Lipids of a citric-acid-producing Aspergillus niger strain grown in copper- and in manganese-supplemented media

A citric-acid-producing Aspergillus niger strain was cultivated in conditions favouring citric acid biosynthesis and in conditions hindering it. During both extreme processes, the mycelia were analysed for their lipid content, individual lipid classes, the content of sterols and free fatty acids. Since phospholipids, especially phosphatidylcholine and sterols, play an essential role in membrane permeability one can conclude that the differences observed substantially contribute to citric acid excretion into fermentation media. The difference in sterol composition was the most pronounced. Citric-acid-excreting mycelia contained lower quantities of sterols and ergosterol was the only component. A. niger mycelia grown in conditions hindering citric acid accumulation contained higher amounts of sterols with ergosterol as the main component and six other sterol components representing a minor amount.Offprint requests to: K. Jernejc     

Effect of various surfactants (cationic,anionic and non-ionic) on the growth of <Emphasis Type="Italic">Aspergillus parasiticus</Emphasis> (NRRL 2999) in relation to aflatoxin production

The effect of surfactants (two cationic, one anionic and three non-ionic) at 0.001, 0.01, 0.1 and 1.0 % concentrations on aflatoxin production, ergosterol content and sugar consumption by Aspergillus parasiticus (NRRL 2999) in YES liquid culture medium is reported. At 0.01% concentration, the cationic surfactants, cetyl dimethyl ammonium bromide (CDAB) and dodecyl trimethyl ammonium bromide (DTAB), and the anionic surfactant, sodium dodecyl sulfate (SDS), completely inhibited spore germination, while DTAB also inhibited the production of ergosterol and toxin (p < 0.05). At a concentration of 0.001%, CDAB was found to enhance toxin production, while SDS was found to inhibit it when compared with other surfactants. Non-ionic surfactants, polyoxyethylene sorbitan monolaurate (Tween-20), polyoxyethylene lauryl ether (Brij-35) and ethoxylated p-tert-octylphenol (Triton X-100) delayed the spore germination up to day 5 at all concentrations and inhibited toxin and ergosterol production at 0.001% concentration. The affect was found to be dose-dependent from 0.001% to 1%, for Triton X-100 only. Positive correlation between ergosterol content and toxin production in the presence of different surfactants at various time periods (3, 5, 7, 9 and 12 days) was found. Tween-20 was most effective in inhibiting toxin production on day 7, when aflatoxin production was found to be maximal in control group. Sugar consumption was directly proportional to the ergosterol content, showing a significant correlation with aflatoxin production.     

Comparison of citric acid production from glycerol and glucose by different strains of <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

A wild type strain A-101 of Y. lipolytica and its three acetate-negative mutants (Wratislavia 1.31, Wratislavia AWG7, and Wratislavia K1) were compared for the production of citric acid from glucose and glycerol (pure and crude) in batch cultures. The substrates were used either as single carbon sources or as mixtures of glucose and pure or crude glycerol. The kinetic parameters, i.e., the volumetric citric acid production rate and yield obtained in the study show that the Wratislavia 1.31 and Wratislavia AWG7 strains produced the highest amount of citric acid from glycerol, with a yield from 0.40 to 0.53 g g⁻¹. This substrate was found to be a better carbon source for the biosynthesis of citric acid than glucose. The results obtained with the same strains have shown low content of isocitric acid and polyols, such as erythritol and mannitol. Y. lipolytica A-101 strain produced the highest amount of isocitric acid, from 13.8 to 21% isocitric acid in the sum of citric acids. However, the highest concentrations of erythritol were found in cultures with Y. lipolytica Wratislavia K1, from 18.1 to 30 g l⁻¹, for glucose and pure glycerol, respectively.     

Production of added‐value metabolites by Yarrowia lipolytica growing in olive mill wastewater‐based media under aseptic and non‐aseptic conditions

Yarrowia lipolytica ACA‐YC 5033 was grown on glucose‐based media in which high amounts of olive mill wastewaters (OMWs) had been added. Besides shake‐flask aseptic cultures, trials were also performed in previously pasteurized media while batch bioreactor experiments were also done. Significant decolorization (～58%) and remarkable removal of phenolic compounds (～51% w/w) occurred, with the latter being amongst the highest ones reported in the international literature, as far as yeasts were concerned during their growth on phenol‐containing media. In nitrogen‐limited flask fermentations the microorganism produced maximum citric acid quantity ≈19.0 g/L [simultaneous yield of citric acid produced per unit of glucose consumed (Y_Cit/Glc)≈0.74 g/g]. Dry cell weight (DCW) values decreased at high phenol‐containing media, but, on the other hand, the addition of OMWs induced reserve lipid accumulation. Maximum citric acid concentration achieved (≈52.0 g/L; Y_Cit/Glc≈0.64 g/g) occurred in OMW‐based high sugar content media (initial glucose added at ≈80.0 g/L). The bioprocess was successfully simulated by a modified logistic growth equation. A satisfactory fitting on the experimental data occurred while the optimized parameter values were found to be similar to those experimentally measured. Finally, a non‐aseptic (previously pasteurized) trial was performed and its comparison with the equivalent aseptic experiment revealed no significant differences. Yarrowia lipolytica hence can be considered as a satisfactory candidate for simultaneous OMWs bioremediation and the production of added‐value compounds useful for the food industry.     

Rolle der n-Alkane in Melasse-Nährmedium beim Oberflächenverfahren der Citronensäurefermentation

The investigation of unfitness of beet molasses for citric acid production shows the presence of hydroacarbons in a toxic fraction of lipid extracts derived from antifoaming agents used in the suger industry. The model experiments demonstrate that these compounds dispersed in water solutions of the medium create on the surface of growing spores a layer which isolates them from the surrounding and prevents their normal growth. The inhibition effect of hydrocarbons on Aspergillus niger increases with degree of their dispersion in the water phase and is promoted by surface active substances e.g. emulgators present in antifoaming additives.     

Enhanced solid‐state citric acid bio‐production using apple pomace waste through surface response methodology

Aims: To evaluate the potential of apple pomace (AP) supplemented with rice husk for hyper citric acid production through solid‐state fermentation by Aspergillus niger NRRL‐567. Optimization of two key parameters, such as moisture content and inducer (ethanol and methanol) concentration was carried out by response surface methodology. Methods and Results: In this study, the effect of two crucial process parameters for solid‐state citric acid fermentation by A. niger using AP waste supplemented with rice husk were thoroughly investigated in Erlenmeyer flasks through response surface methodology. Moisture and methanol had significant positive effect on citric acid production by A. niger grown on AP (P < 0·05). Higher values of citric acid on AP by A. niger (342·41 g kg^?1 and 248·42 g kg^?1 dry substrate) were obtained with 75% (v/w) moisture along with two inducers [3% (v/w) methanol and 3% (v/w) ethanol] with fermentation efficiency of 93·90% and 66·42%, respectively depending upon the total carbon utilized after 144 h of incubation period. With the same optimized parameters, conventional tray fermentation was conducted. The citric acid concentration of 187·96 g kg^?1 dry substrate with 3% (v/w) ethanol and 303·34 g kg^?1 dry substrate with 3% (v/w) methanol were achieved representing fermentation efficiency of 50·80% and 82·89% in tray fermentation depending upon carbon utilization after 120 h of incubation period. Conclusions: Apple pomace proved to be the promising substrate for the hyper production of citric acid through solid‐state tray fermentation, which is an economical technique and does not require any sophisticated instrumentation. Significance and Impact of the Study: The study established that the utilization of agro‐industrial wastes have positive repercussions on the economy and will help to meet the increasing demands of citric acid and moreover will help to alleviate the environmental problems resulting from the disposal of agro‐industrial wastes.     

Ergosterol production from molasses by genetically modified <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Ergosterol is an economically important metabolite produced by fungi. Recombinant Saccharomyces cerevisiae YEH56(pHXA42) with increased capacity of ergosterol formation was constructed by combined overexpression of sterol C-24(28) reductase and sterol acyltransferase in the yeast strain YEH56. The production of ergosterol by this recombinant strain using cane molasses (CM) as an inexpensive carbon source was investigated. An ergosterol content of 52.6 mg/g was obtained with 6.1 g/l of biomass from CM medium containing 60 g/l of total sugar in 30 h in shake flask. The ergosterol yield was enhanced through the increasing cell biomass by supplementation of urea to a concentration of 6 g/l in molasses medium. Fermentation was performed in 5-l bioreactor using the optimized molasses medium. In batch fermentation, the effect of agitation velocity on ergosterol production was examined. The highest ergosterol yield was obtained at 400 rpm that increased 60.4 mg/l in comparison with the shake flask culture. In fed-batch fermentation, yeast cells were cultivated, firstly, in the starting medium containing molasses with 20 g/l of total sugar, 1.68 g/l of phosphate acid, and 6 g/l of urea (pH 5.4) for 5 h, then molasses containing 350 g/l of total sugar was fed exponentially into the bioreactor to keep the ethanol level in the broth below 0.5%. After 40 h of cultivation, the ergosterol yield reached 1,707 mg/l, which was 3.1-fold of that in the batch fermentation.     

Ram horn peptone as a source of citric acid production by <Emphasis Type="Italic">Aspergillus niger</Emphasis>, with a process

The present study deals with the production of citric acid from a ram horn peptone (RHP) by Aspergillus niger NRRL 330. A medium from RHP and a control medium (CM) were compared for citric acid production using A. niger in a batch culture. For this purpose, first, RHP was produced. Ram horns were hydrolyzed by treatment with acids (6 N H₂SO₄, 6 N HCl) and neutralizing solutions. The amounts of protein, nitrogen, ash, some minerals, total sugars, total lipids and amino acids of the RHP were determined. RHP was compared with peptones with a bacto-tryptone from casein and other peptones. The results from RHP were similar to those of standard peptones. The optimal concentration of RHP for the production of citric acid was found to be 4% (w/w). A medium prepared from 4% RHP was termed ram horn peptone medium (RHPM). In comparison with CM, the content of citric acid in RHPM broth (84 g/l) over 6 days was 35% higher than that in CM broth (62 g/l). These results show that citric acid can be produced efficiently by A. niger from ram horn.     

Continuous production of citric acid from dairy wastewater using immobilized<Emphasis Type="Italic">Aspergillus niger</Emphasis> ATCC 9142

The continuous production of citric acid from dairy wastewater was investigated using calcium-alginate immobilizedAspergillus niger ATCC 9142. The citric acid productivity and yield were strongly affected by the culture conditions. The optimal pH, temperature, and dilution rate were 3.0, 30°C, and 0.025 h⁻¹, respectively. Under optimal culture conditions, the maximum productivity, concentration, and yield of citric acid produced by the calcium-alginate immobilizedAspergillus niger were 160 mg L⁻¹ h⁻¹, 4.5 g/L, and 70.3% respectively. The culture was continuously perfored for 20 days without any apparent loss in citric acid productivity. Conversely, under the same conditions with a batch shake-flask culture, the maximum productivity, citric acid concentration, and yield were only 63.3 mg L⁻¹ h⁻¹, 4.7 g/L and 51.4%, respectively. Therefore, the results suggest that the bioreactor used in this study could be potentially used for continuous citric acid production from dairy wastewater by applying calcium-alginate immobilizedAspergillus niger.     

Zur Kinetik der Mischsubstratutilisation bei der Citronensäure-akkumulation durch Saccharomycopsis lipolytica EH 59

The mechanism and the kinetic of the assimilation of mixed substrates during the organism growth and the product excretion by strain of Saccharomycopsis lipolytica have been studied. The assimilation of citric acid for the organism growth was prevented when glucose and/or n-paraffins are present as substrates. Citric acid concentrations higher than 30 g/l in the fermentation medium decrease the growth rate on the substrate glucose. Kinetic studies of the mixed substrate assimilation by means of a n-tetradecane-1-C-labelled paraffin fraction proved that in discontinuous as well as in continuous 1-stage-processes for microbial production of citric acid glucose as substrate is only used for the organism growth whereas the n-paraffin fraction is only used for the acid excretion.     

Antifungal activity of cysteine,its effect on C-21 oxygenated lanosterol derivatives and other lipids in Inonofus obliquus,in vitro

The antifungal activity of cysteine (2-amino-3-mercaptopropionic acid) on mycelial growth and the production of lanosterol, 3,-hydroxy-lanosta-8,24-dien-21-al, 3,-21,dihydroxy-lanosta-8,24-diene, trametenolic acid and ergosterol were investigated in solid and liquid cultures ofInonotus obliquus at cysteine concentrations of 0.9 and 9.0 mm by means of thinlayer chromatography densitometry. Cysteine elicited the production of ergosterol in all the cultures and at a concentration of 0.9 mm distinctly elicited the production of 3,-hydroxy-lanosta-8,24-dien-21-al. At 9.0 mm, cysteine had greater antifungal activity than at 0.9 mm, decreasing growth and the production of metabolities.     

Buffer-stimulated citrate efflux in Penicillium simplicissimum: an alternative charge balancing ion flow in case of reduced proton backflow?

Organic acids excreted by filamentous fungi may be used to win metals from industrial secondary raw materials. For a future commercial use a high production rate of organic acids is necessary. The conditions under which the commercially used fungus Aspergillus niger excretes high amounts of citric acid can not be maintained in metal leaching processes. However, Penicillium simplicissimum showed an enhanced citric acid efflux in the presence of an industrial filter dust containing 50% zinc oxide. Because Good buffers of high molarity were able to mimic the effect of zinc oxide, the high buffering capacity of zinc oxide and not an effect of the zinc ions was held responsible for the enhanced citric acid efflux. The presence of ammonium and trace elements reduced this buffer-stimulated citric acid efflux, whereas the plant hormone auxine canceled this reduction. This citric acid efflux was influenced by a depolarization of the membrane: the freely permeable compound tetraphenylphosphoniumbromide decreased the citric acid efflux, without decreasing intracellular citric acid or consumption of glucose and oxygen. Vanadate, an inhibitor of the plasma membrane H⁺-ATPase also reduced the buffer-stimulated citric acid efflux. The role of the efflux of citrate anions as an alternative charge balancing ion flow in case of impaired backflow of extruded protons because of a high extracellular buffering capacity is discussed.Abbreviations CCCP carbonyl cyanide m-chlorophenylhydrazone - delta electrochemical potential gradient - DES diethylstilbestrol - DMSO dimethyl sulfoxide - TAPS N-tris(hydroxymethyl)methyl-3-aminopropanesulfonic acid - TEA triethanolamine - TFP trifluoperazine - TPP tetraphenylphosphonium bromide     

Regulation of sterol biosynthesis inSaccharomyces cerevisiae

Sterol synthesis inSaccharomyces cerevisiae was primarily controlled by the growth rate. At low specific growth rates the intermediates of ergosterol biosynthesis prevailed in cells. At the same time, the total sterol content reached about 6% of dry matter whereas the content of ergosterol was only 2–2.5%, which seems to be the maximum value forS. cerevisiae. After esterification with fatty acids these sterol intermediates are stored in lipid globules together with reserve triacylglycerols. The sporulatingS. cerevisiae cells contained 3.5% sterols and 1.5% ergosterol of dry matter.     

Elaboration and application of mathematical model for estimation of mould contamination of some building materials based on ergosterol content determination

The study presents a mathematical function describing a correlation between the amount of ergosterol and the number of colony-forming units (CFU) of mould contaminating selected building materials such as: a block of cellular concrete, gypsum—carton board and gypsum—carton board covered with emulsion paint. The dependence obtained for a particular material as well as an average dependence for all the investigated materials has been described by means of an exponential equation. It has been found out that there is high, statistically significant correlation between ergosterol content and CFU number of mould in all of the building materials. The correlation coefficients have ranged from r=0.790 to 0.933. The elaborated equation describing the above dependence can be applied to estimate mould contamination by means of culture methods within the range 10³–10⁸ CFU/m² of the surface. In addition, the estimated level of ergosterol in these materials has been shown to be the criterion by which to evaluate the degree of filamentous fungal contamination. It has been assessed that an ergosterol content exceeding the level of 3.96 mg/m² indicates the active development of mould. This criterion has been applied to evaluate several building materials i.e.: concrete, gypsum board, emulsion coatings, brick, plaster, wallpaper, glass wool, mineral wool and wood. No statistically significant differences have been observed between CFU number of mould calculated from a model equation on the basis of the ergosterol content and CFU number of mould experimentally determined by traditional methods. The results presented in this paper show that the elaborated equation of correlation between the ergosterol content and CFU number of mould can be applied to estimate mould contamination of different building materials, based on the determination of ergosterol.     

Microbial production of citric acid in fixed-bed column bioreactors

Summary Aspergillus niger NRRL 567 was cultured on the solid substrate, fruit pomace, in fixed-bed column bioreactors to produce citric acid. The rates of substrate consumption and citric acid production were strongly influenced by (1) the rate of aeration, (2) the fermentation temperature, (3) the initial moisture content of the substrate, and (4) the size of the inoculum. This culture method yielded approximately 130 g of citric acid per kg of apple pomace fermented under optimum conditions.     

Continuous citric acid fermentation by <Emphasis Type="Italic">Candida oleophila</Emphasis> under nitrogen limitation at constant C/N ratio

Summary The central aspect of this work was to investigate the influence of nitrogen feed rate at constant C/N ratio on continuous citric acid fermentation by Candida oleophila ATCC 20177. Medium ammonia nitrogen and glucose concentrations influenced growth and production. Space-time yield (STY) meaning volumetric productivity, biomass specific productivity (BSP), product concentration, product selectivity and citrate/isocitrate ratio increased with increasing residence time (RT). BSP increased in an exponential mode lowering nitrogen feed rates. Highest BSP for citric acid of 0.13 g/(g h) was achieved at lowest NH₄Cl concentration of 1.5 g/l and highest STY (1.2 g/l h) with 3 g NH₄Cl/l at a RT of 25 h. Citric acid 74.2 g/l were produced at 58 h RT and 6 g NH₄Cl/l. Glucose uptake rate seems to be strictly controlled by growth rate of the yeast cells. Optimum nitrogen concentration and adapted C/N ratio are essential for successful continuous citric acid fermentation. The biomass-specific nitrogen feed rate is the most important factor influencing continuous citric acid production by yeasts. Numerous chemostat experiments showed the feasibility of continuous citrate production by yeasts.     

Metabolism of Yarrowia lipolytica Grown on Ethanol under Conditions Promoting the Production of α-Ketoglutaric and Citric Acids: A Comparative Study of the Central Metabolism Enzymes

A comparative study of the enzymes of tricarboxylic acid (TCA) and glyoxylate cycles in the mutant Yarrowia lipolytica strain N1 capable of producing -ketoglutaric acid (KGA) and citric acid showed that almost all enzymes of the TCA cycle are more active under conditions promoting the production of KGA. The only exception was citrate synthase, whose activity was higher in yeast cells producing citric acid. The production of both acids was accompanied by suppression of the glyoxylate cycle enzymes. The activities of malate dehydrogenase, aconitase, NADP-dependent isocitrate dehydrogenase, and fumarase were higher in cells producing KGA than in cells producing citric acid.     

Citric acid production from glucose. I. Growth and excretion kinetics in a stirred fermentor

The growth and citric acid production kinetics of Saccharomycopsis lipolytica on glucose are investigated in an aerated stirred fermentor. Cellular growth first proceeds exponentially until exhaustion of ammonia in the fermentation medium. Cells then continue to grow at a reduced rate with a concomitant decrease in intracellular nitrogen content. Citric and isocitric acid production starts at the end of the growth phase. During about 80 hr excretion proceeds at a constant rate of 0.7 g/liter/hr for citric acid and 0.1 g/liter/hr for isocitric acid. The final citric and isocitric acid concentrations are 95 and 10g/liter, respectively. During acid excretion cellular respiration accounts for 60 and 35% of consumed oxygen and glucose. Both acid and CO₂ production rates follow a Michaelis–Menten-type dependence on oxygen concentration with Michaelis–Menten constants of 0.9 and 0.15 mg/liter for acid and CO₂ productions, respectively.