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Articles by Christoph Wittmann in JoVE

 JoVE Immunology and Infection

Customization of Aspergillus niger Morphology Through Addition of Talc Micro Particles


JoVE 4023 3/15/2012

Institute of Biochemical Engineering, Technische Universität Braunschweig

A method to precisely generate and to comprehensively characterize morphology of filamentous fungus Aspergillus niger is described, which allows the mathematical correlation of morphological appearance and productivity.

Other articles by Christoph Wittmann on PubMed

In Vivo Analysis of Intracellular Amino Acid Labelings by GC/MS

Derivatization of Small Biomolecules for Optimized Matrix-assisted Laser Desorption/ionization Mass Spectrometry

Matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOFMS) is a powerful tool for the measurement of low molecular mass compounds of biological interest. The limitations for this method are the volatility of many analytes, possible interference with matrix signals or bad ionization or desorption behavior of the compounds. We investigated the application of well-known and straightforward one-pot derivatization procedures to circumvent these problems. The derivatizations tested allow the measurement and the labeling of alcohols, aldehydes and ketones, carboxylic acids, alpha-ketocarboxylic acids and amines.

Correcting Mass Isotopomer Distributions for Naturally Occurring Isotopes

In one method of metabolic flux analysis, simulated mass spectrometry data is fitted to measured mass distributions of metabolites that are isolated from cultures with defined feeding of (13)C-labeled substrates. Doing so, simulated mass distributions must be corrected for the presence of naturally occurring isotopes. A method that was recently introduced for this purpose consists of consecutive correction steps for each isotope of each element in the considered compound. Here we show that all isotopes of each individual element must, however, be corrected in one single step. Furthermore, it is shown that the source of information with respect to isotopic compositions of the elements needs to be chosen with care.

Metabolic Physiology of Aroma-producing Kluyveromyces Marxianus

Kluyveromyces marxianus has a high potential for industrial production of aroma compounds, such as 2-phenylethanol, which is derived in a bioconversion from L-phenylalanine. In the present work the product yield of K. marxianus in batch cultivation was estimated as 0.65 mol 2-phenylethanol/mol L-phenylalanine and thus significantly below the theoretical optimum of 1 mol/mol. By a comprehensive approach of stoichiometric balancing and GC-MS analysis of various substrates and products of K. marxianus a detailed insight into its metabolism was gained. For this purpose ring-labelled ((13)C(6)) L-phenylalanine and naturally labelled glucose were applied as substrates in tracer studies in batch culture. The produced aroma compounds 2-phenylethanol and 2-phenylethylacetate stem exclusively from the supplied L-phenylalanine, whereas glucose was not converted into these products because of efficient feed-back inhibition of prephenate dehydratase in the L-phenylalanine biosynthetic pathway. It could be further shown that the supplied L-phenylalanine completely covers the anabolic cellular demand for this amino acid. Quantification of (13)CO(2) in the exhaust gas provided clear evidence for catabolic breakdown of L-phenylalanine during cultivation. Metabolic balancing around the pool of free intracellular L-phenylalanine revealed a significant loss of L-phenylalanine into catabolic and anabolic pathways. While 73.3% of L-phenylalanine was converted into 2-phenylethanol or 2-phenylethylacetate, 22.4% was catabolized through the cinnamate pathway and 4.3% was directed towards protein biosynthesis. Catabolic breakdown of L-phenylalanine via hydroxylation to L-tyrosine could be excluded. In addition to an insight into metabolic functioning and regulation of 2-phenylethanol-producing K. marxianus, the approach presented here provides important information on potential targets for genetic optimization of 2-phenylethanol-producing yeasts.

Genealogy Profiling Through Strain Improvement by Using Metabolic Network Analysis: Metabolic Flux Genealogy of Several Generations of Lysine-producing Corynebacteria

A comprehensive approach of metabolite balancing, (13)C tracer studies, gas chromatography-mass spectrometry, matrix-assisted laser desorption ionization-time of flight mass spectrometry, and isotopomer modeling was applied for comparative metabolic network analysis of a genealogy of five successive generations of lysine-producing Corynebacterium glutamicum. The five strains examined (C. glutamicum ATCC 13032, 13287, 21253, 21526, and 21543) were previously obtained by random mutagenesis and selection. Throughout the genealogy, the lysine yield in batch cultures increased markedly from 1.2 to 24.9% relative to the glucose uptake flux. Strain optimization was accompanied by significant changes in intracellular flux distributions. The relative pentose phosphate pathway (PPP) flux successively increased, clearly corresponding to the product yield. Moreover, the anaplerotic net flux increased almost twofold as a consequence of concerted regulation of C(3) carboxylation and C(4) decarboxylation fluxes to cover the increased demand for lysine formation; thus, the overall increase was a consequence of concerted regulation of C(3) carboxylation and C(4) decarboxylation fluxes. The relative flux through isocitrate dehydrogenase dropped from 82.7% in the wild type to 59.9% in the lysine-producing mutants. In contrast to the NADPH demand, which increased from 109 to 172% due to the increasing lysine yield, the overall NADPH supply remained constant between 185 and 196%, resulting in a decrease in the apparent NADPH excess through strain optimization. Extrapolated to industrial lysine producers, the NADPH supply might become a limiting factor. The relative contributions of PPP and the tricarboxylic acid cycle to NADPH generation changed markedly, indicating that C. glutamicum is able to maintain a constant supply of NADPH under completely different flux conditions. Statistical analysis by a Monte Carlo approach revealed high precision for the estimated fluxes, underlining the fact that the observed differences were clearly strain specific.

Integrated Optical Sensing of Dissolved Oxygen in Microtiter Plates: a Novel Tool for Microbial Cultivation

Microtiter plates with integrated optical sensing of dissolved oxygen were developed by immobilization of two fluorophores at the bottom of 96-well polystyrene microtiter plates. The oxygen-sensitive fluorophore responded to dissolved oxygen concentration, whereas the oxygen-insensitive one served as an internal reference. The sensor measured dissolved oxygen accurately in optically well-defined media. Oxygen transfer coefficients, k(L)a, were determined by a dynamic method in a commercial microtiter plate reader with an integrated shaker. For this purpose, the dissolved oxygen was initially depleted by the addition of sodium dithionite and, by oxygen transfer from air, it increased again after complete oxidation of dithionite. k(L)a values in one commercial reader were about 10 to 40 h(-1). k(L)a values were inversely proportional to the filling volume and increased with increasing shaking intensity. Dissolved oxygen was monitored during cultivation of Corynebacterium glutamicum in another reader that allowed much higher shaking intensity. Growth rates determined from optical density measurement were identical to those observed in shaking flasks and in a stirred fermentor. Oxygen uptake rates measured in the stirred fermentor and dissolved oxygen concentrations measured during cultivation in the microtiter plate were used to estimate k(L)a values in a 96-well microtiter plate. The resulting values were about 130 h(-1), which is in the lower range of typical stirred fermentors. The resulting maximum oxygen transfer rate was 26 mM h(-1). Simulations showed that the errors caused by the intermittent measurement method were insignificant under the prevailing conditions.

Free Intracellular Amino Acid Pools During Autonomous Oscillations in Saccharomyces Cerevisiae

In the present work dynamic changes of free intracellular amino acid pools during autonomous oscillations of Saccharomyces cerevisiae were quantified in glucose-limited continuous cultivations. At a dilution rate of D = 0.22 h(-1) cyclic changes with a period of 120 min were found for many variables such as carbon dioxide production rate, dissolved oxygen, pH, biomass content, and various metabolite concentrations. On the basis of the observed dynamic patterns, free intracellular amino acids were classified to show oscillatory, stationary, or chaotic behavior. Amino acid pools such as serine, alanine, valine, leucine, or lysine were subjected to clear oscillations with a frequency of 120 min, identical to that of other described cultivation variables, indicating that there is a direct correlation between the periodic changes of amino acid concentrations and the metabolic oscillations on the cellular level. The oscillations of these amino acids were unequally phase-delayed and had different amplitudes of oscillation. Accordingly, they exhibited different patterns in phase plane plots vs. intracellular trehalose. Despite the complex and marked metabolic changes during oscillation, selected intracellular amino acids such as histidine, threonine, isoleucine, or arginine remained about constant. Concentrations of glutamate and glutamine showed a chaotic behavior. However, the ratio of glutamate to glutamine concentration was found to be oscillatory, with a period of 60 min and a corresponding figure eight-shaped pattern in a plot vs. trehalose concentration. Considering the described diversity, it can be concluded that the observed periodic changes are neither just the consequence of low or high rates of protein biosynthesis/degradation nor correlated to changing cell volumes during oscillation. The ratio between doubling time (189 min) and period of oscillation of intracellular amino acids (120 min) was 1:6. The fact that there is a close relationship between doubling time and period of oscillation underlines that the described autonomous oscillations are cell-cycle-associated.

Characterization and Application of an Optical Sensor for Quantification of Dissolved O2 in Shake-flasks

On-line measurement of dissolved O2 in shake-flasks was realized via immobilized sensor spots containing a fluorophore with an O2-dependent luminescent decay time. An unaffected sensor signal during 80 autoclaving cycles suggests multi-usage of sensor equipped shake-flasks. The sensor had a response time of 6 s. Quantification of gas-liquid mass transfer revealed maximum kLa values of 150 h(-1), from which maximum O2 transfer capacity of 33 mM h(-1) was calculated. Liquid volume and shaking frequency have a strong influence on kLa. Exemplified by cultivations of Corynebacterium glutamicum the importance of shaking rate for O2 supply of bacterial cultures is shown. Sampling of microbial cultures with intermittent shaking of a few minutes can cause O2 limitation. Based on the results of this work a simple and straightforward tool is now available for accurate O2 sensing in shake-flasks, which are widely used in microbial cultivations.

Dynamic Calibration and Dissolved Gas Analysis Using Membrane Inlet Mass Spectrometry for the Quantification of Cell Respiration

A membrane inlet mass spectrometer connected to a miniaturized reactor was applied for dynamic dissolved gas analysis. Cell samples were taken from 7 mL shake flask cultures of Corynebacterium glutamicum ATCC 13032, and transferred to the 12 mL miniaturized reactor. There, oxygen uptake and carbon dioxide and its mass isotopomer production rates were determined using a new experimental procedure and applying nonlinear model equations. A novel dynamic method for the calibration of the membrane inlet mass spectrometer using first-order dynamics was developed. To derive total dissolved concentration of all carbon dioxide species (C(T)) from dissolved carbon dioxide concentration ([CO(2)](aq)), the ratio of C(T) to [CO(2)](aq) was determined by nonlinear parameter estimation, whereas the mass transfer coefficient of CO(2) was determined by the Wilke-Chang correlation. Subsequently, the suitability of the model equations for respiration measurements was examined using residual analysis and the Jarque-Bera hypothesis test. The resulting residuals were found to be random with normal distribution, which proved the adequacy of the application of the model for cell respiration analysis. Hence, dynamic changes in respiration activities could be accurately analyzed using membrane inlet mass spectrometry with the novel calibration method.

Software Tool for Automated Processing of 13C Labeling Data from Mass Spectrometric Spectra

Comparative Metabolic Flux Analysis of Lysine-producing Corynebacterium Glutamicum Cultured on Glucose or Fructose

A comprehensive approach to (13)C tracer studies, labeling measurements by gas chromatography-mass spectrometry, metabolite balancing, and isotopomer modeling, was applied for comparative metabolic network analysis of lysine-producing Corynebacterium glutamicum on glucose or fructose. Significantly reduced yields of lysine and biomass and enhanced formation of dihydroxyacetone, glycerol, and lactate in comparison to those for glucose resulted on fructose. Metabolic flux analysis revealed drastic differences in intracellular flux depending on the carbon source applied. On fructose, flux through the pentose phosphate pathway (PPP) was only 14.4% of the total substrate uptake flux and therefore markedly decreased compared to that for glucose (62.0%). This result is due mainly to (i) the predominance of phosphoenolpyruvate-dependent phosphotransferase systems for fructose uptake (PTS(Fructose)) (92.3%), resulting in a major entry of fructose via fructose 1,6-bisphosphate, and (ii) the inactivity of fructose 1,6-bisphosphatase (0.0%). The uptake of fructose during flux via PTS(Mannose) was only 7.7%. In glucose-grown cells, the flux through pyruvate dehydrogenase (70.9%) was much less than that in fructose-grown cells (95.2%). Accordingly, flux through the tricarboxylic acid cycle was decreased on glucose. Normalized to that for glucose uptake, the supply of NADPH during flux was only 112.4% on fructose compared to 176.9% on glucose, which might explain the substantially lower lysine yield of C. glutamicum on fructose. Balancing NADPH levels even revealed an apparent deficiency of NADPH on fructose, which is probably overcome by in vivo activity of malic enzyme. Based on these results, potential targets could be identified for optimization of lysine production by C. glutamicum on fructose, involving (i) modification of flux through the two PTS for fructose uptake, (ii) amplification of fructose 1,6-bisphosphatase to increase flux through the PPP, and (iii) knockout of a not-yet-annotated gene encoding dihydroxyacetone phosphatase or kinase activity to suppress overflow metabolism. Statistical evaluation revealed high precision of the estimates of flux, so the observed differences for metabolic flux are clearly substrate specific.

In-depth Profiling of Lysine-producing Corynebacterium Glutamicum by Combined Analysis of the Transcriptome, Metabolome, and Fluxome

An in-depth analysis of the intracellular metabolite concentrations, metabolic fluxes, and gene expression (metabolome, fluxome, and transcriptome, respectively) of lysine-producing Corynebacterium glutamicum ATCC 13287 was performed at different stages of batch culture and revealed distinct phases of growth and lysine production. For this purpose, 13C flux analysis with gas chromatography-mass spectrometry-labeling measurement of free intracellular amino acids, metabolite balancing, and isotopomer modeling were combined with expression profiling via DNA microarrays and with intracellular metabolite quantification. The phase shift from growth to lysine production was accompanied by a decrease in glucose uptake flux, the redirection of flux from the tricarboxylic acid (TCA) cycle towards anaplerotic carboxylation and lysine biosynthesis, transient dynamics of intracellular metabolite pools, such as an increase of lysine up to 40 mM prior to its excretion, and complex changes in the expression of genes for central metabolism. The integrated approach was valuable for the identification of correlations between gene expression and in vivo activity for numerous enzymes. The glucose uptake flux closely corresponded to the expression of glucose phosphotransferase genes. A correlation between flux and expression was also observed for glucose-6-phosphate dehydrogenase, transaldolase, and transketolase and for most TCA cycle genes. In contrast, cytoplasmic malate dehydrogenase expression increased despite a reduction of the TCA cycle flux, probably related to its contribution to NADH regeneration under conditions of reduced growth. Most genes for lysine biosynthesis showed a constant expression level, despite a marked change of the metabolic flux, indicating that they are strongly regulated at the metabolic level. Glyoxylate cycle genes were continuously expressed, but the pathway exhibited in vivo activity only in the later stage. The most pronounced changes in gene expression during cultivation were found for enzymes at entry points into glycolysis, the pentose phosphate pathway, the TCA cycle, and lysine biosynthesis, indicating that these might be of special importance for transcriptional control in C. glutamicum.

Minibioreactors

The performance of currently available minibioreactors with volumes below about 100 ml is reviewed. Bioreactors are characterized by their area of application, by mass transfer and mixing characteristics and by their suitability for on-line monitoring and control. The review comprises shaken bioreactors such as shake-flasks, microtiter plates and test-tubes, stirred bioreactors including spinner-flasks for the cultivation of mammalian cells and various special reactors particularly involving on-line monitoring as e.g. membrane inlet mass spectrometry and NMR.

Impact of the Cold Shock Phenomenon on Quantification of Intracellular Metabolites in Bacteria

In the present work the effect of quenching on quantification of intracellular metabolites in Corynebacterium glutamicum was investigated. C. glutamicum showed a high sensitivity to cold shock. Quenching of the cells by -50 degrees C buffered methanol prior to cell separation and extraction led to drastically reduced concentrations for free intracellular amino acids compared to those for nonquenched filtration. As demonstrated for glutamate and glutamine, this was clearly due to a more than 90% loss of these compounds from the cell interior into the medium during quenching. With lower methanol concentration in the quenching solution the metabolic losses were significantly lower but still amounted to about 30%. Due to the fact that quenching with ice-cold NaCl (0.9%) also resulted in significantly lower pool sizes for intracellular amino acids, a basic cold shock phenomenon is most likely the reason for the observed effects. The results clearly demonstrate that quenching combined with cell separation for concentration of the cells and removal of the medium is not applicable for intracellular metabolite analysis in C. glutamicum. Sampling by quick filtration without quenching allows complete cell separation and authentic quantification of intracellular metabolite pools exhibiting time constants significantly larger than sampling time.

Metabolic Network Analysis of Lysine Producing Corynebacterium Glutamicum at a Miniaturized Scale

We present a straightforward approach comprising (13)C tracer experiments at 200-microL volume in 96-well microtiter plates with on-line measurement of dissolved oxygen for quantitative high-throughput metabolic network analysis at a miniaturized scale. This method was successfully applied for cultivation and (13)C metabolic flux analysis of two mutants of lysine producing Corynebacterium glutamicum (ATCC 13287 and ATCC 21543). Microtiter-plate cultivations showed excellent accordance in kinetics and stoichiometry of growth and product formation as well as in intracellular flux distributions as compared with parallel shake-flask experiments. These cultivations further allowed clear identification of strain-specific flux differences such as increased flux toward lysine, increased flux through the pentose phosphate pathway (PPP), decreased flux through the tricarboxylic (TCA) cycle, and increased dihydroxyacetone formation in C. glutamicum ATCC 21543 compared with ATCC 13287. The present approach has strong potential for broad quantitative screening of metabolic network activities, especially those involving high-cost tracer substrates.

Metabolic Network Simulation Using Logical Loop Algorithm and Jacobian Matrix

A novel method to accomplish efficient numerical simulation of metabolic networks for flux analysis was developed. The only inputs required are the set of stoichiometric balances and the atom mapping matrices of all components of the reaction network. The latter are used to automatically calculate isotopomer mapping matrices. Using the symbolic toolbox of MATLAB the analytical solution of the stoichiometric balance equation system, isotopomer balances and the analytical Jacobian matrix of the total set of stoichiometric and isotopomer balances are created automatically. The number of variables in the isotopomer distribution equation system is significantly reduced applying modified isotopomer mapping matrices. These allow lumping of several consecutive isotopomer reactions into a single one. The solution of the complete system of equations is improved by implementing an iterative logical loop algorithm and using the analytical Jacobian matrix. This new method provided quick and robust convergence to the root of such equation systems in all cases tested. The method was applied to a network of lysine producing Corynebacterium glutamicum. The resulting equation system with the dimension of 546 x 546 was directly derived from 12 isotopomer balance equations. The results obtained yielded identical labeling patterns for metabolites as compared to the relaxation method.

Metabolic Fluxes in Corynebacterium Glutamicum During Lysine Production with Sucrose As Carbon Source

Metabolic fluxes in the central metabolism were determined for lysine-producing Corynebacterium glutamicum ATCC 21526 with sucrose as a carbon source, providing an insight into molasses-based industrial production processes with this organism. For this purpose, 13C metabolic flux analysis with parallel studies on [1-(13C)Fru]sucrose, [1-(13C)Glc]sucrose, and [13C6Fru]sucrose was carried out. C. glutamicum directed 27.4% of sucrose toward extracellular lysine. The strain exhibited a relatively high flux of 55.7% (normalized to an uptake flux of hexose units of 100%) through the pentose phosphate pathway (PPP). The glucose monomer of sucrose was completely channeled into the PPP. After transient efflux, the fructose residue was mainly taken up by the fructose-specific phosphotransferase system (PTS) and entered glycolysis at the level of fructose-1,6-bisphosphate. Glucose-6-phosphate isomerase operated in the gluconeogenetic direction from fructose-6-phosphate to glucose-6-phosphate and supplied additional carbon (7.2%) from the fructose part of the substrate toward the PPP. This involved supply of fructose-6-phosphate from the fructose part of sucrose either by PTS(Man) or by fructose-1,6-bisphosphatase. C. glutamicum further exhibited a high tricarboxylic acid (TCA) cycle flux of 78.2%. Isocitrate dehydrogenase therefore significantly contributed to the total NADPH supply of 190%. The demands for lysine (110%) and anabolism (32%) were lower than the supply, resulting in an apparent NADPH excess. The high TCA cycle flux and the significant secretion of dihydroxyacetone and glycerol display interesting targets to be approached by genetic engineers for optimization of the strain investigated.

Dynamics of Intracellular Metabolites of Glycolysis and TCA Cycle During Cell-cycle-related Oscillation in Saccharomyces Cerevisiae

In the present work LC-MS/MS was applied to measure the concentrations of intermediates of glycolysis and TCA cycle during autonomous, cell-cycle synchronized oscillations in aerobic, glucose-limited chemostat cultures of Saccharomyces cerevisiae. This study complements previously reported oscillations in carbon dioxide production rate, intracellular concentrations of trehalose and various free amino acids, and extracellular acetate and pyruvate in the same culture. Of the glycolytic intermediates, fructose 1,6-bisphosphate, 2- and 3-phosphoglycerate, and phosphoenolpyruvate show the most pronounced oscillatory behavior, the latter three compounds oscillating out of phase with the former. This agrees with previously observed metabolic control by phosphofructokinase and pyruvate kinase. Although individually not clearly oscillating, several intermediates of the TCA cycle, i.e., alpha-ketoglutarate, succinate, fumarate, and malate, exhibited increasing concentration during the cell cycle phase with high carbon flux through glycolysis and TCA cycle. The average mass action ratios of beta-phosphoglucomutase and fumarase agreed well with previously determined in vitro equilibrium constants. Minor differences resulted for phosphoglucose isomerase and enolase. Together with the observed close correlation of the pool sizes of the involved metabolites, this might indicate that, in vivo, these reactions are operating close to equilibrium, whereby care must be taken due to possible differences between in vivo and in vitro conditions. Combining the data with previously determined intracellular amino acid levels from the same culture, a few clear correlations between catabolism and anabolism could be identified: phosphoglycerate/serine and alpha-ketoglutarate/lysine exhibited correlated oscillatory behavior, albeit with different phase shifts. Oscillations in intracellular amino acids might therefore be, at least partly, following oscillations of their anabolic precursors.

In Vivo Quantification of Intracellular Amino Acids and Intermediates of the Methionine Pathway in Corynebacterium Glutamicum

Theoretical Aspects of 13C Metabolic Flux Analysis with Sole Quantification of Carbon Dioxide Labeling

The potential of using sole respirometric CO2 labeling measurement for 13C metabolic flux analysis was investigated by metabolic simulations. For this purpose a model was created, considering all CO2 forming and consuming reactions in the central catabolic and anabolic pathways. To facilitate the interpretation of the simulation results, the underlying metabolic network was parameterized by physiologically meaningful flux parameters such as flux partitioning ratios at metabolic branch points and reaction reversibilities. For real case flux scenarios of the industrial amino acid producer Corynebacterium glutamicum and different commercially available (13)C-labeled tracer substrates, observability and output sensitivity towards key flux parameters was investigated. Metabolic net fluxes in the central metabolism, involving, e.g. glycolysis, pentose phosphate pathway, tricarboxylic acid cycle, anaplerotic carboxylation, and glyoxylate pathway were found to be determinable by the respirometric approach using a combination of [1-13C] and [6-13C] glucose in two parallel studies. The reversibilities of bidirectional reactions influence the isotopic labeling of CO2 only to a negligible degree. On one hand, they therefore cannot be determined. On the other hand, their precise values are not required for the quantification of net fluxes. Computer-aided optimal experimental design was carried out to predict the quality of the information from the respirometric tracer experiments and identify suitable tracer substrates. A combination of [1-13C] and [6-13C] glucose in two parallel studies was found to yield a similar quality of information as compared to an approach with mass spectrometric labeling analysis of secreted products. The quality of information can be further increased by additional studies with [1,2-13C2] or [1,6-13C2] glucose. Respirometric tracer studies with sole labeling analysis of CO2 are therefore promising for 13C metabolic flux analysis.

Characterization of the Metabolic Shift Between Oxidative and Fermentative Growth in Saccharomyces Cerevisiae by Comparative 13C Flux Analysis

One of the most fascinating properties of the biotechnologically important organism Saccharomyces cerevisiae is its ability to perform simultaneous respiration and fermentation at high growth rate even under fully aerobic conditions. In the present work, this Crabtree effect called phenomenon was investigated in detail by comparative 13C metabolic flux analysis of S. cerevisiae growing under purely oxidative, respiro-fermentative and predominantly fermentative conditions.

Application of Cation-exchange Membranes for Characterisation and Imaging Ammonia-oxidising Bacteria in Soils

A new approach, in which ammonia-oxidizing bacteria (AOB) are entrapped from soil onto cation-exchange membranes, was applied to identify terrestrial AOB by fluorescence in situ hybridization (FISH). An experimental hot spot of ammonia oxidation was developed by establishing a gradient of ammonium substrate (200 to <20 mg NH4+-N l(-1)) diffused through the cation-exchange membranes incubated in soil for 6 months. By this approach we were able to characterise and image indigenous AOB populations growing in heavily oil-polluted soil using FISH and sequence analysis of PCR-amplified 16S rRNA genes, respectively. The FISH results revealed that Nitrosospira-like AOB were dominant on the ammonium-enriched membranes incubated in the soil. Fourteen unique Nitrosospira-like 16S rRNA gene sequences belonging to clusters 2 and 3 were recovered from the soil-incubated membranes and from the soil, suggesting the importance of Nitrosospira-like AOB in the oil-polluted landfarming soil.

Amplified Expression of Fructose 1,6-bisphosphatase in Corynebacterium Glutamicum Increases in Vivo Flux Through the Pentose Phosphate Pathway and Lysine Production on Different Carbon Sources

The overexpression of fructose 1,6-bisphosphatase (FBPase) in Corynebacterium glutamicum leads to significant improvement of lysine production on different sugars. Amplified expression of FBPase via the promoter of the gene encoding elongation factor TU (EFTU) increased the lysine yield in the feedback-deregulated lysine-producing strain C. glutamicum lysCfbr by 40% on glucose and 30% on fructose or sucrose. Additionally formation of the by-products glycerol and dihydroxyacetone was significantly reduced in the PEFTUfbp mutant. As revealed by 13C metabolic flux analysis on glucose the overexpression of FBPase causes a redirection of carbon flux from glycolysis toward the pentose phosphate pathway (PPP) and thus leads to increased NADPH supply. Normalized to an uptake flux of glucose of 100%, the relative flux into the PPP was 56% for C. glutamicum lysCfbr PEFTUfbp and 46% for C. glutamicum lysCfbr. The flux for NADPH supply was 180% in the PEFTUfbp strain and only 146% in the parent strain. Amplification of FBPase increases the production of lysine via an increased supply of NADPH. Comparative studies with another mutant containing the sod promoter upstream of the fbp gene indicate that the expression level of FBPase relates to the extent of the metabolic effects. The overexpression of FBPase seems useful for starch- and molasses-based industrial lysine production with C. glutamicum. The redirection of flux toward the PPP should also be interesting for the production of other NADPH-demanding compounds as well as for products directly stemming from the PPP.

Quantification of S-adenosyl Methionine in Microbial Cell Extracts

A sensitive method for quantification of S-adenosyl methionine (SAM) in microbial cell extracts was developed and applied to Corynebacterium glutamicum. The method is based on SAM being completely hydrolyzed into (18)O-homoserine when extracted in boiling H(2) (18)O and thus can be clearly distinguished by GC-MS analysis from naturally labeled homoserine present in the cell extract. Additional quantification of the total homoserine pool, representing both SAM and homoserine, via HPLC allows separate determination of both metabolites.

Accumulation of Homolanthionine and Activation of a Novel Pathway for Isoleucine Biosynthesis in Corynebacterium Glutamicum McbR Deletion Strains

In the present work, the metabolic consequences of the deletion of the methionine and cysteine biosynthesis repressor protein (McbR) in Corynebacterium glutamicum, which releases almost all enzymes of methionine biosynthesis and sulfate assimilation from transcriptional regulation (D. A. Rey, A. Pühler, and J. Kalinowski, J. Biotechnol. 103:51-65, 2003), were studied. C. glutamicum ATCC 13032 DeltamcbR showed no overproduction of methionine. Metabolome analysis revealed drastic accumulation of a single metabolite, which was not present in the wild type. It was identified by isotopic labeling studies and gas chromatography/mass spectrometry as L-homolanthionine {S-[(3S)-3-amino-3-carboxypropyl]-L-homocysteine}. The accumulation of homolanthionine to an intracellular concentration of 130 mM in the DeltamcbR strain was accompanied by an elevated intracellular homocysteine level. It was shown that cystathionine-gamma-synthase (MetB) produced homolanthionine as a side reaction. MetB showed higher substrate affinity for cysteine (Km = 260 microM) than for homocysteine (Km = 540 microM). The cell is able to cleave homolanthionine at low rates via cystathionine-beta-lyase (MetC). This cleavage opens a novel threonine-independent pathway for isoleucine biosynthesis via 2-oxobutanoate formed by MetC. In fact, the deletion mutant exhibited an increased intracellular isoleucine level. Metabolic flux analysis of C. glutamicum DeltamcbR revealed that only 24% of the O-acetylhomoserine at the entry of the methionine pathway is utilized for methionine biosynthesis; the dominating fraction is either stored as homolanthionine or redirected towards the formation of isoleucine. Deletion of metB completely prevents homolanthionine accumulation, which is regarded as an important step in the development of C. glutamicum strains for biotechnological methionine production.

Metabolic Pathway Analysis for Rational Design of L-methionine Production by Escherichia Coli and Corynebacterium Glutamicum

Metabolic pathway analysis was carried out to predict the metabolic potential of Corynebacterium glutamicum and Escherichia coli for the production of L-methionine. Based on detailed stoichiometric models for these organisms, this allowed the calculation of the theoretically optimal methionine yield and related metabolic fluxes for various scenarios involving different mutants and process conditions. The theoretical optimal methionine yield on the substrates glucose, sulfate and ammonia for the wildtype of C. glutamicum is 0.49 (C-mol) (C-mol)(-1), whereas the E. coli wildtype exhibits an even higher potential of 0.52 (C-mol) (C-mol)(-1). Both strains showed completely different optimal flux distributions. C. glutamicum has a high flux through the pentose phosphate pathway (PPP), whereas the TCA cycle flux is very low. Additionally, it recruits a metabolic cycle, which involves 2-oxoglutarate and glutamate. In contrast, E. coli does minimize the flux through the PPP, and the flux through the TCA cycle is high. The improved potential of the E. coli wildtype is due to its membrane-bound transhydrogenase and its glycine cleavage system as shown by additional simulations with theoretical mutants. A key point for maximizing methionine yield is the choice of the sulfur source. Replacing sulfate by thiosulfate or sulfide increased the maximal theoretical yield in C. glutamicum up to 0.68 (C-mol) (C-mol)(-1). A further increase is possible by the application of additional C1 sources. The highest theoretical potential was obtained for C. glutamicum applying methanethiol as combined source for C1 carbon and sulfur (0.91 (C-mol) (C-mol)(-1)). Substrate requirement for maintenance purposes reduces theoretical methionine yields. In the case of sulfide used as sulfur source a maintenance requirement of 9.2 mmol ATP g(-1) h(-1), as was observed under stress conditions, would reduce the maximum theoretical yield from 67.8% to 47% at a methionine production rate of 0.65 mmol g(-1) h(-1). The enormous capability of both organisms encourages the development of biotechnological methionine production, whereby the use of metabolic pathway analysis, as shown, provides valuable advice for future strategies in strain and process improvement.

Respirometric 13C Flux Analysis--Part II: in Vivo Flux Estimation of Lysine-producing Corynebacterium Glutamicum

A novel method for metabolic flux studies of central metabolism which is based on respirometric (13)C flux analysis, i.e., parallel (13)C tracer studies with online CO(2) labeling measurements is applied to flux quantification of a lysine-producing mutant of Corynebacterium glutamicum. For this purpose, 3 respirometric (13)C labeling experiments with [1-(13)C(1)], [6-(13)C(1)] and [1,6-(13)C(2)] glucose were carried out in parallel. All fluxes comprising the reactions of glycolysis, of TCA cycle, of C3- and C4-metabolite interconversion and of lysine biosynthesis as well as the net reactions in the pentose phosphate pathway could be quantified solely using experimental data obtained from CO(2) labeling and extracellular rate measurements. At key branch points, 68+/-5% of glucose 6-phosphate were observed to be metabolized into pentose phosphate pathway and 48+/-1% of pyruvate into TCA cycle via pyruvate dehydrogenase. The results showed a good agreement with the previous studies using (13)C tracer cultivation and GC/MS analysis of proteinogenic amino acids. Also, respiratory quotient calculated from flux estimates using redox balance showed a high accordance with the value determined directly from the measured specific rates of O(2) consumption and CO(2) production. The results strongly support that the respirometric (13)C metabolic flux analysis is suited as an alternative to the conventional methods to study functional and regulatory activities of cells. The developed method is applicable to study growing or non-growing cells, primary and secondary metabolism and immobilized cells. Due to the non-accumulating nature of CO(2) labeling and instantaneous nature of the resulting fluxes, the method can also be used for dynamic profiling of metabolic activities. Therefore, it is complementary to conventional methods for metabolic flux analysis.

Respirometric 13C Flux Analysis, Part I: Design, Construction and Validation of a Novel Multiple Reactor System Using On-line Membrane Inlet Mass Spectrometry

A novel method for (13)C flux analysis based on on-line CO(2) labeling measurements is presented. This so-called respirometric (13)C flux analysis requires multiple parallel (13)C labeling experiments using differently labeled tracer substrates. In Part I of the work, a membrane-inlet mass spectrometry-based measurement system with 6 parallel reactors with each 12 ml liquid volume and associated experimental and computational methods for the respirometric (13)C data acquisition and evaluation are described. Signal dynamics after switching between membrane probes follow exactly first-order allowing extrapolation to steady state. Each measurement cycle involving 3 reactors takes about 2 min. After development of a dynamic calibration method, the suitability and reliability of the analysis was examined with a lysine-producing mutant of Corynebacterium glutamicum using [1-(13)C(1)], [6-(13)C(1)], [1,6-(13)C(2)] glucose. Specific rates of oxygen uptake and CO(2) production were estimated with an error less than +/-0.3 mmol g(-1) h(-1) and had +/-3% to +/-10% deviations between parallel reactors which is primarily caused by inaccuracies in initial biomass concentration. The respiratory quotient could be determined with an uncertainty less than +/-0.02 and varied only +/-3% between reactors. Fractional labeling of CO(2) was estimated with much higher precision of about +/-0.001 to +/-0.005. The detailed statistical analysis suggested that these data should be of sufficient quality to allow physiological interpretation and metabolic flux estimation. The obtained data were applied for the respirometric (13)C metabolic flux analysis in Part II.

Comparative Study on Central Metabolic Fluxes of Bacillus Megaterium Strains in Continuous Culture Using 13C Labelled Substrates

Fluxes of central carbon metabolism [glycolysis, pentose phosphate pathway (PPP), tricarboxylic acid cycle (TCA cycle), biomass formation] were determined for several Bacillus megaterium strains (DSM319, WH320, WH323, MS941) in C- and N-limited chemostat cultures by (13)C labelling experiments. The labelling patterns of proteinogenic amino acids were analysed by GC/MS and therefrom flux ratios at important nodes within the metabolic network could be calculated. On the basis of a stoichiometric metabolic model flux distributions were estimated for the different B. megaterium strains used at various cultivation conditions. Generally all strains exhibited similar metabolic flux distributions, however, several significant changes were found in (1) the glucose flux entering the PPP via the oxidative branch, (2) the reversibilities within the PPP, (3) the relative fluxes of pyruvate and acetyl-CoA fed to the TCA cycle, (4) the fluxes around the pyruvate node involving a futile cycle.

Transcriptional and Metabolic Responses of Bacillus Subtilis to the Availability of Organic Acids: Transcription Regulation is Important but Not Sufficient to Account for Metabolic Adaptation

The soil bacterium Bacillus subtilis can use sugars or organic acids as sources of carbon and energy. These nutrients are metabolized by glycolysis, the pentose phosphate pathway, and the Krebs citric acid cycle. While the response of B. subtilis to the availability of sugars is well understood, much less is known about the changes in metabolism if organic acids feeding into the Krebs cycle are provided. If B. subtilis is supplied with succinate and glutamate in addition to glucose, the cells readjust their metabolism as determined by transcriptome and metabolic flux analyses. The portion of glucose-6-phosphate that feeds into the pentose phosphate pathway is significantly increased in the presence of organic acids. Similarly, important changes were detected at the level of pyruvate and acetyl coenzyme A (acetyl-CoA). In the presence of organic acids, oxaloacetate formation is strongly reduced, whereas the formation of lactate is significantly increased. The alsSD operon required for acetoin formation is strongly induced in the presence of organic acids; however, no acetoin formation was observed. The recently discovered phosphorylation of acetolactate decarboxylase may provide an additional level of control of metabolism. In the presence of organic acids, both types of analyses suggest that acetyl-CoA was catabolized to acetate rather than used for feeding the Krebs cycle. Our results suggest that future work has to concentrate on the posttranslational mechanisms of metabolic regulation.

Matrix-assisted Laser Desorption/ionization Time-of-flight Mass Spectrometry for Metabolic Flux Analyses Using Isotope-labeled Ethanol

We describe a novel method for the determination of the concentration and labeling degree of ethanol originating from 1-13C-labeling experiments. This method is suitable for high-throughput metabolic flux analysis because of the possible parallel sample preparation and fast final analysis using matrix-assisted laser desorption/ionization time-of-flight mass spectrometry (MALDI-TOFMS). In a closed vial containing culture supernatant, ethanol is enzymatically oxidized to acetaldehyde. The acetaldehyde formed evaporates and is readily trapped in a second enclosed but open vial containing acidified 2,4-dinitrophenylhydrazine (DNPH). The 2,4-acetaldehyde dinitrophenylhydrazone (Ac-DNPH) that is formed is insoluble under these conditions. This leads to a constant conversion rate of the acetaldehyde produced from ethanol after 14 h minimum incubation time. MALDI-TOFMS was used to quantify the formed Ac-DNPH with [13C2]-ethanol as internal standard. The relative signal intensities of the unlabeled ethanol derivative as well as of [1-13C]-ethanol were linearly related to the ethanol concentration within a range of 1 to 50 mM with a limit of detection of 0.6 mM, a range which is sufficient for flux analysis in microtiter plate fermentation experiments. The method allows the estimation of the [1-13C]-ethanol originating from 1-13C-labeling experiments of Saccharomyces cerevisiae strains. In experiments where the expected flux range was exceeded, unlabeled ethanol was determined with a linear range from 30 to 500 mM. Ethanol quantification using this method was compared with enzymatic analysis and exhibited differences of less than 3.3% on average. Comparison of flux partitioning ratios between glycolysis and the pentose-phosphate pathway (PPP) based on MALDI-TOFMS and gas chromatography (GC)/MS methods showed good agreement, with differences for ethanol and alanine labeling of only 4.3%.

Physiology of the Yeast Kluyveromyces Marxianus During Batch and Chemostat Cultures with Glucose As the Sole Carbon Source

Growth, substrate consumption, metabolite formation, biomass composition and respiratory parameters of Kluyveromyces marxianus ATCC 26548 were determined during aerobic batch and chemostat cultivations, using mineral medium with glucose as the sole carbon source, at 30 degrees C and pH 5.0. Carbon balances closed within 95-101% in all experiments. A maximum specific growth rate of 0.56 h(-1), a biomass yield on glucose of 0.51 g g(-1), and a maximum specific consumption of oxygen of 11.1 mmol g(-1) h(-1) were obtained during batch cultures. The concentration of excreted metabolites was very low at the culture conditions applied, representing 6% of the consumed carbon at most. Acetate and pyruvate were excreted to a larger extent than ethanol under the batch conditions, and the protein content accounted for 54.6% of the biomass dry weight. Steady states were obtained during chemostats at dilution rates of 0.1, 0.25 and 0.5 h(-1). At the two former dilution rates, cells grew at carbon limitation and the biomass yield on glucose was similar to that obtained under the batch conditions. Metabolite formation was rather low, accounting for a total of 0.005 C-mol C-mol(-1) substrate. At 0.5 h(-1), although the biomass yield on glucose was similar to the value obtained under the above-mentioned conditions, the cultivation was not under carbon limitation. Under this condition, 2-oxoglutarate, acetate, pyruvate and ethanol were the prevalent metabolites excreted. Total metabolite formation only accounted to 0.056 C-mol C-mol(-1) of substrate. A very high protein and a low carbohydrate content (71.9% and 9.6% of biomass dry weight, respectively) were measured in cells under this condition. It is concluded that K. marxianus aligns with the so-called aerobic-respiring or Crabtree-negative yeasts. Furthermore, it has one of the highest growth rates among yeasts, and a high capacity of converting sugar into biomass, even when carbon is not the limiting nutrient. These results provide useful data regarding the future application of K. marxianus in processes aimed at the production of biomass-linked compounds, with high yields and productivities.

Fluxome Analysis Using GC-MS

Fluxome analysis aims at the quantitative analysis of in vivo carbon fluxes in metabolic networks, i. e. intracellular activities of enzymes and pathways. It allows investigating the effects of genetic or environmental modifications and thus precisely provides a global perspective on the integrated genetic and metabolic regulation within the intact metabolic network. The experimental and computational approaches developed in this area have revealed fascinating insights into metabolic properties of various biological systems. Most of the comprehensive approaches for metabolic flux studies today involve isotopic tracer studies and GC-MS for measurement of the labeling pattern of metabolites. Initially developed and applied mainly in the field of biomedicine these GC-MS based metabolic flux approaches have been substantially extended and optimized during recent years and today display a key technology in metabolic physiology and biotechnology.

Sampling for Metabolome Analysis of Microorganisms

In the present work we investigated the most commonly applied methods used for sampling of microorganisms in the field of metabolomics in order to unravel potential sources of error previously ignored but of utmost importance for accurate metabolome analysis. To broaden the significance of our study, we investigated different Gram-negative and Gram-positive bacteria, i.e., Bacillus subtilis, Corynebacterium glutamicum, Escherichia coli, Gluconobacter oxydans, Pseudomonas putida, and Zymononas mobilis, and analyzed metabolites from different catabolic and anabolic intracellular pathways. Quenching of cells with cold methanol prior to cell separation and extraction led to drastic loss (>60%) of all metabolites tested due to unspecific leakage. Using fast filtration, Gram-negative bacteria also revealed a significant loss (>80%) when inappropriate washing solutions with low ionic strength were applied. Adapting the ionic strength of the washing solution to that of the cultivation medium could almost completely avoid this problem. Gram-positive strains did not show significant leakage independent of the washing solution. Fast filtration with sampling times of several seconds prior to extraction appears to be a suitable approach for metabolites with relatively high intracellular level and low turnover such as amino acids or TCA cycle intermediates. Comparison of metabolite levels in the culture supernatant and the cell interior revealed that the common assumption of whole broth quenching protocols attributing the metabolites found exclusively to the intracellular pools may not be valid in many cases. In such cases a differential approach correcting for medium-contained metabolites is required.

Metabolic Flux Engineering of L-lysine Production in Corynebacterium Glutamicum--over Expression and Modification of G6P Dehydrogenase

In the present work, metabolic flux engineering of Corynebacterium glutamicum was carried out to increase lysine production. The strategy focused on engineering of the pentose phosphate pathway (PPP) flux by different genetic modifications. Over expression of the zwf gene, encoding G6P dehydrogenase, in the feedback-deregulated lysine-producing strain C. glutamicum ATCC 13032 lysC(fbr) resulted in increased lysine production on different carbon sources including the two major industrial sugars, glucose and sucrose. The additional introduction of the A243T mutation into the zwf gene and the over expression of fructose 1,6-bisphosphatase resulted in a further successive improvement of lysine production. Hereby the point mutation resulted in higher affinity of G6P dehydrogenase towards NADP and reduced sensitivity against inhibition by ATP, PEP and FBP. Overall, the lysine yield increased up to 70% through the combination of the different genetic modifications. Through strain engineering formation of trehalose was reduced by up to 70% due to reduced availability of its precursor G6P. Metabolic flux analysis revealed a 15% increase of PPP flux in response to over expression of the zwf gene. Overall a strong apparent NADPH excess resulted. Redox balancing indicated that this excess is completely oxidized by malic enzyme.

Response of the Central Metabolism of Escherichia Coli to Modified Expression of the Gene Encoding the Glucose-6-phosphate Dehydrogenase

The deletion of the zwf gene encoding G6PDH activity led to restructuring of the carbon flux through central metabolism in Escherichia coli, though over-expression of this gene had only minor consequences for overall carbon flux. The modified carbon flux seen in the zwf deletion mutant enabled alternative routes of anabolic precursor formation and an adequate supply of NADPH synthesis via a modified TCA cycle to be generated so as to sustain growth rates comparable to the WT.

Response of Fluxome and Metabolome to Temperature-induced Recombinant Protein Synthesis in Escherichia Coli

The response of the central carbon metabolism of Escherichia coli to temperature-induced recombinant production of human fibroblast growth factor was studied on the level of metabolic fluxes and intracellular metabolite levels. During production, E. coli TG1:plambdaFGFB, carrying a plasmid encoded gene for the recombinant product, revealed stress related characteristics such as decreased growth rate and biomass yield and enhanced by-product excretion (acetate, pyruvate, lactate). With the onset of production, the adenylate energy charge dropped from 0.85 to 0.60, indicating the occurrence of a severe energy limitation. This triggered an increase of the glycolytic flux which, however, was not sufficient to compensate for the increased ATP demand. The activation of the glycolytic flux was also indicated by the readjustment of glycolytic pool sizes leading to an increased driving force for the reaction catalyzed by phosphofructokinase. Moreover, fluxes through the TCA cycle, into the pentose phosphate pathway and into anabolic pathways decreased significantly. The strong increase of flux into overflow pathways, especially towards acetate was most likely caused by a flux redirection from pyruvate dehydrogenase to pyruvate oxidase. The glyoxylate shunt, not active during growth, was the dominating anaplerotic pathway during production. Together with pyruvate oxidase and acetyl CoA synthase this pathway could function as a metabolic by-pass to overcome the limitation in the junction between glycolysis and TCA cycle and partly recycle the acetate formed back into the metabolism.

Effect of Different Carbon Sources on Central Metabolic Fluxes and the Recombinant Production of a Hydrolase from Thermobifida Fusca in Bacillus Megaterium

The recombinant Bacillus megaterium strain WH323 was employed for the inducible production and secretion of recombinant Thermobifida fusca hydrolase (TFH). Continuous cultivations were carried out in a chemostat using either glucose or pyruvate as sole carbon source. A remarkable increase of produced TFH was detected for the pyruvate-dependent cultivation compared to glucose-dependent growth. Estimation of intracellular carbon fluxes through the central metabolism for both growth conditions using (13)C-labelled substrates revealed noticeable changes of the fluxes through the tricarboxylic acid cycle, the pentose phosphate pathway and around the pyruvate node when protein production was induced. With pyruvate as sole carbon source the observed alterations of the fluxes yielded an increased production of ATP and NADPH both required for the anabolism. Additionally, the analysis of the corresponding secretome revealed significantly reduced amounts of extracellular proteases in the medium compared to glucose-grown cultivations. Thus, pyruvate-dependent chemostat cultivation was identified as a favourable condition for production and secretion of recombinant TFH using B. megaterium as production host.

Metabolic Flux Screening of Saccharomyces Cerevisiae Single Knockout Strains on Glucose and Galactose Supports Elucidation of Gene Function

New methods for an extended physiological characterization of yeast at a microtiter plate scale were applied to 27 deletion mutants of Saccharomyces cerevisiae cultivated on glucose and galactose as sole carbon sources. In this way, specific growth rates, specific rates of glucose consumption and ethanol production were determined. Flux distribution, particularly concerning branching into the pentose phosphate pathway was determined using a new (13)C-labelling method using MALDI-ToF-mass spectrometry. On glucose, the growth was predominantly fermentative whereas on galactose respiration was more active with correspondingly lower ethanol production. Some deletion strains showed unexpected behavior providing very informative data about the function of the corresponding gene. Deletion of malic enzyme gene, MAE1, did not show any significant phenotype when grown on glucose but a drastically increased branching from glucose 6-phosphate into the pentose phosphate pathway when grown on galactose. This allows the conclusion that MAE1 is important for the supply of NADPH during aerobic growth on galactose.

Complete Genome Sequence of the Myxobacterium Sorangium Cellulosum

The genus Sorangium synthesizes approximately half of the secondary metabolites isolated from myxobacteria, including the anti-cancer metabolite epothilone. We report the complete genome sequence of the model Sorangium strain S. cellulosum So ce56, which produces several natural products and has morphological and physiological properties typical of the genus. The circular genome, comprising 13,033,779 base pairs, is the largest bacterial genome sequenced to date. No global synteny with the genome of Myxococcus xanthus is apparent, revealing an unanticipated level of divergence between these myxobacteria. A large percentage of the genome is devoted to regulation, particularly post-translational phosphorylation, which probably supports the strain's complex, social lifestyle. This regulatory network includes the highest number of eukaryotic protein kinase-like kinases discovered in any organism. Seventeen secondary metabolite loci are encoded in the genome, as well as many enzymes with potential utility in industry.

Metabolic Responses to Pyruvate Kinase Deletion in Lysine Producing Corynebacterium Glutamicum

ABSTRACT:

The Yeast Kluyveromyces Marxianus and Its Biotechnological Potential

Strains belonging to the yeast species Kluyveromyces marxianus have been isolated from a great variety of habitats, which results in a high metabolic diversity and a substantial degree of intraspecific polymorphism. As a consequence, several different biotechnological applications have been investigated with this yeast: production of enzymes (beta-galactosidase, beta-glucosidase, inulinase, and polygalacturonases, among others), of single-cell protein, of aroma compounds, and of ethanol (including high-temperature and simultaneous saccharification-fermentation processes); reduction of lactose content in food products; production of bioingredients from cheese-whey; bioremediation; as an anticholesterolemic agent; and as a host for heterologous protein production. Compared to its congener and model organism, Kluyveromyces lactis, the accumulated knowledge on K. marxianus is much smaller and spread over a number of different strains. Although there is no publicly available genome sequence for this species, 20% of the CBS 712 strain genome was randomly sequenced (Llorente et al. in FEBS Lett 487:71-75, 2000). In spite of these facts, K. marxianus can envisage a great biotechnological future because of some of its qualities, such as a broad substrate spectrum, thermotolerance, high growth rates, and less tendency to ferment when exposed to sugar excess, when compared to K. lactis. To increase our knowledge on the biology of this species and to enable the potential applications to be converted into industrial practice, a more systematic approach, including the careful choice of (a) reference strain(s) by the scientific community, would certainly be of great value.

Analysis of 13C Labeling Enrichment in Microbial Culture Applying Metabolic Tracer Experiments Using Gas Chromatography-combustion-isotope Ratio Mass Spectrometry

The applicability of gas chromatography-combustion-isotope ratio mass spectrometry (GC-C-IRMS) for the quantification of 13C enrichment of proteinogenic amino acids in metabolic tracer experiments was evaluated. Measurement of the 13C enrichment of proteinogenic amino acids from cell hydrolyzates of Corynebacterium glutamicum growing on different mixtures containing between 0.5 and 10% [1-13C]glucose shows the significance of kinetic isotope effects in metabolic flux studies at low degree of labeling. We developed a method to calculate the 13C enrichment. The approach to correct for these effects in metabolic flux studies using delta13C measurement by GC-C-IRMS uses two parallel experiments applying substrate with natural abundance and 13C-enriched tracer substrate, respectively. The fractional enrichment obtained in natural substrate is subtracted from that of the enriched one. Tracer studies with C. glutamicum resulted in a statistically identical relative fractional enrichment of 13C in proteinogenic amino acids over the whole range of applied concentrations of [1-13C]glucose. The current findings indicate a great potential of GC-C-IRMS for labeling quantification in 13C metabolic flux analysis with low labeling degree of tracer substrate directly in larger scale bioreactors.

Appropriate Sampling for Intracellular Amino Acid Analysis in Five Phylogenetically Different Yeasts

Methanol quenching and fast filtration, the two most common sampling protocols in microbial metabolome analysis, were validated for intracellular amino acid analysis in phylogenetically different yeast strains comprising Saccharomyces cerevisiae, Kluyveromyces marxianus, Pichia pastoris, Schizosaccharomyces pombe and Zygosaccharomyces bailii. With only few exceptions for selected amino acids, all yeasts exhibited negligible metabolite leakage during quenching with 60% cold buffered methanol. Slightly higher leakage was observed with increasing methanol content in the quenching solution. Fast filtration resulted in identical levels for intracellular amino acids in all strains tested. The results clearly demonstrate the validity of both approaches for leakage-free sampling of amino acids in yeast.

Physiological Response of Corynebacterium Glutamicum to Oxidative Stress Induced by Deletion of the Transcriptional Repressor McbR

In the present work the metabolic response of Corynebacterium glutamicum to deletion of the global transcriptional regulator McbR, which controls, e.g. the expression of enzymes of L-methionine and L-cysteine biosynthesis and sulfur assimilation, was studied. Several oxidative stress proteins were significantly upregulated among about 40 proteins in response to deletion of McbR. Linked to this oxidative stress, the mutant exhibited a 50 % reduced growth rate, a 30 % reduced glucose uptake rate and a 30 % reduced biomass yield. It also showed metabolic flux rerouting in response to the deletion. NADPH metabolism was strongly altered. In contrast to the wild-type, the deletion strain supplied significantly more NADPH than required for anabolism, indicating the activity of additional NADPH-consuming reactions. These involved enzymes of oxidative stress protection. Through redirection of metabolic carbon flux in the central catabolism, including a 40 % increased tricarboxylic acid (TCA) cycle flux, the mutant revealed an enhanced NADPH supply to provide redox power for the antioxidant systems. This, however, was not sufficient to compensate for the oxidative stress, as indicated by the drastically disturbed redox equilibrium. The NADPH/NADP+ ratio in C. glutamicum DeltamcbR was only 0.29, and thus much lower than that of the wild-type (2.35). Similarly, the NADH/NAD+ ratio was substantially reduced from 0.18 in the wild-type to 0.08 in the mutant. Deletion of McbR is regarded as a key step towards biotechnological L-methionine overproduction in C. glutamicum. C. glutamicum DeltamcbR, however, did not overproduce L-methionine; this was very likely linked to the low availability of NADPH. Since oxidative stress is often observed in industrial production processes, engineering of NADPH metabolism could be a general strategy for improvement of production strains. Unlike the wild-type, C. glutamicum DeltamcbR contained large granules with high phosphorus content. The storage of these energy-rich polyphosphates is probably the result of a large excess of formation of ATP, as revealed by estimation of the underlying fluxes linked to energy metabolism.

Metabolite Profiling Studies in Saccharomyces Cerevisiae: an Assisting Tool to Prioritize Host Targets for Antiviral Drug Screening

ABSTRACT:

Investigation of the Central Carbon Metabolism of Sorangium Cellulosum: Metabolic Network Reconstruction and Quantification of Pathway Fluxes

In the present work, the metabolic network of primary metabolism of the slow-growing myxobacterium Sorangium cellulosum was reconstructed from the annotated genome sequence of the type strain So ce56. During growth on glucose as the carbon source and asparagine as the nitrogen source, So ce56 showed a very low growth rate of 0.23 d-(1), equivalent to a doubling time of 3 days. Based on a complete stoichiometric and isotopomer model of the central metabolism, 13C metabolic flux analysis was carried out for growth with glucose as carbon and asparagine as nitrogen sources. Normalized to the uptake flux for glucose (100%), cells recruited glycolysis (51%) and the pentose phosphate pathway (48%) as major catabolic pathways. The Entner-Doudoroff pathway and glyoxylate shunt were not active. A high flux through the TCA cycle (118%) enabled a strong formation of ATP, but cells revealed a rather low yield for biomass. Inspection of fluxes linked to energy metabolism revealed that S. cellulosum utilized only 10% of the ATP formed for growth, whereas 90% is required for maintenance. This explains the apparent discrepancy between the relatively low biomass yield and the high flux through the energy-delivering TCA cycle. The total flux of NADPH supply (216%) was higher than the demand for anabolism (156%), indicating additional reactions for balancing of NADPH. The cells further exhibited a highly active metabolic cycle, interconverting C3 and C4 metabolites of glycolysis and the TCA cycle. The present work provides the first insight into fluxes of the primary metabolism of myxobacteria, especially for future investigation on the supply of cofactors, building blocks, and energy in myxobacteria, producing natural compounds of biotechnological interest.

OpenFLUX: Efficient Modelling Software for 13C-based Metabolic Flux Analysis

ABSTRACT:

Metabolic Fluxes in the Central Carbon Metabolism of Dinoroseobacter Shibae and Phaeobacter Gallaeciensis, Two Members of the Marine Roseobacter Clade

In the present work the central carbon metabolism of Dinoroseobacter shibae and Phaeobacter gallaeciensis was studied at the level of metabolic fluxes. These two strains belong to the marine Roseobacter clade, a dominant bacterial group in various marine habitats, and represent surface-associated, biofilm-forming growth (P. gallaeciensis) and symbiotic growth with eukaryotic algae (D. shibae). Based on information from recently sequenced genomes, a rich repertoire of pathways has been identified in the carbon core metabolism of these organisms, but little is known about the actual contribution of the various reactions in vivo.

Metabolic Engineering of the Tricarboxylic Acid Cycle for Improved Lysine Production by Corynebacterium Glutamicum

In the present work, lysine production by Corynebacterium glutamicum was improved by metabolic engineering of the tricarboxylic acid (TCA) cycle. The 70% decreased activity of isocitrate dehydrogenase, achieved by start codon exchange, resulted in a >40% improved lysine production. By flux analysis, this could be correlated to a flux shift from the TCA cycle toward anaplerotic carboxylation.

Flux Design: In Silico Design of Cell Factories Based on Correlation of Pathway Fluxes to Desired Properties

The identification of genetic target genes is a key step for rational engineering of production strains towards bio-based chemicals, fuels or therapeutics. This is often a difficult task, because superior production performance typically requires a combination of multiple targets, whereby the complex metabolic networks complicate straightforward identification. Recent attempts towards target prediction mainly focus on the prediction of gene deletion targets and therefore can cover only a part of genetic modifications proven valuable in metabolic engineering. Efficient in silico methods for simultaneous genome-scale identification of targets to be amplified or deleted are still lacking.

Analysis and Engineering of Metabolic Pathway Fluxes in Corynebacterium Glutamicum

The Gram-positive soil bacterium Corynebacterium glutamicum was discovered as a natural overproducer of glutamate about 50 years ago. Linked to the steadily increasing economical importance of this microorganism for production of glutamate and other amino acids, the quest for efficient production strains has been an intense area of research during the past few decades. Efficient production strains were created by applying classical mutagenesis and selection and especially metabolic engineering strategies with the advent of recombinant DNA technology. Hereby experimental and computational approaches have provided fascinating insights into the metabolism of this microorganism and directed strain engineering. Today, C. glutamicum is applied to the industrial production of more than 2 million tons of amino acids per year. The huge achievements in recent years, including the sequencing of the complete genome and efficient post genomic approaches, now provide the basis for a new, fascinating era of research - analysis of metabolic and regulatory properties of C. glutamicum on a global scale towards novel and superior bioprocesses.

Systems-wide Metabolic Pathway Engineering in Corynebacterium Glutamicum for Bio-based Production of Diaminopentane

In the present work the Gram-positive bacterium Corynebacterium glutamicum was engineered into an efficient, tailor-made production strain for diaminopentane (cadaverine), a highly attractive building block for bio-based polyamides. The engineering comprised expression of lysine decarboxylase (ldcC) from Escherichia coli, catalyzing the conversion of lysine into diaminopentane, and systems-wide metabolic engineering of central supporting pathways. Substantially re-designing the metabolism yielded superior strains with desirable properties such as (i) the release from unwanted feedback regulation at the level of aspartokinase and pyruvate carboxylase by introducing the point mutations lysC311 and pycA458, (ii) an optimized supply of the key precursor oxaloacetate by amplifying the anaplerotic enzyme, pyruvate carboxylase, and deleting phosphoenolpyruvate carboxykinase which otherwise removes oxaloacetate, (iii) enhanced biosynthetic flux via combined amplification of aspartokinase, dihydrodipicolinate reductase, diaminopimelate dehydrogenase and diaminopimelate decarboxylase, and (iv) attenuated flux into the threonine pathway competing with production by the leaky mutation hom59 in the homoserine dehydrogenase gene. Lysine decarboxylase proved to be a bottleneck for efficient production, since its in vitro activity and in vivo flux were closely correlated. To achieve an optimal strain having only stable genomic modifications, the combination of the strong constitutive C. glutamicum tuf promoter and optimized codon usage allowed efficient genome-based ldcC expression and resulted in a high diaminopentane yield of 200 mmol mol(-1). By supplementing the medium with 1 mgL(-1) pyridoxal, the cofactor of lysine decarboxylase, the yield was increased to 300 mmol mol(-1). In the production strain obtained, lysine secretion was almost completely abolished. Metabolic analysis, however, revealed substantial formation of an as yet unknown by-product. It was identified as an acetylated variant, N-acetyl-diaminopentane, which reached levels of more than 25% of that of the desired product.

Optimized Bioprocess for Production of Fructofuranosidase by Recombinant Aspergillus Niger

A comprehensive approach of bioprocess design at various levels was used to optimize microbial production of extracellular fructofuranosidase, important as biocatalyst to derive fructooligosaccharides with broad application in food or pharmaceutical industry. For production, the recombinant strain Aspergillus niger SKAn1015 was used, which expresses the fructofuranosidase encoding gene suc1 under control of a strong constitutive promoter. In a first screening towards an optimized medium, glucose, nitrate, Fe(2+), and Mn(2+) were identified as beneficial for production. A minimal medium with optimized concentration of these key nutrients, obtained by central composite design experiments and quadratic modelling, provided a threefold increased fructofuranosidase activity in the culture supernatant (400 U/mL) as compared to the originally described medium. Utilizing the optimized medium, the process was then transferred from shake flask into a fed-batch-operated bioreactor. Hereby, the intended addition of talc microparticles allowed engineering the morphology of A. niger into a highly active mycelial form, which strongly boosted production. Fructofuranosidase production was highly specific as confirmed by sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis. The secreted enzyme activity of 2,800 U/mL, corresponding to about 3 g/L of fructofuranosidase, achieved by the microparticle-enhanced fed-batch process, is tenfold higher than that of any other process reported so far, so that the presented bioprocess strategy appears as a milestone towards future industrial fructofuranosidase production.

Identification and Elimination of the Competing N-acetyldiaminopentane Pathway for Improved Production of Diaminopentane by Corynebacterium Glutamicum

The present work describes the development of a superior strain of Corynebacterium glutamicum for diaminopentane (cadaverine) production aimed at the identification and deletion of the underlying unknown N-acetyldiaminopentane pathway. This acetylated product variant, recently discovered, is a highly undesired by-product with respect to carbon yield and product purity. Initial studies with C. glutamicum DAP-3c, a previously derived tailor-made diaminopentane producer, showed that up to 20% of the product occurs in the unfavorable acetylated form. The strain revealed enzymatic activity for diaminopentane acetylation, requiring acetyl-coenzyme A (CoA) as a donor. Comparative transcriptome analysis of DAP-3c and its parent strain did not reveal significant differences in the expression levels of 17 potential candidates annotated as N-acetyltransferases. Targeted single deletion of several of the candidate genes showed NCgl1469 to be the responsible enzyme. NCgl1469 was functionally assigned as diaminopentane acetyltransferase. The deletion strain, designated C. glutamicum DAP-4, exhibited a complete lack of N-acetyldiaminopentane accumulation in medium. Hereby, the yield for diaminopentane increased by 11%. The mutant strain allowed the production of diaminopentane as the sole product. The deletion did not cause any negative growth effects, since the specific growth rate and glucose uptake rate remained unchanged. The identification and elimination of the responsible acetyltransferase gene, as presented here, display key contributions of a superior C. glutamicum strain producing diaminopentane as a future building block for bio-based polyamides.

Towards Methionine Overproduction in Corynebacterium Glutamicum--methanethiol and Dimethyldisulfide As Reduced Sulfur Sources

In the present work, methanethiol and dimethyldisulfide were investigated as sulfur source for methionine synthesis in Corynebacterium glutamicum. In silico pathway analysis has predicted a high methionine yield for these reduced compounds provided that they can be utilized. Wild type cells were able to grow on methanethiol and on dimethyldisulfide as sole sulfur source, respectively. Isotope labeling studies with mutant strains exhibiting targeted modification of methionine biosynthesis gave detailed insight into the underlying pathways involved in assimilation of methanethiol and dimethyldisulfide. Both sulfur compounds are incorporated as entire molecule, adding the terminal S-CH3 group to O-acetylhomoserine. In this reaction, methionine is directly formed. MetY (O-acetylhomoserine sulfhydrylase) was identified as enzyme catalyzing this reaction. Deletion of metY resulted in methionine auxotrophic strains grown on methanethiol or dimethyldisulfide as sole sulfur source. Plasmid based overexpression of metY in the delta metY background restored the capability to grow on methanethiol or dimethyldisulfide as sole sulfur source. In vitro studies with the C. glutamicum wild type revealed a relatively low activity of MetY for methanethiol (63 mU/mg) and dimethyldisulfide (61 mU/mg). Overexpression of metY increased the in vitro activity to 1780 mU/mg and was beneficial for methionine production, since the intracellular methionine pool was increased two-fold in the engineered strain. This positive effect was limited by depletion of the metY substrate O-acetylhomoserine, requesting for further metabolic engineering targets towards competitive production strains.

Metabolic Fluxes and Beyond-systems Biology Understanding and Engineering of Microbial Metabolism

The recent years have seen tremendous progress towards the understanding of microbial metabolism on a higher level of the entire functional system. Hereby, huge achievements including the sequencing of complete genomes and efficient post-genomic approaches provide the basis for a new, fascinating era of research-analysis of metabolic and regulatory properties on a global scale. Metabolic flux (fluxome) analysis displays the first systems oriented approach to unravel the physiology of microorganisms since it combines experimental data with metabolic network models and allows determining absolute fluxes through larger networks of central carbon metabolism. Hereby, fluxes are of central importance for systems level understanding because they fundamentally represent the cellular phenotype as integrated output of the cellular components, i.e. genes, transcripts, proteins, and metabolites. A currently emerging and promising area of research in systems biology and systems metabolic engineering is therefore the integration of fluxome data in multi-omics studies to unravel the multiple layers of control that superimpose the flux network and enable its optimal operation under different environmental conditions.

Morphology Engineering of Aspergillus Niger for Improved Enzyme Production

Supplementation with silicate microparticles was used as novel approach to control the morphological development of Aspergillus niger, important as the major world source of citric acid and higher-value enzymes, in submerged culture. With careful variation of size and concentration of the micromaterial added, a number of distinct morphological forms including pellets of different size, free dispersed mycelium, and short hyphae fragments could be reproducibly created. Aluminum oxide particles similarly affected morphology, showing that this effect is largely independent of the chemical particle composition. Image analysis of morphological development of A. niger during the cultivation process showed that the microparticles influence the morphology by collision-induced disruption of conidia aggregates and probably also the hindrance of new spore-spore interactions in the very early stage of the process. Exemplified for different recombinant A. niger strains enzyme production could be strongly enhanced by the addition of microparticles. Linked to the formation of freely dispersed mycelium, titers for glucoamylase (GA) expressed as intracellular enzyme (88 U/mL) and fructofuranosidase secreted into the supernatant (77 U/mL), were up to fourfold higher in shake flasks. Moreover, accumulation of the undesired by-product oxalate was suppressed by up to 90%. The microparticle strategy could be successfully transferred to fructofuranosidase production in bioreactor, where a final titer of 160 U/mL could be reached. Using co-expression of GA with green fluorescent protein, enzyme production was localized in the cellular aggregates of A. niger. For pelleted growth, protein production was maximal only within a thin layer at the pellet surface and markedly decreased in the pellet interior, whereas the interaction with the microparticles created a highly active biocatalyst with the dominant fraction of cells contributing to production.

From Zero to Hero--design-based Systems Metabolic Engineering of Corynebacterium Glutamicum for L-lysine Production

Here, we describe the development of a genetically defined strain of l-lysine hyperproducing Corynebacterium glutamicum by systems metabolic engineering of the wild type. Implementation of only 12 defined genome-based changes in genes encoding central metabolic enzymes redirected major carbon fluxes as desired towards the optimal pathway usage predicted by in silico modeling. The final engineered C. glutamicum strain was able to produce lysine with a high yield of 0.55 g per gram of glucose, a titer of 120 g L(-1) lysine and a productivity of 4.0 g L(-1) h(-1) in fed-batch culture. The specific glucose uptake rate of the wild type could be completely maintained during the engineering process, providing a highly viable producer. For these key criteria, the genetically defined strain created in this study lies at the maximum limit of classically derived producers developed over the last fifty years. This is the first report of a rationally derived lysine production strain that may be competitive with industrial applications. The design-based strategy for metabolic engineering reported here could serve as general concept for the rational development of microorganisms as efficient cellular factories for bio-production.

Metabolic Engineering of Corynebacterium Glutamicum for Production of 1,5-diaminopentane from Hemicellulose

In the present work, the bio-based production of 1,5-diaminopentane (cadaverine), an important building block for bio-polyamides, was extended to hemicellulose a non-food raw material. For this purpose, the metabolism of 1,5-diaminopentane-producing Corynebacterium glutamicum was engineered to the use of the C(5) sugar xylose. This was realized by heterologous expression of the xylA and xylB genes from Escherichia coli, mediating the conversion of xylose into xylulose 5-phosphate (an intermediate of the pentose phosphate pathway), in a defined diaminopentane-producing C. glutamicum strain, recently obtained by systems metabolic engineering. The created mutant, C. glutamicum DAP-Xyl1, exhibited efficient production of the diamine from xylose and from mixtures of xylose and glucose. Subsequently, the novel strain was tested on industrially relevant hemicellulose fractions, mainly containing xylose and glucose as carbon source. A two-step process was developed, comprising (i) enzymatic hydrolysis of hemicellulose from dried oat spelts, and (ii) biotechnological 1,5-diaminopentane production from the obtained hydrolysates with the novel C. glutamicum strain. This now opens a future avenue towards bio-based 1,5-diaminopentane and bio-polyamides thereof from non-food raw materials.

Filamentous Fungi in Good Shape: Microparticles for Tailor-made Fungal Morphology and Enhanced Enzyme Production

Filamentous fungi such as Aspergillus niger are important biocatalysts for industrial production of various enzymes as well as organic acids or antibiotics. In suspended culture these microorganisms exhibit a complex morphology which typically has a strong influence on their production properties. In this regard, we have recently shown that the addition of inorganic micro particles to the culture medium is a straightforward and elegant approach to precisely tame fungal morphology. For A. niger a full range of morphological forms from pellets with different diameters to free mycelium could be adjusted by supplementation with talc powder. Aluminium oxide particles similarly affected morphology, showing that this effect is largely independent of the chemical particle composition. Exemplified for different recombinant A. niger strains enzyme production could be strongly enhanced by the addition of microparticles. This was demonstrated for the production of fructofuranosidase, an important high-value biocatalyst for pre-biotic fructo-oligosaccharides, by recombinant A. niger. In a microparticle enhanced fed-batch process, a highly productive mycelium could be achieved. The enzyme titre of 2800 U/mL finally reached was more then tenfold higher then that of any other process reported so far. Here we provide additional insights into the novel production process. This includes the confirmation of the highly selective production of the target enzyme fructofuranosidase using MALDI-TOF MS analysis. Moreover, we show that the obtained enzyme suspension can be efficiently used with minimal pre-treatment for the biosynthesis of short chain fructooligosaccharides of the inulin type, such as 1-kestose and 1-nystose, prebiotics with substantial commercial interest. In particular, these compounds are highly attractive for human consumption, since they have been shown to reduce the risk of colon cancer. In summary, the use of microparticles opens a new avenue of engineering fungal morphology into the desired form for specific production processes.

Bio-based Production of the Platform Chemical 1,5-diaminopentane

In the rising era of bio-economy, the five carbon compound 1,5-diaminopentane receives increasing interest as platform chemical, especially as innovative building block for bio-based polymers. The vital interest in bio-based supply of 1,5-diaminopentane has strongly stimulated research on the development of engineered producer strains. Based on the state-of-art knowledge on the pathways and reactions linked to microbial 1,5-diaminopentane metabolism, the review covers novel systems metabolic engineering approaches towards hyper-producing cell factories of Corynebacterium glutamicum or Escherichia coli. This is integrated into the whole value chain from renewable feedstocks via 1,5-diaminopentane to innovative biopolymers involving bioprocess engineering considerations for economic supply.

Metabolic Engineering of Cellular Transport for Overproduction of the Platform Chemical 1,5-diaminopentane in Corynebacterium Glutamicum

The present work describes the development of a superior strain of Corynebacterium glutamicum for diaminopentane (cadaverine) production via metabolic engineering of cellular transport processes. In C. glutamicum DAP-3c, a tailor-made producer, the diaminopentane forming enzyme, lysine decarboxylase, was inhibited in vivo by its end-product, suggesting a potential bottleneck at the level of the export. The previously proposed lysine exporter lysE was shown not to be involved in diaminopentane export. Its deletion did not reduce diaminopentane secretion and could therefore be exploited to completely eliminate the export of lysine, an undesired by-product. Genome-wide transcription profiling revealed the up-regulation of 35 candidate genes as response to diaminopentane overproduction, including several transporters. The highest expression increase (2.6-fold) was observed for a permease, encoded by cg2893. Targeted gene deletion in the producer resulted in a 90% reduced diaminopentane secretion. Genome-based overexpression of the exporter, however, revealed a 20% increased yield, a 75% reduced formation of the undesired by-product N-acetyl-diaminopentane and a substantially higher viability, reflected by increased specific rates for growth, glucose uptake and product formation. Similarly, deletion of cg2894, TetR type repressor neighboring the permease gene, resulted in improved production properties. The discovery and amplification of the permease, as presented here, displays a key contribution towards superior C. glutamicum strains for production of the platform chemical diaminopentane. The exact function of the permease remained unclear. Its genetic modification had pronounced effects on various intracellular pools of the biosynthetic pathway, which did not allow a final conclusion on its physiological role, although a direct contribution to diaminopentane export appears possible.

Bio-based Production of Chemicals, Materials and Fuels -Corynebacterium Glutamicum As Versatile Cell Factory

Since their discovery almost 60 years ago, Corynebacterium glutamicum and related subspecies are writing a remarkable success story in industrial biotechnology. Today, these gram-positive soil bacteria, traditionally well-known as excellent producers of l-amino acids are becoming flexible, efficient production platforms for various chemicals, materials and fuels. This development is intensively driven by systems metabolic engineering concepts integrating systems biology and synthetic biology into strain engineering.

Systems Biology of Recombinant Protein Production Using Bacillus Megaterium

The Gram-negative bacterium Escherichia coli is the most widely used production host for recombinant proteins in both academia and industry. The Gram-positive bacterium Bacillus megaterium represents an increasingly used alternative for high yield intra- and extracellular protein synthesis. During the past two decades, multiple tools including gene expression plasmids and production strains have been developed. Introduction of free replicating and integrative plasmids into B. megaterium is possible via protoplasts transformation or transconjugation. Using His(6)- and StrepII affinity tags, the intra- or extracellular produced proteins can easily be purified in one-step procedures. Different gene expression systems based on the xylose controlled promoter P(xylA) and various phage RNA polymerase (T7, SP6, K1E) driven systems enable B. megaterium to produce up to 1.25g of recombinant protein per liter. Biomass concentrations of up to 80g/l can be achieved by high cell density cultivations in bioreactors. Gene knockouts and gene replacements in B. megaterium are possible via an optimized gene disruption system. For a safe application in industry, sporulation and protease-deficient as well as UV-sensitive mutants are available. With the help of the recently published B. megaterium genome sequence, it is possible to characterize bottle necks in the protein production process via systems biology approaches based on transcriptome, proteome, metabolome, and fluxome data. The bioinformatical platform (Megabac, http://www.megabac.tu-bs.de) integrates obtained theoretical and experimental data.

Integration of in Vivo and in Silico Metabolic Fluxes for Improvement of Recombinant Protein Production

The filamentous fungus Aspergillus niger is an efficient host for the recombinant production of the glycosylated enzyme fructofuranosidase, a biocatalyst of commercial interest for the synthesis of pre-biotic sugars. In batch culture on a minimal glucose medium, the recombinant strain A. niger SKAn1015, expressing the fructofuranosidase encoding suc1 gene secreted 45U/mL of the target enzyme, whereas the parent wild type SKANip8 did not exhibit production. The production of the recombinant enzyme induced a significant change of in vivo fluxes in central carbon metabolism, as assessed by (13)C metabolic flux ratio analysis. Most notably, the flux redistribution enabled an elevated supply of NADPH via activation of the cytosolic pentose phosphate pathway (PPP) and mitochondrial malic enzyme, whereas the flux through energy generating TCA cycle was reduced. In addition, the overall possible flux space of fructofuranosidase producing A. niger was investigated in silico by elementary flux mode analysis. This provided theoretical flux distributions for multiple scenarios with differing production capacities. Subsequently, the measured flux changes linked to improved production performance were projected into the in silico flux space. This provided a quantitative evaluation of the achieved optimization and a priority ranked target list for further strain engineering. Interestingly, the metabolism was shifted largely towards the optimum flux pattern by sole expression of the recombinant enzyme, which seems an inherent attractive property of A. niger. Selected fluxes, however, changed contrary to the predicted optimum and thus revealed novel targets-including reactions linked to NADPH metabolism and gluconate formation.

Microbial Production of the Drugs Violacein and Deoxyviolacein: Analytical Development and Strain Comparison

Violacein and deoxyviolacein display a broad range of interesting biological properties but their production is rarely distinguished due to the lack of suitable analytical methods. An HPLC method has been developed for the separation and quantification of violacein and deoxyviolacein and can determine the content of both molecules in microbial cultures. A comparison of different production microorganisms, including recombinant Escherichia coli and the natural producer Janthinobacterium lividum, revealed that the formation of violacein and deoxyviolacein is strain-specific but showed significant variation during growth although the ratio between the two compounds remained constant.

Systems and Synthetic Metabolic Engineering for Amino Acid Production - the Heartbeat of Industrial Strain Development

With a world market of more than four million tons per year, l-amino acids are among the most important products in industrial biotechnology. The recent years have seen a tremendous progress in the development of tailor-made strains for such products, intensively driven from systems metabolic engineering, which upgrades strain engineering into a concept of optimization on a global scale. This concept seems especially valuable for efficient amino acid production, demanding for a global modification of pathway fluxes - a challenge with regard to the high complexity of the underlying metabolism, superimposed by various layers of metabolic and transcriptional control.

Debottlenecking Recombinant Protein Production in Bacillus Megaterium Under Large Scale Conditions - Targeted Precursor Feeding Designed from Metabolomics

In the present work the impact of large production scale was investigated for Bacillus megaterium expressing green fluorescent protein (GFP). Specifically designed scale-down studies, mimicking the intermittent and continuous nutrient supply of large and small scale processes, were carried out for this purpose. The recombinant strain revealed a 40% reduced GFP yield for the large scale conditions. In line with extended carbon loss via formation of acetate and carbon dioxide, this indicated obvious limitations in the underlying metabolism of B. megaterium under the large scale conditions. Quantitative analysis of intracellular amino acids via validated fast filtration protocols revealed that their level strongly differed between the two scenarios. During cultivation in large-scale set-up, the availability of most amino acids, serving as key building blocks of the recombinant protein, was substantially reduced. This was most pronounced for tryptophan, aspartate, histidine, glutamine and lysine. In contrast alanine was increased, probably related to a bottleneck at the level of pyruvate which also triggered acetate overflow metabolism. The pre-cursor quantifications could then be exploited to verify the presumed bottlenecks and improve recombinant protein production under large scale conditions. Addition of only 5 mM tryptophan, aspartate, histidine, glutamine and lysine to the feed solution increased the GFP yield by 100%. This rational concept of driving the lab scale productivity of recombinant microorganisms under suboptimal feeding conditions emulating large scale can easily be extended to other processes and production hosts. Biotechnol. Bioeng. © 2012 Wiley Periodicals, Inc.

Industrial Biotechnology of Pseudomonas Putida and Related Species

Since their discovery many decades ago, Pseudomonas putida and related subspecies have been intensively studied with regard to their potential application in industrial biotechnology. Today, these Gram-negative soil bacteria, traditionally known as well-performing xenobiotic degraders, are becoming efficient cell factories for various products of industrial relevance including a full range of unnatural chemicals. This development is strongly driven by systems biotechnology, integrating systems metabolic engineering approaches with novel concepts from bioprocess engineering, including novel reactor designs and renewable feedstocks.

Improved Enzyme Production by Bio-pellets of Aspergillus Niger: Targeted Morphology Engineering Using Titanate Microparticles

The present study describes the design of bio-pellet morphologies of the industrial working horse Aspergillus niger strains in submerged culture. The novel approach recruits the intended addition of titanate microparticles (TiSiO(4), 8 µm) to the growth medium. As tested for two recombinant strains producing fructofuranosidase and glucoamylase, the enzyme titer by the titanate-enhanced cultures in shake flasks was increased 3.7-fold to 150 U/mL (for fructofuranosidase) and 9.5-fold to 190 U/mL (for glucoamylase) as compared to the control. This could be successfully utilized for improved enzyme production in stirred tank reactors. Stimulated by the particles, the achieved final glucoamylase activity of 1,080 U/mL (fed-batch) and 320 U/mL (batch) was sevenfold higher as compared to the conventional processes. The major reason for the enhanced production was the close association between the titanate particles and the fungal cells. Already below 2.5 g/L the micromaterial was found inside the pellets, including single particles embedded as 50-150 µm particle aggregates in the center resulting in core shell pellets. With increasing titanate levels the pellet size decreased from 1,700 µm (control) to 300 µm. Fluorescence based resolution of GFP expression revealed that the large pellets of the control were only active in a 200 µm surface layer. This matches with the critical penetration depth for nutrients and oxygen typically observed for fungal pellets. The biomass within the titanate derived fungal pellets, however, was completely active. This was due a reduced thickness of the biomass layer via smaller pellets as well as the core shell structure. Moreover, also the created loose inner pellet structure enabled a higher mass transfer and penetration depths for up to 500 µm. The creation of core-shell pellets has not been achieved previously by the addition of microparticles, for example, made of talc or alumina. Due to this, the present work opens further possibilities to use microparticles for tailor-made morphology design of filamentous fungi, especially for pellet based processes which have a long and strong industrial relevance for industrial production.

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