Inactivation of aflatoxin B1 by using the synergistic effect of hydrogen peroxide and gamma radiation.

Inactivation of aflatoxin B1 was studied by using gamma radiation and hydrogen peroxide. A 100-krad dose of gamma radiation was sufficient to inactivate 50 micrograms of aflatoxin B1 in the presence of 5% hydrogen peroxide, and 400 krad was required for total degradation of 100 micrograms of aflatoxin in the same system. Degradation of aflatoxin B1 was confirmed by high-pressure liquid chromatographic and thin-layer chromatographic analysis. Ames microsomal mutagenicity test showed loss of aflatoxin activity. This method of detoxification also reduces the toxin levels effectively in artificially contaminated groundnuts.     

Inactivation of aflatoxin B1 by using the synergistic effect of hydrogen peroxide and gamma radiation

Inactivation of aflatoxin B1 was studied by using gamma radiation and hydrogen peroxide. A 100-krad dose of gamma radiation was sufficient to inactivate 50 micrograms of aflatoxin B1 in the presence of 5% hydrogen peroxide, and 400 krad was required for total degradation of 100 micrograms of aflatoxin in the same system. Degradation of aflatoxin B1 was confirmed by high-pressure liquid chromatographic and thin-layer chromatographic analysis. Ames microsomal mutagenicity test showed loss of aflatoxin activity. This method of detoxification also reduces the toxin levels effectively in artificially contaminated groundnuts.     

Conditions for induction of bacteriophage from lysogenic Bacillus megaterium with aflatoxin B1.

The present study was conducted to determine whether or not aflatoxin B1 was an effective inducing agent for lysogenic bacteria and to characterize some of the parameters involved in induction. A lysogenic strain of Bacillus megaterium (NRRL-B-3695) and an indicator strain of this species (NRRL-B-3694) were used. Cultures of the lysogenic strain were incubated for various periods of time in the presence of aflatoxin B1. Plaque-forming units as well as colony-forming units were then determined. Results of the present study indicated that bacteriophage lysogenizing B. megaterium could be induced with aflatoxin B1. The optimum concentration for induction was 25 micrograms of toxin per ml of early-log-phase culture. Evidence suggested that: (i) higher concentrations of aflatoxin B1 formed hydrophobic complexes which would not efficiently induce B. megaterium; (ii) the toxic effect of aflatoxin B1 severely limited the number of cells which could be induced prior to killing action of the toxin; and (iii) concentrations less than 25 micrograms of aflatoxin B1 per ml were not efficient inducers of bacteriophage production nor did they demonstrate the toxic effect observed at higher concentrations.     

Conditions for induction of bacteriophage from lysogenic Bacillus megaterium with aflatoxin B1.

The present study was conducted to determine whether or not aflatoxin B1 was an effective inducing agent for lysogenic bacteria and to characterize some of the parameters involved in induction. A lysogenic strain of Bacillus megaterium (NRRL-B-3695) and an indicator strain of this species (NRRL-B-3694) were used. Cultures of the lysogenic strain were incubated for various periods of time in the presence of aflatoxin B1. Plaque-forming units as well as colony-forming units were then determined. Results of the present study indicated that bacteriophage lysogenizing B. megaterium could be induced with aflatoxin B1. The optimum concentration for induction was 25 micrograms of toxin per ml of early-log-phase culture. Evidence suggested that: (i) higher concentrations of aflatoxin B1 formed hydrophobic complexes which would not efficiently induce B. megaterium; (ii) the toxic effect of aflatoxin B1 severely limited the number of cells which could be induced prior to killing action of the toxin; and (iii) concentrations less than 25 micrograms of aflatoxin B1 per ml were not efficient inducers of bacteriophage production nor did they demonstrate the toxic effect observed at higher concentrations.     

Phenol and trichloroethylene degradation by Pseudomonas cepacia G4: kinetics and interactions between substrates.

Intact cells of Pseudomonas cepacia G4 completely degraded trichloroethylene (TCE) following growth with phenol. Degradation kinetics were determined for both phenol, used to induce requisite enzymes, and TCE, the target substrate. Apparent Ks and Vmax values for degradation of phenol by cells were 8.5 microM and 466 nmol/min per mg of protein, respectively. At phenol concentrations greater than 50 microM, phenol degradation was inhibited, yielding an apparent second-order inhibitory value, KSI, of 0.45 mM as modeled by the Haldane expression. A partition coefficient for TCE was determined to be 0.40 +/- 0.02, [TCEair]/[TCEwater], consistent with Henry's law. To eliminate experimental problems associated with TCE volatility and partitioning, a no-headspace bottle assay was developed, allowing for direct and accurate determinations of aqueous TCE concentration. By this assay procedure, apparent Ks and Vmax values determined for TCE degradation by intact cells were 3 microM and 8 nmol/min per mg of protein, respectively. Following a transient lag period, P. cepacia G4 degraded TCE at concentrations of at least 300 microM with no apparent retardation in rate. Consistent with Ks values determined for degradation, TCE significantly inhibited phenol degradation.     

Phenol and trichloroethylene degradation by Pseudomonas cepacia G4: kinetics and interactions between substrates

Intact cells of Pseudomonas cepacia G4 completely degraded trichloroethylene (TCE) following growth with phenol. Degradation kinetics were determined for both phenol, used to induce requisite enzymes, and TCE, the target substrate. Apparent Ks and Vmax values for degradation of phenol by cells were 8.5 microM and 466 nmol/min per mg of protein, respectively. At phenol concentrations greater than 50 microM, phenol degradation was inhibited, yielding an apparent second-order inhibitory value, KSI, of 0.45 mM as modeled by the Haldane expression. A partition coefficient for TCE was determined to be 0.40 +/- 0.02, [TCEair]/[TCEwater], consistent with Henry's law. To eliminate experimental problems associated with TCE volatility and partitioning, a no-headspace bottle assay was developed, allowing for direct and accurate determinations of aqueous TCE concentration. By this assay procedure, apparent Ks and Vmax values determined for TCE degradation by intact cells were 3 microM and 8 nmol/min per mg of protein, respectively. Following a transient lag period, P. cepacia G4 degraded TCE at concentrations of at least 300 microM with no apparent retardation in rate. Consistent with Ks values determined for degradation, TCE significantly inhibited phenol degradation.     

Degradation of 2,4-dinitrophenol by free and immobilized cells of Rhodococcus erythropolis HL PM-1

Degradation of 2,4-dinitrophenol (2,4-DNP) by the cells of Rhodococcus erythropolis HL PM-1 was studied. The enzymes involved in 2,4-DNP degradation were inducible, and their resynthesis took place during the process. Cell immobilization by embedding into agar gels decreased the degrader activity. Maximum rates of 2,4-DNP degradation by free and immobilized cells were 10.0 and 5.4 nmol/min per mg cells, respectively. The concentration dependence of 2,4-DNP degradation was typical of substrate inhibition kinetics. The immobilized cells were used in a model reactor designed for 2,4-DNP biodegradation. Its maximum capacity was 0.45 nmol/min per mg cells at a volumetric flow rate of 20 h-1. The reactor operated for 14 days without losing capacity; its half-lifetime equaled 16 days.     

Aflatoxin B1 Uptake by Flavobacterium aurantiacum and Resulting Toxic Effects

Removal of aflatoxin B(1) from liquid cultures by resting and growing cells of Flavobacterium aurantiacum NRRL B-184 was studied. Spectrophotometic and thin-layer techniques served as aflatoxin assays. Cells grown in the presence of 5 ppm or higher levels of aflatoxin developed aberrant morphological forms. These toxin concentrations partially inhibited growth, and the nature of the inhibition suggested that aflatoxin interfered with cell wall synthesis. Incubation of 1.0 x 10(11) resting cells per milliliter with 7.0 mug/ml of aflatoxin B(1) during a 4-hr period facilitated complete toxin removal from a buffered aqueous medium. Autoclaved cells and cell wall preparations could remove a fraction of the aflatoxin of a test system. However, the toxin removed by autoclaved cells and cell walls could be extracted by washing with water but the aflatoxin B(1) removed by intact cells could not be extracted into the liquid phase. The uptake of aflatoxin B(1) by resting cells was sensitive to temperature and pH. Ruptured preparations of F. aurantiacum were not able to remove or modify the aflatoxin in an aqueous solution.     

Aflatoxin formation,lipid synthesis,and glucose metabolism by Aspergillus parasiticus during incubation with and without agitation

Glucose utilization, growth of mold, and synthesis of aflatoxin and total lipid by Aspergillus parasiticus were studied with cultures that were incubated statically and with agitation. With both cultural conditions, maximal toxin formation occurred at 5 days which coincided with the end of rapid mold growth and rapid uptake of glucose. The toxin concentration decreased as incubation continued. The pattern for formation and depletion of total lipid was similar to that for aflatoxin. Maximal yields of toxin and of total lipid did not coincide with maximal production of mold mycelium. Incubation with agitation enhanced mold growth, consumption of glucose, and production of aflatoxin and total lipid during the first 3 days. Generally, more growht occured in agitated cultures, but maximal yields of aflatoxin and total lipid were lower than in quiescent cultures. The need for limited, but not excessive, O₂ for synthesis of aflatoxin and lipid also was demonstrated by varying the volume of medium in flasks that were incubated quiescently. Incorporation of [1-¹⁴C] glucose into aflatoxin indicated that limiting the O₂ supply and thereby favoring glucose catabolism via the Embden-Meyerhof pathway enhanced toxin formation. Aflatoxin formation also was greater when oxidative respiration of the mold was restricted by a metabolic inhibitor. Results suggest that the degree of aeration of the culture is important in controlling biosynthesis of aflatoxin.     

The fate of aflatoxin in naturally contaminated corn during the ethanol fermentation

Corn naturally contaminated with aflatoxin was used as a substrate in the ethanol fermentation. Distribution of toxin in several process and recovery fractions was identified. Although little degradation of the mycotoxin occurred during fermentation, no toxin appeared in the distilled alcohol. As accumulation of toxin in spent grains represents a potential problem in use of the material as animal feed, several decontamination procedures were tested. Sodium hydroxide, ammonium hydroxide, sodium hypochlorite, and hydrogen peroxide were identified as efficient agents of toxin degradation.     

Effects of Oxygen-Releasing Materials on Aerobic Bacterial Degradation Processes

The aerobic microbial degradation of p-nitrophenol (PNP) and phenol was examined under oxygen-limiting conditions in the presence of three known oxygen-releasing materials: (1) polyvinylidene chloride-encapsulated sodium percarbonate; (2) REGENESIS oxygen-releasing compound (magnesium peroxide); and (3) PermeOx® solid peroxygen (calcium peroxide). The degradation of PNP or phenol in buffered solutions was measured in 40-mL reaction chambers containing 25 to 300 mg of oxygen-releasing materials in the presence of immobilized chemical-degrading bacteria. Radiometric studies were used to determine total chemical mineralization and material balances of ¹⁴C-residues. Degradation of PNP and phenol increased in proportion to both the supplemented amount and the relative oxygen content of each oxygen-releasing material. Comparison of actual to theoretical degradation, based on stoichiometry of balanced equations for mineralization, showed that chemical uptake (primary degradation) at lower concentrations of oxygen-releasing materials was two-fold higher than could be mineralized theoretically. Radiometric studies confirmed the relationships between chemical uptake, cellular ¹⁴C-residues, mineralization, and the concentration of oxygen-releasing material. Further studies with PermeOx(identified supplementation levels required to support aerobic bacterial mineralization of PNP and phenol at levels similar to those of aerobic controls. These results show how the concentration of oxygen-releasing materials affects the rate and extent of aerobic chemical under oxygen-limiting conditions.     

Degradation of 2,4-dichlorophenoxyacetic acid by mixed cultures of bacteria

Summary We explored the feasibility of using mixed cultures for herbicide degradation, with the ultimate aim of application for effluent treatment. The present study reports on mixed cultures which were developed to grow aerobically with 2,4-dichlorophenoxyacetic acid (2,4-D) as the sole carbon substrate. Degradation of 2,4-D was verified by HPLC and UV-spectroscopic analysis of the residual 2,4-D concentration in the test cultures. Cultures that were initially developed with 2,4-D also grew readily with glucose, but the degradation of 2,4-D was effectively prevented under mixed substrate conditions. Mamor intermediates or metabolites resulting from 2,4-D degradation were not detected with the HPLC methodology except 2,4-dichlorophenol which appeared to accumulate transiently in the growth medium.     

Direct visual detection of aflatoxin synthesis by minicolonies of Aspergillus species

Single-spore colonies of Aspergillus flavus and Aspergillus parasiticus, grown for 4 to 5 days at 25 degrees C on a coconut extract agar containing sodium desoxycholate as a growth inhibitor, produced aflatoxin, readily detectable as blue fluorescent zones under long-wave (365 nm) UV light. Over 100 colonies per standard petri dish were scored for aflatoxin production by this procedure. Progeny from some strains remained consistently stable for toxin production after repeated subculture, whereas instability for toxin synthesis was revealed among progeny from other strains. Spore color markers were used to rule out cross-contamination in monitoring strains. A yellow-spored and nontoxigenic strain of A. flavus, reported previously to produce aflatoxin in response to cycloheximide treatment, proved to be toxin negative even after repeated exposure to cycloheximide. Extended series of progeny from another strain of A. flavus and from a strain of A. parasiticus were each compared by this plating procedure and by fluorometric analysis for aflatoxin when grown in a coconut extract broth. Both of these strains showed variation for toxin synthesis among their respective progeny, and specific progeny showed a good correlation for aflatoxin synthesis when examined by the two procedures.     

Direct visual detection of aflatoxin synthesis by minicolonies of Aspergillus species.

Single-spore colonies of Aspergillus flavus and Aspergillus parasiticus, grown for 4 to 5 days at 25 degrees C on a coconut extract agar containing sodium desoxycholate as a growth inhibitor, produced aflatoxin, readily detectable as blue fluorescent zones under long-wave (365 nm) UV light. Over 100 colonies per standard petri dish were scored for aflatoxin production by this procedure. Progeny from some strains remained consistently stable for toxin production after repeated subculture, whereas instability for toxin synthesis was revealed among progeny from other strains. Spore color markers were used to rule out cross-contamination in monitoring strains. A yellow-spored and nontoxigenic strain of A. flavus, reported previously to produce aflatoxin in response to cycloheximide treatment, proved to be toxin negative even after repeated exposure to cycloheximide. Extended series of progeny from another strain of A. flavus and from a strain of A. parasiticus were each compared by this plating procedure and by fluorometric analysis for aflatoxin when grown in a coconut extract broth. Both of these strains showed variation for toxin synthesis among their respective progeny, and specific progeny showed a good correlation for aflatoxin synthesis when examined by the two procedures.     

Induction of aflatoxin biosynthesis inAspergillus parasiticus by ascorbic acid-mediated lipid peroxidation

The effect ofl-ascorbic acid on the biosynthesis of aflatoxin inAspergillus parasiticus was studied. Ascorbic acid at lower concentrations did not inhibit the growth of fungus but markedly induced aflatoxin biosynthesis. At a concentration of 1000 ppm of ascorbic acid, 4.8-fold higher levels of aflatoxin were detected. Copper did not enhance the induction of toxin synthesis by ascorbic acid when added to the growth medium. Ascorbic acid at 1000 ppm was also found to induce aflatoxin synthesis in resting mycelia. Chloroform (1% vol/vol) was found to induce aflatoxin synthesis under similar conditions. Ascorbic acid in the presence of ferrous ion can cause lipid peroxidation, which in turn is responsible for the induction of aflatoxin synthesis. During the induction of aflatoxin synthesis by ascorbic acid, the uptake of carbon source (acetate) was not affected. This observation suggests that on ascorbic acid treatment a precursor or an intermediate of aflatoxin biosynthesis is synthesized in vivo and is responsible for the higher levels of toxin without increasing the uptake of acetate.     

Toxin production by Clostridium botulinum type A under various fermentation conditions.

The time of appearance and the quantity of toxin produced by the Hall strain of Clostridium botulinum type A were examined under various conditions. A 70-liter fermentor and a complex medium consisting of 2% casein hydrolysate and 1% yeast extract plus an appropriate concentration of glucose were employed. Optimal conditions for toxin production were as follows: a nitrogen overlay at a rate of 5 liters/min, an agitation rate of 50 rpm, a temperature of 35 degrees C, and an initial glucose concentration of 1.0% with the pH uncontrolled. Under these conditions, the maximum toxin concentration (6.3 x 10(5) mouse median lethal doses/ml) was attained within 24 h. Cell lysis was apparently not required to obtain maximum toxin concentrations under the fermentation conditions described.     

Toxin production by Clostridium botulinum type A under various fermentation conditions.

The time of appearance and the quantity of toxin produced by the Hall strain of Clostridium botulinum type A were examined under various conditions. A 70-liter fermentor and a complex medium consisting of 2% casein hydrolysate and 1% yeast extract plus an appropriate concentration of glucose were employed. Optimal conditions for toxin production were as follows: a nitrogen overlay at a rate of 5 liters/min, an agitation rate of 50 rpm, a temperature of 35 degrees C, and an initial glucose concentration of 1.0% with the pH uncontrolled. Under these conditions, the maximum toxin concentration (6.3 x 10(5) mouse median lethal doses/ml) was attained within 24 h. Cell lysis was apparently not required to obtain maximum toxin concentrations under the fermentation conditions described.     

Effect of fermentation conditions on toxin production by Clostridium botulinum type B.

To obtain high yields of toxin for the preparation of purified neurotoxoids, we examined the time of appearance and the quantity of toxin produced by the Bean strain of Clostridium botulinum type B under various conditions by using a fermentor system. The medium employed consisted of 2.0% casein hydrolylsate and 1.5% yeast extract plus an appropriate concentration of glucose. The maximum toxin concentration (4 x 10(5) to 5 x 10(5) mouse median lethal doses per ml) was attained within 48 h under the following fermentation conditions: an initial glucose concentration of 0.5 or 1.0%, a temperature of 35 degrees C, a nitrogen overlay at a rate of 5 liters/min, and an agitation rate of 50 rpm.     

Aspergillus flavus and other mycoflora of groundnut kernels in Israel and the absence of aflatoxin

More than 300 groundnut (peanut) samples collected from different regions of Israel were examined by ELISA for aflatoxin contamination. Samples were designated for export, local consumption or for sowing. None of the samples were contaminated with the toxin. However, when kernels were kept at high humidity (RH?99%), aflatoxin could be frequently detected seven days after incubation and the toxin was not uniformly distributed among kernels.Aspergillus niger, A flavus, Penicillium citrinum andP pinophilum were the dominant fungi and no differences were observed among cultivars. Almost half of the commercial samples examined were devoid ofA flavus. Other fungi identified wereA tamaril, A amstelodami, P rubrum, Rhizoctonia solani, Macrophomina phaseolina, Rhizopus spp., Sclerotium rolfsll, Fusarium andAlternaria spp; the two last ones comprising a group of low incidence. Although groundnut samples that containA flavus—infected kernels are moderately common, the local climate and agrotechniques In use in Israel are not conducive to aflatoxin accumulation. Nevertheless infected kernels may become a threat to health if stored under inadequate conditions.     

Xylitol production from high xylose concentration: evaluation of the fermentation in bioreactor under different stirring rates

AIMS: To investigate the production of xylitol by the yeast Candida guilliermondii FTI 20037, in a bioreactor, from rice straw hemicellulosic hydrolysate with a high xylose concentration. METHODS AND RESULTS: Batch fermentation was carried out with rice straw hemicellulosic hydrolysate containing about 85 g xylose l(-1), in a stirred-tank bioreactor at 30 degrees C, under aeration of 1.3 vvm (volume of air per volume of medium per min) and different stirring rates (200, 300 and 500 rev min(-1)). The bioconversion of xylose into xylitol by the yeast depended on the stirring rate, the maximum xylitol yield (YP/S = 0.84 g g(-1)) being achieved at 300 rev min-1, with no need to pretreat the hydrolysate for purification. CONCLUSIONS: To determine the most adequate oxygen transfer rate is fundamental to improving the xylose-to-xylitol bioconversion by C. guilliermondii. SIGNIFICANCE AND IMPACT OF THE STUDY: For the microbial production of xylitol to be economically viable, the initial concentration of xylose in the lignocellulosic hydrolysate should be as high as possible, as with high substrate concentrations it is possible to increase the final product concentration. Nevertheless, there are few reports on the use of high xylose concentrations. Considering a process in bioreactor, from rice straw hemicellulosic hydrolysate, this is an innovator work.