Effects of ascorbic acid and uracil on exo-polysaccharide production with Hericium erinaceus in liquid culture

Hericium erinaceus is a well known edible and medicinal mushroom used in East-Asia. Recently, H. erinaceus has attracted a lot of attention owing to its antitumor, immuno-modulatory, and cytotoxic effect. It has been postulated that the fruiting body of H. erinaceus contains a polysaccharide that is similar to β-D-glucan, which is known to have antitumor activity against Sarcoma 180. However, optimized liquid culture conditions for enhanced polysaccharide productivity have yet to be developed, which is a necessary step for industrial applications. Therefore, the aim of this study was to determine the optimal liquid culture conditions for maximum polysaccharide production. In shake flask cultures, the optimal concentration of ascorbic acid was found to be 2.0 g/L, which prevented the broth from changing color from yellow to black. The optimal culture conditions were determined to be 23°C, 200 rpm, and a 10% inoculum size, at an uncontrolled initial pH. In addition, the modified medium contained 20 g/L glucose, 10 g/L yeast extract, and 2.0 g/L ascorbic acid. The maximum mycelial biomass and exo-polysaccharide (EPS) production in the modified medium containing uracil was 13.43 and 1.26 g/L, respectively.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Comparison of culture methods on exopolysaccharide production in the submerged culture of Cordyceps militaris and process optimization

Aims: To improve exopolysaccharides (EPS) production of Cordyceps militaris (C. militaris), effects of different culture method on mycelial biomass and EPS production in the submerged culture of C. militaris were investigated. Methods and Results: A new two‐stage fermentation process for EPS production of C. militaris was designed in this work. Central composite design (CCD) was utilized to optimize the two‐stage fermentation process. The results showed that the two‐stage fermentation process for EPS production was superior to other culture method (conventional static culture and shake culture). CCD revealed that the optimum values of the test variables for EPS production were shaken for 140 h followed by 130‐h static culture. The maximum EPS production reached 3·2 g l^?1 under optimized two‐stage culture and was about 2·3‐fold and 1·6‐fold in comparison with those of original static culture and shake culture. Conclusions: It was indicated that a new two‐stage culture method obtained in this work possessed a high potential for the industrial production for EPS of C. militaris. Significance and Impact of the Study: The fundamental information obtained in this work is complementary to those of previous investigations on the submerged culture of C. militaris for the production of bioactive metabolites.     

Optimisation of submerged culture conditions for the production of mycelial biomass and exopolysaccharide byPleurotus nebrodensis

The optimisation of submerged culture conditions and nutritional requirements was studied for the production of exopolysaccharide (EPS) fromPleurotus nebrodensis. The optimal temperature and initial pH for both mycelial growth and EPS production in shake flask cultures were 25 °C and 8.0, respectively. Maltose was found the most suitable carbon source for both mycelial biomass and EPS production. Yeast extract was favourable nitrogen source for both mycelial biomass and EPS production. Optimum concentration of each medium component was determined using the orthogonal matrix method. The optimal combination of the media constituents for mycelial growth and EPS production was as follows: 200 g l^?1 bran, 25 g l^?1 maltose, 3 g l^?1 yeast extract, 1 g l^?1 KH₂PO₄, 1 g l^?1 MgSO₄ 7H₂O. Under the optimal conditions, the mycelial biomass (4.13 g l^?1) and EPS content (2.40 g l^?1) ofPleurotus nebrodensis was 2.3 and 3.6 times compared to the control with basal medium respectively.     

Optimization of submerged culture conditions for the mycelial growth and exo-biopolymer production by Cordyceps militaris

AIMS: The objective of the present study was to determine the optimal culture conditions for exo-biopolymer production by Cordyceps militaris in shake flask culture. METHODS AND RESULTS: The optimal temperature and initial pH for both mycelial growth and exo-biopolymer production by Cordyceps militaris in shake flask culture were found to be 20 degrees C and 6.0, respectively. Sucrose (40 g x l(-1)) and corn steep powder (10 g x l(-1)) were the most suitable carbon and nitrogen source for both mycelial growth and exo-biopolymer production. CONCLUSION: Under optimal culture conditions, the maximum exo-biopolymer concentration in a 5-l jar fermenter indicated 10.3 g x l(-1), which was approximately three times higher than that in shake flask culture. SIGNIFICANCE AND IMPACT OF THE STUDY: This process can have a significant impact on the industrial scale when sucrose and corn steep powder were used as carbon and nitrogen source.     

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.     

Effects of C/N ratio and trace elements on mycelial growth and exo-polysaccharide production of <Emphasis Type="Italic">Tricholoma matsutake</Emphasis>

Although its demand increased greatly due to the volatile strong flavor and bioactive molecules, little information has been about the cultural characteristics of Tricholoma matsutake. In this study, we investigated the optimal medium composition of liquid culture with the goal of shortening the culture period, and to maximize polysaccharide production and mycelial growth. From these experiments we found that the optimal medium contained 40 g/L, glucose; 30 g/L, yeast extract; 1.5 g/L, KH₂PO₄; and 1 g/L MgSO₄·7H₂O. In flask culture, the maximum mycelial growth and polysaccharide production were 22.45 and 5.3 g/L, which were about 9 and 3 g/L higher than that at the basal medium, respectively.     

蝉拟青霉液体发酵条件优化

采用液体发酵蝉拟青霉,对蝉拟青霉的发酵条件进行优化,以提高蝉拟青霉胞外多糖产量及生物量。摇瓶发酵条件下,在单因素基础上设计正交实验确定各因素的最佳组合。优化后得最佳发酵培养基:蔗糖8%,牛肉膏0.75%,酵母膏0.125%,MgSO_4·7H_2O 0.3%,KH_2PO_4 0.2%,麸皮0.5%。该条件下胞外多糖产量为5.96 g/L,生物量为42 g/L,较优化前提高了1倍。采用发酵罐进行扩大培养,对分批发酵时的初糖浓度进行了优化,并分析了补料分批发酵对发酵过程的影响。发酵罐培养时最适初糖浓度为5%,此时生物量最高为38 g/L,多糖含量最高为5.5 g/L;采用补料分批发酵时,多糖产量最高为5.89 g/L,生物量最高为40 g/L,效果优于分批发酵。     

Statistical optimization of simple culture conditions to produce biomass of an ochratoxigenic mould biocontrol yeast strain

Aim: To maximize biomass production of an ochratoxigenic mould–controlling strain of Lachancea thermotolerans employing response surface methodology (RSM). Methods and Results: Using Plackett–Burman screening designs (PBSD) and central composite designs (CCD), an optimized culture medium containing (g l^?1): fermentable sugars (FS), 139·2, provided by sugar cane molasses (CMz), (NH₄)₂HPO₄ (DAP), 9·0, and yeast extract (YE), 2·5, was formulated. Maximal cell concentration obtained after 24 h at 28°C was 24·2 g l^?1cell dry weight (CDW). The mathematical model obtained was validated in experiments performed in shaken‐flask cultures and also in aerated bioreactors. Maximum yield and productivity values achieved were, respectively, of 0·23 g CDW/g FS in a medium containing (g l^?1): FS, 87·0; DAP, 7·0; YE, 1·0; and of 0·96 g CDW l^?1 h^?1 in a medium containing (g l^?1): FS, 150·8 plus DAP, 6·9. Conclusions: Optimized culture conditions for maximizing yeast biomass production determined in flask cultures were applicable at a larger scale. The highest yield values were attained in media containing relatively low‐CMz concentrations supplemented with DAP and YE. Yeast extract would not be necessary if higher productivity is the aim. Significance and Impact of the Study: Cells of L. thermotolerans produced aerobically could be sustainably produced in a medium just containing cheap carbon, nitrogen and phosphorus sources. Response surface methodology allowed the fine‐tuning of cultural conditions.     

Stimulation of indirubin production by KNO3 depletion in indole-supplemented suspension culture of Polygonum tinctorium

Summary Indole when added at 20 mM to shake flask cultures of Polygonum tinctorium cells on 16th day increased indirubin production from 41 mg/l to 126 mg/l. Use of KNO₃ depleted media stimulated indirubin formation up to 88% and 26% in shake flasks and air-lift bioreactors, respectively.     

Detection of ginkgolide A in Ginkgo biloba cell cultures

Ginkgo biloba cells were cultured in two 500 mL shake flasks and in 2 L and 6 L immobilization bioreactors using MS medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30 g.L^–1 sucrose. Specific growth rates were 0.06 d^–1, 0.11 d^–1 and 0.07 d^–1 for the 2 L and 6 L bioreactors and shake flask cultures, respectively. Extracellular phosphate, nitrate, ammonium and carbohydrate uptake rates of the bio reactor cultures were approximately 17 to 39% slower than those of shake flask cultures. The specific oxygen uptake and carbon dioxide transfer rates of immobilized Ginkgo biloba cells ranged from 0.027 to 0.041 mmol O₂.g^–1.d.w.hr^–1 (maximum uptake at 14 days) and 0.020 to 0.057 mmol CO₂g. ^–1.d.w.hr^–1 (maximum production at 14 days). Extracts from the biomass of the two immobilized and shake flask suspension cultures were analysed for ginkgolide A by GC-MS. Yields of 7, 17, 19 and 7 ng.g. ^–1d.w. of ginkgolide A were determined for shake flask 1, shake flask 2 and the 2 L and 6 L immobilized cultures, respectively. Traces of ginkgolide B were detected with the signal to noise ratio, however, being too low for positive confirmation of this last product.Abbreviations CTR Carbon dioxide transfer rate - DO Dissolved oxygen - g.d.w. Gram dry weight - GA Ginkgolide A - GB Ginkgolide B - GC Gas chromatography - GC-MS Gas chromatography-mass spectrometry - HPLC High performance liquid chromatography - K Kinetin - MS Murashige and Skoog salt medium - N₁K₁MS Complete Murashige and Skoog medium supplemented with 1 mg.L^–1 NAA, 0.1 mg.L^–1 K and 30g.L^–1 sucrose - NAA Naphthaleneacetic acid - OTR Oxygen transfer rate - PAF Platelet Aggregating Factor - q_CO2 Specific carbon dioxide production rate - q_O2 Specific oxygen uptake rate - u Specific growth rate     

Microwell engineering characterization for mammalian cell culture process development

Experimentation in shaken microplate formats offers a potential platform technology for the rapid evaluation and optimization of cell culture conditions. Provided that cell growth and antibody production kinetics are comparable to those found in currently used shake flask systems then the microwell approach offers the possibility to obtain early process design data more cost effectively and with reduced material requirements. This work describes a detailed engineering characterization of liquid mixing and gas–liquid mass transfer in microwell systems and their impact on suspension cell cultures. For growth of murine hybridoma cells producing IgG1, 24‐well plates have been characterized in terms of energy dissipation (P/V) (via Computational Fluid Dynamics, CFD), fluid flow, mixing and oxygen transfer rate as a function of shaking frequency and liquid fill volume. Predicted k_La values varied between 1.3 and 29 h^?1; liquid‐phase mixing time, quantified using iodine decolorization experiments, varied from 1.7 s to 3.5 h; while the predicted P/V ranged from 5 to 35 W m^?3. CFD simulations of the shear rate predicted hydrodynamic forces will not be detrimental to cells. For hybridoma cultures however, high shaking speeds (>250 rpm) were shown to have a negative impact on cell growth, while a combination of low shaking speed and high well fill volume (120 rpm, 2,000 µL) resulted in oxygen limited conditions. Based on these findings a first engineering comparison of cell culture kinetics in microwell and shake flask formats was made at matched average energy dissipation rates. Cell growth kinetics and antibody titer were found to be similar in 24‐well microtiter plates and 250 mL shake flasks. Overall this work has demonstrated that cell culture performed in shaken microwell plates can provide data that is both reproducible and comparable to currently used shake flask systems while offering at least a 30‐fold decrease in scale of operation and material requirements. Linked with automation this provides a route towards the high throughput evaluation of robust cell lines under realistic suspension culture conditions. Biotechnol. Bioeng. 2010; 105: 260–275. © 2009 Wiley Periodicals, Inc.     

From field sampling to pneumatic bioreactor mycelia production of the ectomycorrhizal mushroom Laccaria trichodermophora

In order to increase survival rates of greenhouse seedlings destined for restoration and conservation programs, successful mycorrhization of the seedlings is necessary. To reforest forest ecosystems, host trees must be inoculated with ectomycorrhizal fungi and, in order to guarantee a sufficient supply of ectomycorrhizal inoculum, it is necessary to develop technologies for the mass production of ectomycorrhizal fungi mycelia. We selected the ectomycorrhizal fungus Laccaria trichodermophora, due to its ecological traits and feasible mycelia production in asymbiotic conditions. Here, we report the field sampling of genetic resources, as well as the highly productive nutritional media and cultivation parameters in solid cultures. Furthermore, in order to achieve high mycelial production, we used strain screening and evaluated pH, carbon source concentration, and culture conditions of submerged cultures in normal and baffled shake flasks. The higher productivity culture conditions in shake flasks were selected for evaluation in a pneumatic bioreactor, using modified BAF media with a 10 g/L glucose, pH 5.5, 25 °C, and a volumetric oxygen transfer coefficient (K_La) of 36 h⁻¹. Under those conditions less biomass (12–37 %) was produced in the pneumatic bioreactor compared with the baffled shake flasks. This approach shows that L. trichodermophora can generate a large biomass concentration and constitute the biotechnological foundation of its mycelia mass production.     

Production of capsular polysaccharide from Escherichia coli K4 for biotechnological applications

The production of industrially relevant microbial polysaccharides has recently gained much interest. The capsular polysaccharide of Escherichia coli K4 is almost identical to chondroitin, a commercially valuable biopolymer that is so far obtained from animal tissues entailing complex and expensive extraction procedures. In the present study, the production of capsular polysaccharide by E. coli K4 was investigated taking into consideration a potential industrial application. Strain physiology was first characterized in shake flask experiments to determine the optimal culture conditions for the growth of the microorganism and correlate it to polysaccharide production. Results show that the concentration of carbon source greatly affects polysaccharide production, while the complex nitrogen source is mainly responsible for the build up of biomass. Small-scale batch processes were performed to further evaluate the effect of the initial carbon source concentration and of growth temperatures on polysaccharide production, finally leading to the establishment of the medium to use in following fermentation experiments on a bigger scale. The fed-batch strategy next developed on a 2-L reactor resulted in a maximum cell density of 56 g_cww/L and a titre of capsular polysaccharide equal to 1.4 g/L, approximately ten- and fivefold higher than results obtained in shake flask and 2-L batch experiments, respectively. The release kinetics of K4 polysaccharide into the medium were also explored to gain insight into the mechanisms underlying a complex aspect of the strain physiology.     

Dissolved oxygen levels affect dimorphic growth by the entomopathogenic fungus Isaria fumosorosea

The entomopathogenic fungus Isaria fumosorosea is capable of dimorphic growth (hyphal or yeast-like) in submerged culture. Using 250-mL baffled flasks, culture volumes of 50, 100, 150, and 200 mL were grown in a shaker incubator at 350 rpm and 28°C. Dissolved oxygen (DO) was continuously monitored using a non-invasive oxygen monitoring system. Culture volumes of 50 mL maintained DO concentrations above 10% throughout the 3-day growth period and accumulated biomass and produced blastospores more rapidly (1.2×10⁹ blastospores mL^?1 in 2 days) than the other culture volumes tested. Dissolved oxygen was depleted in culture volumes of 100, 150, and 200 mL after 20.5, 16.8, and 13.5 h, respectively. The DO in 150 and 200 mL cultures remained exhausted (<3%) throughout the growth period resulting in significantly lower blastospore yields and increased hyphal growth. These results were used to establish oxygen levels (>20% DO) for I. fumosorosea growth in 100-L bioreactors resulting in blastospore production (1.1×10⁹ blastospores mL^?1 in 2 days) comparable to highly aerated, low volume shake flask cultures. In addition, maintaining higher DO levels resulted in increased blastospore production by cultures of I. fumosorosea grown on low-cost nitrogen sources (cottonseed meal and soy flour) that previously elicited excessive hyphal growth. These studies showed that oxygen availability is essential for significant yeast-like growth by I. fumosorosea cultures and that continuous monitoring of oxygen concentrations in shake flask cultures can be used to establish aeration conditions for bioreactors.     

The improvement of cephalosporin C production by fed-batch culture ofCephalosporium acremonium M25 using rice oil

The objective of this study is to improve cephalosporin C (CPC) production by optimization of medium and culture conditions. A statistical method was introduced to optimize the main culture medium. The main medium for CPC production was optimized using a statistical method. Glucose and corn steep liquor (CSL) were found to be the most effective factors for CPC production. Glucose and CSL were optimized to 2.84 and 6.68%, respectively. CPC production was improved 50% by feeding of 5% rice oil at day 3rd and 5th day during the shake flask culture ofC. acremonium M25. The effect of agitation speeds on CPC production in a 2.5-L bioreactor was also investigated with fed-batch mode. The maximum cell mass (54.5 g/L) was obtained at 600 rpm. However, the maximum CPC production (0.98 g/L) was obtained at 500 rpm. At this condition, the maximum CPC production was improved about 132% compared to the result with batch flask culture.     

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.     

Optimization of submerged culture condition for the production of mycelial biomass and exopolysaccharides by Agrocybe cylindracea

The optimization of submerged culture conditions and nutritional requirements was studied for the production of exopolysaccharide (EPS) from Agrocybe cylindracea ASI-9002 using the statistically based experimental design in a shake flask culture. Both maximum mycelial biomass and EPS were observed at 25 degrees C. The optimal initial pH for the production of mycelial biomass and EPS were found to be pH 4.0 and pH 6.0, respectively. Subsequently, optimum concentration of each medium component was determined using the orthogonal matrix method. The optimal combination of the media constituents for mycelial growth was as follows: maltose 80 g/l, Martone A-1 6 g/l, MgSO4 x 7H2O 1.4 g/l, and CaCl2 1.1 g/l; for EPS production: maltose 60 g/l, Martone A-1 6 g/l, MgSO4 x 7H2O 0.9 g/l, and CaCl2 1.1 g/l. Under the optimal culture condition, the maximum EPS concentration achieved in a 5-l stirred-tank bioreactor indicated 3.0 g/l, which is about three times higher than that at the basal medium.     

Characteristics of transformedPanax ginseng C.A. Meyer hairy roots: Growth and nutrient profile

Ginseng (Panax ginseng C.A. Meyer) hairy root cultures, which are established via the infection of ginseng root discs withRhizobium rhizogenes, have been used to construct profiles of both biomass growth and nutrient consumption in flask cultures. In a 250 mL shake flask culture, the maximum biomass was observed on the 59th day of the culture period, at 216.8 g (fresh wt) per liter or 11.4 g (dry wt) per liter. The hairy roots were determined to have a growth rate of 0.355 g-DW/g cells/day during the exponential growth phase and a maximum specific growth rate on day 7. Total ginseng saponin and phenolic compound contents were noted to have increased within the latter portion of the culture period. Linear correlations between increases in biomass weight and nutrient uptake were used to imply the conductivity yield 2.60 g-DW/(L·mS) and carbon yield 0.45 g-DW/(g sugar) in the 250 mL flask cultures. The biomass yield when two different nitrogen sources were used (ammonia and nitrate) was shown to remain approximately constant, at 0.47 g-DW/(l·mM NH₄) and 0.33 g-DW/(L·mM NO₃); it remained at these levels for 16 days with the ammonia, and for 24 days with the nitrate. The biomass yield when a phosphate source was used was also shown to remain approximately constant for 9 days, at 3.17 g-DW/(L·mM PO₄), with an R² of 0.99.     

Production of red pigments byMonascus purpureus in submerged culture

For the purpose of mass producingMonascus red pigments optimum medium composition and environmental conditions were investigated in submerged flask cultures. The optimum carbon and nitrogen sources were determined to be 30 g/L of glucose and 1.5 g/L of monosodium glutamate (MSG). Of the three metals examined, Fe²⁺ showed the stronges stimulatory effect on pigment production and some stimulatory effect was also found in Mn²⁺. Optimum pH and agitation speed were determined to be 6.5 and 700 rpm, respectively. Under the optimum culture conditions batch fermentation showed that the maximum biomass yield and specific productivity of red pigments were 0.20 g DCW/g glucose and, 32.5 OD₅₀₀ g DCW⁻¹ h⁻¹, respectively.