment method used to select species from a natural inoculum source and based on their capacity to transfer electrons to iron oxydes (Fe(III)) has been studied. A decrease of electroactive performances of the biofilm linked to the divergence of microbial selection led to a limitation of the number of iron-enrichment steps. However, enrichment on Fe(III) presents an efficient alternative to pre-select electroactive species with an increase of coulombic efficiency from 30±4% to 99±8% in comparison with a biofilm obtained with a non-acclimated inoculum. Finally, the addition of exogenous bacteria from a dark fermenter on the electroactive biofilm revealed a decrease of electroactivity with a decrease of maximum current density produced. This diminution could be explained by a lower substrate transfer due to an apparent thickening of the biofilm. Nevertheless, the stability of microbial composition and of bacterial quantity on the anode suggests that a production of exopolymers (EPS) occurred.