Process optimization for the production of diosgenin with Trichoderma reesei

Based on the response surface methodology, an effective microbial system for diosgenin production from enzymatic pretreated Dioscorea zingiberensis tubers with Trichoderma reesei was studied. The fermentation medium was optimized with central composite design (3⁵) depended on Plackett–Burmann design which identified significant impacts of peptone, K₂HPO₄ and Tween 80 on diosgenin yield. The effects of different fermentation conditions on diosgenin production were also studied. Four parameters, i.e. incubation period, temperature, initial pH and substrate concentration were optimized using 4⁵ central composite design. The highest diosgenin yield of 90.57% was achieved with 2.67% (w/v) of peptone, 0.29% (w/v) of K₂HPO₄, 0.73% (w/v) of Tween 80 and 9.77% (w/v) of substrate, under the condition of pH 5.8, temperature 30 °C. The idealized incubation time was 6.5 days. After optimization, the product yield increased by 33.70% as compared to 67.74 ± 1.54% of diosgenin yield in not optimized condition. Scale-up fermentation was carried out in a 5.0 l bioreactor, maximum diosgenin yield of 90.17 ± 3.12% was obtained at an aeration of 0.80 vvm and an agitation rate of 300 rpm. The proposed microbial system is clean and effective for diosgenin production and thus more environmentally acceptable than the traditional acid hydrolysis.     

Pilot production of Clonostachys rosea conidia in a solid‐state fermentor optimized using response surface methodology

The nonpathogenic, saprophytic fungus Clonostachys rosea is one of the most powerful fungal biological control agents (BCAs). However, the production of fungal BCAs is still a major constraint for their large‐scale use and commercialization. Here, we developed a novel solid‐fermentation reactor that is light transparent and ventilated both at the top and the bottom, and optimized C. rosea cultivation conditions in solid‐state fermentation using response surface methodology. The growth area of spores provided by the novel fermentor was two times that of the traditional one. A quadratic polynomial model was developed, which indicated the effects of variables on the conidia yield. The greatest spore production of 3.50 × 10¹⁰ spores/g‐dry‐matter was obtained after 11 days at the initial moisture content of 69.2% w/w, the medium thickness of 3.84 cm, and the porosity of 0.37%. The optimized spore yield was increased by one order of magnitude. The fermentation time was shortened from 15 to 11 days. With the novel solid‐fermentation reactor, increase in C. rosea spores production and decrease in fermentation time were achieved. Current data imply that both the novel solid‐fermentation reactor designed and the optimized fermentation conditions are suitable for industrial‐scale C. rosea spore production.     

Optimization of an ethanol production medium in very high gravity fermentation

Concentrations of Mg²⁺, glycine, yeast extract, biotin, acetaldehyde and peptone were optimized by a uniform design process for ethanol production by Saccharomyces cerevisiae. Using non-linear step-wise regression analysis, a predictive mathematical model was established. Concentrations of Mg²⁺ and peptone were identified as the critical factors: 50 mM Mg²⁺ and 1.5% (w/v) peptone in the medium increased the final ethanol titre from 14.2% (v/v) to 17% (v/v) in 48 h.     

Improving probiotic spore yield using rice straw hydrolysate

Spore-forming Bacillus sp. has been extensively studied for their probiotic properties. In this study, an acid-treated rice straw hydrolysate was used as carbon source to produce the spores of Bacillus coagulans. The results showed that this hydrolysate significantly improved the spore yield compared with other carbon sources such as glucose. Three significant medium components including rice straw hydrolysate, MnSO₄ and yeast extract were screened by Plackett–Burman design. These significant variables were further optimized by response surface methodology (RSM). The optimal values of the medium components were rice straw hydolysate of 27% (v/v), MnSO₄ of 0·78 g l⁻¹ and yeast extract of 1·2 g l⁻¹. The optimized medium and RSM model for spore production were validated in a 5 l bioreactor. Overall, this sporulation medium containing acid-treated rice straw hydrolysate has a potential to be used in the production of B. coagulans spores.     

Media optimization for biosurfactant production by <Emphasis Type="Italic">Rhodococcus erythropolis</Emphasis> MTCC 2794: artificial intelligence versus a statistical approach

This paper entails a comprehensive study on production of a biosurfactant from Rhodococcus erythropolis MTCC 2794. Two optimization techniques—(1) artificial neural network (ANN) coupled with genetic algorithm (GA) and (2) response surface methodology (RSM)—were used for media optimization in order to enhance the biosurfactant yield by Rhodococcus erythropolis MTCC 2794. ANN and RSM models were developed, incorporating the quantity of four medium components (sucrose, yeast extract, meat peptone, and toluene) as independent input variables and biosurfactant yield [calculated in terms of percent emulsification index (% EI₂₄)] as output variable. ANN-GA and RSM were compared for their predictive and generalization ability using a separate data set of 16 experiments, for which the average quadratic errors were ~3 and ~6%, respectively. ANN-GA was found to be more accurate and consistent in predicting optimized conditions and maximum yield than RSM. For the ANN-GA model, the values of correlation coefficient and average quadratic error were ~0.99 and ~3%, respectively. It was also shown that ANN-based models could be used accurately for sensitivity analysis. ANN-GA-optimized media gave about a 3.5-fold enhancement in biosurfactant yield.     

<Emphasis Type="Italic">Bacillus amyloliquefaciens</Emphasis> Spore Production Under Solid-State Fermentation of Lignocellulosic Residues

This study was conducted to elucidate cultivation conditions determining Bacillus amyloliquefaciens B-1895 growth and enhanced spore formation during the solid-state fermentation (SSF) of agro-industrial lignocellulosic biomasses. Among the tested growth substrates, corncobs provided the highest yield of spores (47?×?10¹⁰ spores g^?1 biomass) while the mushroom spent substrate and sunflower oil mill appeared to be poor growth substrates for spore formation. Maximum spore yield (82?×?10¹⁰ spores g^?1 biomass) was achieved when 15 g corncobs were moistened with 60 ml of the optimized nutrient medium containing 10 g peptone, 2 g KH₂PO₄, 1 g MgSO₄·7H₂O, and 1 g NaCl per 1 l of distilled water. The cheese whey usage for wetting of lignocellulosic substrate instead water promoted spore formation and increased the spore number to 105?×?10¹⁰ spores g^?1. Addition to the cheese whey of optimized medium components favored sporulation process. The feasibility of developed medium and strategy was shown in scaled up SSF of corncobs in polypropylene bags since yield of 10?×?10¹¹ spores per gram of dry biomass was achieved. In the SSF of lignocellulose, B. amyloliquefaciens B-1895 secreted comparatively high cellulase and xylanase activities to ensure good growth of the bacterial culture.     

β-galactosidase-catalyzed synthesis of 3-O-β-D-galactopyranosyl-sn-glycerol: Optimization by response surface methodology

In this study, the synthesis of 3-O-β-D-galactopyranosyl-sn-glycerol (GG) was performed by the reverse hydrolysis of D-galactose and glycerol using β-galactosidase from Kluyveromyces lactis. Four process variables, reaction temperature (30.0–45.0?°C), reaction time (24–48?h), enzyme concentration (150.00–350.00?U/mL), and substrate molar ratio (glycerol:D-galactose, 7.5:12.5?mmol/mmol) were investigated and optimized via response surface methodology (RSM) for optimal GG synthesis. Both quadratic equations and the optimal reaction conditions were established. Results showed that the four variables, i.e., reaction temperature, reaction time, enzyme concentration, and substrate molar ratio had significant (p?β-galactosidase concentration and 8.65:1.00 of substrate molar concentration ratio (glycerol: D-galactose) at 39.8?°C and 48?h of reaction. Under these conditions, the GG concentration was 140.03?g/L and GG yield was 55.71%, which both were close to the predicted values (143.26?g/L and 56.73%). This finding proves the RSM to be a useful tool in optimizing process conditions for GG synthesis.     

Anaerobic glycerol production by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strains under hyperosmotic stress

Glycerol formation is vital for reoxidation of nicotinamide adenine dinucleotide (reduced form; NADH) under anaerobic conditions and for the hyperosmotic stress response in the yeast Saccharomyces cerevisiae. However, relatively few studies have been made on hyperosmotic stress under anaerobic conditions. To study the combined effect of salt stress and anaerobic conditions, industrial and laboratory strains of S. cerevisiae were grown anaerobically on glucose in batch-cultures containing 40 g/l NaCl. The time needed for complete glucose conversion increased considerably, and the specific growth rates decreased by 80–90% when the cells were subjected to the hyperosmotic conditions. This was accompanied by an increased yield of glycerol and other by-products and reduced biomass yield in all strains. The slowest fermenting strain doubled its glycerol yield (from 0.072 to 0.148 g/g glucose) and a nearly fivefold increase in acetate formation was seen. In more tolerant strains, a lower increase was seen in the glycerol and in the acetate, succinate and pyruvate yields. Additionally, the NADH-producing pathway from acetaldehyde to acetate was analysed by overexpressing the stress-induced gene ALD3. However, this had no or very marginal effect on the acetate and glycerol yields. In the control experiments, the production of NADH from known sources well matched the glycerol formation. This was not the case for the salt stress experiments in which the production of NADH from known sources was insufficient to explain the formed glycerol.     

红色诺卡菌固体培养基配方的优化

应用响应面优化设计法优化固体培养基配方,增大红色诺卡菌的固体培养细胞生物量。首先用Plackett-Burman法从现有培养基组分中找到影响红色诺卡菌细胞生物量的关键因素,再通过最陡爬坡法确定细胞生物量最大的配方,用作中心组合设计(Central Composite Design, CCD)实验的基础起始值,拟合数学模型方程,最后找到最优组分的组合。优化的配方转移至企业实施放大实验,对结果进行验证和比较。试验结果表明,培养基各组分中影响红色诺卡菌细胞生物量的关键因素为蛋白胨、NaCl、牛肉膏;最优固体培养基配方:蛋白胨42 g/L、牛肉膏8 g/L、NaCl 1.2 g/L、甘油10 mL/L、Na_2HPO_4·12H_2O 0.3 g/L、琼脂20 g/L。在细胞生物量方面最优固体培养基配方比原配方高104%。响应面优化设计可用于提高红色诺卡菌细胞生物量固体培养基的优化,也为红色诺卡菌培养条件、液体发酵的优化研究提供参考。     

Deletion of the <Emphasis Type="Italic">CgTPI</Emphasis> Gene Encoding Triose Phosphate Isomerase of <Emphasis Type="Italic">Candida glycerinogenes</Emphasis> Inhibits the Biosynthesis of Glycerol

The yeast Candida glycerinogenes produces a high yield of glycerol only in response to a medium-osmotic stress, but little is known about the relationship between osmoadaptation and glycerol metabolism. The CgTPI gene encoding triose phosphate isomerase of C. glycerinogenes was cloned and sequenced, and its functionality was confirmed by complementation of Saccharomyces cerevisiae tpi1 Δ. The roles of CgTpip in the glycerol biosynthesis and the osmoadaptation were investigated. Unlike S. cerevisiae tpi1 Δ and Klyuveromyces lactis tpi1 Δ, the mutant lacking CgTPI significantly decreased the rate of glucose consumption and the glycerol yield. Furthermore, the mutants decreased osmotolerance to glucose and NaCl. The results suggest that CgTPI might be crucial for a high yield of glycerol by C. glycerinogenes. The inhibition of glycerol biosynthesis might be related to the reduced ability of osmoadaptation to high external osmolarity. To our knowledge, this is the first report that inactivation of a yeast TPI gene inhibits the biosynthesis of glycerol.     

Water availability affects the growth,accumulation of compatible solutes and the viability of the biocontrol agent Epicoccum nigrum

Growth of the biocontrol fungus Epicoccum nigrum was more sensitive to ionic solute water stress (NaCl) than non-ionic (glycerol) on potato dextrose-based media at –0.5, –3.0 and –5.5 MPa water potentials. Subsequent physiological manipulation of growth of E. nigrum in glycerol-modified media to –3.0 MPa water potential resulted in a significant increase in the accumulation of compatible solutes in both mycelial liquid cultures and spores, but no enhanced accumulation of the desiccation protectant trehalose, when compared to unmodified media (–0.5MPa). The main solute accumulated was glycerol, followed by arabitol. In temporal studies over 20 days maximum accumulation of glycerol occurred in 5-d old cultures with water stressed cultures having 250× greater amounts than those from unmodified medium. The arabitol content was also higher in mycelium and spores produced under water stress. The difference was maximum after 15 days growth. Glucose content decreased over time in mycelial colonies but increased in spores. The germination of conidia from the two treatments was similar, regardless of compatible solute content, even at –9.25 MPa water potential stress. However, germ tube extension was significantly increased at this water potential level. The production of E. nigrum spores at –3.0 MPa water potential resulted in improved survival when stored fresh at 4 and 25 °C. However, freeze-drying severely affected the viability of spores produced on both media (–0.5 or 3.0 MPa). Accumulation of compatible solutes may assist the fungus in better ecological competence and establishment in the phyllosphere, where water availability is often limited.This revised version was published online in October 2005 with corrections to the Cover Date.     

Shake-flask and bench-scale stirred tank bioreactor production optimization of a thermoalkaline protease from Bacillus cereus SIU1 using one-factor-at-a-time and response surface (statistical) methodologies

Abstract

We report the optimization of production of a halotolerant, thermoalkaline protease by Bacillus cereus SIU1, at shake-flask and bench-scale bioreactor level, using conventional and response surface methods. The basal medium supplemented with optimized (w/v) 0.8% glucose, 1.5% peptone, and 0.4% yeast extract produced 224 Uml^{? 1} alkaline protease after 20 h incubation. Enzyme yield was further increased to 491 Uml^{? 1} when the fermentation broth was supplemented with 0.02% (w/v) Ca²⁺. Optimization of physical factors resulted in still higher protease level of 651 Uml^{? 1} within 18 h fermentation at initial pH 9.0, 50°C, and 150 rpm agitation. Statistically designed experiments revealed significant effects of peptone and CaCl₂ on protease production. A maximum of 749 protease Uml^{? 1} was produced at optimum factor levels (w/v) of peptone 1.75%, yeast extract 0.4%, CaCl₂ 0.025%, and pH 9.0 after 18 h incubation. Optimization of agitation and aeration rates in bench-scale bioreactors further enhanced the enzyme yield to 941 protease Uml^{? 1} at 125 rpm and 2.0 vvm aeration. Optimization of protease production by conventional and statistical approaches resulted in a ～10.7-fold increase (941 Uml^{? 1}) compared to un-optimized conditions (88 Uml^{? 1}).     

Medium optimization for keratinase production in hair substrate by a new <Emphasis Type="Italic">Bacillus subtilis</Emphasis> KD-N2 using response surface methodology

Culture medium for keratinase production from hair substrate by a new Bacillus subtilis strain, KD-N2, was optimized. Effects of culture conditions on keratinase production were tested, and optimal results were obtained with 10% inocula (v/v), 16 g/L hair substrate, an initial pH value of 6.5 and a culture volume of 20 mL. Several carbon sources (sucrose, cornflour) and nitrogen sources (yeast extract, tryptone and peptone) had positive effects on keratinase production, with sucrose giving optimal results. To improve keratinase yield, statistically based experimental designs were applied to optimize the culture medium. Fractional factorial design (FFD) experiments showed that MgSO₄ and K₂HPO₄ were the most significant factors affecting keratinase production. Further central composite design (CCD) experiments indicated that the optimal MgSO₄ and K₂HPO₄ concentrations were 0.91 and 2.38 g/L, respectively. Using an optimized fermentation medium (g/L: NaCl 1.0, CaCl₂ 0.05, KH₂PO₄ 0.7, sucrose 3, MgSO₄ 0.91, K₂HPO₄ 2.38), keratinase activity increased to 125 U/mL, an approximate 1.7-fold increase over the previous activity (75 U/mL). Human hair was degraded during the submerged cultivation.     

Glycerol production in relation to the ATP pool and heat production rate of the yeasts Debaryomyces hansenii and Saccharomyces cerevisiae during salt stress

Changes in glycerol production and two parameters related to energy metabolism i. e. the heat production rate and the ATP pool, were assayed during growth of Saccharomyces cerevisiae and Debaryomyces hansenii in 4 mM and 1.35 M NaCl media. For both of the yeasts, the specific ATP pool changed during the growth cycle and reached maximum values around 10 nmol per mg dry weight in both types of media. The levels of glycerol were markedly enhanced by high salinity. In the presence of 1.35 M NaCl, D. hansenii retained most of its glycerol produced intracellularly, while S. cerevisiae extruded most of the glycerol to the environment. The intracellular glycerol level of S. cerevisiae equalled or exceeded that of D. hansenii, however, with values never lower than 3 mol per mg dry weight at all phases of growth. When D. hansenii was grown at this high salinity the intracellular level of glycerol was found to correlate with the specific heat production rate. No such correlation was found for S. cerevisiae. We concluded that during salt stress, D. hansenii possesses the capacity to regulate the metabolism of glycerol to optimize growth, while S. cerevisiae may not be able to regulate when exposed to different demands on the glycerol metabolism.     

Statistical optimization of alkaline xylanase production from <Emphasis Type="Italic">Streptomyces violaceoruber</Emphasis> under submerged fermentation using response surface methodology

Response surface methodology employing central composite design (CCD) was used to optimize fermentation medium for the production of cellulase-free, alkaline xylanase from Streptomyces violaceoruber under submerged fermentation. The design was employed by selecting wheat bran, peptone, beef extract, incubation time and agitation as model factors. A second-order quadratic model and response surface method showed that the optimum conditions for xylanase production (wheat bran 3.5 % (w/v), peptone 0.8 % (w/v), beef extract 0.8 % (w/v), incubation time 36 h and agitation 250 rpm) results in 3.0-fold improvement in alkaline xylanase production (1500.0 IUml⁻¹) as compared to initial level (500.0 IUml⁻¹) after 36 h of fermentation, whereas its value predicted by the quadratic model was 1347 IUml⁻¹. Analysis of variance (ANOVA) showed a high coefficient of determination (R²) value of 0.9718, ensuring a satisfactory adjustment of the quadratic model with the experimental data. The economical and cellulase-free nature of xylanase would enhance its applicability in pulp and paper industry.     

Enhanced lignin peroxidase synthesis by Phanerochaete Chrysosporium in solid state bioprocessing of a lignocellulosic substrate

Summary A solid state fermentation (SSF) process for the production of lignin peroxidase was optimized to enhance enzyme production by Phanerochaete chrysosporium. Optimization of the corncob SSF medium caused a significant reduction in fermentation time to give maximum lignin peroxidase yield. Supplementation of the SSF medium by low concentrations of peptone, yeast extract and Tween-80 enhanced lignin peroxidase production. Maximum yield of lignin peroxidase was 13.7 U/gds (units per gram dry substrate) noted after 5 days of SSF with 70% moisture and 20% (v/w) inoculum.     

Continuous cultures of Clostridium acetobutylicum: culture stability and low-grade glycerol utilisation

Continuous cultures of two strains of Clostridium acetobutylicum were stable for over 70 d when grown on glucose/glycerol mixtures. Butanol was the major fermentation end-product, accounting for 43 to 62% (w/w) of total products. Low-grade glycerol [65% (w/v) purity] could replace commercial glycerol [87% (w/v) purity], leading to a similar fermentation pattern: a butanol yield of 0.34 (mol/mol), a butanol productivity of 0.42 g l^–1 h^–1 and a 84% (w/w) glycerol consumption were attained when cultures were grown at pH 6 and D = 0.05 h^–1; butanol accounted for 94% (w/w) of total solvents. These values are among the highest reported in literature for C. acetobutylicum simple chemostats.     

Inhibition of Bacillus spores by combinations of heat,potassium sorbate,NaCl and pH

Viability of spores of Bacillus cereus was totally inhibited at 85°C over 30 min by adding 0.4% (w/v) potassium sorbate with 6% (w/v) NaCl at pH 4.5. Viability of B. stearothermophilus spores was totally inhibited at 95°C for 45 min in a buffer at pH 4.2 containing 0.8% (w/v) potassium sorbate and 8% (w/v) NaCl. A synergistic inhibitory effect was demonstrated in some of the combinations. The inhibition may be due to interference with the heat-resistance apparatus of the spores.O.B. Oloyede was and J. Scholefield is with the Department of Bioscience & Biotechnology, Food Science Division, University of Strathclyde, Glasgow G1 1SD, UK. O.B. Oloyede is now with the Department of Biochemistry, University of Ilorin, Ilorin, Nigeria.     

Optimization of the culture condition for an antitumor bacterium Serratia proteamacula 657 and identification of the active compounds

Exploration of novel active anti-tumor compounds from marine microbes for pharmaceutical applications has been a continuously hot spot in natural product research. Bacterial growth and metabolites may greatly vary under different culture conditions. In this study, the effects of different culture conditions and medium components on the growth and bioactive metabolites of Serratia proteamacula 657, an anti-tumor bacterium found in our previous study, were investigated. The results showed that lower temperature, weak acidic condition and solid fermentation favored the bacterial growth and the production of active compounds. Four components in the culture medium, NaCl, peptone, yeast extract and MgSO₄, were found important to the bacterial growth and active compounds production in medium optimization. Under the optimized condition of solid state fermentation at pH 6.0–7.0, 23–25 °C, with the MgSO₄-free medium containing 10.0 g/L peptone, 1.0 g/L yeast extract and 19.45 g/L NaCl, the antitumor activity of S. proteamacula 657 and the yield of crude extracts increased about 15 times and 6 times than the sample obtained in the original liquid fermentation, respectively. The active components in the metabolites of S. proteamacula 657 were identified as a homolog of prodigiosin, a red bacterial pigment, based on the analysis of the NMR and GC–MS. The bacterium S. proteamacula 657, which is adapted to lower temperature, produced prodigiosin-like pigments with highly antitumor activity, suggesting the bacterium is a potential new source for prodigiosin production.