Selective production of bikaverin in a fluidized bioreactor with immobilized Gibberella fujikuroi

The best culture medium composition for the production of bikaverin by Gibberella fujikuroi in shake-flasks, i.e. 100 g glucose l^–1; 1 g NH₄Cl l^–1; 2 g rice flour l^–1; 5 g KH₂PO₄ l^–1 and 2.5 g MgSO₄ l^–1, was obtained through a fractional factorial design and then scaled-up to a fluidized bioreactor. The effects of carbon and nitrogen concentrations, inoculum size, aeration, flow rate and bead sizes on batch bikaverin production using immobilized G. fujikuroi in a fluidized bioreactor were determined by an orthogonal experimental design. Concentrations of up to 6.83 g bikaverin l^–1 were obtained when the medium contained 100 g glucose l^–1 and 1 g NH₄Cl l^–1 with an inoculum ratio of 10% v/v, an aeration rate of 3 volumes of air per volume of medium min^–1, and a bead size of 3 mm. Based on dry weight, the bikaverin production was 30–100 times larger than found in submerged culture and approximately three times larger than reported for solid substrate fermentation.     

Bikaverin,an antibiotic fromGibberella fujikuroi,effective againstLeishmania brasiliensis

The red quinone C₂₀H₁₄O₈ (mp 322–324), named bikaverin was isolated from mycelium ofGibberella fujikuroi. Bikaverin is specifically effective againstLeishmania brasiliensis while is not effective against other protozoa, bacteria and fungi. For production of bikaverin in a submerged culture the most convenient media are those with a natural source of nitrogen (corn-steep liquor, soyabean meal) in which the content of bikaverin ranged from 1.0 to 1.7% of dry weight of mycelium.     

A possible mechanism of metabolic regulation in Gibberella fujikuroi using a mixed carbon source of glucose and corn oil inferred from analysis of the kinetics data obtained in a stirrer tank bioreactor

A nonstructured model was used to study the dynamics of gibberellic acid production in a stirred tank bioreactor. Experimental data were obtained from submerged batch cultures of Gibberella fujikuroi (CDBB H‐984) grown in varying ratios of glucose‐corn oil as the carbon source. The nitrogen depletion effect was included in mathematical model by considering the specific kinetic constants as a linear function of the normalized nitrogen consumption rate. The kinetics of biomass growth and consumption of phosphate and nitrogen were based on the logistic model. The traditional first‐order kinetic model was used to describe the specific consumption of glucose and corn oil. The nitrogen effect was solely included in the phosphate and corn oil consumption and biomass growth. The model fit was satisfactory, revealing the dependence of the kinetics with respect to the nitrogen assimilation rate. Through simulations, it was possible to make diagrams of specific growth rate and specific rate of substrate consumptions, which was a powerful tool for understanding the metabolic interactions that occurred during the various stages of fermentation process. This kinetic analysis provided the proposal of a possible mechanism of regulation on growth, substrate consumptions, and production of gibberellic acid (GA₃) in G. fujikuroi. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1169–1180, 2013     

Stimulation of bikaverin production by sucrose and by salt starvation in Fusarium fujikuroi

The fungus Fusarium fujikuroi (Gibberella fujikuroi mating group C) exhibits a rich secondary metabolism that includes the synthesis of compounds of biotechnological interest, such as gibberellins, bikaverin, and carotenoids. The effect of the carbon source on their production was checked using a two-phase incubation protocol, in which nine different sugars were added upon transfer of the fungus from repressed to appropriate inducing conditions, i.e., nitrogen starvation for gibberellins and bikaverin and illumination for carotenoids production. Most of the carbon sources allowed the synthesis of these metabolites in significant amounts. However, bikaverin production was strongly increased by the presence of sucrose in comparison to other carbon sources, an effect not exhibited for the production of gibberellins and carotenoids. The bikaverin inducing effect was enhanced in the absence of phosphate and/or sulfate. Similar results were also observed in carotenoid-overproducing strains known to be altered in bikaverin production. The induction by salt starvation, but not by sucrose, correlated with an increase in messenger RNA levels of gene bik1, encoding a polyketide synthase of the bikaverin pathway.     

Immobilized growing cells of Gibberella fujikuroi P-3 for production of gibberellic acid and pigment in batch and semi-continuous cultures

Summary The performance of immobilized growing cells of Gibberella fujikuroi P-3 was affected by the immobilization agent used, nature and age of cells, mycelial cell density, size of beads and inclusion of linseed oil. The beads, prepared by using standardized procedures, could be used for 8 cycles without affecting productivity in semicontinuous culture. The rate of production of gibberellic acid was 0.58–0.66 mg/l/h. An inverted conical fluidized bioreactor, based on the design employed in continuous plant cell culture, was adopted. This bioreactor offers many advantages. The pigment produced by the fungus is not similar to bikaverin, norbikaverin and O-dimethylanhydrofusarubin, the known polyketides.     

Transformation of the filamentous fungus Gibberella fujikuroi using the Aspergillus niger niaD gene encoding nitrate reductase

Summary A transformation system for Gibberella fujikuroi based on the Aspergillus niger nitrate reductase gene (niaD) was developed. A strain (designated SG140) carrying a non-reverting niaD mutation (niaD11) was generated by screening mutagenised cells for non-growth on nitrate as sole nitrogen source. Transformation frequencies of 1–2 transformants per g DNA were observed when strain SG140 was transformed to nitrate utilisation. Southern blot analyses of niaD⁺ transformants showed that the vector DNA sequences were integrated into the chromosomal DNA. The results demonstrate that the A. niger niaD gene is expressed in G. fujikuroi.     

Effects of growth retardants on gibberellin biosynthesis inGibberella fujikurai and on growth of wheat seedlings

2-chloroethylphosphonic acid, unlike chlorocholinechloride, does not suppress gibberellin biosynthesis inGibberella fujikuroi cultures, and nullifies the effect of applied gibberellin A₃ on wheat seedling growth. Presented at the International Symposium “Plant Growth Regulators” on June 18 – 22, 1984 at Liblice, Czechoslovakia.     

Bioprocess strategies and recovery processes in gibberellic acid fermentation

Gibberellic acid (GA₃) is a commercially important plant growth hormone, which is gaining much more attention all over the world due to its effective use in agriculture and brewing industry. Industrially it is produced by submerged fermentation technique using Ascomycetous fungusGibberella fujikuroi. Solid state and immobilized cell fermentation techniques had also been developed as an alternative to obtain higher yield of GA₃. This review summarizes the problems of GA₃ fermentation such as production of co-secondary metabolites along with GA₃, substrate inhibition and degradation of GA₃ to biologically inert compound gibberellenic acid, which limits the yield of GA₃ in the fermentation medium. These problems can be overcome by various bioprocessing strategiese.g. two-stage and fed batch cultivation processes. Further research on bioreactor operation strategies such as continuous and/or extractive fermentation with or without cell recycle/retention system need to be investigated for improvement in yield and productivity. Down stream processing for GA₃ isolation is also a challenge and procedures available for the same have been critically evaluated.     

Regulation of Carotenogenesis and Secondary Metabolism by Nitrogen in Wild-Type Fusarium fujikuroi and Carotenoid-Overproducing Mutants

The fungus Fusarium fujikuroi (Gibberella fujikuroi MP-C) produces metabolites of biotechnological interest, such as gibberellins, bikaverins, and carotenoids. Gibberellin and bikaverin productions are induced upon nitrogen exhaustion, while carotenoid accumulation is stimulated by light. We evaluated the effect of nitrogen availability on carotenogenesis in comparison with bikaverin and gibberellin production in the wild type and in carotenoid-overproducing mutants (carS). Nitrogen starvation increased carotenoid accumulation in all strains tested. In carS strains, gibberellin and bikaverin biosynthesis patterns differed from those of the wild type and paralleled the expression of key genes for both pathways, coding for geranylgeranyl pyrophosphate (GGPP) and kaurene synthases for the former and a polyketide synthase for the latter. These results suggest regulatory connections between carotenoid biosynthesis and nitrogen-controlled biosynthetic pathways in this fungus. Expression of gene ggs1, which encodes a second GGPP synthase, was also derepressed in the carS mutants, suggesting the participation of Ggs1 in carotenoid biosynthesis. The carS mutations did not affect genes for earlier steps of the terpenoid pathway, such as fppS or hmgR. Light induced carotenoid biosynthesis in the wild type and carRA and carB levels in the wild-type and carS strains irrespective of nitrogen availability.     

Capture of volatile metabolites for tracking the evolution of gibberellic acid in a solid-state culture of Gibberella fujikuroi

The evolution of volatile compounds produced during solid substrate cultivation (SSC) of Gibberella fujikuroi on wheat bran was tracked looking for volatile metabolites related with GA₃ production. Ethyl acetate and isoamyl acetate gave identical profiles and sharp increases that abated as the production of GA₃ began, while ent-kaurene displayed a profile matching that of the development of GA₃. ent-Kaurene is a precursor in the synthesis of gibberellins and was the most abundant compound found.     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

Optimization of S-adenosyl-L-methionine production by Kluyveromyces lactis on whey in batch culture using a mathematical model

Growth, lactose utilization and S-adenosyl-l-methionine (AdoMet) production by Kluyveromyces lactis AM-65 on whey in batch fermentation were investigated and an unstructured model of the process has been derived. The optimal set of parameters was estimated by fitting the model to experimental results. After incubation for 20 h the optimal fermentation conditions (28.5 °C, pH 5.3, agitation at 270 rpm) resulted in AdoMet production at 1.55 g l^–1.     

Impact of ammonium permeases mepA, mepB, and mepC on nitrogen-regulated secondary metabolism in Fusarium fujikuroi

In Fusarium fujikuroi, the production of gibberellins and bikaverin is repressed by nitrogen sources such as glutamine or ammonium. Sensing and uptake of ammonium by specific permeases play key roles in nitrogen metabolism. Here, we describe the cloning of three ammonium permease genes, mepA, mepB, and mepC, and their participation in ammonium uptake and signal transduction in F. fujikuroi. The expression of all three genes is strictly regulated by the nitrogen regulator AreA. Severe growth defects of ΔmepB mutants on low-ammonium medium and methylamine uptake studies suggest that MepB functions as the main ammonium permease in F. fujikuroi. In ΔmepB mutants, nitrogen-regulated genes such as the gibberellin and bikaverin biosynthetic genes are derepressed in spite of high extracellular ammonium concentrations. mepA mepB and mepC mepB double mutants show a similar phenotype as ΔmepB mutants. All three F. fujikuroi mep genes fully complemented the Saccharomyces cerevisiae mep1 mep2 mep3 triple mutant to restore growth on low-ammonium medium, whereas only MepA and MepC restored pseudohyphal growth in the mep2/mep2 mutant. Overexpression of mepC in the ΔmepB mutants partially suppressed the growth defect but did not prevent derepression of AreA-regulated genes. These studies provide evidence that MepB functions as a regulatory element in a nitrogen sensing system in F. fujikuroi yet does not provide the sensor activity of Mep2 in yeast, indicating differences in the mechanisms by which nitrogen is sensed in S. cerevisiae and F. fujikuroi.     

Kinetic analysis of the uptake of glucose and corn oil used as carbon sources in batch cultures of <Emphasis Type="Italic">Gibberella fujikuroi</Emphasis>

This study determined the specific uptake rate of glucose and corn oil substrates used as carbon sources in batch cultures of Gibberella fujikuroi. We tested three biological models of growth rate: Monod, logistic and lag-exponential. With respect to the substrate consumption rate, we tested two models: constant cell yield (CCY) and law of mass action (LMA). The experimental data obtained from the culture with glucose as substrate correlated satisfactorily with the logistic/LMA model, indicating that the cell yield was variable. In the case of corn oil as carbon source, considering total residual lipids as substrate in the culture broth, the model with the best correlation was the lag-exp/CCY model. The quantification by GC of the three main fatty acids (linoleic, oleic and palmitic) in the culture medium showed a cumulative behavior, with a maximum concentration of each acid at 36 h. We established a more explicit mechanism of the consumption of corn oil, consisting of two stages: generation of fatty acids by hydrolysis and consumption by cellular uptake. The kinetic of hydrolysable lipids was of first order. We found that the hydrolysis rate of corn oil is not a limiting factor for the uptake of fatty acids by the microorganism. We also established, based on the analysis of the identical mathematical structure of consumption kinetics, that the uptake of fatty acids is faster than the uptake of glucose.     

Characterization of gibberellin producing strains of Fusarium moniliforme based on DNA polymorphism

The gibberellins are one of the major groups of growth promoting hormones and are secondary metabolites of the fungus Fusarium moniliforme (Perfect stage: Gibberella fujikuroi). Sixteen strains of Fusarium from different geographical regions and different hosts were analysed for their ability to produce gibberellins (GA) and for genetic relatedness by random amplified polymorphic DNA (RAPD). Range of gibberellin production varied between 28.9 to 600.0 mg g^-1 dry weight of mycelium in different strains of Fusarium. RAPD analysis showed completely different pattern between high, moderate and low producing strains. High producers formed nearly identical RAPD patterns, whereas the low and moderate producers gave heterologous amplification patterns. Since Fusarium pallidoroseum was in another group, it was possible to distinguish between different species of the genus Fusarium by RAPD. These investigations may find an application in the diagnosis of unknown Fusarium species and in distinguishing isolates of Gibberella fujikuroi within the section of Liseola. This revised version was published online in June 2006 with corrections to the Cover Date.     

Comparison of alternative kinetic models for estimating the specific growth rate of Gibberella fujikuroi by image analysis techniques

Summary A new equation is proposed in order to obtain a consistent and accurate correlation between morphometric data of growing mycelia of Gibberella fujikuroi in solid media and its observed specific growth rates ( _obs) in stirred fermenters. A critical analysis is made of previous data and models.     

Inhibitory effect of dihydroxyacetone onGluconobacter oxydans: Kinetic aspects and expression by mathematical equations

Summary Microbial conversion of glycerol into dihydroxyacetone (DHA) byGluconobacter oxydans was subjected to inhibition by excess substrate. Comparison of cultures containing increasing initial DHA contents (0 to 100 g l^–1) demonstrated that DHA also inhibited this fermentation process. The first effect was on bacterial growth (cellular development stopped when DHA concentration reached 67 gl^–1), and then on oxidation of glycerol (DHA synthesis only occurred when the DHA concentration in the culture medium was lower than 85 g l^–1). Productivity, specific rates and, to a lesser extent, conversion yields decreased as initial concentrations of DHA increased. The changes in the specific parameters according to increasing initial DHA contents were described by general equations. These formulae satisfactorily express the concave aspect of the curves and the reduction in biological activity when the cells were in contact with DHA concentrations of up to 96 g l^–1.Abbreviations X, S, P biomass, substrate, product concentrations - r _x,r _s,r _p rates of growth, consumption and production - ,q _s,q _p specific rates of growth, glycerol consumption and DHA production - Y _x/s, Y_p/s conversion yields of substrate into biomass and product - K _s constant of affinity of cells to the substrate - K _ip product inhibition constant - P _m threshold concentration of DHA in substrate     

Growth and laccase production by Pleurotus ostreatus in submerged and solid-state fermentation

Pleurotus ostreatus showed atypical laccase production in submerged vs. solid-state fermentation. Cultures grown in submerged fermentation produced laccase at 13,000 U l⁻¹, with a biomass production of 5.6 g l⁻¹ and four laccase isoforms. However, cultures grown in solid-state fermentation had a much lower laccase activity of 2,430 U l⁻¹, biomass production of 4.5 g l⁻¹, and three laccase isoforms. These results show that P. ostreatus performs much better in submerged fermentation than in solid-state fermentation. This is the first report that shows such atypical behavior in the production of extracellular laccases by fungi.