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.     

Optimization of <Emphasis Type="Italic">Verticillium lecanii</Emphasis> spore production in solid-state fermentation on sugarcane bagasse

Verticillium lecanii is an entomopathogen with high potential in biological control of pests. We developed a solid-state fermentation with sugarcane bagasse as carrier absorbing liquid medium to propagate V. lecanii spores. Using statistical experimental design, we optimized the medium composition for spore production. We first used one-factor-at-a-time design to identify corn flour and yeast extract as the best carbon and nitrogen sources for the spore production of V. lecanii. Then, we used two-level fractional factorial design to confirm corn flour, yeast extract, and KH₂PO₄ as important factors significantly affecting V. lecanii spore production. Finally, we optimized these selected variables using a central composite design and response surface method. The optimal medium composition was (grams per liter): corn flour 35.79, yeast 8.69, KH₂PO₄ 1.63, K₂HPO₄ 0.325, and MgSO₄ 0.325. Under optimal conditions, spore production reached 1.1 × 10¹⁰ spores/g dried carrier, much higher than that on wheat bran (1.7 × 10⁹ spores/g initial dry matter).     

Optimization of culture conditions and medium components for the production of mycelial biomass and exo-polysaccharides with Cordyceps militaris in liquid culture

Both crude exo-biopolymers and mycelial biomass, produced by liquid culture of Cordyceps species, are believed to possess several potential health benefits. As a result of its known biological activities, Cordyceps militaris has been extensively characterized in regards to potential medicinal applications. However, optimized liquid culture conditions for enhanced polysaccharide productivity have yet to be developed, which is a necessary step for industrial applications. Therefore, in this study, the liquid culture conditions were optimized for maximal production of mycelial biomass and exo-polysaccharide (EPS) by C. militaris. The effects of medium composition, environmental factors, and C/N ratio were investigated. Among these variables 80 g, glucose; 10 g, yeast extract; 0.5 g, MgSO₄·7H₂O; and 0.5 g, KH₂PO₄ in 1 L distilled water were found to be the most suitable carbon, nitrogen, and mineral sources, respectively. The optimal temperature, initial pH, agitation, and aeration were determined to be 24°C, uncontrolled pH, 200 rpm, and 1.5 vvm, respectively. Under these optimal conditions, mycelial growth in shake flask cultures and 5 L jar bioreactors was 29.43 and 40.60 g/L, respectively, and polysaccharide production in shake flask cultures and 5 L jar bioreactors was 2.53 and 6.74 g/L, respectively.     

Optimization of medium composition for improving biomass production of Lactobacillus plantarum Pi06 using the Taguchi array design and the Box-Behnken method

An immune-enhancing strain, Lactobacillus plantarum Pi06, isolated from a healthy infant was used for biomass production following optimization of the medium in shake-flask culture. Preliminary studies showed that commercial MRS medium and cultivation under static conditions generated higher biomass production than four other tested media with or without a shaking condition. The selected medium composition, consisting of glucose, yeast extract, soy peptone, ammonium citrate, and corn steep liquor, was further optimized using a systematic method that integrated the Taguchi array design and the Box-Behnken method. The response effects of these factors were first investigated using Taguchi design under an L ₁₆ (4⁵) array. The suggested medium composition, derived from Statistica 7.1 using the Taguchi design, was applied to cultivate cells and a biomass of 7.16 g dry cell weight (DCW)/L was obtained. Response surface methodology based on the Box-Behnken method for the three response variables of glucose, yeast extract, and corn steep liquor was then used to further increase the biomass level to 8.94 g DCW/L. The resulting optimum medium consisted of 35 g/L glucose, 35 g/L yeast extract, and 40 mL/L corn steep liquor. Compared with the initial medium, the biomass yield was improved from 4.31 to 8.94 g DCW/L, an enhancement of approximately 107%.     

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。     

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 production of angiotensin converting enzyme inhibitor from <Emphasis Type="Italic">Flammulina velutipes</Emphasis>

The angiotensin-converting enzyme (ACE) inhibitory effect was tested in the culture broth from submerged mycelial cultures of 20 basidiomycetes. The ACE inhibitory effect of culture broth from Flammulina velutipes strain 414 was the highest (52.8%), followed by Lentinus edodes strains 2 (44.4%) and 16 (41.3%). Nutritional requirements for the production of ACE inhibitory substance from F. velutipes were studied. Sucrose, ammonium acetate, and glutamic acid were chosen for the maximum production of ACE inhibitory substance. The optimal medium composition was (g/l): sucrose 20, ammonium acetate 5, glutamic acid 2, KH₂PO₄ 3, MgSO₄·7H₂O 0.8, and yeast extract 0.5. Under optimal culture conditions, the ACE inhibitory effect was more than 80%. Received 04 May 2002/ Accepted in revised form 11 June 2002     

Production of Alcaligenes xylosoxydans EMS33 in a Bench-scale Fermenter

Summary Optimization of medium composition and pH for chitinase production by the Alcaligenes xylosoxydans mutant EMS33 was carried out in the present study and the optimized medium composition and conditions were evaluated in a fermenter. The medium components screened initially using Plackett–Burman design were (NH₄)₂SO₄, MgSO₄ 7H₂O, KH₂PO₄, yeast extract, Tween 20 and chitin in shake flask experiments. The significant medium components identified by the Plackett–Burman method were MgSO₄ 7H₂O, Tween 20 and chitin. Central composite response surface methodology was applied to further optimize chitinase production. The optimized values of MgSO₄ 7H₂O, Tween 20, chitin and pH were found to be 0.6 g/l, 0.05 g/l, 11.5 g/l and 8.0, respectively. Chitinase and biomass production of Alcaligenes xylosoxydans EMS33, was studied in a 2-l fermenter containing (g/l): chitin, 11.5; yeast extract, 0.5; (NH₄)₂SO₄, 1; MgSO₄ 7H₂O, 0.6; KH₂PO₄, 1.36 and Tween 20, 0.05. The highest chitinase production was 54 units/ml at 60 h and pH 8.0 when the dissolved O₂ concentration was 60%, whereas the highest biomass production was achieved at 36 h and pH 7.5 without any dissolved O₂ control.     

Statistical optimization of medium components for improved synthesis of riboflavin by Eremothecium ashbyii

Statistical designs were used to determine optimum levels of medium nutrients for riboflavin production in shake flask fermentation. The medium components considered include molasses, sesame seed cake (SSC), yeast extract, KH₂PO₄, MgSO₄·7H₂O, NaCl and Tween-80. Information about the effects of different medium components on riboflavin production were investigated by using the Plackett-Burman experimental design. MgSO₄·7H₂O and NaCl were found to significantly influence the riboflavin production (confidence levels above 70%). For obtaining the mutual interaction between the variables required, for achieving the optimal concentrations, a 2²-factorial central composite design was employed. The optimal concentrations for the enhanced production of riboflavin were (g/l): molasses =50.0 (glucose equivalents); SSC =50.0; yeast extract =2.0; KH₂PO₄=2.0; MgSO₄·7H₂O=0.117 and NaCl =1.13.     

Cost-effective optimization of gellan gum production by Sphingomonas paucimobilis using corn steep liquor

Abstract

Gellan gum, produced by Sphingomonas paucimobilis, is increasingly used in food and pharmaceutical industries as stabilizing, emulsifying, texturing and gelling agents. However, its high production costs may limit its full commercial potential. Therefore, in this study, we investigated ways to reduce gellan gum production costs and improve yields. We first revealed corn steep liquor (CSL) as a cost-effective nutrient source that can improve gellan gum yields. We then systematically optimized culture conditions even further, and revealed that the addition of Triton X-100 surfactant and selected inorganic nitrogen sources improved gellan gum production. Under our optimized conditions (glucose 33.75?g/L, CSL 10?g/L, urea 2.5?g/L, MgSO₄ 1.08?g/L, KH₂PO₄ 3.24?g/L, K₂SO₄ 1?g/L and Triton X-100 0.75?g/L), we yielded a maximum concentration of 14.41?g/L, which was about 1.5-fold higher than non-optimized CSL-based medium. Our findings highlight the use of CSL as a cost effective and promising nutrient source for industrial production of gellan gum.     

戊糖乳杆菌发酵培养基氮源条件的优化

对戊糖乳杆菌发酵培养基的氮源条件进行了优化。通过单因素实验及响应面分析优化利用木糖高产乳酸的戊糖乳杆菌发酵培养基的不同氮源组合。优化得到的牛肉膏与柠檬酸氢二铵复合的最佳组成为牛肉膏17.72 g/L,柠檬酸氢二铵1.91 g/L,得到乳酸实际最大产量42.37 g/L。添加玉米浆与酵母粉和无机氮源复合的最佳组成为玉米浆46.54 g/L,酵母粉21.95 g/L,柠檬酸氢二铵9.95 g/L,可得到乳酸最大产量41.06 g/L。通过响应面优化减少了有机氮源的种类。牛肉膏与柠檬酸氢二铵的复合得到了更高的乳酸产量,且减少了有机氮源用量,节约了成本。玉米浆与酵母粉的复合解决了单一玉米浆造成的木糖利用速率过低的问题,同样得到较高浓度的乳酸。     

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.     

Application of statistically-based experimental designs for the optimization of nisin production from whey

Statistically-based experimental designs were applied for the optimization of nisin production by Lactococcus lactis in a whey-based medium. Yeast extract, KH₂PO₄, and MgSO₄ were identified to have significant effects on nisin biosynthesis by a Plackett–Burman design. These three significant factors were subsequently optimized using central composite design, and the optimal conditions were determined to be 12.067 g l^–1 for yeast extract, 0.569 g l^–1 for KH₂PO₄, and 0.572 g l^–1 for MgSO₄. The validity of the optimal conditions was verified by a separate experiment.     

Statistical optimization of medium components for the production of xylanase byAspergillus niger KK2 in submerged cultivation

Medium composition was optimized for the production of xylanase byAspergillus niger KK2 using statistical experimental designs. Corn steep liquor (CSL) and industrial yeast extract (IYE) were the most important factors affecting xylanase activity. The medium that produced the optimum conditions for the production of xylanase contained 3% rice straw, 1% wheat bran, 6.3% CSL, 0.15% IYE, and 0.5% KH₂PO₄. After 4 days of cultivation under optimized conditions in a 2.5-L stirred tank reactor the activity and productivity of xylanase were 620 IU/mL and 6,458 IU/L.h, respectively. The highest xylanase activity obtained using the optimized medium was 80% greater than the activity obtained using basal medium. The xylanase activity predicted by a polynomial model was 670 IU/ml.     

Optimization of nutrient parameters for lovastatin production by <Emphasis Type="Italic">Monascus purpureus</Emphasis> MTCC 369 under submerged fermentation using response surface methodology

Lovastatin, an inhibitor of HMG-CoA reductase, was produced by submerged fermentation using Monascus purpureus MTCC 369. Five nutritional parameters screened using Plackett–Burman experimental design were optimized by Box–Behnken factorial design of response surface methodology for lovastatin production in shake flask cultures. Maximum lovastatin production of 351 mg/l were predicted in medium containing 29.59 g/l dextrose, 3.86 g/l NH₄Cl, 1.73 g/l KH₂PO₄, 0.86 g/l MgSO₄·7H₂O, and 0.19 g/l MnSO₄·H₂O using response surface plots and point prediction tool of DESIGN EXPERT 7.0 (Statease, USA) software.     

Optimization of media components for enhanced arachidonic acid production by <Emphasis Type="Italic">Mortierella alpina</Emphasis> under submerged cultivation

Mortierella alpina, an oleaginous zygomycete is a potent producer of arachidonic acid, the pharmaceutically and nutraceutically important polyunsaturated fatty acid of the n-6 series. It serves a wide variety of purposes, from being a purely structural element in phospholipids to being involved in signal transduction, and as a substrate for a host of derivatives involved in second messenger function. Arachidonic acid has applications in diverse areas including infant and geriatric nutrition. In the present study, the interactive effects of four major media constituents on arachidonic acid production were investigated by applying a central composite rotatable design (CCRD) and response surface methodology (RSM). The independent variables, which were selected byconcentrations of glucose, corn solids, KH₂PO₄, and KNO₃ influenced the production of biomass, total lipid, and arachidonic acid by M. alpina. A second-order polynomial was fitted by multiple regression analysis of the experimental data. The optimum conditions (glucose 10.0 g/L, corn solids 5.0 g/L, KH₂PO₄ 1.0 g/L, and KNO₃ 1.0 g/L) resulted in maximum production of arachidonic acid (1.39 g/L) and the corresponding biomass and total lipid concentrations were 12.49 and 5.87 g/L, respectively.     

Solid state cultivation of Streptomyces clavuligerus for cephamycin C production

Solid state cultivation of Streptomyces clavuligerus for cephamycin C production was carried out in a system consisting of wheat rawa 5 g; cotton seed deoiled cake 5 g; sunflower cake 0·5 g; corn steep liquor 1 g; MgSO₄.7H₂O 0·06 g; CaCO₃ 0·1 g; K₂HPO₄ 4·4 g; with initial moisture content of 80%, initial pH 6·5 and a fermentation temperature in the range 28–30°C. The fermentation cycle was about 5 days. Streptomyces clavuligerus growth was observed on the 2nd day and production of cephamycin C was initiated on 3rd day. Abundant mycelial growth was observed from the 3rd day and reached stationary phase by the 5th day. Cephamycin C was produced maximally at a rate of 15 mg/g substrate on the 5th day and was stable until the 30th day with only marginal decrease in titre.     

Use of response surface methodology to study the effect of media composition on aflatoxin production by Aspergillus flavus

Aflatoxins are one of the most important secondary metabolites. These extrolites are produced by a number of Aspergillus fungi. In this study, we demonstrate the effect of media components and enhanced aflatoxin yield shown by A. flavus using response surface methodology in response to different nutrients. Different components of a chemically defined media that influence the aflatoxin production were monitored using Plackett–Burman experimental design and further optimized by Box–Behnken factorial design of response surface methodology in liquid culture. Interactions were studied with five variables, namely sorbitol, fructose, ammonium sulfate, KH₂PO₄, and MgSO₄.7H₂O. Maximum aflatoxin production was envisaged in medium containing 4.94 g/l sorbitol, 5.56 g/l fructose, 0.62 g/l ammonium sulfate, 1.33 g/l KH₂PO₄, and 0.65 g/l MgSO₄·7H₂O using response surface plots and the point prediction tool of the DESIGN EXPERT 8.1.0 (Stat-Ease, USA) software. However, a production of 5.25 μg/ml aflatoxin production was obtained, which was in agreement with the prediction observed in verification experiment. The other component (MgSO₄.7H₂O) was found to be an insignificant variable.     

Optimization of polyhydroxybutyrate production by <Emphasis Type="Italic">Bacillus</Emphasis> sp. CFR 256 with corn steep liquor as a nitrogen source

Polyhydroxyalkanotes (PHAs), the eco-friendly biopolymers produced by many bacteria, are gaining importance in curtailing the environmental pollution by replacing the non-biodegradable plastics derived from petroleum. The present study was carried out to economize the polyhydroxybutyrate (PHB) production by optimizing the fermentation medium using corn steep liquor (CSL), a by-product of starch processing industry, as a cheap nitrogen source, by Bacillus sp. CFR 256. Response surface methodology (RSM) was used to optimize the fermentation medium using the variables such as corn steep liquor (5–25 g l⁻¹), Na₂HPO₄ 2H₂O (2.2–6.2 g l⁻¹), KH₂PO₄ (0.5–2.5 g l⁻¹), sucrose (5–55 g l⁻¹) and inoculum concentration (1–25 ml l⁻¹). Central composite rotatable design (CCRD) experiments were carried out to study the complex interactions of the variables. The optimum conditions for maximum PHB production were (g l⁻¹): CSL-25, Na₂HPO₄ 2H₂O-2.2, KH₂PO₄ − 0.5, sucrose − 55 and inoculum − 10 (ml l⁻¹). After 72 h of fermentation, the amount of PHA produced was 8.20 g l⁻¹ (51.20% of dry cell biomass). It is the first report on optimization of fermentation medium using CSL as a nitrogen source, for PHB production by Bacillus sp.     

Biochemical and kinetic evaluation of lipase and biosurfactant assisted ex novo synthesis of microbial oil for biodiesel production by Yarrowia lipolytica utilizing chicken tallow

The present study explores the production of biodiesel, a sustainable replacement for depleting fossil fuel by utilizing microbial oil, which was procured from Yarrowia lipolytica employing chicken tallow as the carbon substrate. Chicken tallow, yeast extract, and MgSO₄·7H₂O were screened for biomass production through Plackett–Burman design. Further, Box–Behnken design analysis was performed, and the optimal concentration of the medium variables was found to be 20 g/L of chicken tallow, 7.0 g/L of yeast extract, and 0.45 g/L of MgSO₄·7H₂O.The various parameters viz., pH (6), temperature (30 °C), RPM (150), inoculum volume (5%, v/v), and C/N ratio (100) were optimized for maximal biomass and lipid yield, and lipid content. Nile red-stained cells were observed for intracellular lipid bodies using fluorescence microscopy, and its fluorescence intensity was measured bythe flow cytometer. The dimorphic transition and substrate assimilation of Y. lipolytica were analyzed using scanning electron microscopy (SEM), and Fourier transform infrared spectroscopy (FT-IR). Batch kinetic studies revealed the concomitant synthesis of microbial lipid (4.16 g/L), lipase (43 U/mL), and biosurfactant (1.41 g/L). The GC-MS analysis of microbial oil presented the fatty acid profile as oleic acid (49.15%), palmitic acid (29.83%), stearic acid (11.43%), linoleic acid (3.83%), palmitoleic acid (3.77%), and myristic acid (1.32%).