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.     

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.     

Stimulatory effects of Coix lacryma-jobi oil on the mycelial growth and metabolites biosynthesis by the submerged culture of Ganoderma lucidum

Effects of Coix lacryma-jobi oil (CLO) addition on the mycelia growth and production of bioactive metabolites, such as triterpenoids, exopolysaccharide (EPS), and intracellular polysaccharide (IPS) in the submerged culture of Ganoderma lucidum were studied. The results showed that when a level of 2% CLO was added at the beginning of culture, the biomass, triterpenoids, EPS, and IPS productions reached a maximum of 10.71 g/L, 92.94 mg/L, 0.33 g/L, and 0.389 g/L, respectively, that were 3.34-fold, 2.76-fold, 2.2-fold, and 2.23-fold compared to that of control. Analysis of fermentation kinetics of G. lucidum suggested that glucose concentration in the culture of CLO-added group decreased more quickly as compared to the control group from day 2 to day 7 of fermentation process, while the triterpenoids and polysaccharides biosynthesis were promoted at the same culture period. However, the culture pH profile was not affected by the addition of CLO. There were no new components in the two types of polysaccharides obtained by the addition of CLO. Enzyme activities analysis indicated CLO or its fatty acids affected the synthesis level of phosphoglucose isomerase and α-phosphoglucomutase at different stage.     

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.     

Novel hypoglycemic effects of Ganoderma lucidum water-extract in obese/diabetic (+db/+db) mice

In this study, we evaluated the pharmacological effects of Ganoderma lucidum (G. lucidum) (water-extract) (0.003, 0.03 and 0.3 g/kg, 4-week oral gavage) consumption using the lean (+db/+m) and the obese/diabetic (+db/+db) mice. Different physiological parameters (plasma glucose and insulin levels, lipoproteins-cholesterol levels, phosphoenolpyruvate carboxykinase (PEPCK), 3-hydroxy-3-methylglutaryl coenzyme A reductase (HMG CoA reductase) and isolated aorta relaxation of both species were measured and compared. G. lucidum (0.03 and 0.3 g/kg) lowered the serum glucose level in +db/+db mice after the first week of treatment whereas a reduction was observed in +db/+m mice only fed with 0.3 g/kg of G. lucidum at the fourth week. A higher hepatic PEPCK gene expression was found in +db/+db mice. G. lucidum (0.03 and 0.3 g/kg) markedly reduced the PEPCK expression in +db/+db mice whereas the expression of PEPCK was attenuated in +db/+m mice (0.3 g/kg G. lucidum). HMG CoA reductase protein expression (in both hepatic and extra-hepatic organs) and the serum insulin level were not altered by G. lucidum. These data demonstrate that G. lucidum consumption can provide beneficial effects in treating type 2 diabetes mellitus (T2DM) by lowering the serum glucose levels through the suppression of the hepatic PEPCK gene expression.     

Improving the lactic acid production of Actinobacillus succinogenes by using a novel fermentation and separation integration system

This work describes the development of a novel integrated system for lactic acid production by Actinobacillus succinogenes. Fermentation and separation were integrated with the use of a microfiltration (MF) membrane, and lactic acid was recovered by resin adsorption following MF. The fermentation broth containing residual sugar and nutrients was then recycled back into the fermenter after lactic acid adsorption. This novel approach overcame the problem of product inhibition and extended the cell growth period from 41 h to 120 h. Production of lactic acid was improved by 23% to 183.4 g L⁻¹. The overall yield and productivity for glucose were 0.97 g g⁻¹ and 1.53 g L⁻¹ h⁻¹, respectively. These experimental results indicate that the integrated system could benefit continuous production of lactic acid at high levels.     

Triterpenoid biosynthesis and the transcriptional response elicited by nitric oxide in submerged fermenting Ganoderma lucidum

Ganoderic triterpenoid (GT) is a promising anti-tumour constituent in Ganoderma lucidum. The aim of this study was to investigate induction by and a possible signalling mechanism of nitric oxide (NO) for GT synthesis. Compared to the control, the biomass decreased by 43.5% at 120 h and the GT yield increased by 40.94% at 72 h in the presence of a 5 mM NO donor sodium nitroprusside supplement. The gene expression profiles of G. lucidum in response to NO were investigated by RNA-sequencing. Functional annotation and an enrichment analysis of the differentially expressed genes indicated that NO inhibited mycelial growth probably via the suppression of the glycolysis genes involved in carbohydrate metabolism. NO may function directly as a regulator of gene expression in the mevalonate pathway to induce GT biosynthesis, and the hyper-production of GT in response to NO could also be accomplished by a signalling function involving Ca²⁺ and a reactive oxygen species (ROS) pathway. The results of this study are useful for large-scale GT production and can facilitate further studies on the endogenous signalling pathways involved in the GT biosynthetic pathway.     

Carboxymethylation of a polysaccharide extracted from Ganoderma lucidum enhances its antioxidant activities in vitro

The chemical carboxylmethylated polysaccharide (C-GLP), which derived from water-insoluble crude Ganoderma lucidum polysaccharide (GLP), was prepared. Water solubility, chemical characterization, and antioxidant activities in vitro of C-GLP were determined. The solubility of C-GLP in distilled water reached 100 mg/ml, which was much higher than the solubility of GLP. Chemical analysis indicated that C-GLP was composed of Glc:Man:Gal = 33.0:1.0:3.4 with a molecular weight of 1.8 × 10⁶ Da and a carboxymethyl content of 11.07%. The signals of carboxymethyl were found in IR and ¹³C NMR spectra. Moreover, a high antioxidant activity of C-GLP was observed, especially in scavenging of hydroxyl radical (83.7% at 5 mg/ml) and hydrogen peroxide (51.6% at 10 mg/ml). This study indicates the effects of carboxymethylation on water-insoluble polysaccharide and explores a potential antioxidant in food industry and pharmaceuticals.     

Purification and characterization of a novel proteinase A inhibitor from Ganoderma lucidum by submerged fermentation

A novel proteinase A inhibitor was purified from Ganoderma lucidum. The purification was carried out by ethanol precipitation (50–80%), ACA44 gel filtration and Source 30Q anion exchange, respectively. The molecular mass of the inhibitor was 38 kDa as estimated via SDS-PAGE and gel filtration. Its carbohydrate content was up to 70%. β-Elimination revealed that the linkage between the glycan and the core protein backbone might be O-linkage. This inhibitor showed a remarkable heat stability. By investigating the interaction between this inhibitor and a variety of proteinases, it is indicated that the inhibitor was more specific against yeast proteinase A than other proteinases. The dissociation constants (Ki) and concentration required for 50% inhibition (IC₅₀) for proteinase A were 2.7 × 10⁻⁶ M and 0.16 mg/ml, respectively.     

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.     

Bench-scale fermentation of Trichoderma viride on wastewater sludge: Rheology,lytic enzymes and biocontrol activity

Conidiation and lytic enzyme production by Trichoderma viride at different solids concentration of pre-treated municipal wastewater sludge was examined in a 15-L fermenter. The maximum conidia concentration (5.94 × 10⁷ CFU mL⁻¹ at 96 h) was obtained at 30 g L⁻¹ suspended solids. The maximum lytic enzyme activities were achieved around 12–30 h of fermentation. Bioassay against a fungal phytopathogen, Fusarium sp. showed maximum activity in the sample drawn around 96 h of fermentation at 30 g L⁻¹ suspended solids concentration. Entomotoxicity against spruce budworm larvae showed maximum value ≈17290 SBU μL⁻¹ at 30 g L⁻¹ suspended solids concentration at the end of fermentation (96 h). Plant bioassay showed dual action of T. viride, i.e., disease prevention and growth promotion. The rheological analyses of fermentation sludges showed the pseudoplastic behaviour. In order to maintain required dissolved oxygen concentration ≥30%, the agitation and aeration requirements significantly increased at 35 g L⁻¹ compared to 30 and 25 g L⁻¹. The oxygen uptake rate and volumetric oxygen mass transfer coefficient, k_La at 35 g L⁻¹ did not increase in comparison to 30 g L⁻¹ due to rheological complexity of the broth during fermentation. Thus, the successful fermentation operation of the biocontrol fungus T. viride is a rational indication of its potential for mass-scale production for agriculture and forest sector as a biocontrol agent.     

A novel medium for the production of cephamycin C by Nocardia lactamdurans using solid-state fermentation

In this study, Nocardia lactamdurans NRRL 3802 was explored for the first time for production of cephamycin C by using solid-state fermentation. The effects of various substrates, moisture content, inoculum size, initial pH of culture medium, additional nitrogen source and amino acids were investigated for the maximum production of cephamycin C by N. lactamdurans NRRL 3802 in solid-state fermentation. Subsequently, selected fermentation parameters were further optimized by response surface methodology (RSM). The soybean flour as a substrate with moisture content of 65%, initial pH of culture medium of 6.5 and inoculum size of 10⁹ CFU/ml (2 × 10⁸ CFU/gds) at 28 ± 2 °C after 4 days gave maximum production of 15.75 ± 0.27 mg/gds of cephamycin C as compared to 8.37 ± 0.23 mg/gds before optimization. Effect of 1,3-diaminopropane on cephamycin C production was further studied, which further increased the yield to 27.64 ± 0.33 mg/gds.     

Fermentative production of succinic acid from straw hydrolysate by Actinobacillus succinogenes

In this work, straw hydrolysates were used to produce succinic acid by Actinobacillus succinogenes CGMCC1593 for the first time. Results indicated that both glucose and xylose in the straw hydrolysates were utilized in succinic acid production, and the hydrolysates of corn straw was better than that of rice or wheat straw in anaerobic fermentation of succinic acid. However, cell growth and succinic acid production were inhibited when the initial concentration of sugar, which was from corn straw hydrolysate (CSH), was higher than 60 g l^?1. In batch fermentation, 45.5 g l^?1 succinic acid concentration and 80.7% yield were attained after 48 h incubation with 58 g l^?1 of initial sugar from corn straw hydrolysate in a 5-l stirred bioreactor. While in fed-batch fermentation, concentration of succinic acid achieved 53.2 g l^?1 at a rate of 1.21 g l^?1 h^?1 after 44 h of fermentation. Our work suggested that corn straw could be utilized for the economical production of succinic acid by A. succinogenes.     

Significance of protein elicitor isolated from Tuber melanosporum on the production of ganoderic acid and Ganoderma polysaccharides during the fermentation of Ganoderma lucidum

Under the elicitation of protein elicitor isolated from the culture mycelia of Tuber melanosporum, the biosynthesis of ganoderic acids (GA) was significantly stimulated during Ganoderma lucidum fermentation. Compared with our previous results that, GA content was inhibited by polysaccharide elicitor isolated from T. melanosporum, while improved by the elicitor of polysaccharide and protein, protein was identified to be the exact component inducing GA biosynthesis in this work. G. lucidum cell growth was significantly inhibited by elicitor of polysaccharide and protein, and polysaccharide elicitor did not inhibit the cell growth. In this work, the remarkable inhibition on the cell growth was considerably eliminated under the elicitation of protein elicitor isolated from T. melanosporum. These suggested maybe the interaction of polysaccharide and protein components existed in the inhibition on the cell growth of G. lucidum. Not only GA content but also total GA accumulation obtained the highest values after the elicitation of protein elicitor. The maximal GA production of 260.5 ± 5.6 mg/L was 31.2% higher than the control. Under the elicitation of protein elicitor, the production of extracellular polysaccharide (EPS) and the content of intracellular polysaccharide (IPS) were also enhanced; however, total IPS accumulation was lower. GA biosynthesis was also significantly affected by the addition time of protein elicitor, whose optimal value was the culture of day 4.     

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.     

Use of lignocellulosic wastes of pecan (Carya illinoinensis) in the cultivation of Ganoderma lucidum

Background

The wastes of pecan nut (Carya illinoinensis (Wangenh.) K. Koch) production are increasing worldwide and have high concentrations of tannins and phenols.

Comparison of lipopeptide biosurfactants production by Bacillus subtilis strains in submerged and solid state fermentation systems using a cheap carbon source: Some industrial applications of biosurfactants

Biosurfactants, in general has the potential to aid in the recovery of subsurface organic contaminants (environmental remediation) or crude oils (oil recovery). However, high production and purification costs limit its use in these high-volume applications. In the present study, the efficiency of two Bacillus subtilis strains viz., DM-03 and DM-04 for the production of biosurfactants in two fermentation systems viz., solid state fermentation (SSF) and submerged fermentation (SmF) was compared. Both the B. subtilis strains produced appreciable and equal amount of crude lipopeptide biosurfactants (B. subtilis DM-03: 80.0 ± 9 mg/gds in SmF and 67.0 ± 6 mg/gds in SSF; B. subtilis DM-04: 23.0 ± 5.0 mg/gds in SmF and 20.0 ± 2.5 mg/gds in SSF) in the two different fermentation systems using potato peels as cheap carbon source. These thermostable lipopeptide biosurfactants produced by B. subtilis strains either in SSF or in SmF, exhibited strong emulsifying property and could release appreciable amount of oil from saturated sand pack column. Further, it was shown by biochemical analysis, RP-HPLC profile and IR spectra that there is no qualitative and qualitative differences in the composition of crude biosurfactants produced either in SmF or in SSF system.     

High production of poly-β-hydroxybutyrate (PHB) by an Azotobacter vinelandii mutant altered in PHB regulation using a fed-batch fermentation process

A mixed fermentation strategy based on exponentially fed-batch cultures (EFBC) and nutrient pulses with sucrose and yeast extract was developed to achieve a high concentration of PHB by Azotobacter vinelandii OPNA, which carries a mutation on the regulatory systems PTSNtr and RsmA-RsmZ/Y, that negatively regulate the synthesis of PHB. Culture of the OPNA strain in shake flaks containing PY-sucrose medium significantly improved growth and PHB production with respect to the results obtained from the cultures with the parental strain (OP). When the OPNA strain was cultured in a batch fermentation keeping constant the DOT at 4%, the maximal growth rate (0.16 h⁻¹) and PHB yield (0.30 g_PHB g_Suc⁻¹) were reached. Later, in EFBC, the OPNA strain increased three fold the biomass and 2.2 fold the PHB concentration in relation to the values obtained from the batch cultures. Finally, using a strategy of exponential feeding coupled with nutrient pulses (with sucrose and yeast extract) the production of PHB increased 7-fold to reach a maximal PHB concentration of 27.3 ± 3.2 g L⁻¹ at 60 h of fermentation. Overall, the use of the mutant of A. vinelandii OPNA, impaired in the PHB regulatory systems, in combination with a mixed fermentation strategy could be a feasible strategy to optimize the PHB production at industrial level.