Effect of modified MRS medium on production and purification of antimicrobial peptide ST4SA produced by Enterococcus mundtii

Highest antimicrobial activity of peptide ST4SA (51,200 AU/mL) was recorded after 14 h of growth in MRS broth with optimal production at pH 6.0 or 6.5. Growth of strain ST4SA in the presence of tryptone, yeast extract, or a combination of the two, yielded 102,400 AU/mL. An increase in production of peptide ST4SA to 102,400 AU/mL was recorded in the presence of 20.0 g/L fructose, but decreased to 25,600 AU/mL in the presence of lactose (20.0 g/L) or mannose (20.0 g/L) as sole carbon source. Lower activity (25,600 AU/mL) was recorded when 2.0 g/L K₂HPO₄ was replaced by 2.0 g/L KH₂PO₄ in MRS broth. An increase of K₂HPO₄ to 10.0 g/L and 20.0 g/L resulted in higher activity (102,400 AU/mL). Addition of glycerol to MRS broth had a negative effect on peptide ST4SA production. Production of peptide ST4SA required the presence of magnesium sulphate, manganese sulphate and 5.0 g/L sodium acetate. Exclusion of tri-ammonium citrate from the medium resulted in reduction of activity to 3,200 AU/mL. Maximum activity (102,400 AU/mL) was recorded in MRS supplemented with 1.0 ppm Vit. C, DL-6,8-thioctic acid or thiamine, respectively. Growth of Listeria ivanovii susbp. ivanovii ATCC 19119 in the presence of peptide ST4SA (12,800 AU/mL) resulted in 99% cell lysis after 18 h. Improved production of peptide ST4SA was recorded in MRS broth (Biolab) pre-treated with Amberlite XAD-1180. Precipitation with ammonium sulphate, followed by gel filtration chromatography, yielded the highest level of peptide ST4SA. This paper describes the partially deproteination of growth medium to facilitate peptide ST4SA purification.     

Integrated enzyme purification and immobilization processes with immobilized metal affinity adsorbents

Silica-based immobilized metal affinity chromatography adsorbents with various ligand densities were prepared for the purification and immobilization of poly(His)-tagged d-hydantoinase (DHTase). An adsorbent with a ligand density of 13.0 μmol Cu²⁺/g gel exhibiting the optimal selectivity and a capacity of 1.4 mg/g gel toward the poly(His)-tagged enzyme was identified. The adsorbent was used for the one-step purification of His-tagged enzymes from crude cell lysate with a purity above 90%. The silica-based affinity adsorbents are particularly well suited for industrial scale operations due to their robustness. A packed-bed bioreactor with the DHTase-loaded adsorbents was used for the continuous conversion of d,l-p-hydroxyphenylhydantoin (d,l-HPH) to N-carbamoyl-d-hydroxyphenylglycine, an intermediate for the production of d-hydroxylphenylglycine. Under optimal conditions, 60 °C and pH 8.0, a conversion of 60% was obtained at a residence time of 30 min. Upon extended operation, the catalytic activity of the biocatalysts declined significantly due to enzyme leakage and enzyme denaturation. The extent of enzyme leakage can be attenuated by crosslinking with glutaraldehyde. In this study, we successfully demonstrate that a packed-bed bioreactor containing silica-based IMAC adsorbents can be used for the direct purification and immobilization of poly(His)-tagged enzymes for biotransformation.     

Improved 2,3-butanediol production from corncob acid hydrolysate by fed-batch fermentation using Klebsiella oxytoca

Corncob acid hydrolysate, detoxed by sequently boiling, overliming and activated charcoal adsorption, was used for 2,3-butanediol production by Klebsiella oxytoca ACCC 10370. The effects of acetate in hydrolysate and pH on 2,3-butanediol production were investigated. It was found that acetic acid in hydrolysate inhibited the growth of K. oxytoca while benefited the 2,3-butanediol yield. With the increase in acetic acid concentration in medium from 0 to 4 g/l, the lag phase was prolonged and the specific growth rate decreased. The acetic acid inhibition on cell growth can be alleviated by adjusting pH to 6.3 prior to fermentation and a substrate fed-batch strategy with a low initial acetic acid concentration. Under the optimum condition, a maximal 2,3-butanediol concentration of 35.7 g/l was obtained after 60 h of fed-batch fermentation, giving a yield of 0.5 g/g reducing sugar and a productivity of 0.59 g/h l.     

Toxin production,retention, and extracellular release by Dinophysis acuminata during extended stationary phase and culture decline

Dinophysis spp. produce diarrhetic shellfish poisoning (DSP) toxins and pectenotoxins. The extent to which the dinoflagellate cells retain their toxicity in stationary phase, a period when cells are most toxic, and their transition into cell death is not known. Here we present results on the production, recycling, retention, and release of toxins from a monoculture of Dinophysis acuminata during these two important stages. Once stationary phase was reached, cultures were divided between light and dark treatments to identify if light influenced toxin dynamics. Light was required for long-term cell maintenance (>2 months) of D. acuminata in the absence of prey, however, in the dark, cells in stationary phase survived on reserves alone for four weeks before beginning to decline. Cells maintained relatively constant levels of intracellular OA (0.39 ± 0.03 pg/cell, 0.44 ± 0.05 pg/cell), DTX1 (0.45 ± 0.09 pg/cell, 0.64 ± 0.10 pg/cell) and PTX2 (10.4 ± 1.4 pg/cell, 11.0 ± 1.9 pg/cell) in the dark and light treatments, respectively, throughout stationary phase and into culture decline. Toxin production was only apparent during late exponential and early stationary growth when cells were actively dividing. In general, the concentration of dissolved (extracellular) toxin in the medium significantly increased upon culture aging and decline; cells did not appear to be actively or passively releasing toxin during stationary phase, but rather extracellular release was likely a result of cell death. Light availability did not have an apparent effect on toxin production, quotas, or intracellular vs. extracellular distribution. Together these results suggest that a bloom of D. acuminata would retain its cellular toxicity or potency as long as the population is viable, and that cells under conditions of low light (e.g., at the boundary or below euphotic zone) and/or minimal prey could maintain toxicity for extended periods.     

Improvement of acetoin reductase activity enhances bacitracin production by Bacillus licheniformis

Bacitracin fermentation by Bacillus licheniformis in this work showed three characteristics: (1) the extracellular propionate, butyrate, acetoin and 2,3-butanediol accumulates under conditions of low dissolved oxygen (zero after 4 h cultivation), reaching a total content of approximately 11.1 g/L; (2) cell growth occurs quickly subsequent to cell autolysis and the second growth; and (3) there is a low content of 2,3-butanediol, a reduced product of acetoin catalyzed by acetoin reductase, in the culture process. In this study, addition of MnCl₂ (0.3 mg/L) to the production medium increased the acetoin reductase activity, redirected the NADH oxidation partly from the propionate- and butyrate-production pathways to the 2,3-butanediol synthesis pathway, reduced the intracellular NADH/NAD⁺ ratio, and facilitated cell growth, ultimately achieving a 11.6% increase in bacitracin production (1076 U/mL) versus the control. The results provide useful information regarding large-scale bacitracin production by B. licheniformis.     

An integrated bioreactor-expanded bed adsorption system for the removal of acetate to enhance the production of alpha-interferon-2b by Escherichia coli

A stirred tank bioreactor (STB) integrated with an expanded bed adsorption (EBA) system containing anion-exchange resin (Diaion WA30) was developed for in situ removal of acetate to increase the production of α-interferon-2b (α-PrIFN-2b) by Escherichia coli (E. coli). Although the total acetate (9.79 g/L) secreted by E. coli in the integrated STB/EBA system was higher than that in a bioreactor with dispersed resin or a conventional batch bioreactor, cell growth (14.97 g/L) and α-PrIFN-2b production (867.4 μg/L) were significantly improved owing to the high efficiency of acetate removal from the culture. The production of α-PrIFN-2b in the integrated STB/EBA system was improved by 3-fold and 1.4-fold over that obtained in a conventional batch bioreactor and a bioreactor containing dispersed resins, respectively.     

Direct ethanol production from N-acetylglucosamine and chitin substrates by Mucor species

Chitin, which is a polymer of β-(1–4) linked N-acetyl-d-glucosamine (GlcNAc) residues, is one of the most abundant renewable resources in nature, after cellulose. In this study, we found some native Mucor strains, which can use GlcNAc and chitin substrates as carbon sources for growth and ethanol production. One of these strains, M. circinelloides NBRC 6746 produced 18.6 ± 0.6 g/l of ethanol from 50 g/l of GlcNAc after 72 h and the maximum ethanol production rate was 0.75 ± 0.1 g/l/h. Furthermore, M. circinelloides NBRC 4572 produced 6.00 ± 0.22 and 0.46 ± 0.04 g/l of ethanol from 50 g/l of colloidal chitin and chitin powder after 16 and 12 days, respectively. We also found an extracellular chitinolytic enzyme producing strain M. ambiguus NBRC 8092, and successfully improved ethanol productivity of NBRC 4572 from colloidal chitin using crude chitinolytic enzyme derived from NBRC 8092. The ethanol titer reached 9.44 ± 0.10 g/l after 16 days. These results were the first bioethanol production from GlcNAc and chitin substrates by native organisms, and also suggest that these Mucor strains have great potential for the simultaneous saccharification and fermentation (SSF) of chitin biomass.     

A laboratory study of producing docosahexaenoic acid from biodiesel-waste glycerol by microalgal fermentation

Crude glycerol is the primary by-product in the biodiesel industry, which is too costly to be purified into to higher quality products used in the health and cosmetics industries. This work investigated the potential of using the crude glycerol to produce docosahexaenoic acid (DHA, 22:6 n-3) through fermentation of the microalga Schizochytrium limacinum. The results showed that crude glycerol supported alga growth and DHA production, with 75–100 g/L concentration being the optimal range. Among other medium and environmental factors influencing DHA production, temperature, trace metal (PI) solution concentration, ammonium acetate, and NH₄Cl had significant effects (P < 0.1). Their optimal values were determined 30 mL/L of PI, 0.04 g/L of NH₄Cl, 1.0 g/L of ammonium acetate, and 19.2 °C. A highest DHA yield of 4.91 g/L with 22.1 g/L cell dry weight was obtained. The results suggested that biodiesel-derived crude glycerol is a promising feedstock for production of DHA from heterotrophic algal culture.     

Comparison of two matrices for selective recovery of C595 diabody fragment (dbFv) from Escherichia coli lysates

A comparative study of the performance of two types of adsorbent (Streamline Quartz Base and Upfront Matrices), derivatized with the same affinity ligand (RPAP) to recover C595 diabody fragment (dbFv) from Escherichia coli lysates has been undertaken. Both streamline and Upfront Matrices are characterized by a particle size range of 100–300 μm. Streamline has a density of 1.20 g cm⁻³ and ligand concentration of 0.85 μmol ml⁻¹. Upfront has a density of 1.35 g cm⁻³ and ligand concentration of 0.83 μmol ml⁻¹. The release of C595 dbFv from E. coli cells was achieved by a chemical lysis method. The recovery performance of both adsorbents was evaluated in terms of operational productivity and elution yield of C595 dbFv in packed bed (clarified feedstock) and expanded bed (unclarified and clarified feedstock) chromatography systems. Streamline and Upfront adsorbents exhibited diabody operational productivities of 131 and 202 mg l⁻¹, respectively, with an elution yield of 92 and 94%, respectively, in packed bed operation. Streamline and Upfront adsorbents exhibited diabody operational productivities of 54.5 and 123.7 mg l⁻¹, respectively, with an elution yield of 89 and 92%, respectively, in expanded bed operation.     

Use of different carbon sources in cultivation of recombinant Pichia pastoris for angiostatin production

To improve the growth of recombinant Pichia pastoris with a phenotype of Mut^S and expression of angiostatin, the effects of glycerol, sorbitol, acetate and lactic acid which were, respectively, added together with methanol in the expression phase, were studied in a 5-l fermentor. Methanol concentration was automatically controlled at 5 g/l by a methanol monitor and control system, while the feeding of the other carbon source was manually adjusted. The angiostatin production level was 108 mg/l when glycerol was added at an initial rate of 2.3 g/h and gradually increased to 9.9 g/h within an induction period of 96 h. The angiostatin concentration was 141 mg/l as sorbitol was used, while only 52 mg/l were obtained on acetate. The highest angiostatin production of 191 mg/l was achieved as lactic acid was used; whose feeding rate was gradually increased from 2.6 to 11.3 g/h. Lactic acid accumulated during the induction phase and reached 6.3 g/l at the end of fermentation. However, the accumulation of lactic acid did not interfere with angiostatin production, indicating that lactic acid to be a non-repressive carbon source. The average productivity and specific productivity of angiostatin obtained on lactic acid and methanol were, respectively, 2.96 and 0.044 mg/(g h), 1.7- and 2.5-fold of those obtained in the fermentation fed with glycerol and methanol.     

Xylose-based hydrolysate from eucalyptus extract as feedstock for poly(lactate-co-3-hydroxybutyrate) production in engineered Escherichia coli

Woody extract-derived hemicellulosic hydrolysate, which was obtained from dissolving pulp manufacturing, was utilized as feedstock for the production of poly(lactate-co-3-hydroxybutyrate) [P(LA-co-3HB)] in engineered Escherichia coli. The hydrolysate was composed of mainly xylose and galactose, and contained impurities mainly acetate, which was found to inhibit the polymer synthesis rather than the cell growth. Thus, acetate and other impurities were removed through active charcoal and ion-exchange columns. Using the purified hydrolysate, P(LA-co-3HB) was successfully produced (cell dry weight 8.6 g/L, polymer concentration 5.4 g/L, LA fraction 5.5 mol%, polymer content 62.4%), the amount of which was comparable to that obtained using reagent grade xylose and galactose. Therefore, the hydrolysate from woody extract is considered as an abundant, inexpensive and efficient feedstock applicable to consolidated process for P(LA-co-3HB) production, when the removal of acetic acid was satisfactorily accomplished.     

Statistical media optimization for growth and PHB production from methanol by a methylotrophic bacterium

Media components were optimized by statistical design for cell growth and PHB production of Methylobacterium extorquens DSMZ 1340. Four important components of growth media were optimized by central composite design. The growth increased from an OD = 1.35 for Choi medium as control to an OD = 2.15 for optimal medium. Then media components for PHB production were optimized. Optimization of five important factors was conducted by response surface method. The optimal composition of PHB production medium was found to be at 7.8 (g/L) Na₂HPO₄ · 12H₂O, and surprisingly at zero concentration of (NH₄)₂SO₄, KH₂PO₄, MgSO₄ and MnSO₄. The PHB production was found to be 2.95 (g/L) at this medium. RSM results indicated that a deficiency of nitrogen and magnesium is crucial for PHB accumulation in this microorganism. Also, PHB production was carried out in a 5 L fermentor at the optimum condition which resulted in 9.5 g/L PHB and 15.4 g/L cell dry weight with 62.3% polymer content.     

Embryo production in superstimulated llamas pre-treated to inhibit follicular growth

Llamas are monotocous and the length of their gestation period varies between 342 and 350 days. Thus the average number of offspring any female can produce throughout her reproductive life is very limited to spread a desired genome. The multiple ovulation and embryo transfer (MOET) technique allows an alternative to this limitation and reduces the generation interval. The objective of this study was to evaluate embryo recovery in superstimulated llamas which had previously been hormone-treated to inhibit follicular growth. A total of 50 female llamas were monitored daily via rectal palpation and ultrasound and divided according to their ovarian follicular growth into four phases. The females in each phase were then randomly divided into two groups: A (n = 20) received a single dose of 1 mg of estradiol benzoate (EB) on the first day of the treatment + 100 mg of progesterone (P4) i.m. for 5 days with 5 animals per phase and B (n = 20) received 1 mg EB at onset + 150 mg P4 i.m. for a period of 5 days with 5 animals per phase. Group C (n = 10) or control did not receive any prior hormonal treatment and the females were in follicular phase I. All groups were monitored daily and, in the presence of ovarian follicles smaller than the dominant size at the end of treatment, all were superstimulated with 1000 IU eCG. For plasma progesterone concentration recording, daily blood samples were collected from days ?1 to 5 in the treated females in Group A and B. No significant differences were observed regarding the inhibition of follicle growth and in the plasma progesterone concentrations between Group A and B. The ovarian response to superstimulation was 56.2%, 71.4% and 90%, with the average number of dominant follicles produced per female being 4.4 ± 0.9; 4.8 ± 0.7 and 4.6 ± 0.6 in Groups A, B and C, respectively. The embryo recovery rate was 77.7%; 90% and 66.7% and the average number of embryos recovered per female was 2.9 ± 0.9; 2.6 ± 0.9 and 2.4 ± 0.8 for Groups A, B and C, respectively. In Groups A and B, the static follicular phase (III) seemed to be ideal for initiating the assisted reproductive technique of MOET. Although prior administration of P4 + EB seems to have no effect on the number of females that responded to the superstimulation treatments, the number of embryos recovered showed a tendency to be higher when ovarian follicle growth inhibition was performed beforehand.     

Enhanced production of periplasmic interferon alpha-2b by Escherichia coli using ion-exchange resin for in situ removal of acetate in the culture

The possibility of using in situ addition of anion-exchange resin for the removal of acetate in the culture aimed at improving growth of E. coli and expression of periplasmic human interferon-α2b (PrIFN-α2b) was studied in shake flask culture and stirred tank bioreactor. Different types of anion-exchange resin were evaluated and the concentration of anion-exchange resin was optimized using response surface methodology. The addition of anion-exchange resins reduced acetate accumulation in the culture, which in turn, improved growth of E. coli and enhanced PrIFN-α2b expression. The presence of anion-exchange resins did not influence the physiology of the cells. The weak base anion-exchange resins, which have higher affinity towards acetate, yielded higher PrIFN-α2b expression as compared to strong anion-exchange resins. High concentrations of anion-exchange resin showed inhibitory effect towards growth of E. coli as well as the expression of PrIFN-α2b. The maximum yield of PrIFN-α2b in shake flask culture (501.8 μg/L) and stirred tank bioreactor (578.8 μg/L) was obtained at ion exchange resin (WA 30) concentration of 12.2 g/L. The production of PrIFN-α2b in stirred tank bioreactor with the addition of ion exchange resin was about 1.8-fold higher than that obtained in fermentation without ion exchange resin (318.4 μg/L).     

Effect of heating rate on pDNA production by E. coli

The effects of heating rate (HR) on the performance of two-phase (batch followed by fed-batch) high cell-density cultivations (HCDC) of E. coli DH5α for the production of plasmid DNA (pDNA) were investigated. Optimal temperatures for the HCDC, as selected from shake flask experiments at constant temperatures between 30 and 45 °C, were 35 °C for biomass accumulation in the batch phase and 42 °C for inducing pDNA replication during the fed-batch. In HCDC the temperature was increased at HR of 0.025, 0.05, 0.10 and 0.25 °C/min and the performance of the cultivations were compared to a HCDC run at constant temperature (35 °C). Compared to constant 35 °C, heat-induced HCDC accumulated up to 50% less biomass within the same cultivation time and acetate and glucose accumulated to high concentrations. The overall specific productivity (Q_P) and average pDNA yield (Y_p/x) in HCDC at 35 °C were 0.22 ± 0.02 mg/g h and 5.3 ± 0.00 mg/g, respectively. Such parameters were maximum at a HR of 0.05 °C/min, reaching 0.56 ± 0.06 mg/g h and 9.3 ± 0.6 mg/g, respectively. At HR above 0.5 °C/min, Y_p/x remained relatively constant, whereas Q_P tended to decrease. The supercoiled pDNA fraction remained around 80% at all HR. Bioreactors were equipped with a capacitance/conductivity probe. In all cases biomass concentration correlated closely with the capacitance signal and acetate and glucose accumulation was accompanied by an increase in the conductivity signal. Thus, it was possible to calculate acetate and biomass concentrations, as well as μ, from online capacitance and conductivity signals using estimators. Altogether, in this study it was shown that it is possible to maximize pDNA productivity by choosing an appropriate HR and that relevant parameters can be estimated by capacitance/conductivity signals, which are useful for better process control and development.     

Evaluation of adsorbents for separation and purification of paclitaxel from plant cell cultures

In this study, we evaluated the efficiency of different adsorbents for the removal of plant-derived impurities during the pre-purification of paclitaxel from plant cell cultures. Using the synthetic adsorbents sylopute and active clay and their major components SiO₂ and MgO, we performed adsorbent treatment and analyzed the paclitaxel precipitates recovered from hexane precipitation. When SiO₂ was used, the highest purity (～58.1%) and yield (～91.5%) of paclitaxel were obtained. We also determined differences in the effectiveness of the adsorbent treatment according to changes in the surface area, pore volume and pore diameter of SiO₂. Adsorbent treatment was more effective when pore diameter was larger (silica I [2.19 nm] < silica II [4.92 nm] < silica III [9.07 nm]). The highest purity (～74.3%) and yield (～92.9%) of paclitaxel were obtained when silica III was used in the adsorbent treatment. Pore diameter had a greater effect on the removal of plant-derived impurities during the pre-purification of paclitaxel compared with surface area and pore volume. This result could be confirmed by HPLC analysis of the absorbent after treatment and TGA of the organic substances that were bonded to the adsorbent.     

Simultaneous production of single cell protein and killer toxin by Wickerhamomyces anomalus HN1-2 isolated from mangrove ecosystem

The yeast Wickerhamomyces anomalus (the previous name was Pichia anomala) HN1-2 isolated from the mangrove ecosystem was found to be able to produce high level of both killer toxin and single cell protein. When the killer yeast cells were grown by batch cultivation in 5-l fermentor, crude protein in the cells, cell mass, reducing sugar, and diameter of the inhibition zone reached 56.0 g per 100 g of cell dry weight, 7.3 g per liter, 9.5 g per liter, and 19.0 mm, respectively within 12 h and this yeast synthesized a large amount of the essential amino acids, such as lysine (7.8%), methionine (1.8%), and leucine (9.0%). The crude killer toxin produced by the killer yeast isolate HN1-2 could kill the cells of Lodderomyces elongisporus, Candida albicans, Metschnikowia bicuspidata, Pichia guilliermondii, Saccharomyces cerevisiae, Yarrowia lipolytica, and Kluyveromyces aestuarii, which were widely distributed in natural marine environments. The results also showed that the undesirable yeast could be avoided during cell growth of the killer yeast.     

Optimizing l-(+)-lactic acid production by thermophile Lactobacillus plantarum As.1.3 using alternative nitrogen sources with response surface method

The effects of five alternative nitrogen sources, namely, malt sprout (MS), corn steep liquor (CSL), NH₄Cl, NH₄NO₃ and diamine citrate (DC) were investigated on the l-(+)-lactic acid (LA) production by thermophile Lactobacillus plantarum As.1.3. Through the statistical analysis of the results by three steps of response surface methodology (RSM) design, MS and CSL were found to have significant effects on the LA production and their optimal concentrations in the medium should be 16.0 g/L and 12.0 g/L, respectively. The verification of the optimized medium showed that the maximum specific growth rate (μ_m) was 1.09 h⁻¹, the cell yield coefficient (Y_X/S) and the l-(+)-lactic acid yield coefficient (Y_P/S) were 0.233 (OD₆₂₀/g) and 0.98 (g/g), and the maximum volumetric productivity and the average volumetric productivity were 13.0 g/L h and 3.20 g/L h, respectively. The results indicate that the LA production can also be enhanced with the inexpensive nitrogen source alternatives.     

Ethanol and acetate synthesis from waste gas using batch culture of Clostridium ljungdahlii

Single inorganic carbon source was used for production of chemicals and fuels via fermentation processes. Clostridium ljungdahlii, a strictly anaerobic autotrophic bacterium, was grown on synthesis gas to produce acetate and ethanol from gaseous substrates. C. ljungdahlii was grown on a various concentrations of carbon monoxide with synthesis gas total pressures of 0.8–1.8 atm with an interval of 0.2 atm. The cell and product yields were 0.015 g cell/g CO and 0.41 g acetate/g CO, respectively. Formation of acetate was steady and the production trend was about the same for all of the gases initial pressure and at constant cell density. The ethanol concentration was enhanced by the initial presence of hydrogen and carbon dioxide in the liquid phase. There was no substrate inhibition while C. ljungdahlii was grown in the batch fermentation, even at high system pressure of 1.6 and 1.8 atm. A desired product molar ratio of ethanol:acetate (5:1) was achieved with total gas pressure of 1.6 and 1.8 atm.     

Evaluation of single cell oil from Aureobasidium pullulans var. melanogenum P10 isolated from mangrove ecosystems for biodiesel production

In this study, the yeast strain P10 which was identified to be a member of Aureobasidium pullulans var. melanogenum isolated from the mangrove ecosystems was found to be able to accumulate high content of oil in its cells. After optimization of the medium for lipid production and cell growth by the yeast strain P10, it was found that 8.0 g of glucose per 100 ml, 0.02 g of yeast extract per 100 ml, 0.02 g of ammonium sulfate per 100 ml, pH 6.0 in the medium were the most suitable for lipid production. During 10-l fermentation, a titer was 66.3 g oil per 100 g of cell dry weight, cell mass was 1.3 g per 100 ml, a yield was 0.11 g of oil per g of consumed sugar and a productivity was 0.0009 g of oil per g of consumed sugar per h within 120 h. At the same time, only 0.07 g of reducing sugar per 100 ml was left in the fermented medium. The compositions of the fatty acids produced were C_16:0 (26.7%), C_16:1(1.7%), C_18:0 (6.1%), C_18:1 (44.5%), and C_18:2 (21.0%). The biodiesel produced from the extracted lipid could be burnt well.