Significance of metal ion supplementation in the fermentation medium on the structure and anti-tumor activity of Tuber polysaccharides produced by submerged culture of Tuber melanosporum

The significance of metal ion supplementation in the fermentation medium on the structure and anti-tumor activity of Tuber polysaccharides was systematically studied in the submerged fermentation of Tuber melanosporum. The lowest weight-average molecular weight (M_w) (i.e., 115.3 × 10⁴ g/mol) of intracellular polysaccharides (IPS) was obtained when Mg²⁺ and K⁺ was added in the fermentation medium. The IPS with the lower M_w exhibited a higher inhibition ratio against S-180 tumor cells. The compact conformation of extracellular polysaccharides (EPS) was formed when only K⁺ was supplied in the fermentation medium. Interestingly, EPS with compact conformation exhibited a higher inhibition ratio (i.e., 59.2%) than EPS with branched polymer chain (i.e., 9.2%) against A549 tumor cells. The highest inhibition ratio for EPS with α-glycosidic linkages against the tumor cell line HepG2 reached 32.2% when Mg²⁺ or K⁺ was supplied in the fermentation medium. The addition of metal ion Mg²⁺, K⁺, and their combination to the fermentation medium is a vital factor affecting the structures of Tuber polysaccharides, which further determine their anti-tumor activities. The information obtained in this work will be useful for the efficient and directed production of polysaccharides with anti-tumor activities by the submerged fermentation of edible fungi mycelium.     

Biosynthesis of selenium-containing polysaccharides with antioxidant activity in liquid culture of Hericium erinaceum

The effects of inorganic selenium (sodium selenite) and Selol containing selenitetriglycerides synthesized from sunflower oil on mycelial growth and selenium-containing extracellular (EPS) and intracellular (IPS) polysaccharides production were examined in shake flask cultures of Hericium erinaceum.Unlike sodium selenite which inhibited mycelial growth, Selol increased in biomass production in a dose-dependent manner. Selol also dramatically enhanced EPS formation to 2.25 g/L which is 2.5–fold higher than in the control. Selenium content in EPS and IPS obtained from Selol-enriched medium reached a maximum of 4.89 and 4.69 mg/g, respectively.The in vitro antioxidant activities of polysaccharides were evaluated by reducing power, inhibition of lipid peroxidation, and 1,1-diphenyl-dipicrylhydrazyl radicals scavenging assays. The selenium-containing EPS showed an excellent antioxidant activity correlated well with increasing concentrations.The results suggested that selenium-containing EPS from H. erinaceum submerged culture should be explored as a novel selenium source in dietary supplements, with potent antioxidant properties.     

Production of polysaccharides from Ganoderma lucidum (CCRC 36041) under limitations of nutrients

This research studied the production of polysaccharides from Ganoderma lucidum under the various limitations of nutrients, including carbon-source, nitrogen-source, phosphate-source, magnesium-source, and dissolved oxygen. The different responses of polysaccharide production were observed under different limitations of nutrients. The concentration of polysaccharides was from 1.79 g/L decreasing to 0.91 g/L when the concentration of glucose was from 60 g/L decreasing to 20 g/L. The highest specific polysaccharide production was found at 60 g/L glucose media with 0.299 g/g-cell, and the lowest molecular weight was found in carbon-source limitation. Under nitrogen-source limitation the concentration of cells was low, but both polysaccharide production (1.61 g/L) and specific polysaccharide production (0.492 g/g-cell) were the highest. The lowest molecular weight of polysaccharides was found under nitrogen-source limitation. Both the phosphate-source and magnesium-source limitations showed low cell growth. With the phosphate-source limitation both low polysaccharide production and a lower molecular weight of polysaccharides was found. In the magnesium-source limitation low polysaccharide production, but a higher molecular weight of polysaccharides, was found. For the factor of oxygen supply the best polysaccharide production was found with sufficient oxygen for the first 5 days’ cultivation and then, after changing to oxygen limitation for another 5 days’ cultivation. On the other hand, the highest molecular weight of polysaccharides was found from the beginning with oxygen limitation throughout the process of fermentation.     

Multi-fed batch culture integrated with three-stage light irradiation and multiple additions of copper ions for the hyperproduction of ganoderic acid and Ganoderma polysaccharides by the medicinal mushroom Ganoderma lucidum

To further enhance the accumulation of the bioactive metabolite ganoderic acid (GA) by fermentation of the medicinal mushroom Ganoderma lucidum, a novel integrated strategy was developed by simultaneously adopting a strategy of multiple Cu²⁺ additions, three-stage light irradiation and multi-pulse feeding of carbon and nitrogen sources. Maximal GA content (i.e., 4.1 mg/100 mg DW) and production (i.e., 720.8 mg/L) were obtained using the novel integrated strategy. Not only the biomass but also the total GA production obtained in this work is the highest reported for a shaker flask culture of G. lucidum. This work is useful for the large-scale production of GA by G. lucidum fermentation.     

Performance analyses of a pH-shift and DOT-shift integrated fed-batch fermentation process for the production of ganoderic acid and Ganoderma polysaccharides by medicinal mushroom Ganoderma lucidum

Investigations on Ganoderma lucidum fermentation suggested that the responses of the cell growth and metabolites biosynthesis to pH and dissolved oxygen tension (DOT) were different. The ganoderic acid (GA) production of 321.6 mg/L was obtained in the pH-shift culture by combining a 4-day culture at pH 3.0 with the following 6-day culture at pH 4.5, which was higher by 45% and 300% compared with the culture at pH 3.0 and 4.5, respectively. The GA production of 487.1 mg/L was achieved in the DOT-shift culture by combining a 6-day culture at 25% of DOT with a following 6-day culture at 10% of DOT, which was higher by 43% and 230% compared with the culture at 25% and 10% of DOT, respectively. A fed-batch fermentation process by combining the above-mentioned pH-shift and DOT-shift strategies resulted in a significant synergistic enhancement of GA accumulation up to 754.6 mg/L, which is the highest reported in the submerged fermentation of G. lucidum in stirred-tank bioreactor.     

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).     

A novel membrane-surface liquid co-culture to improve the production of laccase from Ganoderma lucidum

In this work, a laccase producer, Ganoderma lucidum, was separated and identified according to its morphological characteristics and phylogenetic data. A 4000 U/l and 8500 U/l of laccase activity was obtained in 500 ml flask by submerged culture and biomembrane-surface liquid culture (BSLC), respectively. Furthermore, the novel biomembrane-surface liquid co-culture (BSLCc) was developed by adding Saccharomyces cerevisiae to reactor in order to shorten the fermentation period and improve laccase production. Laccase activity obtained by BSLCc, 23 000 U/l, is 5.8 and 2.7 times of that obtained by submerged culture and BSLC, respectively. In addition, laccase production by BSLCc was successfully scaled-up to 100 l reactor, and 38 000 U/l of laccase activity was obtained on day 8. The mechanism of overproducing laccase by BSLCc was investigated by metabolism pathway analysis of glucose. The results show glucose limitation in fermentation broth induces the secretion of laccase. The addition of S. cerevisiae, on one hand, leads to an earlier occurrence of glucose limitation state, and thus shortens the fermentation time; on the other hand, it also results in the appearance of a series of metabolites of the yeast including organic acids, ethanol, glycerol and so forth in fermentation broth, and both polyacrylamide gel electrophoresis analysis and enzyme activity detection of laccase show that these metabolites contribute to the improvement of laccase activity.     

Production,characterization and antioxidant activities in vitro of exopolysaccharides from endophytic bacterium Paenibacillus polymyxa EJS-3

The production, characterization and antioxidant activities in vitro of exopolysaccharides (EPS) from endophytic bacterium Paenibacillus polymyxa EJS-3 were investigated. For EPS production, the preferable culture conditions were 24 °C and pH 8 for 60 h with sucrose and yeast extract as the carbon and nitrogen sources, respectively. Notably, sucrose concentration was the prominent factor, and the maximum yield of EPS (22.82 g/L) was obtained at a sucrose concentration of 160 g/L. The crude EPS was purified by chromatography of DEAE-52 and Sephadex G-100, affording EPS-1 and EPS-2 with molecular weights of 1.22 × 10⁶ and 8.69 × 10⁵ Da, respectively. They were composed of mannose, fructose and glucose in a molar ratio of 2.59:29.83:1 and 4.23:36.59:1, respectively. In addition, both crude and purified EPS showed strong scavenging activities on superoxide and hydroxyl radicals, and their antioxidant activities decreased in the order of crude EPS > EPS-2 > EPS-1.     

Enhanced exopolysaccharide production and biological activity of Lactobacillus rhamnosus ZY with calcium and hydrogen peroxide

Exopolysaccharides (EPS) are important food and drug additives with beneficial antioxidant, anticancer, and immune-related effects on human health. However, the EPS is limited by low yields and the need for complex culture conditions in fermentation. Here, we report that hydrogen peroxide and calcium stimulated probiotic activity and production of crude exopolysaccharide (c-EPS) by Lactobacillus rhamnosus ZY. Accordingly, supplementation with 3 mM H₂O₂ allowed c-EPS biosynthesis to reach 567 mg/L after 24 h. Addition of both CaCl₂ and H₂O₂ resulted in a c-EPS yield of 2498 mg/L after 12 h, over 9-fold higher than that of an anaerobic culture. We observed that exposure to calcium and hydrogen peroxide made the cells more hydrophobic and led to the over-expression of GroEL, NADH peroxidase, and glyceraldehyde 3-phosphate dehydrogenase, thus increasing energy storage and EPS production. Chromatographic analysis revealed c-EPS was composed mainly of mannose (5.1%), galactose (15.3%), glucose (20–30%), and rhamnose (50–60%). Preliminary in vitro tests revealed that H₂O₂ and CaCl₂ enhanced the 2,2-diphenyl-1-picrylhydrazyl and hydroxyl radical scavenging capacities, resulting in a notable protective effect against oxidative damage in NIH/3T3 cells. Our study provides a simple and cost-effective approach for achieving high yields of good quality EPS using Lactobacillus rhamnosus.     

Improvement of ganoderic acid production by fermentation of Ganoderma lucidum with cellulase as an elicitor

Two-stage cultivation of Ganoderma lucidum was performed for the enhanced production of ganoderic acid (GA). Cellulase was identified to be an effective elicitor for the improvement of GA production, and GA titer reached 1334.5 mg/l compared to the control (779.6 mg/l) using lactose as the substrate without cellulase addition. Loading of 5 mg/l cellulase on day 3 resulted in the maximal GA titer of 1608 mg/l. To our knowledge, this is the first time that cellulase was used as the elicitor to enhance GA production. Submerged fermentation in a 2.0-l bioreactor was also conducted with cellulase as the elicitor, and as a result the maximal GA titer of 1252.7 mg/l was obtained on day 12. This is so far the best GA production obtained in submerged fermentation of G. lucidum.     

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus for acetic acid production

Mixed culture of Saccharomyces cerevisiae and Acetobacter pasteurianus was carried out for high yield of acetic acid. Acetic acid production process was divided into three stages. The first stage was the growth of S. cerevisiae and ethanol production, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. The second stage was the co-culture of S. cerevisiae and A. pasteurianus, fermentation temperature and aeration rate were maintained at 34 °C and 0.4 vvm, respectively. The third stage was the growth of A. pasteurianus and production of acetic acid, fermentation temperature and aeration rate were controlled at 32 °C and 0.2 vvm, respectively. Inoculation volume of A. pasteurianus and S. cerevisiae was 16% and 0.06%, respectively. The average acetic acid concentration was 52.51 g/L under these optimum conditions. To enhance acetic acid production, a glucose feeding strategy was subsequently employed. When initial glucose concentration was 90 g/L and 120 g/L glucose was fed twice during fermentation, acetic acid concentration reached 66.0 g/L.     

Fed-batch fermentation of Tuber melanosporum for the hyperproduction of mycelia and bioactive Tuber polysaccharides

For the first time, a fed-batch fermentation process of Tuber melanosporum was developed for the efficient production of bioactive mycelia and Tuber polysaccharides. Each 1.67 g/L of peptone and 8.33 g/L of yeast extract were added on day 3, 6, and 9, respectively, and sucrose was fed to maintain its concentration around 35–5 g/L when its residual level decreased to 10–5 g/L. Then, the maximal biomass, the production of extracellular polysaccharides (EPS) and intracellular polysaccharides (IPS) reached 53.72 ± 2.57 g DW/L, 7.09 ± 0.62 and 4.43 ± 0.21 g/L, respectively. Compared with the batch culture conducted in the enriched medium, the biomass, the production of EPS and IPS were enhanced by 55.8%, 222.3% and 103.2%, respectively. Not only the cell density but also the production of EPS and IPS were the highest ever reported in truffle fermentation, and the biomass was also the highest as ever reported in mushroom fermentation.     

Culture filtrate of root endophytic fungus Piriformospora indica promotes the growth and lignan production of Linum album hairy root cultures

The effect of addition of autoclaved and filter-sterilized culture filtrate of Piriformospora indica (a root endophytic fungus) to the growing Linum album hairy root cultures on growth and lignan production was investigated. The addition resulted in a significant enhancement in lignan production and growth. The podophyllotoxin and 6-methoxypodophyllotoxin (the lignans) concentrations were maximally improved by 3.8 times (233.8 mg/L) and 4.4 times (131.9 mg/L) in comparison to control cultures, respectively, upon addition of 3.0% (v/v) filter-sterilized culture filtrate of P. indica to the hairy root cultures of L. album for exposure time of 48 h. This increase in the lignan content also coincided with the increase in phenylalanine ammonia lyase activity, which was 3.1-fold (371.4 μkat/kg protein) higher compared to control cultures under the same conditions. The maximal increase in hairy root biomass was, however, obtained under different conditions; it was enhanced by 1.4 times (21.8 g/L) in comparison to control cultures, when 2% (v/v) filter-sterilized culture filtrate was in contact with L. album cultures for 96 h.     

Evaluation of lactic acid bacterial strains of boza for their exopolysaccharide and enzyme production as a potential adjunct culture

Boza is a non-alcoholic beverage obtained from fermented cereals. Thirteen lactic acid bacteria (LAB), previously isolated from boza were identified and evaluated to determine the various technological properties for selecting appropriate strains as adjunct culture in boza. Each isolate was checked for purity, Gram-stained and tested for the catalase and oxidase activity and then subjected to identification by polymerase chain reaction (PCR) with partial 16S rRNA gene sequencing. The tests for carbohydrate fermentation and enzyme profiles were carried out with the API 50 CHL and API ZYM galleries, respectively. Exopolysaccharide (EPS) production of strains was determined by Fourier transform infrared spectroscopy (FT-IR) and quantified by the phenol sulphuric acid method. To our best knowledge, this is the first study reporting on Lactococcus garvieae (E32), Pediococcus parvulus (E42) and Streptococcus macedonicus (A15) in boza. All strains, except S. macedonicus (A15) produced EPS. Leuconostoc citreum (E55) and Lactococcus lactis (A47) were the highest EPS producing strains, yielding 2.39 ± 0.49 and 1.98 ± 0.23 g/L of EPS, respectively. Lactobacillus paracasei (D41), Lactobacillus plantarum (B2), Lactococcus lactis (F39) and among low-EPS producing strains Lactobacillus coryniformis (C55), L. paracasei (E8), and P. parvulus (E42) were evaluated to be promising candidates as potential adjunct culture in boza. The variety of enzyme production was also concern. Lc. garvieae (E32) was found to produce the largest variety of enzymes among the strains. FT-IR spectroscopy can be used for the assessment of EPS production by microorganisms reliably and accurately.     

Metabolic engineering of Clostridium tyrobutyricum for enhanced butyric acid production from glucose and xylose

Clostridium tyrobutyricum is a promising microorganism for butyric acid production. However, its ability to utilize xylose, the second most abundant sugar found in lignocellulosic biomass, is severely impaired by glucose-mediated carbon catabolite repression (CCR). In this study, CCR in C. tyrobutyricum was eliminated by overexpressing three heterologous xylose catabolism genes (xylT, xylA and xlyB) cloned from C. acetobutylicum. Compared to the parental strain, the engineered strain Ct-pTBA produced more butyric acid (37.8 g/L vs. 19.4 g/L) from glucose and xylose simultaneously, at a higher xylose utilization rate (1.28 g/L·h vs. 0.16 g/L·h) and efficiency (94.3% vs. 13.8%), resulting in a higher butyrate productivity (0.53 g/L·h vs. 0.26 g/L·h) and yield (0.32 g/g vs. 0.28 g/g). When the initial total sugar concentration was ~120 g/L, both glucose and xylose utilization rates increased with increasing their respective concentration or ratio in the co-substrates but the total sugar utilization rate remained almost unchanged in the fermentation at pH 6.0. Decreasing the pH to 5.0 significantly decreased sugar utilization rates and butyrate productivity, but the effect was more pronounced for xylose than glucose. The addition of benzyl viologen (BV) as an artificial electron carrier facilitated the re-assimilation of acetate and increased butyrate production to a final titer of 46.4 g/L, yield of 0.43 g/g sugar consumed, productivity of 0.87 g/L·h, and acid purity of 98.3% in free-cell batch fermentation, which were the highest ever reported for butyric acid fermentation. The engineered strain with BV addition thus can provide an economical process for butyric acid production from lignocellulosic biomass.     

Cellulose ethanol production from waste newsprint by simultaneous saccharification and fermentation using Saccharomyces cerevisiae KNU5377

A thermotolerant ethanol-fermenting yeast, Saccharomyces cerevisiae KNU5377, isolated from a sludge of a local industrial complex stream in Korea, was evaluated for its capability for lignocellulosic ethanol production from waste newsprint in high temperature. In this fermentation, most of dry-defibrated waste newspaper was first saccharified at 50 °C for 108 h using a commercial cellulase and, then with the last addition of dry-defibrated newsprints to the pre-saccharified broth, simultaneous saccharification and fermentation (SSF) of 1.0 L of reaction mixture was carried out at 40 °C, slowly being dropped from 50 °C, for further 72 h in a 5 L fermentor by inoculating the overnight culture of KNU5377. The maximum production of 8.4% (v/v) ethanol was obtained when 250 g (w/v)/L of dry-defibrated waste newspaper was used for ethanol production by SSF. These results suggest that S. cerevisiae KNU5377 is very useful for cellulose ethanol production by the SSF system.     

Pectinase production by Aspergillus niger LB-02-SF is influenced by the culture medium composition and the addition of the enzyme inducer after biomass growth

The production of pectinase by Aspergillus niger LB-02-SF was focused on a submerged cultivation, before it was evaluated in a solid-state process. This study involved the creation of a defined culture medium and an evaluation of the effects of the addition of the enzyme inducer, citrus pectin, to the medium after the intense biomass growth phase. A culture medium formulated without glucose allowed a reduction of biomass growth and greater pectinase production, facilitated by the control of process parameters such as mixing, pH and oxygen supply. The addition of pectin when a minimum pH of 2.7 was reached at 22 h of cultivation did not affect fungal growth. The maximum biomass concentration was 11.0 g/L at 48 h, a value similar to that observed for the control, in which pectin was included in the medium at the beginning of the process (11.5 g/L, at 41 h). However, this condition favored the production of 14 U/mL pectinase, which was approximately 40% higher than the value observed for the control. These results show that pectinase production by A. niger in a submerged cultivation is strongly affected by the medium composition as well as the delayed addition of pectin to the fermentation broth.     

Effects of culture conditions on the mycelial growth and bioactive metabolite production in submerged culture of Cordyceps militaris

The influence of initial pH value, various nitrogen sources, plant oils, and modes of propagation (shake-flask and static culture) on the production of biomass, exopolysaccharide (EPS), adenosine and, in particular, cordycepin, by Cordyceps militaris CCRC 32219 were investigated. Optimal conditions for mycelial growth, EPS and cordycepin production were observed at relatively low pH. Amongst organic sources, yeast extract (YE) was favorable for EPS and cordycepin production, while corn steep powder (CSP) was favorable for adenosine production. A lower C/N ratio was favorable for adenosine and cordycepin production; however, too low a C/N ratio led to diminished production. All plant oils tested stimulate mycelial growth and EPS production of C. militaris, but they did not show much effect on the adenosine and cordycepin production. A two-stage fermentation process by combining shake-flask fermentation with static culture significantly enhanced cordycepin production. A Box–Behnken experimental design was employed to optimize the production of cordycepin, which showed that the optimum conditions to produce cordycepin by C. militaris CCRC 32219 were at pH 6, YE concentration of 45 g/l and 8.0 day of the shake culture followed by 16 days of the static culture. Under the optimized conditions, the maximum production (2214.5 mg/l) of cordycepin was obtained, which is much higher than those reported up to date.