Defining an optimal carbon source/methionine feed strategy for growth and cephalosporin C formation by Cephalosporium acremonium.

The effect of the method of methionine addition, growth-limiting carbon source (glucose vs sucrose), and culture growth rate on cephalosporin C production was investigated in a Cephalosporium acremonium defined medium fed batch fermentation. Batch addition of methionine, at a concentration of 3 g/L, prior to the start of a fed sucrose fermentation was found to interfere with the ability of the culture to utilize this sugar, thus limiting growth and decreasing cephalosporin C production. Batch methionine addition had no effect on glucose-limited cultures. Concurrent exponential feeding of methionine with sucrose improved both culture growth and productivity. Under the control of identical carbon source limiting feed profiles, sucrose was observed to support greater cephalosporin C production than glucose. Optimal cephalosporin C production in a C. acremonium defined medium fed batch fermentation was obtained through controlling culture growth during the rapid growth phase at a relatively low level with respect to mumax (mu approximately 0.036 h-1) until achieving a desired cell mass with a concurrent sucrose and methionine feed, followed by maintaining relatively vigorous growth (mu approximately 0.01 h-1) with sucrose for the duration of the fermentation.     

Kinetics of polysaccharide B-1459 fermentation

Polysaccharide gum was made by fermentation with Xanthomonas campestris NRRL B-1459 in a medium of glucose, minerals, and distillers' solubles. The effect of distillers' solubles on growth rate can be described by the familiar saturation equation. Although a quasistoichiometric relationship was observed between nitrogen utilization and growth, total nitrogen supply was not growth limiting, nor was polymer formation growth associated. Cell growth primarily took place in the early part of the fermentation; polysaccharide biosynthesis occurred throughout the fermentation. Glucose was converted to polysaccharide at a fairly constant yield, which was 70–80% of glucose consumed, under optimum conditions. The kinetic patterns observed indicate that multistage continuous fermentation will be suitable for polysaccharide production.     

Influence of end-products inhibition and nutrient limitations on the growth of Lactococcus lactis subsp. lactis

Lactococcus lactis was grown in a simple synthetic medium with glucose as substrate, enabling the precise quantification of each nutrient's contribution to growth. As expected, for the growth of lactic acid bacteria, the growth rate decreased progressively during the cultivation after a short period of exponential growth. End-products of fermentation, predominantly lactate and in minor amounts formate, acetate and ethanol, accumulated within the medium. Growth of the bacterium in fresh media supplemented with these end-products showed that the concentrations attained in the fermentor had no significant influence on the growth rate. As regards nutrients, vitamins and magnesium were never limiting during the culture. On the other hand, amino acid concentrations decreased, some of them being totally consumed and exhausted from the medium before growth ceased. However, growth in reconstituted media constructed with the amino acid concentrations remaining at different times of cultivation showed that amino acid depletion could not account for the observed growth decrease. Batch culture supernatant fluid was used as cultivation medium. Growth rates observed in supernatant cultures supplemented with various nutrients, compared to non-supplemented supernatant, showed that no addition improved growth. Finally, it was concluded that in the experimental conditions used in this study, growth inhibition was predominantly due to phenomena other than lactate inhibition and nutritional limitations, and hence associated with unidentified compounds produced in the fermentation.     

Acetate inhibition of Pseudomonas putida

To study the effect of acetate inhibition on the parameters of yield and maintenance for bacterial growth, Pseudomonas putida ATCC 23467 was grown in a minimal salts medium with acetate as the sole carbon source with limiting and with excess quantities of urea in the feed medium. The behavior of the chemostat cultures under sole acetate limitation results in low residual acetate present in the fermentation broth. These cultures can be described satisfactorily using the equation q(s) = D/Y(g) + m, i.e., the acetate is consumed only for growth and maintenance,. Those cultures in which urea was limiting or where urea was present in large excess contained significant amounts of residual acetate in the broth. For these cultures it was necessary to add a third term for acetate inhibition to the above expression.     

Metabolic profiles and aprE expression in anaerobic cultures of Bacillus subtilis using nitrate as terminal electron acceptor

Cultures using nitrate as the terminal electron acceptor were conducted in Schaeffer's medium to evaluate the growth performance and metabolic profiles of Bacillus subtilis, and its potential to express the aprE (subtilisin) gene under anoxic conditions. Nitrate was converted to ammonia through nitrite reduction; and different product profiles were observed during the growth phase when nitrate was added at various concentrations (4-24 mM) to Schaeffer's medium containing glucose (4 g l(-1)). If nitrate was not limiting, then acetic acid and acetoin were accumulated, suggesting a limitation of reduced cofactors but, if nitrate became limiting, then lactic acid and butanediol were accumulated, suggesting an excess of reduced cofactors. Due to a strong lysis at the onset of the end of the growth phase, sporulation frequency and aprE expression were negligible in anaerobic batch cultures. Fed-batch fermentation allowed the development of a stationary phase through a continuous supply of glucose and nitrate. In this case, sporulation frequency was almost null, but interestingly aprE expression was similar to that found in aerobic cultures.     

Requirement of heme for growth of Bacteroides fragilis.

Heme or protoporphyrin IX was required for growth of Bacteroides fragilis in a defined medium. The amount of heme necessary for half-maximal growth was 2 to 10 ng/ml (3.8 to 15 pmol/ml) among the Bacteroides species and strains tested. The growth rate, metabolic products from glucose fermentation, and cell yields were affected by the concentration of heme in the medium and by the length of time the culture was incubated. When heme was growth limiting (4 ng/ml), growth rates decreased by 50%, cultures started producing lactic and fumaric acids, and the cell yields declined. The cell yield for B. fragilis (ATCC 25285) at 24 h in medium containing 6.5 microgram of heme per ml was 69 g (dry weight) of cells per mol of glucose compared to 16 g (dry weight) of cells per mol of glucose with 4 ng of heme per ml. B. fragilis was unable to grow in defined medium when a porphyrin precursor, delta-aminolevulenic acid or porphobilinogen, was added in place of heme.     

Growth, maintenance and fermentation pattern of the salt-tolerant lactic acid bacterium Tetragenococcus halophila in anaerobic glucose limited retention cultures

The homofermentative lactic acid bacterium Tetragenococcus halophila showed mixed acid fermentation at low growth-rates under glucose limiting conditions and in the presence of 10% NaCl. Maximum growth yields in fermentors with cell retention were not affected by pH, but maintenance requirement was at pH 5.2 four times higher than at pH 7.0. Despite the high salt-concentration of the medium, maintenance requirements were low compared to other lactic acid bacteria. The possible causes of the observed differences in maintenance requirements are discussed.     

Effects of nutrients on the production of AK-111-81 macrolide antibiotic by Streptomyces hygroscopicus

The influence of different carbon and nitrogen sources on the production of AK-111-81 nonpolyenic macrolide antibiotic by Streptomyces hygroscopicus 111-81 was studied. Substitution of glucose with lactose or glycerol significantly affected maximal antibiotic AK-111-81 productivity as the growth rate was close to that of the basal fermentation medium. Addition of ammonium succinate to the fermentation medium markedly increased the antibiotic productivity as the growth rate was low. Divalent ions as Mn2+, Cu2+, Fe2+ stimulated AK-111-81 antibiotic biosynthesis. These results allow us to develop a new fermentation medium showing 6-fold increase of AK-111-81 antibiotic formation compared with the basal fermentation medium.     

Drug resistance marker-aided genome shuffling to improve acetic acid tolerance in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Acetic acid existing in a culture medium is one of the most limiting constraints in yeast growth and viability during ethanol fermentation. To improve acetic acid tolerance in Saccharomyces cerevisiae strains, a drug resistance marker-aided genome shuffling approach with higher screen efficiency of shuffled mutants was developed in this work. Through two rounds of genome shuffling of ultraviolet mutants derived from the original strain 308, we obtained a shuffled strain YZ2, which shows significantly faster growth and higher cell viability under acetic acid stress. Ethanol production of YZ2 (within 60 h) was 21.6% higher than that of 308 when 0.5% (v/v) acetic acid was added to fermentation medium. Membrane integrity, higher in vivo activity of the H⁺-ATPase, and lower oxidative damage after acetic acid treatment are the possible reasons for the acetic acid-tolerance phenotype of YZ2. These results indicated that this novel genome shuffling approach is powerful to rapidly improve the complex traits of industrial yeast strains.     

Microcalorimetry: A tool for the study of the biodegradability of straw by mixed bacterial cultures

Summary The biodegradability of straw by a mixed bacterial culture obtained from a pile of weeds was studied by microcalorimetry. All the cultures were grown at 30°C under anaerobic conditions in microcalorimetric vessels. The fermentation thermograms, obtained using well defined conditions, were very reproducible. The quantities of heat produced during straw degradation were found to be proportional to the quantity of straw introduced at the beginning of the fermentation.The recovered carbon was also found to be proportional to the initial quantity of straw. From both microcalorimetric and chemical analysis it was concluded that the limiting factor of the straw degradation was the cellulolytic activity of the mixed culture. This is supported by the fact that commercially available cellulase added to the growth medium increases the amount of straw degradation by about four times. The heat associated with fermentation of each cellulose monomer (C₆H₁₀O₅) was found to be 120 kJ, a value which is close to the heat associated with hexose fermentation by pure cultures. In conclusion, we propose that microcalorimetry can be used as a powerful tool for the analysis of the biodegradability of complex heterogeneous substrate by pure or mixed cultures.     

Glycine origin of the methyl substituent on C7'-N of octodiose for the biosynthesis of apramycin

Apramycin is unique in the aminoglycoside family due to its octodiose moiety. However, either the biosynthesis process or the precursors involved are largely unknown. Addition of glycine, as well as serine or threonine, to the Streptomyces tenebrabrius UD2 fermentation medium substantially increases the production of apramycin with little effect on the growth of mycelia, indicating that glycine and/or serine might be involved in the biosynthesis of apramycin. The 13C-NMR analysis of [2-13C] glycine-fed (25% enrichment) apramycin showed that glycine specifically and efficiently incorporated into the only N-CH3 substituent of apramycin on the C7' of the octodiose moiety. We noticed that the in vivo concentration of S-adenosyl methionine increased in parallel with the addition of glycine, while the addition of methione in the fermentation medium significantly decreased the productivity of apramycin. Therefore, the methyl donor function of glycine is proposed to be involved in the methionine cycle but methionine itself was proposed to inhibit the methylation and methyl transfer processes as previously reported for the case of rapamycin. The 15N NMR spectra of [2-13C,15N]serine labeled apramycin indicated that serine may also act as a limiting precursor contributing to the -NH2 substituents of apramycin.     

Production of trypsin inhibitor by a Cephalosporium sp.

Conditions for the production of the trypsin inhibitor from Cephalosporium sp. KM 388 were investigated. Polypeptone-meat extract-glucose medium supported excellent production of the trypsin inhibitor. In this medium, polypeptone and meat extract were utilized both as carbon and nitrogen sources and as limiting substrates for the cell growth. Glucose was consumed during the stationary growth phase and prevented the disappearance of inhibitor activity. Cephalosporium sp. KM 388 grew at a rate of a first-order reaction for the cell concentrations. Trypsin inhibitor production paralleled cell growth. At 27 degrees C the maximum specific rates of growth and inhibitor production were 0.14 h-1 and 2.1 U of inhibitor/h per mg of cell, respectively. The production rate and the maximum yield of the inhibitor were increased 1.5- and 1.2-fold, respectively, when the initial pH 6.3 was maintained throughout the fermentation.     

Production of trypsin inhibitor by a Cephalosporium sp.

Conditions for the production of the trypsin inhibitor from Cephalosporium sp. KM 388 were investigated. Polypeptone-meat extract-glucose medium supported excellent production of the trypsin inhibitor. In this medium, polypeptone and meat extract were utilized both as carbon and nitrogen sources and as limiting substrates for the cell growth. Glucose was consumed during the stationary growth phase and prevented the disappearance of inhibitor activity. Cephalosporium sp. KM 388 grew at a rate of a first-order reaction for the cell concentrations. Trypsin inhibitor production paralleled cell growth. At 27 degrees C the maximum specific rates of growth and inhibitor production were 0.14 h-1 and 2.1 U of inhibitor/h per mg of cell, respectively. The production rate and the maximum yield of the inhibitor were increased 1.5- and 1.2-fold, respectively, when the initial pH 6.3 was maintained throughout the fermentation.     

Parameters Affecting Ethyl Ester Production by Saccharomyces cerevisiae during Fermentation

Volatile esters are responsible for the fruity character of fermented beverages and thus constitute a vital group of aromatic compounds in beer and wine. Many fermentation parameters are known to affect volatile ester production. In order to obtain insight into the production of ethyl esters during fermentation, we investigated the influence of several fermentation variables. A higher level of unsaturated fatty acids in the fermentation medium resulted in a general decrease in ethyl ester production. On the other hand, a higher fermentation temperature resulted in greater ethyl octanoate and decanoate production, while a higher carbon or nitrogen content of the fermentation medium resulted in only moderate changes in ethyl ester production. Analysis of the expression of the ethyl ester biosynthesis genes EEB1 and EHT1 after addition of medium-chain fatty acid precursors suggested that the expression level is not the limiting factor for ethyl ester production, as opposed to acetate ester production. Together with the previous demonstration that provision of medium-chain fatty acids, which are the substrates for ethyl ester formation, to the fermentation medium causes a strong increase in the formation of the corresponding ethyl esters, this result further supports the hypothesis that precursor availability has an important role in ethyl ester production. We concluded that, at least in our fermentation conditions and with our yeast strain, the fatty acid precursor level rather than the activity of the biosynthetic enzymes is the major limiting factor for ethyl ester production. The expression level and activity of the fatty acid biosynthetic enzymes therefore appear to be prime targets for flavor modification by alteration of process parameters or through strain selection.     

Vitamin B12 enhances the stimulation of DNA synthesis by serum in resting cultures of 3T6 cells

When low levels of serum are used to stimulate resting cultures of 3T6 cells the limiting factor in increasing DNA synthesis is a low molecular weight component, rather than a polypeptide growth factor. The former component is absent from Dulbecco's modified Eagle's medium (DEM) but present in Waymouth medium. We identify the essential component as vitamin B₁₂. Addition of vitamin B₁₂ to DEM increases the effectiveness of low levels of serum, as assessed both by [³H]TdR incorporation and autoradiography. Thus cultures of 3T6 cells in vitamin B₁₂-supplemented DEM offer a useful in vitro system for testing the mitogenic potency of polypeptides and serum fractions.     

3-Hydroxypropionaldehyde guided glycerol feeding strategy in aerobic 1,3-propanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis>

3-Hydroxypropionaldehyde (3-HPA) is a toxic intermediary metabolite in the biological route of 1,3-propanediol biosynthesis from glycerol. 3-HPA accumulated in culture medium would arouse an irreversible cessation of the fermentation process. The role of substrate (glycerol) on 3-HPA accumulation in aerobic fermentation was investigated in this paper. 1,3-Propanediol oxidoreductase and glycerol dehydratase, two key enzyme catalyzing reactions of 3-HPA formation and consumption, were sensitive to high concentration of 3-HPA. When the concentration of 3-HPA increased to a higher level in medium (ac 10 mmol/L), the activity of 1,3-propanediol oxidoreductase in cell decreased correspondingly, which led to decrease of the 3-HPA conversion rate, then the 3-HPA concentration increasing was accelerated furthermore. 3-HPA accumulation in culture medium was triggered by this positive feedback mechanism. In the cell exponential growth phase, the reaction catalyzed by 1,3-propanediol oxidoreductase was the rate limiting step in 1,3-propanediol production. The level of 3-HPA in culture medium could be controlled by the substrate (glycerol) concentration, and lower level of glycerol could avoid 3-HPA accumulating to a high, lethal concentration. In fed batch fermentation, under the condition of initial glycerol concentration 30 g/L, and keeping glycerol concentration lower than 7–8 g/L in cell exponential growth phase, 3-HPA accumulation could not be incurred. Based on this result, a glycerol feeding strategy was set up in fed batch fermentation. Under the optimized condition, 50.1 g/L of 1,3-propanediol was produced in 24 h, and 73.1 g/L of final 1,3-propanediol concentration was obtained in 54 h.     

Enhancement of antibiotic and secondary metabolite detection from filamentous fungi by growth on nutritional arrays

Aims: We asked to what extent does the application of the OSMAC (one strain, many compounds) approach lead to enhanced detection of antibiotics and secondary metabolites in fungi? Protocols for bacterial microfermentations were adapted to grow fungi in nutritional arrays. Methods and Results: Protocols for microfermentations of non‐sporulating fungi were validated using known antifungal‐producing fungi. Detection of antifungal activity was often medium dependent. The effects of medium arrays and numbers of strains on detection of antifungal signals were modelled by interpolation of rarefaction curves derived from matrices of positive and negative extracts. Increasing the number of fermentation media for any given strain increased the probability of detection of growth inhibition of Candida albicans. Increasing biodiversity increased detection of antifungal phenotypes, however, nutritional arrays could partly compensate for lost antibiotic phenotypes when biodiversity was limiting. Conclusions: Growth and extraction in microtiter plates can enable a discovery strategy emphasizing low‐cost medium arrays that can better exploit the metabolic potential of strains. Significance and Impact of the Study: Increasing fermentation parameters raise the probability of detecting bioactive metabolites from strains. The protocols can be used to pre‐select strains and their growth conditions for scale up that will most likely yield antibiotics and secondary metabolites.     

Significance of pantothenate for glucose fermentation by Oenococcus oeni and for suppression of the erythritol and acetate production

The heterofermentative lactic acid bacterium Oenococcus oeni requires pantothenic acid for growth. In the presence of sufficient pantothenic acid, glucose was converted by heterolactic fermentation stoichiometrically to lactate, ethanol and CO2. Under pantothenic acid limitation, substantial amounts of erythritol, acetate and glycerol were produced by growing and resting bacteria. Production of erythritol and glycerol was required to compensate for the decreasing ethanol production and to enable the synthesis of acetate. In ribose fermentation, there were no shifts in the fermentation pattern in response to pantothenate supply. In the presence of pantothenate, growing O. oeni contained at least 10.2 microM HSCoA, whereas the HSCoA content was tenfold lower after growth in pantothenate-depleted media. HSCoA and acetyl-CoA are cosubstrates of phosphotransacetylase and acetaldehyde dehydrogenase from the ethanol pathway. Both enzymes were found with activities commensurate with their function in ethanol production during heterolactic fermentation. From the kinetic data of the enzymes and the HSCoA and acetyl-CoA contents, it can be calculated that, under pantothenate limitation, phosphotransacetylase, and in particular acetaldehyde dehydrogenase activities become limiting due to low levels of the cosubstrates. Thus HSCoA deficiency represents the major limiting factor in heterolactic fermentation of glucose under pantothenate deficiency and the reason for the shift to erythritol, acetate, and glycerol fermentation.     

Variation of bagasse crystallinity and cellulase activity during the fermentation of Cellulomonas bacteria

A characteristic behavior of the fermentation process was observed during the growth of Cellulomonas on sugarcane bagasse. At the early stage of the fermentation the crystallinity index of bagasse increased, suggesting that the major metabolized fraction corresponded to the hemicellulose during this stage. Some time later the crystallinity achieved a steady state and then deceased, which indicated that the most complex structure of bagasse was being attacked. The analysis of the cellulolytic activity of extracellular enzyme in the medium showed a sharp increase followed by an abrupt leveling off and decline in activity. These results along with the reduction of crystallinity index and bagasse utilization (70%) justify the assumption that the C₁ component was present in the cellulase complex synthesized by the bacteria.     

Structured kinetic model to represent the utilization of multiple substrates in complex media during rifamycin B fermentation

Industrial fermentations typically use media that are balanced with multiple substitutable substrates including complex carbon and nitrogen source. Yet, much of the modeling effort to date has mainly focused on defined media. Here, we present a structured model that accounts for growth and product formation kinetics of rifamycin B fermentation in a multi-substrate complex medium. The phenomenological model considers the organism to be an optimal strategist with an in-built mechanism that regulates the sequential and simultaneous uptake of the substrate combinations. This regulatory process is modeled by assuming that the uptake of a substrate depends on the level of a key enzyme or a set of enzymes, which may be inducible. Further, the fraction of flux through a given metabolic branch is estimated using a simple multi-variable constrained optimization. The model has the typical form of Monod equation with terms incorporating multiple limiting substrates and substrate inhibition. Several batch runs were set up with varying initial substrate concentrations to estimate the kinetic parameters for the rifamycin overproducer strain Amycolatopsis mediterranei S699. Glucose and ammonium sulfate (AMS) demonstrated significant substrate inhibition toward growth as well as product formation. The model correctly predicts the experimentally observed regulated simultaneous uptake of the substitutable substrate combinations under different fermentation conditions. The modeling results may have applications in the optimization and control of rifamycin B fermentation while the modeling strategy presented here would be applicable to other industrially important fermentations.