Short Communication: Effect of manganese on polysaccharide production and cellular pigmentation in the fungus Aureobasidium pullulans

Manganese supplementation resulted in higher polysaccharide levels and reduced cellular pigmentation by more than 8- or 17-fold after growth for 7d of the fungus Aureobasidium pullulans ATCC 42023 on sucrose or corn syrup, respectively, as a carbon source. The melanin content of the polysaccharide elaborated by ATCC 42023 cells also decreased if MnCl2 was added to the medium. The pullulan content of the polysaccharide synthesized by ATCC 42023 on sucrose was found to increase with increasing levels of manganese, whereas it was lower during growth on corn syrup if manganese was present.     

Polysaccharide production by a reduced pigmentation mutant of the fungus Aureobasidium pullulans

Abstract A reduced pigmentation mutant was isolated from Aureobasidium pullulans ATCC 42023 by chemical mutagenesis and was subsequently characterized. The pigment melanin was present not only in A. pullulans cells but also contaminated the elaborated polysaccharide and thus, was measured in both fractions. Cellular and polysaccharide melanin levels of the mutant strain were at least 11-fold and 18-fold reduced, respectivelu, compared toits parent strain after 7 days of growth at 30°C whether sucrose or glucose served as the carbon source in the culture medium. Polysaccharide and cell dry weight levels of the mutant were very similar to those observed for the parent after growth on sucrose or glucose as the source of carbon over a period of 7 days at 30°C. The pullulan content of the polysaccharide produced by the parent or mutant strain was lower for sucrose-grown cells than for glucose-grown cells. It was also noted that the pullulan content of the polysaccharide elaborated by the mutant strain was slightly higher than that of the polysaccharide produced by the parent strain after growth on either sucrose or glucose.     

Polysaccharide production by sponge-immobilized cells of the fungus Aureobasidium pullulans

T.P. WEST AND B.R.-H. STROHFUS. 1996. Cells of the fungus Aureobasidium pullulans ATCC 42023 were immobilized in sponge cubes and examined for their ability to elaborate the polysaccharide pullulan in relation to carbon source. It was found that fungal cells grown on corn syrup, sucrose or glucose as a carbon source could be immobilized in sponge cubes and that comparable cell weights and viable cell concentrations were immobilized. Independent of the carbon source tested, the immobilized fungal cells could be used at least three times for the production of polysaccharide. The immobilized A. pullulans cells elaborated the highest polysaccharide levels in the culture medium after 5–7 d of growth at 30°C.     

Polysaccharide production by a reduced pigmentation mutant of Aureobasidium pullulans NYS-1

AIMS: To isolate a reduced pigmentation mutant of Aureobasidium pullulans NYS-1 and characterize its cellular pigmentation plus its polysaccharide and biomass production relative to carbon source. METHODS AND RESULTS: Cellular pigmentation, polysaccharide levels and biomass production by the isolated mutant NYSRP-1 were analysed relative to carbon source. Cellular pigmentation of the mutant was lower than its parent strain using either carbon source. The mutant elaborated higher polysaccharide levels on sucrose than on corn syrup. The pullulan content of the polysaccharide synthesized and biomass production by the mutant rose as the carbon source concentration was increased. CONCLUSION: It is feasible to isolate a reduced pigmentation mutant from strain NYS-1 that exhibits elevated polysaccharide production using corn syrup as a carbon source. SIGNIFICANCE AND IMPACT OF THE STUDY: The mutant provides an advantage for commercial pullulan production because of its reduced pigmentation and enhanced polysaccharide synthesis.     

Effect of nitrogen source on pullulan production by Aureobasidium pullulans grown in a batch bioreactor

Pullulan production by Aureobasidium pullulans ATCC 201253 using selected nitrogen sources was studied in a medium using corn syrup as a carbon source. Independent of the corn syrup concentration present, the use of corn steep liquor or hydrolysed soy protein as a nitrogen source instead of ammonium sulphate did not elevate polysaccharide production by ATCC 201253 cells grown in an aerated, batch bioreactor containing 4 litres of medium. Pullulan production on corn steep liquor or hydrolysed soy protein as a nitrogen source became more comparable as the concentration of corn syrup was increased. Cell weights after 7 days of growth on any of the nitrogen sources were similar. The viscosity of the polysaccharide on day 7 was highest for cells grown on ammonium sulphate and 12.5% corn syrup. The pullulan content of the polysaccharide elaborated by ammonium sulphate-grown cells on day 7 decreased as the corn syrup level rose in the medium while the pullulan content of polysaccharide produced by cells grown on corn steep liquor or soytone generally increased.     

Polysaccharide production by immobilized Aureobasidium pullulans cells in batch bioreactors.

Cells of the fungus Aureobasidium pullulans ATCC 201253 were entrapped within 4% agar cubes or 5% calcium alginate beads and were examined for their production of the polysaccharide pullulan in batch bioreactors. The batch bioreactors were utilized twice for 168 hours of polysaccharide production in medium containing corn syrup as a carbon source. The agar-entrapped cells produced nearly equivalent pullulan concentrations during both production cycles. The alginate-entrapped cells produced higher polysaccharide levels during the second cycle compared to the levels observed during the initial cycle. The agar-entrapped cells elaborated a polysaccharide with a higher pullulan content than did the alginate-entrapped cells during both production cycles.     

Polysaccharide production by immobilized Aureobasidium pullulans cells in batch bioreactors

Cells of the fungus Aureobasidium pullulans ATCC 201253 were entrapped within 4% agar cubes or 5% calcium alginate beads and were examined for their production of the polysaccharide pullulan in batch bioreactors. The batch bioreactors were utilized twice for 168 hours of polysaccharide production in medium containing corn syrup as a carbon source. The agar-entrapped cells produced nearly equivalent pullulan concentrations during both production cycles. The alginate-entrapped cells produced higher polysaccharide levels during the second cycle compared to the levels observed during the initial cycle. The agar-entrapped cells elaborated a polysaccharide with a higher pullulan content than did the alginate-entrapped cells during both production cycles.     

Isolation of a mutant strain of Pseudomonas sp ATCC 31461 exhibiting elevated polysaccharide production

A mutant strain of the bacterium Pseudomonas sp. ATCC 31461 that exhibited elevated production of the polysaccharide gellan on glucose or corn syrup as a carbon source was isolated. Gellan production by the mutant strain was about twofold higher than its parent strain on glucose or corn syrup after 48 h of growth, and about 1.4-fold higher after 72 h. An increase in biomass production was not correlated with enhanced gellan synthesis by the mutant strain. The increased gellan production by the mutant strain on either carbon source resulted in an increase in its culture medium viscosity and the viscosity of the isolated polysaccharide produced by glucose-grown cells. No differences in the glucuronic acid content of the polysaccharides produced by the mutant and parent strains were observed. Journal of Industrial Microbiology & Biotechnology (2002) 29, 185–188 doi:10.1038/sj.jim.7000278 Received 13 February 2002/ Accepted in revised form 20 May 2002     

Pullulan production by <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis> cells immobilized in chitosan beads

Fungal cells of Aureobasidium pullulans ATCC 201253 were immobilized by entrapment in chitosan beads, and the immobilized cells were investigated for their ability to produce the polysaccharide pullulan using batch fermentation. The 1% chitosan-entrapped fungal cells were capable of producing pullulan for two cycles of 168 h using corn syrup as a carbon source. Pullulan production by the immobilized cells increased by 1.6-fold during the second production cycle (5.0 g/l) relative to the first production cycle (3.1 g/l) with the difference in production being statistically significant after 168 h. The productivity of the immobilized cells increased during the second production cycle while its pullulan content decreased. The level of cell leakage from the support remained unchanged for both production cycles.     

Enhanced production of pigment-free pullulan by a morphogenetically arrested Aureobasidium pullulans (ATCC 42023) in a two-stage fermentation with shift from soy bean oil to sucrose

A two-stage fermentation process was established for the production of pigment-free pullulan by the yeast-like fungus Aureobasidium pullulans (ATCC 42023). In the first stage, starting at pH 4.5 with soy bean oil as the carbon source and glutamate as the nitrogen source, a cell mass of about 15 g l^–1 dry cell weight was obtained, the population being restricted mainly to the yeast form of the microorganism (yeast form more than 90% of total cells) and the formation of pigment in the culture being prevented. Small amounts of pullulan (less than 2 g l^–1) are produced at this phase, and the viscosity remained low throughout the entire growth stage. When the oil and glutamate source were nearly exhausted (below 5% of initial amounts), the cells were shifted to a production stage with sucrose as the carbon source with continued nitrogen depletion. Production of pullulan started immediately with no lag period. During 50 h of the production phase more than 35 g l^–1 of pullulan was produced (productivity approx. 0.7 g l^–1), resulting in a large increase in the viscosity of the broth. The production yield of pollulan on the sugar was about 0.6 g g^–1. Morphogenesis from the yeast form of the microorganism to chlamydospores was still restrained and no pigment was formed in the culture during the production stage. A pigment-free polysaccharide, with a molecular mass in the range of 600–750 kDa, was recovered from the supernatant of the broth after solvent precipitation.     

Ability of casamino acids to support gellan production by Sphingomonas paucimobilis ATCC 31461

The ability of casamino acids and vitamin-assay casamino acids to support gellan production by Sphingomonas paucimobilis ATCC 31461 was examined in a medium containing glucose or corn syrup as the carbon source relative to yeast extract supplementation. When glucose or corn syrup served as the carbon source, the presence of yeast extract in the growth medium stimulated gellan production by strain ATCC 31461 on casamino acids. Using vitamin-assay casamino acids as the nitrogen source, the addition of vitamins lowered gellan synthesis by glucose-grown cells regardless of yeast extract supplementation while gellan elaboration by corn syrup-grown strain ATCC 31461 cells could only be increased by supplementing vitamins into medium lacking yeast extract. Independent of carbon source, the absence of yeast extract in the medium reduced biomass production. Biomass production by the strain grown on either carbon source was increased by supplementing vitamins in the medium containing yeast extract.     

Effect of temperature on bacterial gellan production

The effect of temperature on the production of the polysaccharide gellan by the bacterium Sphingomonas paucimobilis ATCC 31461 was studied in relation to carbon source. When glucose served as the carbon source, gellan formation by the strain was highest after 72 h of growth at an incubation temperature of 30–31 °C. Polysaccharide production by the sphingomonad cells grown on corn syrup for 72 h was maximal at an incubation temperature of 31 °C. The highest cellular productivity in elaborating gellan was observed at 31 °C after 72 h of growth independent of the carbon source utilized.     

Effect of culture medium pH on bacterial gellan production.

The effect of the initial pH of the culture medium used in the production of the exopolysaccharide gellan by the bacterium Pseudomonas species ATCC 31461, when glucose or corn syrup served as the carbon source, was investigated. With glucose as the carbon source, exopolysaccharide formation was highest after 72 h of growth when the initial pH of the culture medium was 6.8 to 7.4. Polysaccharide production by the bacterial cells grown on corn syrup for 72 h was maximal when the initial pH of the medium was 7.0 or 7.2. Cell weights of the strain after 72 h tended to be higher for the glucose-grown cells than for the corn syrup-grown cells.     

Succinate transport in Rhizobium leguminosarum.

The transport of succinate was studied in an effective streptomycin-resistant strain of Rhizobium leguminosarum. High levels of succinate transport occurred when cells were grown on succinate, fumarate, or malate, whereas low activity was found when cells were grown on glucose, sucrose, arabinose, or pyruvate as the sole carbon source. Because of the rapid metabolism of succinate after transport into the cells, a succinate dehydrogenase-deficient mutant was isolated in which intracellular succinate accumulated to over 400 times the external concentration. Succinate transport was completely abolished in the presence of metabolic uncouplers but was relatively insensitive to sodium arsenate. Succinate transport was a saturable function of the succinate concentration, and the apparent Km and Vmax values for transport were determined in both the parent and the succinate dehydrogenase mutant. Malate and fumarate competitively inhibited succinate transport, whereas citrate and malonate had no effect. Succinate transport mutants were isolated by transposon (Tn5) mutagenesis. These mutants were unable to transport succinate or malate and were unable to grow on succinate, malate, or fumarate as the sole carbon source. The mutants grew normally on pyruvate, oxaloacetate, citrate, or arabinose, and revertants isolated on succinate minimal medium had regained the ability to grow on malate and fumarate. From these data, we conclude that R. leguminosarum possesses a C4-dicarboxylic acid transport system which is inducible and mediates the active transport of succinate, fumarate, and malate into the cell.     

Dextransucrase constitutive mutants of Leuconostoc mesenteroides B-1299

Leuconostoc mesenteroides B-1299 dextrans are separated into two kinds: fraction L, which is precipitated by an ethanol concentration of 38%, and fraction S, which is precipitated at an ethanol concentration of 40%. Fraction S dextran contained 35% of -1,2 branch linkages, and fraction L contained 27% -1,2 branch linkage with 1% -1,3 branch linkages. We have isolated mutants constitutive for dextransucrase from L. mesenteroides NRRL B-1299 using ethyl methane sulfonate. The mutants produced extracellular as well as cell-associated dextransucrases on glucose media with higher activities (2.5–4.5 times) than what the parental strain produced on sucrose. Based on Penicillium endo-dextranase hydrolysis, mutant B-1299C dextransucrases produced slightly different dextrans when they were elaborated on a glucose medium and on a sucrose medium. Mutant B-1299CA dextransucrase elaborated on a glucose medium and on a sucrose medium synthesized the same dextran, although the dextran was different from those of other mutants and the parental strain. Mutant B-1299CB dextransucrase, elaborated on a glucose medium and on a sucrose medium, formed different dextrans. Differences in water solubility, susceptibility to endo-dextranase hydrolysis, and the physical appearance of the ethanol precipitated dextrans elaborated by different mutants grown on glucose media and sucrose media were found. All mutant dextransucrases elaborated on a glucose medium bound to Sephadex G-200. After activity staining of nondenaturing sodium dodecyl sulfate—polyacrylamide gel electrophoresis activity bands, 184 and 240 Kd for each enzyme preparation, although each dextransucrase formed different dextran(s).     

Constitutive mutants for dextransucrase from Leuconostoc mesenteroides NRRL B-512F

Constitutive mutants for dextransucrase were isolated from cells of Leuconostoc mesenteroides NRRL B-512F by treatment with N-methyl-N′-nitro-N-nitrosoguanidine, growing on an agar plate containing glucose as a carbon source and overlaying a soft agar with sucrose and tetracycline. These mutants were able to produce the enzyme in a liquid media containing sugars other than sucrose, such as glucose, fructose and maltose, without simultaneous synthesis of dextran. The enzyme activity of one mutant strain, SH 3002, was 2- to 3-fold higher than that of the wild strain grown on sucrose. When the concentration of glucose in the medium was increased from 2 to 4%, a 1.7-fold increase of enzyme activity was obtained for the mutant, whereas only a slight increase of the activity was observed on sucrose for both the wild strain and the mutant.     

Production of the fungal exopolysaccharide pullulan by batch-wise and continuous fermentation

A mutant strain of the deuteromycete Aureobasidium pullulans deficient in melanin synthesis was used to investigate the production of the exopolysaccharide pullulan and biomass, respectively. Shake-flask experiments with different carbon sources showed significant differences in pullulan elaboration. Sucrose was most suitable for pullulan synthesis among the carbon sources examined. Fermentations were carried out both batch-wise and continuously in a stirred vessel fermentator. In batch fermentations about 45% of the glucose offered was converted into pullulan at maximum formation rates of 0.16 g/l per hour using standard medium. The yield of polysaccharide could be maintained at 45% in continuous fermentations. At a dilution rate of 0.05 l/h, the formation rate of polysaccharide increased up to 0.35 g/l per hour. Alterations in the nitrogen content of the feed significantly affected the consumption rate of glucose and the production rate of polysaccharide, but final concentrations of biomass were hardly affected. Correspondence to: R. Schuster     

A <Emphasis Type="Italic">Candida guilliermondii</Emphasis> lysine hyperproducer capable of elevated citric acid production

A mutant of the yeast Candida guilliermondii ATCC 9058 exhibiting elevated citric acid production was isolated based upon its ability to overproduce lysine. This method involved the use of a solid medium containing a combination of lysine analogues to identify a mutant that produced a several-fold higher lysine level compared to its parent strain using glucose or glycerol as a carbon source. The mutant strain was also capable of producing more than a fivefold higher citric acid level on glycerol as a carbon source compared to its parent strain. It was concluded that the screening of yeast lysine hyperproducer strains could provide a rapid approach to isolate yeast citric acid hyperproducer strains.     

A yellow polysaccharide-producing bacterium with unusual characteristics

Summary A polysaccharide-producing Gram-negative bacterium was isolated from a sample of hay. It grew best on nitrate-containing media with sucrose as carbon source; the colony form was highly unusual. No polysaccharide was formed on glucose. A spontaneous mutant producing the same polysaccharide on both sucrose- and glucose-containing media was isolated. The polysaccharide has been characterized as an acid heteropolymer containing D-galacturonic acid, D-glucose, D-galactose and D-mannose in the approximate molar ratio 1:1:3:1, together with about 2 mol of acetate. The polysaccharide in aqueous solution was highly viscous with pseudoplastic characteristics.     

Synthesis of Pullulan by Acetone-dried Cells and Cell-free Enzyme from Pullularia pullulans,and the Participation of Lipid Intermediate

It was demonstrated that the polysaccharide, pullulan, was synthesized from sucrose by acetone-dried cells of Pullularia pullulans or from UDPG by cell-free enzyme preparations prepared from the organism. The pullulan formed was estimated by precipitation with ethanol, and determining maltotriose produced after treating the precipitate with Aerobacter isoamylase (pullulanase). Acetone cells (5 g) shaken with 200 ml of 10% sucrose produced over 250 mg of pullulan per 100 ml after 90 hr at 30°C and pH 6.0. Cell-free enzyme produced pullulan from UDPG in the presence of ATP. ATP was essential for the biosynthesis, and ADPG could not replace for UDPG.

In addition, it was observed that a lipid containing glucose residue was formed during, the reaction. The nature of this glucolipid was examined, and possible participation of a lipid intermediate was assumed in the pullulan biosynthesis.