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Introduction: Escherichia coli, a well characterized workhorse in biotechnology, has been used to produce many recombinant proteins and metabolites, but have a major drawback in its tendency to revert to overflow metabolism. This phenomenon occurs when excess sugar triggers the production of mainly acetate under aerobic conditions, a detrimental by-product that reduces carbon efficiency, increases cell maintenance, and ultimately inhibits growth. Although this can be prevented by controlled feeding of the sugar carbon source to limit its availability, gradients in commercial-scale bioreactors can still induce it in otherwise carbon-limited cells. While the underlying mechanisms have been extensively studied, these have mostly used non-limited cultures. In contrast, industrial production typically employs carbon-limited processes, which results in a substantially different cell physiology. Objective: The objective of this study was to evaluate and compare the efficiency of different metabolic engineering strategies with the aim to reduce overflow metabolism and increase the robustness of an industrial 2'-O-fucosyllactose producing strain under industrially relevant conditions. Methods: Three distinct metabolic engineering strategies were compared: i) alterations to pathways leading to and from acetate, ii) increased flux towards the tricarboxylic acid (TCA) cycle, and iii) reduced glucose uptake rate. The engineered strains were evaluated for growth, acetate formation, and product yield under non-limiting batch conditions, carbon limited fed-batch conditions, and after a glucose pulse in fed-batch mode. Results and Discussion: The findings demonstrated that blockage of the major acetate production pathways by deletion of the pta and poxB genes or increased carbon flux into the TCA cycle by overexpression of the gltA and deletion of the iclR genes, were efficient ways to reduce acetate accumulation. Surprisingly, a reduced glucose uptake rate did not reduce acetate formation despite it having previously been shown as a very effective strategy. Interestingly, overexpression of gltA was the most efficient way to reduce acetate accumulation in non-limited cultures, whereas disruption of the poxB and pta genes was more effective for carbon-limited cultures exposed to a sudden glucose shock. Strains from both strategies showed increased tolerance towards a glucose pulse during carbon-limited growth indicating feasible ways to engineer industrial E. coli strains with enhanced robustness.
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Large-scale microbial industrial fermentations have significantly higher absolute pressure and dissolved CO2 concentrations than otherwise comparable laboratory-scale processes. Yet the effect of increased dissolved CO2 (dCO2) levels is rarely addressed in the literature. In the current work, we have investigated the impact of industrial levels of dCO2 (measured as the partial pressure of CO2, pCO2) in an Escherichia coli-based fed-batch process producing the human milk oligosaccharide 2'-fucosyllactose (2'-FL). The study evaluated the effect of high pCO2 levels in both carbon-limited (C-limited) and carbon/nitrogen-limited (C/N-limited) fed-batch processes. High-cell density cultures were sparged with 10%, 15%, 20%, or 30% CO2 in the inlet air to cover and exceed the levels observed in the industrial scale process. While the 10% enrichment was estimated to achieve similar or higher pCO2 levels as the large-scale fermentation it did not impact the performance of the process. The product and biomass yields started being affected above 15% CO2 enrichment, while 30% impaired the cultures completely. Quantitative proteomics analysis of the C-limited process showed that 15% CO2 enrichment affected the culture on the protein level, but to a much smaller degree than expected. A more significant impact was seen in the dual C/N limited process, which likely stemmed from the effect pCO2 had on nitrogen availability. The results demonstrated that microbial cultures can be seriously affected by elevated CO2 levels, albeit at higher levels than expected.
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Microbial cells in bioprocesses are usually described with averaged parameters. But in fact, single cells within populations vary greatly in characteristics such as stress resistance, especially in response to carbon source gradients. Our aim was to introduce tools to quantify population heterogeneity in bioprocesses using a combination of reporter strains, flow cytometry, and easily comprehensible parameters. We calculated mean, mode, peak width, and coefficient of variance to describe distribution characteristics and temporal shifts in fluorescence intensity. The skewness and the slope of cumulative distribution function plots illustrated differences in distribution shape. These parameters are person-independent and precise. We demonstrated this by quantifying growth-related population heterogeneity of Saccharomyces cerevisiae and Escherichia coli reporter strains in steady-state of aerobic glucose-limited chemostat cultures at different dilution rates and in response to glucose pulses. Generally, slow-growing cells showed stronger responses to glucose excess than fast-growing cells. Cell robustness, measured as membrane integrity after exposure to freeze-thaw treatment, of fast-growing cells was strongly affected in subpopulations of low membrane robustness. Glucose pulses protected subpopulations of fast-growing but not slower-growing yeast cells against membrane damage. Our parameters could successfully describe population heterogeneity, thereby revealing physiological characteristics that might have been overlooked during traditional averaged analysis.
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Human Milk Oligosaccharides (HMOs) constitute an important, highly abundant part of mothers' milk delivering many health benefits to the neonate. Until recently, limited availability of HMOs has prevented their use in infant nutrition and impeded research into their biological effects. The shift from chemical synthesis to biotechnological manufacturing has made them accessible in quantities and at prices that are within reach for commercial applications, including infant formula. It accelerated the studies in the field of pre-clinical and clinical HMO biology. This review gives a short overview of HMO manufacturing from the design and optimization of the microbial cell factory and the production of HMOs in the industrial fermentation process to the purification in the downstream process necessary to obtain a final product. Moreover, the transition from chemistry to biotechnology and the current regulatory landscape and commercialization progress are briefly reviewed.
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Bacterias/metabolismo , Biotecnología/métodos , Ingeniería Celular/métodos , Leche Humana/química , Oligosacáridos/biosíntesis , Humanos , Redes y Vías MetabólicasRESUMEN
A control point for keeping redox homeostasis in Saccharomyces cerevisiae during fermentative growth is the dynamic regulation of transcription for the glycerol-3-phosphate dehydrogenase 2 (GPD2) gene. In this study, the possibility to steer the activity of the GPD2 promoter was investigated by placing it in strains with different ability to reoxidise NADH, and applying different environmental conditions. Flow cytometric analysis of reporter strains expressing green fluorescent protein (GFP) under the control of the GPD2 promoter was used to determine the promoter activity at the single-cell level. When placed in a gpd1Δgpd2Δ strain background, the GPD2 promoter displayed a 2-fold higher activity as compared to the strong constitutive glyceraldehyde-3-phosphate dehydrogenase (TDH3). In contrast, the GPD2 promoter was found to be inactive when cells were cultivated in continuous mode at a growth rate of 0.3 h-1 and in conditions with excess oxygen (i.e. with an aeration of 2.5 vvm, and a stirring of 800 rpm). In addition, a clear window of operation where the gpd1Δgpd2Δ strain can be grown with the same efficiency as wild type yeast was identified. In conclusion, the flow cytometry mapping revealed conditions where the GPD2 promoter was either completely inactive or hyperactive, which has implications for its implementation in future biotechnological applications such as for process control of heterologous gene expression.
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Siderophores are biosynthetically produced and secreted by many bacteria, yeasts, fungi and plants, to scavenge for ferric iron (Fe(3+)). They are selective iron-chelators that have an extremely high affinity for binding this trivalent metal ion. The ferric ion is poorly soluble but it is the form of iron that is predominantly found in oxygenated environments. Siderophore uptake in bacteria has been extensively studied and over the last decade, detailed structural information for many of the proteins that are involved in their transport has become available. Specifically, numerous crystal structures for outer membrane siderophore transporters, as well as for soluble periplasmic siderophore-binding proteins, have been reported. Moreover, unique siderophore-binding proteins have recently been serendipitously discovered in humans, and the structures of some of their siderophore-complexes have been characterized. The binding pockets for different ferric-siderophores in these proteins have been described in great molecular detail. In addition to highlighting this structural information, in this review paper we will also briefly discuss the relevant chemical properties of iron, and provide a perspective on our current understanding of the human and bacterial iron uptake pathways. Potential clinical uses of siderophores will also be discussed. The emerging overall picture is that iron metabolism plays an extremely important role during bacterial infections. Because levels of free ferric iron in biological systems are always extremely low, there is serious competition for iron and for ferric-siderophores between pathogenic bacteria and the human or animal host.
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Bacterias/metabolismo , Hierro/metabolismo , Sideróforos/metabolismo , Animales , Humanos , Inmunidad Innata , Hierro/química , Quelantes del Hierro/metabolismo , Quelantes del Hierro/uso terapéutico , Lipocalinas/química , Modelos Moleculares , Conformación Proteica , Sideróforos/química , Sideróforos/uso terapéuticoRESUMEN
Reduction of bicyclo[2.2.2]octane-2,6-dione to (1R, 4S, 6S)-6-hydroxy-bicyclo[2.2.2]octane-2-one by whole cells of Saccharomyces cerevisiae was improved using an engineered recombinant strain and process design. The substrate inhibition followed a Han-Levenspiel model showing an effective concentration window between 12 and 22 g/l, in which the activity was kept above 95%. Yeast growth stage, substrate concentration and a stable pH were shown to be important parameters for effective conversion. The over-expression of the reductase gene YDR368w significantly improved diastereoselectivity compared to previously reported results. Using strain TMB4110 expressing YDR368w in batch reduction with pH control, complete conversion of 40 g/l (290 mM) substrate was achieved with 97% diastereomeric excess (de) and >99 enantiomeric excess (ee), allowing isolation of the optically pure ketoalcohol in 84% yield.
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Compuestos Bicíclicos con Puentes/metabolismo , Saccharomyces cerevisiae/genética , Saccharomyces cerevisiae/metabolismo , Concentración de Iones de Hidrógeno , Oxidación-Reducción , Saccharomyces cerevisiae/enzimología , Proteínas de Saccharomyces cerevisiae/genética , Proteínas de Saccharomyces cerevisiae/metabolismo , Estereoisomerismo , Especificidad por Sustrato/genéticaRESUMEN
The two main metabolic pathways involved in sugar metabolism, i.e., the pentose phosphate pathway (PPP) and the glycolytic pathway (GP), were amperometrically monitored using a double-mediator system composed of menadione and ferricyanide. With the use of the Saccharomyces cerevisiae deletion mutant, EBY44, lacking the gene encoding for the branch point enzyme phosphoglucose isomerize, selective amperometric monitoring of the PPP, mainly producing NADPH, and the GP, mainly producing NADH, could be achieved. It was found that the bioelectrocatalytic current was primarily originating from NADPH. This conclusion was supported by metabolite flux analysis, confirming that, in the presence of menadione, the cells increase the rate of NADPH-producing reactions although these processes might be detrimental to cell survival. The higher rate of in vivo NADPH-dependent menadione reduction can be ascribed to the fact that the intracellular NADPH/NADP(+) ratio is much higher than NADH/NAD(+) as well as that the former ratio is more tightly controlled. This tight control over the cofactor ratios is lost upon cell disintegration as observed from spectrophotometric assays using crude cell extract, and amperometric investigations of permeabilized cells indicate a higher rate of NADH- than NADPH-dependent menadione reduction. These in vitro experiments show a higher activity of NADH-dependent than NADPH-dependent menadione-reducing dehydrogenases in S. cerevisiae cells.
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Electroquímica/métodos , Glucólisis , Vía de Pentosa Fosfato , Saccharomyces cerevisiae/metabolismo , Catálisis , NADP/biosíntesisRESUMEN
A screening of non-conventional yeast species and several Saccharomyces cerevisiae (baker's yeast) strains overexpressing known carbonyl reductases revealed the S. cerevisiae reductase encoded by YMR226c as highly efficient for the reduction of the diketones 1 and 2 to their corresponding hydroxyketones 3-6 (Scheme 1) in excellent enantiomeric excesses. Bioreduction of 1 using the genetically engineered yeast TMB4100, overexpressing YMR226c, resulted in >99% ee for hydroxyketone (+)-4 and 84-98% ee for (-)-3, depending on the degree of conversion. Baker's yeast reduction of diketone 2 resulted in >98% ee for the hydroxyketones (+)-5 and (+)-6. However, TMB4100 led to significantly higher conversion rates (over 40 fold faster) and also a minor improvement of the enantiomeric excesses (>99%).
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Compuestos Bicíclicos con Puentes/metabolismo , Saccharomyces cerevisiae/genética , Saccharomyces cerevisiae/metabolismo , Compuestos Bicíclicos con Puentes/química , Ingeniería Genética/métodos , Cetonas/química , Cetonas/metabolismo , Oxidación-Reducción , Oxidorreductasas/genética , Oxidorreductasas/metabolismo , Saccharomyces cerevisiae/enzimologíaRESUMEN
Pure chiral molecules are needed in the pharmaceutical and chemical industry as intermediates for the production of drugs or fine chemicals. Microorganisms represent an attractive alternative to chemical synthesis since they have the potential to generate single stereoisomers in high enantiomeric excess (ee). The baker's yeast Saccharomyces cerevisiae can notably reduce dicarbonyl compounds (in particular alpha- and beta-diketones and keto esters) to chiral alcohols with high ee. However, products are formed at a low rate. Moreover, large amounts of co-substrate are required for the regeneration of NADPH that is the preferred co-factor in almost all the known dicarbonyl reductions. Traditionally, better ee, reduction rate and product titre have been achieved via process engineering. The advent of recombinant DNA technology provides an alternative strategy to improve productivity and yield by strain engineering. This review discusses two aspects of strain engineering: (i) the generation of strains with higher reductase activity towards dicarbonyl compounds and (ii) the optimisation of co-substrate utilisation for NADPH cofactor regeneration.
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Oxidorreductasas de Alcohol/genética , Ingeniería Genética/métodos , Cetonas/metabolismo , Saccharomyces cerevisiae/enzimología , Saccharomyces cerevisiae/genética , Oxidorreductasas de Alcohol/metabolismo , Aldehído Reductasa , Aldo-Ceto Reductasas , Cetonas/química , Saccharomyces cerevisiae/metabolismo , Proteínas de Saccharomyces cerevisiae/genética , Proteínas de Saccharomyces cerevisiae/metabolismo , Estereoisomerismo , Especificidad por SustratoRESUMEN
This study demonstrated the occurrence of a NADPH-dependent exo-alcohol reductase in the crude membrane fraction of Candida tropicalis. Cytosolic endo-alcohol reductase activity could be separated from the membrane-bound exo-alcohol activity by means of detergent treatment, enabling the preparation of pure exo-alcohol via the enzymatic conversion of the bicyclic diketone, bicyclo[2.2.2]octane-2,6-dione. The exo-alcohol reductase is, to our knowledge, the first membrane-bound NADPH-dependent reductase accepting a xenobiotic carbonyl substrate that was not a steroid. When C. tropicalis was grown on D-sorbitol, a two-fold increase in the exo-reductase activity was observed as compared to when grown on glucose. An in silico comparison at the protein level between putative xenobiotic carbonyl reductases in Candida albicans, C. tropicalis and Saccharomyces cerevisiae was performed to explain why Candida species are often encountered when screening yeasts for novel stereoselective reduction properties. C. albicans contained more reductases with the potential to reduce xenobiotic carbonyl compounds than did S. cerevisiae. C. tropicalis had many membrane-bound reductases (predicted with the bioinformatics program, TMHMM), some of which had no counterpart in the two other organisms. The exo-reductase is suspected to be either a beta-hydroxysteroid dehydrogenase or a polyol dehydrogenase from either the short chain dehydrogenase family or the dihydroflavonol reductase family.