Optimal fermentation conditions for enhanced glutathione production by Saccharomyces cerevisiae FF-8

The influence of feedstock amino acids, salt, carbon and nitrogen sources on glutathione production by Saccharomyces cerevisiae FF-8 was investigated. Glucose, yeast extract, KH2PO4, and L-cysteine were found to be suitable feedstock. Highest glutathione production was obtained after cultivation with shaking for 72 h in a medium containing glucose 3.0% (w/v), yeast extract 3.0%, KH2PO4 0.06% and L-cysteine 0.06%. The glutathione concentration achieved using this medium increased 2.27-fold to 204 mg/l compared to YM basal medium.     

Joint effect of nitrogen sources and B vitamin supplementation of date juice on lactic acid production by Lactobacillus casei subsp. rhamnosus

The use of date juice as a substrate for lactic acid production was investigated. Various nitrogen sources were compared with yeast extract for efficient lactic acid production by Lactobacillus casei subsp. rhamnosus. Among different nitrogen sources added to date juice (yeast extract, ammonium sulfate, tryptic soy, urea, peptone, and casein hydrolysate), yeast extract was the most efficient. The effect of yeast extract could have been due to its B vitamin content. The addition of five B vitamins at less than 25 mg/l to date juice with any nitrogen source enhanced lactic acid production to some extent, except for date juice with yeast extract or urea or peptone. The most significant increase was obtained with ammonium sulfate. Half of the yeast extract content (10 g/l) in a supplemented date juice could be replaced by a mixture of B vitamins at less than 25 mg/l, and ammonium sulfate at 2.6 g/l with no significant decrease in lactic acid production.     

Optimization of culture conditions and medium composition for the production of micrococcin GO5 by Micrococcus sp. GO5

To enhance the production of micrococcin GO5, a bacteriocin produced by Micrococcus sp. GO5, cultivation conditions and medium composition were optimized. The optimal initial pH and temperature for bacteriocin production were 7.0-9.0 and 37 degrees C, respectively. Micrococcus sp. GO5 displayed the highest micrococcin GO5 activity when grown in modified MRS medium that contained lactose or sucrose, rather than glucose, as a carbon source. The maximum bacteriocin activity was obtained in modified MRS medium containing 0.5% tryptone and 1.0% yeast extract as nitrogen sources instead of the other nitrogen sources present in MRS medium. Bacteriocin production was greatly affected by the concentration of K(2)HPO(4); strain GO5 produced eight-fold more bacteriocin in medium containing 2.0-2.5% K(2)HPO(4) than in medium containing 0.2% K(2)HPO(4). The optimal concentration of MgSO(4).7H(2)O for bacteriocin production was 0.5%. The production of micrococcin GO5 was increased 32-fold in shake flask culture and 16-fold in a bioreactor using the optimized medium (TY medium), compared with culturing in MRS medium.     

Exopolysaccharide production and mycelial growth in an air-lift bioreactor using Fomitopsis pinicola

For effective exopolysaccharide production and mycelial growth by a liquid culture of Fomitopsis pinicola in an air-lift bioreactor, the culture temperature, pH, carbon source, nitrogen source, and mineral source were initially investigated in a flask. The optimal temperature and pH for mycelial growth and exopolysaccharide production were 25degrees C and 6.0, respectively. Among the various carbon sources tested, glucose was found to be the most suitable carbon source. In particular, the maximum mycelial growth and exopolysaccharide production were achieved in 4% glucose. The best nitrogen sources were yeast extract and malt extract. The optimal concentrations of yeast extract and malt extract were 0.5 and 0.1%, respectively. K2HPO4 and MgSO4 x 7H2O were found to be the best mineral sources for mycelial growth and exopolysaccharide production. In order to investigate the effect of aeration on mycelial growth and exopolysaccharide production in an air-lift bioreactor, various aerations were tested for 8 days. The maximum mycelial growth and exopolysaccharide production were 7.9 g/l and 2.6 g/l, respectively, at 1.5 vvm of aeration. In addition, a batch culture in an air-lift bioreactor was carried out for 11 days under the optimal conditions. The maximum mycelial growth was 10.4 g/l, which was approximately 1.7-fold higher than that of basal medium. The exopolysaccharide production was increased with increased culture time. The maximum concentration of exopolysaccharide was 4.4 g/l, which was about 3.3-fold higher than that of basal medium. These results indicate that exopolysaccharide production increased in parallel with the growth of mycelium, and also show that product formation is associated with mycelial growth. The developed model in an air-lift bioreactor showed good agreement with experimental data and simulated results on mycelial growth and exopolysaccharide production in the culture of F pinicola.     

The effect of supplementation by different nitrogen sources on the production of lactic acid from date juice by Lactobacillus casei subsp. rhamnosus

Production of lactic acid from date juice by fermentation has been studied using Lactobacillus casei subsp. rhamnosus as the producer organism. The optimum substrate concentration, expressed in its glucose content, was 60 g l(-1). Various nitrogen sources were compared with yeast extract in terms of their efficiency for lactic acid production. None of these nitrogen sources gave lactic acid concentrations as high as that obtained with yeast extract. As yeast extract supplementation was not economically attractive, different proportions of (NH4)2SO4 and yeast extract were used. When the elemental nitrogen ratio of(NH4)2SO4 to yeast extract was 4:1, the substrate use and efficiency of lactic acid production were the same as in date juice supplemented with 20 g l(-1) yeast extract (0:5).     

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 nitrogen source and nitrogen concentration on the production of pyruvate by Torulopsis glabrata

The effect of nitrogen sources including yeast extract, peptone, soybean hydrolyzate and some inorganic nitrogen sources, as well as the nitrogen concentration on the fermentative production of pyruvate by Torulopsis glabrata WSH-IP12 was investigated. The addition of yeast extract greatly inhibited pyruvate accumulation, while peptone was shown to be the most favorable nitrogen source. In flask culture, 15 g l(-1) peptone was needed to consume 80 g l(-1) glucose with 23.4 g l(-1)of pyruvate accumulated. Pyruvate production was markedly dependent on the ratio of carbon to nitrogen (C:N), its production was improved by increasing the concentration of glucose and peptone proportionally and reduced by exclusively increasing the glucose concentration. In a glucose fed-batch culture, cell growth and pyruvate production slowed after 28 h. However, cell growth and pyruvate production recovered after further nitrogen, in the form of peptone and ammonium sulfate, was added to the culture. A final concentration of pyruvate of 54.5 g l(-1) was achieved at 64 h (yield to glucose consumed of 0.471 g g(-l)). By using aqueous ammonia instead of potassium hydroxide for pH control, 57.3 g l(-1) pyruvate with a yield of 0.498 g g(-1) was produced by 55 h. This result further indicates that nitrogen level plays an important role in the production of pyruvate.     

Fermentation study for the production of hepatitis B virus pre-S2 antigen by the methylotrophic yeastHansenula polymorpha

Summary Various physico-chemical parameters have been studied in order to improve the production of hepatitis B virus pre-S2 antigen (middle surface antigen) by the methylotrophic yeastHansenula polymorpha. Antigen production was done in two steps: first, production of cells on glycerol (Phase 1), followed by induction of antigen expression with methanol (Phase 2). Dense cultures ofH. polymorpha, equivalent to 35–40 g/l (dry weight), were readily obtained in small fermenters using minimal medium containing glycerol as carbon source. Antigen expression in this minimal medium, after induction with methanol, was however low and never exceeded 1.6 mg/l of culture. Antigen production was greatly enhanced by adding complex organic nitrogen sources along with methanol at induction time; yeast extract was the best of all the sources tested. In shake flasks, antigen production was proportional to yeast extract concentration up to 7% (w/v) yeast extract. it became clear that the nutritional conditions for good antigen expression were different from those for good biomass production. The effects of yeast extract were reproduced in small fermenters: antigen levels reached 8–9 mg/l in medium containing 6% (w/v) yeast extract during induction with methanol. The mechanisms of yeast extract's effects are still unknown but are probably nutritional. The recombinantH. polymorpha strain produced both periplasmic and intracellular antigen. The periplasmic antigen was shown to be present as 20–22-nm particles and was therefore immunogenic. Immunoblotting indicated that part of the pre-S2 antigen was present as a 24-kDa degradation product. These studies have led to a 140-fold increase in volumetric productivity of antigen and to a 4.6-fold increase in specific production.Part of these results have been presented at the Deuxième Congrès de la Société Française de Microbiologie, Strasbourg, France, September 1989.     

Influence of Culture Parameters on Biological Hydrogen Production by Clostridium saccharoperbutylacetonicum ATCC 27021

Summary Various medium components (carbon and nitrogen sources, iron, inoculum size) and environmental factors (initial pH and the agitation speed) were evaluated for their effects on the rate and the yield of hydrogen production by Clostridium saccharoperbutylacetonicum. Among the carbon sources assessed, cells grown on disaccharides (lactose, sucrose and maltose) produced on the average more than twice (2.81 mol-H2/mol sugar) as much hydrogen as monosaccharides (1.29 mol-H2/mol sugar), but there was no correlation between the carbon source and the production rate. The highest yield (2.83 mol/mol) was obtained in lactose and sucrose but the highest production rate (1.75 mmol/h) in sucrose. Using glucose as carbon source, yeast extract was the best nitrogen source. A parallel increase between the production rate and the yield was obtained by increasing glucose concentration up to 40 g/l (1.76 mol-H2/mol, 3.39 mmol/h), total nitrogen as yeast extract up to 0.1% (1.41 mol/mol, 1.91 mmol/h) and agitation up to 100 rev/min (1.66 mol-H2/mol, 1.86 mmol/h). On the other hand, higher production rates were favoured in preference to the yield at a neutral initial pH 7 (2.27 mmol/h), 1000 mg iron/l or more (1.99 mmol/h), and a larger inoculum size, 10%, (2.36 mmol/h) whereas an initial alkaline pH of 8.5 (1.72 mol/mol), a lower iron concentration of 25 mg/l (1.74 mol/mol) and smaller inoculum size, 1%, (1.85 mol/mol) promoted higher yield over production rate.     

Medium optimization for the production of avermectin B1a by Streptomyces avermitilis 14-12A using response surface methodology

Response surface methodology was employed to optimize the composition of medium for the production of avermectin B1a by Streptomyces avermitilis 14-12A in shaker flask cultivation. Corn starch and yeast extract were found to have significant effects on avermectin B1a production by the Plackett–Burman design. The steepest ascent method was used to access the optimal region of the medium composition, followed by an application of response surface. The analysis revealed that the optimum values of the tested variables were 149.57 g/l corn starch and 8.92 g/l yeast extract. A production of 5128 mg/l, which was in agreement with the prediction, was observed in verification experiment. In comparison to the production of original level (3528 mg/l), 1.45-fold increase had been obtained.     

Optimization of culture conditions for production of antimalarial menisporopsin A by the seed fungus Menisporopsis theobromae BCC 4162

AIMS: The aim of this work was to optimize the production of a novel antimaralial menisporopsin A by the seed fungus Menisporopsis theobromae BCC 4162. METHODS AND RESULTS: Fungal cultures were grown in shake flasks at 25 degrees C in the basal medium with varying carbon and nitrogen sources, aeration rates and initial pH levels. The optimal carbon and nitrogen sources that improved the production of menisporopsin A were 1% fructose and 2.5% meat extract respectively. The production was further enhanced when the culture incubated on a shaker at 200 rev min(-1) with an initial pH of 8. The yield of menisporopsin A cultured under the optimized conditions was increased from 348.30 (obtained from basal medium) to 889.02 mg l(-1), and the cultivation time was reduced from 28 to only 4 days. As a result, the productivity of menisporopsin A was greatly enhanced to 222.26 mg l(-1) day(-1) which is 18-fold higher than that of basal conditions. Larger scale production in a fermenter was also achieved, yielding menisporopsin A at a maximal level of 594.32 mg l(-1) in 4 days. CONCLUSIONS: The optimized culture conditions for menisporopsin A production by M. theobromae BCC 4162 was the cultivation under shaking or agitation at 25 degrees C in fructose-meat extract medium with an initial pH of 8. SIGNIFICANCE AND IMPACT OF THE STUDY: The production of menisporopsin A in a fermenter with a relatively short incubation period could be valuable for further utilization for chemical structure modification and derivatization.     

Production of high molecular weight pullulan by Aureobasidium pullulans HP-2001 with soybean pomace as a nitrogen source

The production of pullulan by Aureobasidium pullulans HP-2001 was enhanced by yeast extract as a nitrogen source as well as soybean pomace. The highest production of pullulan by A. pullulans HP-2001 with yeast extract was 5.5 g/l whereas that of pullulan with soybean pomace was 7.5 g/l. The gas chromatogram of pullulan produced by A. pullulans HP-2001 with soybean pomace as a nitrogen source showed that the major and minor components were glucose and mannose. The FTIR spectra of pullulans produced with yeast extract, a mixture of yeast extract and soybean pomace, and soybean pomace alone exhibited similar features. The increase in content of reducing sugars after pullulanase treatment of pullulans produced with different nitrogen sources indicated that all the pullulans had alpha-(1,6) glucosidic linkages of alpha-(1,4) linked maltotriose units. The average molecular weights of pullulans produced with various concentrations of yeast extract and soybean pomace ranged from 0.17 to 1.32x10(6) and from 1.32 to 5.66x10(6), respectively. All pullulans produced by A. pullulans HP-2001 in this study had the same basic structures, but their ratios of monomeric components were a little different, which might result in the production of pullulans with different molecular weights.     

氮源对L-苏氨酸发酵的影响

以L-苏氨酸生产菌TRFC为供试菌株,研究了氮源对L-苏氨酸发酵的产量和糖酸转化率的影响。首先通过摇瓶实验确定发酵的最佳无机氮源和有机氮源分别为硫酸铵和酵母粉,进一步利用10L罐补料分批发酵确定硫酸铵和酵母粉的最佳用量,继续优化培养条件,采用发酵中后期流加硫酸铵和糖氨混合补料等措施,L-苏氨酸产量得到进一步的提高。在最优发酵条件下,通过10L罐补料分批发酵36h,产酸可达118.9g/L,糖酸转化率为47.6%。     

一株产絮凝剂不动杆菌的筛选及其絮凝特性

从活性污泥中筛选出一株高效的微生物絮凝剂产生菌, 鉴定为鲍曼不动杆菌。蚕豆根尖细胞微核试验未显示该菌株所产絮凝剂具有遗传毒性。该菌产絮凝剂的最佳碳源和氮源分别为葡萄糖和酵母浸出汁, 培养时间为24 h。在絮凝体系中加入Ca2+能明显提高发酵液的絮凝率。在pH为8.0时对高岭土悬浊液和污水具有良好的絮凝效果。     

一株产絮凝剂不动杆菌的筛选及其絮凝特性

从活性污泥中筛选出一株高效的微生物絮凝剂产生菌,鉴定为鲍曼不动杆菌.蚕豆根尖细胞微核试验未显示该菌株所产絮凝剂具有遗传毒性.该菌产絮凝剂的最佳碳源和氮源分别为葡萄糖和酵母浸出汁,培养时间为24 h.在絮凝体系中加入Ca2 能明显提高发酵液的絮凝率.在pH为8.0时对高岭土悬浊液和污水具有良好的絮凝效果.     

Semi-defined Medium for in vitro Cultivation of the Fastidious Insect Pathogenic Fungus Cordyceps unilateralis

Cordyceps unilateralis is a fastidious fungal pathogen affecting ants. Up to now, only the complex and expensive Grace’s insect cell culture medium has been used for in vitro cultivation (as blastospores and mycelium) of this fungus. To obtain an inexpensive and less complicated medium, the effects of carbon and nitrogen sources, salt solution and carbon-to-nitrogen (C:N) ratio on the growth of this fungus were examined. Glucose was the most important factor for blastospore formation, and yeast extract could be used as a nitrogen source for blastospore formation and mycelial growth. A suitable C:N ratio (glucose: yeast extract) was 33.3:1. As a result, a new semi-defined medium was achieved, composed of 26.68 g L⁻¹ glucose, 3.3 g L⁻¹ yeast extract and salt solution. This medium supported blastospore formation and mycelial growth of all tested C. unilateralis isolates.     

Effect of chemical and physical parameters on the production of L-asparaginase from a newly isolated Serratia marcescens SK-07

Aims: The objective of this study is to optimize the levels of carbon and nitrogen sources of the medium in shake flask experiments and evaluate the effect of pH and dissolved oxygen (DO) on the production of l ‐asparaginase from a newly isolated Serratia marcescens SK‐07 in a batch bioreactor. Methods and Results: Central composite rotatable design (CCRD) was applied to optimize the levels of carbon and nitrogen sources of the medium in shake flask experiments. The optimal levels of l ‐asparagine, glucose, yeast extract and peptone were found to be 4·93, 3·81, 3·65 and 1·47 g l^?1, respectively, and maximal l ‐asparaginase production of 25·02 U mg^?1 was obtained under these conditions. Among the carbon sources tested, l ‐asparagine was identified to be the most favourable carbon source for enhanced production of l ‐asparaginase. The maximum l ‐asparaginase production of 29·89 U mg^?1 was achieved in a batch bioreactor at initial pH of 6·5 (uncontrolled) and DO level of 40% in the culture. Conclusions: We have isolated, screened and identified the potential micro‐organism, S. marcescens, for the production of l ‐asparaginase. An overall 5·55‐fold increase in the production was achieved under optimal levels of carbon and nitrogen sources, DO level and at initial pH of 6·5 (uncontrolled). Significance and Impact of the Study: The experiments illustrate the importance of statistical method for optimization of carbon and nitrogen sources and study the effect of physical process parameters on the production of l ‐asparaginase in shake flask and bioreactor, respectively. This study would be helpful for bioprocess development of bacterial l ‐asparaginase production.     

Effects of nitrogen sources on bacteriocin production by Enterococcus faecium A 2000

The production of a novel broad-spectrum antimicrobial peptide enterococcin A 2000, active against Gram-positive and Gram-negative microorganisms includingListeria subsp. andEscherichia coli, byEnterococcus faecium strain A 2000 isolated from the surface of traditional Bulgarian yellow cheese “kash-kaval” is considerably influenced by complex nitrogen sources in the production medium. Medium components, especially peptone and yeast extract, and their concentration contributed to the increase in bacteriocin production during the stationary phase (16–46 h) of cultivation even in the absence of one of the components present in the basal cultivation MRS medium.     

Thermostable alpha-amylase production by an extreme thermophile Bacillus thermooleovorans

AIMS: alpha-Amylase production by a newly isolated thermophile, Bacillus thermooleovorans, was studied under different cultivation conditions. METHODS AND RESULTS: The influence of various carbon and nitrogen sources on alpha-amylase production was quantified in batch fermentation in shake flasks. Starch and tryptone were observed to be the ideal carbon and nitrogen sources, respectively. Cultivation of the organism in a chemically defined medium consisting of glucose, riboflavin, cysteine, MgSO4, K2HPO4 and NaCl led to a near twofold increase in the production of alpha-amylase in comparison with that in the complex medium. The increase in enzyme production was achieved using vitamins and amino acids. When the organism was grown in a laboratory fermenter in the optimized complex medium, the noticeable effects were the near abolition of the lag phase, a 2.2-fold increase in enzyme production and a reduction in optimal production time from 12 to 4-5 h. CONCLUSION: Enhancement of amylase production was achieved under various cultivation conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: Bacillus thermooleovorans produces a calcium-independent and thermostable amylase which can find use in starch saccharification.     

Production of poly-β-hydroxybutyrate by Azotobacter vinelandii UWD in media containing sugars and complex nitrogen sources

Summary Vigorously aerated batch cultures of Azotobacter vinelandii UWD formed < 1 g poly--hydroxybutyrate (PHB)/l in media containing pure sugars and 3 g PHB/l in media containing cane molasses, corn syrup or malt extract. However, > 7 g PHB/l was formed when the medium contained 5% beet molasses. Increased yields of PHB were promoted in the media containing pure or unrefined sugars by the addition of complex nitrogen sources. The greatest effect was obtained with 0.05–0.2% fish peptone (FP), proteose peptone no. 3 or yeast extract. Peptones caused a 1.6-fold increase in residual non-PHB biomass and up to a 25-fold increase in PHB content. Hence the increased PHB formation was not simply due to stimulation of culture growth. The amount of PHB per cell protein formed by UWD in media containing FP was greatest in glucose = corn syrup > malt extract > sucrose = fructose = cane molasses > maltose, as carbon sources. The addition of FP to medium containing beet molasses did not stimulate PHB yield. The peptone effect was most significant in well-aerated cultures, which were fixed nitrogen and consuming glucose at a high rate. An explanation for the peptone effect on PHB yield stimulation is proposed.