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.     

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.     

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.     

Liquid state fermentation of apple pomace sludge for the production of ligninolytic enzymes and liberation of polyphenolic compounds

Ligninolytic enzyme production and polyphenolic compound extraction by liquid-state culture of Phanerochaete chrysosporium ATCC 24275 was investigated by employing apple pomace sludge and synthetic medium. Different physico-chemical and biological parameters namely viscosity, zeta potential and particle size, viability and enzyme production were investigated. The ligninolytic enzyme production was higher in apple pomace sludge (45 U/l of laccase, 220 U/l of MnP and 6.5 U/l of LiP) than in synthetic medium (17 U/l of laccase, 37 U/l of MnP and 6 U/l). These maximal activities were found during the stationary and decline phase. It was also found that enzyme production was strongly correlated with P. chrysoporium viability in both synthetic medium and apple pomace sludge. Moreover, physico-chemical parameters, such as particle size, zeta potential and viscosity were strongly correlated to the viability of P. chrysosporium and to the ligninolytic enzyme production. An increase in polyphenol content extracted by acetone (383–720 mg GAE/l) was observed during fermentation of apple pomace and it was found that the polyphenol content extracted by ethanol increased ～1.5 fold until 67 h of fermentation and later it decreased. It was found that antioxidant activity increased to 35% and eventually decreased based on the change in the polyphenol content.     

Environmental stress and elicitors enhance taxol production by endophytic strains of Paraconiothyrium variabile and Epicoccum nigrum

This study examined the effect of different elicitors (seven, different concentrations) and environmental factors (water activity (a_w), pH) on taxol production by strains of two endophytic fungi, Paraconiothyrium variabile and Epicoccum nigrum, isolated from temperate yew trees. A defined liquid broth medium was modified with elicitors, solute a_w depressors at different pH values. For P. variabile, the best elicitor was salicylic acid at 50 mg/l which gave a taxol yield of 14.7 ± 4.8 μg/l. The study of synergistic effects between elicitor, a_w and pH on taxol production showed that the highest yield of taxol (68.9 ± 11.9 μg/l) was produced under modified ionic stress of 0.98 a_w (KCl) at pH 5 when supplemented with 20 mg/l of salicylic acid. For E. nigrum, serine was the best elicitor which increased yield significantly (29.6 fold) when KCL was used as the a_w depressor (0.98 a_w) at pH 5.0 with 30 mg/l of serine. The maximum taxol yield produced by E. nigrum was 57.1 ± 11.8 μg/l. Surface response models were used to build contour maps to determine the conditions for maximum and marginal conditions for taxol yield in relation to the best elicitor and a_w, and the best pH for the first time. This will be beneficial for identifying key parameters for improvement of taxol yields by endophytic fungi.     

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.     

Effects of gas periodic stimulation on key enzyme activity in gas double-dynamic solid state fermentation (GDD-SSF)

The heat and mass transfer have been proved to be the important factors in air pressure pulsation for cellulase production. However, as process of enzyme secretion, the cellulase formation has not been studied in the view of microorganism metabolism and metabolic key enzyme activity under air pressure pulsation condition. Two fermentation methods in ATPase activity, cellulase productivity, weight lose rate and membrane permeability were systematically compared. Results indicated that gas double-dynamic solid state fermentation had no obviously effect on cell membrane permeability. However, the relation between ATPase activity and weight loss rate was linearly dependent with r = 0.9784. Meanwhile, the results also implied that gas periodic stimulation had apparently strengthened microbial metabolism through increasing ATPase activity during gas double-dynamic solid state fermentation, resulting in motivating the production of cellulase by Trichoderma reesei YG3. Therefore, the increase of ATPase activity would be another crucial factor to strengthen fermentation process for cellulase production under gas double-dynamic solid state fermentation.     

Nutrient control for stationary phase cellulase production in Trichoderma reesei Rut C-30

This work describes the use of nutrient limitations with Trichoderma reesei Rut C-30 to obtain a prolonged stationary phase cellulase production. This period of non-growth may allow for dependable cellulase production, extended fermentation periods, and the possibility to use pellet morphology for easy product separation. Phosphorus limitation was successful in halting growth and had a corresponding specific cellulase production of 5 ± 2 FPU/g-h. Combined with the addition of Triton X-100 for fungal pellet formation and low shear conditions, a stationary phase cellulase production period in excess of 300 h was achieved, with a constant enzyme production rate of 7 ± 1 FPU/g-h. While nitrogen limitation was also effective as a growth limiter, it, however, also prevented cellulase production.     

Kinetic modeling and implementation of superior process strategies for β-galactosidase production during submerged fermentation in a stirred tank bioreactor

This paper reports development and implementation of superior fermentation strategies for β-galactosidase production by Lactobacillus acidophilus in a stirred-tank bioreactor. Process parameters (aeration and agitation) were optimized for the process by application of Central Composite Design. Aeration rate of 0.5 vvm and agitation speed of 250 rpm were most suitable for β-galactosidase production (2001.2 U/L). Further improvement of the operation in pH controlled environment resulted in 2135 U/L of β-galactosidase with productivity of 142.39 U/L h. Kinetic modeling for biomass and enzyme production and substrate utilization were carried out at the aforementioned pH controlled conditions. The logistic regression model (X₀ = 0.01 g/L; X_max = 2.948 g/L; μ_max = 0.59/h; R² = 0.97) was used for mathematical interpretation of biomass production. Mercier's model proved to be better than Luedeking–Piret model in describing β-galactosidase production (P₀ = 0.7942 U/L; P_max = 2169.3 U/L; P_r = 0.696/h; R² = 0.99) whereas the latter was more efficient in mathematical illustration of lactose utilization (m = 0.187 g/g h; Y_x/s = 0.301 g/L; R² = 0.98) among the two used in this study. Strategies like fed-batch fermentation (3694.6 U/L) and semi-continuous fermentation (5551.9 U/L) further enhanced β-galactosidase production by 1.8 and 2.8 fold respectively.     

Effects of intermittent mechanical mixing on solid-state fermentation of wet corn distillers grain with Trichoderma reesei

The influence of mixing on microorganism integrity and product formation is a critical design parameter for solid-state fermentation bioreactors. The effects of intermittent mechanical mixing on the solid-state fermentation of wet corn distillers grain with Trichoderma reesei NRRL 11460 for the production of cellulase were investigated. Experiments were conducted using the unbuffered media at mixing frequencies of 0, 1, 2, 3, and 6 d⁻¹ at 27.5 °C with an initial moisture content of 50%. The results indicate that mixing caused about a tenfold increase in spore production compared to fermentations at static conditions. The cellulase enzyme activity produced was minimally affected by mixing with only a 5–10% decrease in filter paper activity for mechanically mixed fermentations compared to static fermentations. Mixing at lower frequencies of 1, 2, and 3 d⁻¹ caused an increase in CO₂ evolution compared to static conditions and higher mixing frequencies of 6 d⁻¹. A correlation between substrate weight loss and cumulative CO₂ evolution was established. The ability to intermittently mix a solid-state fermentation bioreactor with minimal detrimental effects increases the feasibility of onsite production of enzymes at biofuel facilities to lower the overall production costs of cellulosic biofuels.     

Correlation of pigment production with mycelium morphology in extractive fermentation of Monascus anka GIM 3.592

Extractive fermentation with nonionic surfactants is a potential method for producing Monascus pigments. In this study, the correlation between mycelium morphology and pigment production was investigated in extractive fermentation of Monascus anka GIM 3.592. The results demonstrated that pigment biosynthesis was associated with mycelial morphology and the accumulation of granular inclusions in cells. The physiological status in terms of hyphal and pellet diameters exhibited an excellent correlation with pigment accumulation, especially the yield of extracellular pigment in extractive fermentation (r > 0.85, p < 0.05). Nonionic surfactants could reduce pigment yield by influencing the morphology of hyphae and mycelium pellets. High yields of both intracellular and extracellular pigments could be achieved by controlling variations in hyphal diameters in two-stage extractive fermentation. Moreover, continuous extractive fermentation led to stable pigment production, with a relatively high productivity of total pigments reaching 72.3 AU/day. This study proposed a simple method for monitoring pigment biosynthesis in extractive fermentation using mycelium morphology as an indicating factor.     

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.     

2,3-Butanediol production using Klebsiella oxytoca ATCC 8724: Evaluation of biomass derived sugars and fed-batch fermentation process

For this study, 2,3-butanediol (BD) fermentation from pure and biomass-derived sugar were optimized in shake-flask and 5-L bioreactor levels using Klebsiella oxytoca ATCC 8724. The results showed that 70 g/L of single sugar (glucose or xylose) and 90 g/L of mixed-sugar (glucose:xylose = 2:1) were optimum concentrations for efficient 2,3-BD fermentation. At optimum sugar concentrations, 2,3-BD productivities were 1.03, 0.64 and 0.50 gL⁻¹ h⁻¹, and yields were 0.43, 0.36 and 0.35 g/g in glucose, xylose and mixed-sugar medium, respectively. The lack of simultaneous utilization of glucose and xylose led to the lowest productivity in the mixed-sugar medium. Detoxification of biomass hydrolyzates was necessary for efficient 2,3-BD fermentation when sugar concentrations in the medium was 90 g/L or higher, but not with sugar concentrations of 30 g/L or less. A fed-batch fermentation using glucose medium led to an increase 2,3-BD titer to 79.4 g/L and yields 0.47 g/g, while productivity decreased to 0.79 gL⁻¹ h⁻¹. However, the fed-batch process was inefficient using mixed-sugar and biomass hydrolyzates because of poor xylose utilization. These results indicated that appropriate biomass processing technologies must be developed to generate separate glucose and xylose streams to produce high 2,3-BD titer from biomass-derived sugar using a fed-batch process.     

Achieving high strength vinegar fermentation via regulating cellular growth status and aeration strategy

Implementing of high strength vinegar fermentation is still the mission of vinegar producers. The aim of this study was to carry out high acidity vinegar fermentation efficiently based on comprehensive analysis on bacterial fermentation kinetics characteristics of Acetobacter pasteurianus CICIM B7003-02. In practice, semi-continuous vinegar fermentation was optimized with an optimal discharge/charge ratio of 34% of working volume (v/v), which resulted in a proper growth status of Acetobacter and beneficial to acetification. Then, a two-stage aeration protocol was adopted in the vinegar fermentation in line with the Acetobacter theoretical oxygen demand, by which both vinegar stoichiometric yield and acetification rate were improved effectively. As the final result, a titer of 93.09 ± 0.24 g/L acetic acid was achieved, the average acetification rate was enhanced to a level of 1.83 ± 0.01 g/L/h, and the vinegar stoichiometric yield was promoted to 93.97 ± 0.16%. The strategy and practice worked out from this study provided a valuable reference for performing large scale vinegar fermentation with higher strength.     

Production of pediocin SM-1 by Pediococcus pentosaceus Mees 1934 in fed-batch fermentation: Effects of sucrose concentration in a complex medium and process modeling

Production of pediocin SM-1 by Pediococcus pentosaceus Mees 1934 was investigated in semi-aerobic, pH-controlled, batch and fed-batch fermentations using a complex medium containing sucrose as the main source of carbon. The effects of sucrose concentration were studied in fed-batch fermentations in which a sucrose solution was added at stable feeding rates (5, 7, 9 and 10 g/l/h). The results showed that pediocin is produced as a product of the primary metabolism and its titer could be greatly improved by adjusting the sucrose feeding rate in fed-batch fermentation. The maximum titer of pediocin of 145 AU/ml was obtained in the fed-batch culture with 7 g/l/h feeding rate and that was 119% higher compared to the titer obtained in batch culture. Higher feeding rates (9 and 10 g/l/h) resulted in decreased pediocin yields while biomass levels appeared to be rather unaffected. The specific rate of pediocin formation was also sensitive to sucrose concentration levels. A mathematical model developed on the basis of well-known rate equations for batch and fed-batch cultures and growth associated production, described successfully cell growth, sucrose assimilation, lactate production and pediocin production in fed-batch culture.     

Continuous neomycin production by immobilized cells of Streptomyces marinensis NUV-5 in an airlift bioreactor

Neomycin production by free and calcium alginate immobilized cells was investigated in an airlift reactor. The average volumetric productivity with continuous fermentation (72.97 mg/l/h) was greater than with free cells (45.05 mg/l/h). The total neomycin produced with continuous fermentation was 62% greater than with that of free cells. Immobilized Streptomyces particles showed a half-life of 42 days during continuous fermentation under airlift conditions.     

The effect of gas double-dynamic on mass distribution in solid-state fermentation

The mass distribution regularity in substrate of solid-state fermentation (SSF) has rarely been reported due to the heterogeneity of solid medium and the lack of suitable instrument and method, which limited the comprehensive analysis and enhancement of the SSF performance. In this work, the distributions of water, biomass, and fermentation product in different medium depths of SSF were determined using near-infrared spectroscopy (NIRS) and the developed models. Based on the mass distribution regularity, the effects of gas double-dynamic on heat transfer, microbial growth and metabolism, and product distribution gradient were systematically investigated. Results indicated that the maximum temperature of substrate and the maximum carbon dioxide evolution rate (CER) were 39.5 °C and 2.48 mg/(h g) under static aeration solid-state fermentation (SASSF) and 33.9 °C and 5.38 mg/(h g) under gas double-dynamic solid-state fermentation (GDSSF), respectively, with the environmental temperature for fermentation of 30 ± 1 °C. The fermentation production (cellulase activity) ratios of the upper, middle, and lower levels were 1:0.90:0.78 at seventh day under SASSF and 1:0.95:0.89 at fifth day under GDSSF. Therefore, combined with NIRS analysis, gas double-dynamic could effectively strengthen the solid-state fermentation performance due to the enhancement of heat transfer, the stimulation of microbial metabolism and the increase of the homogeneity of fermentation products.     

High titer production of tetracenomycins by heterologous expression of the pathway in a Streptomyces cinnamonensis industrial monensin producer strain

Streptomyces cinnamonensis C730.1 and C730.7, are industrially mutagenized strains that produce moderate and high levels of the polyketide polyether antibiotic monensin A, respectively, in an oil-based fermentation medium. The possibility that these strains could be used for high titer production of a heterologous polyketide product was investigated by expression of the entire tetracenomycin (TCM) biosynthetic pathway using an integrative plasmid, pSET154. Expression in C730.1 led to stable production of ~0.44 g/l TCM C (the final biosynthetic product) and ~2.69 g/l TCM A2 (the penultimate biosynthetic product), and resulted in a 40% decrease in monensin production. Expression in the C730.7 led to higher levels of TCMs, ~0.6 g/l TCM C and ~4.35 g/l TCM A2, without any detectable decrease in the higher titer monensin production. Abrogation of monensin production in this strain through deletion of the corresponding biosynthetic genes did not lead to higher levels of TCM products. In the case of the C730.7 host, 85% of the TCM C and virtually all of the TCM A2 were intracellular, suggesting feedback inhibition leads to the accumulation of the final pathway intermediate. These observations contrast those made for the native producer Streptomyces glaucescens where the predominant product is TCM C and TCM titers are significantly lower levels (~0.3 g/l), and demonstrate the potential utility of S. cinnamonensis strains as heterologous hosts for high level expression of a variety of polyketide synthase derived products.