Retamycin production by immobilized cells of Streptomyces olindensis ICB20 in repeated-batch cultures

Repeated-batch cultures of Ca-alginate immobilized cells of Streptomyces olindensis ICB20 for retamycin production were carried out in two different bioreactors: a basket-type stirred tank reactor (BSTR) and a bubble column reactor (BCR). Higher average values of retamycin content (R) and productivity (P_R) were achieved in the BSTR cultures (about 1.7 AU and 0.031 AU h⁻¹, respectively) compared to those obtained in the BCR cultures (about 0.6 AU and 0.012 AU h⁻¹, respectively). The BCR, on the other hand, presented significantly better operation stability than the BSTR, which makes the former much more promising regarding future industrial applications.     

Batch culture and repeated-batch culture of Cunninghamella bainieri 2A1 for lipid production as a comparative study

This research was performed based on a comparative study on fungal lipid production by a locally isolated strain Cunninghamella bainieri 2A1 in batch culture and repeated-batch culture using a nitrogen-limited medium. Lipid production in the batch culture was conducted to study the effect of different agitation rates on the simultaneous consumption of ammonium tartrate and glucose sources. Lipid production in the repeated-batch culture was studied by considering the effect of harvesting time and harvesting volume of the culture broth on the lipid accumulation. The batch cultivation was carried out in a 500 ml Erlenmeyer flask containing 200 ml of the fresh nitrogen-limited medium. Microbial culture was incubated at 30 °C under different agitation rates of 120, 180 and 250 rpm for 120 h. The repeated-batch culture was performed at three harvesting times of 12, 24 and 48 h using four harvesting cultures of 60%, 70%, 80% and 90%. Experimental results revealed that nitrogen source (ammonium tartrate) was fully utilized by C. bainieri 2A1 within 24 h in all agitation rates tested. It was also observed that a high amount of glucose in culture medium was consumed by C. bainieri 2A1 at 250 rpm agitation speed during the batch fermentation. Similar results showed that the highest lipid concentration of 2.96 g/L was obtained at an agitation rate of 250 rpm at 120 h cultivation time with the maximum lipid productivity of 7.0 × 10⁻² mg/ml/h. On the other hand, experimental results showed that the highest lipid concentration produced in the repeated-batch culture was 3.30 g/L at the first cycle of 48 h harvesting time using 70% harvesting volume, while 0.23 g/L gamma-linolenic acid (GLA) was produced at the last cycle of 48 h harvesting time using 80% harvesting volume.     

Optimization of a culture medium for ligninolytic enzyme production and synthetic dye decolorization using response surface methodology

A Box-Wilson central composite design was applied to optimize copper, veratryl alcohol and l-asparagine concentrations for Trametes trogii (BAFC 212) ligninolytic enzyme production in submerged fermentation. Decolorization of different dyes (xylidine, malachite green, and anthraquinone blue) by the ligninolytic fluids from the cultures was compared. The addition of copper stimulated laccase and glyoxal oxidase production, but this response was influenced by the medium N-concentration, with improvement higher at low N-levels. The medium that supported the highest ligninolytic production (22.75 U/ml laccase, 0.34 U/ml manganese peroxidase, and 0.20 U/ml glyoxal oxidase) also showed the greatest ability to decolorize the dyes. Only glyoxal oxidase activity limited biodecoloration efficiency, suggesting the involvement of peroxidases in the process. The addition of 1-hydroxybenzotriazole (a known laccase mediator) to the ligninolytic fluids increased both their range and rate of decolorization. The cell-free supernatant did not decolorize xylidine, poly R-478, azure B, and malachite green as efficiently as the whole broth, but results were similar in the case of indigo carmine and remazol brilliant blue R. This indicates that the mycelial biomass may supply other intracellular or mycelial-bound enzymes, or factors necessary for the catalytic cycle of the enzymes. It also implies that this fungus implements different strategies to degrade dyes with diverse chemical structures.     

Enhanced production of fibrinolytic enzyme by a new Xanthomonas oryzae IND3 using low-cost culture medium by response surface methodology

Cardiovascular diseases (CVDs) cause high mortality throughout the world. Existing fibrinolytic agents are highly expensive and have many side effects. Microbial fibrinolytic enzymes are very much considered as novel therapeutic candidate for the treatment of CVDs. Reports on fibrinolytic enzyme from Xanthomonas sp. is lacking. This study reports fibrinolytic enzymes from Xanthomonas oryzae IND3 as it shows hyperactivity on fibrin-agarose plates. This organism utilized various agro-industrial wastes for enzymes production. Among all, cow dung enhanced more enzyme production, hence it was used as the low-cost substrate for statistical optimization of fibrinolytic protease in Solid state fermentation. Response surface methodology was employed to optimize the factors and enhanced yield by 4-fold. The interactions among the variables, viz, sucrose, yeast extract, and pH of the medium were investigated using Central Composite Design (CCD). The predicted fibrinolytic enzyme activity was 2340 U/g, and the observed fibrinolytic enzyme activity was 2294?±?12.8?U/g. The fibrinolytic enzyme degraded blood clot in vitro completely. This study is the first report on statistical optimization of fibrinolytic enzyme production in SSF from Xanthomonas sp. The crude extract has immense activity on proteinaceous wastes. The production of fibrinolytic protease using the low-cost substrate could reduce the production cost of enzyme.     

Maximization of recombinant Helicobacter pylori neutrophil activating protein production in Escherichia coli: improvement of a chemically defined medium using response surface methodology

Medium optimization for the production of constitutive recombinant Helicobacter pylori neutrophil activating protein (NAP) in Escherichia coli was investigated by using response surface methodology. Carbon to nitrogen ratio, concentrations of sodium polyphosphate and magnesium sulfate were considered as independent variables. The optimized medium was a chemically defined medium with a carbon to nitrogen ratio of 14.4 and with concentrations of sodium polyphosphate and magnesium sulfate about 7.1 g l(-1) and 3.04 g l(-1) respectively. The maximum recombinant NAP production level (1184.6 mg l(-1)) was 29.96% higher than that in control medium.     

Use of response surface methodology to optimize culture medium for production of lipase with Candida sp. 99-125

Response surface methodology (RSM) was employed to optimize culture medium for production of lipase with Candida sp. 99-125. In the first step, a Plackett–Burmen design was used to evaluate the effects of different components in the culture medium. Soybean oil, soybean powder and K₂HPO₄ have significant influences on the lipase production. The concentrations of three factors were optimized subsequently using central composite designs and response surface analysis. The optimized condition allowed the production of lipase to be increased from 5000 to 6230 IU/ml in shake flask system. The lipase fermentation in 5 l fermenter reached 9600 IU/ml.     

Enhancing isomaltulose production by recombinant Escherichia coli producing sucrose isomerase: culture medium optimization containing agricultural wastes and cell immobilization

Isomaltulose is a structural isomer of sucrose commercially used in food industries. In this work, recombinant Escherichia coli producing sucrose isomerase (SIase) was used to convert sucrose into isomaltulose. To develop an economical industrial medium, untreated cane molasses (10.63 g l^?1), yeast extract (25.93 g l^?1), and corn steep liquor (10.45 g l^?1) were used as main culture compositions for SIase production. The relatively high SIase activity (14.50 ± 0.11 U mg DCW^?1) was obtained by the recombinant cells. To the best of our knowledge, this is the first investigation on SIase production by engineered E. coli using untreated cane molasses. The recombinant E. coli cells expressing the SIase gene were immobilized in calcium alginate gel in order to improve the efficiency of recycling. The immobilization was most effective with 2 % (w/v) sodium alginate and 3 % (w/v) calcium chloride. The optimal initial biomass for immobilization was 20 % (w/v, wet wt.), with a hardening time of 8 h for cell immobilization. The immobilized E. coli cells exhibited good stability for 30 batches with the productivity of 0.45 g isomaltulose g pellet^?1 h^?1. A continuous isomaltulose formation process using a column reactor remained stable for 40 days with 83 ± 2 % isomaltulose yield, which would be beneficial for economical production of isomaltulose.     

Improved gellan gum production by a newly-isolated Sphingomonas azotifigens GL-1 in a cheese whey and molasses based medium

Gellan gum is a water-soluble exopolysaccharide, it has applications in the food, pharmaceutical and chemical industries. In this study, a gellan gum producing strain was isolated from rice root, and this strain was identified be the species of Sphingomonas azotifigens. The Plackett-Burman design was applied to investigate the main factors affecting gellan gum production by S. azotifigens GL-1 in a molasses and cheese whey based medium; the medium compositions were optimized by response surface methodology. The optimum cheese whey based medium consisted of cheese whey 68.34 g/L, Na₂HPO₄ 14.58 g/L and KH₂PO₄ 7.66 g/L, and the maximum gellan gum production that using this medium was 33.75 ± 1.55 g/L. 14.75 ± 0.65 g/L gellan gum was obtained with an optimized molasses medium, which consisted of molasses 50 g/L, Na₂HPO₄ 9.71 g/L and KH₂PO₄ 5.92 g/L. The molecular weight of gellan gum obtained from two medias were 1.06 × 10⁶ and 0.89 × 10⁶ Da, respectively. The cheese whey-derived gellan gum showed a higher rhamnose, lower glucuronic acid and higher glycerate content compared to the molasses-derived gellan gum. S. azotifigens GL-1 has a high gellan gum production capacity in a cheap medium suggesting it has great potential as an industrial gellan gum producer.     

Use of response surface methodology to optimize culture medium for production of lovastatin by Monascus ruber

Response surface methodology (RSM) was employed to study the effect of culture medium on the production of lovastatin in mixed solid-liquid state (or submerged) cultures by Monascus ruber. The maximal lovastatin yield (131 mg/L, average of three repeats) appeared at the region where the respective concentrations of rice powder, peptone, glycerin, and glucose were around 34.4 g/L, 10.8 g/L, 26.4 ml/L, and 129.2 g/L, respectively. The optimized medium resulted in a significant increase of lovastatin yield, as compared with that obtained by the fermentation of many other M. ruber species.     

Optimization of culture conditions for production of cis-epoxysuccinic acid hydrolase using response surface methodology

Response surface methodology, which allows for rapid identification of important factors and optimization of them to enhance enzyme production, was employed here to optimize culture conditions for the production of cis-epoxysuccinic acid hydrolase from Bordetella sp. strain 1–3. In the first step, a Plackett–Burman design was used to evaluate the effects of nine variables (yeast extract, cis-epoxysuccinic acid, KH₂PO₄, K₂HPO₄ · 3H₂O, MgSO₄ · 7H₂O, trace minerals solution, culture volume, initial pH and incubation time) on the enzyme production. Yeast extract, cis-epoxysuccinic acid and KH₂PO₄ had significant influences on cis-epoxysuccinic acid hydrolase production and their concentrations were further optimized using central composite design and response surface analysis. A combination of adjusting the concentration of yeast extract to 7.8 g/l, cis-epoxysuccinic acid to 9.8 g/l, and KH₂PO₄ to 1.12 g/l would favor maximum cis-epoxysuccinic acid hydrolase production. An enhancement of cis-epoxysuccinic acid hydrolase production from 5.6 U/ml to 9.27 U/ml was gained after optimization.     

Optimization of medium composition for butyric acid production by Clostridium thermobutyricum using response surface methodology

The optimal medium for butyric acid production by Clostridium thermobutyricum in a shake flask culture was studied using statistical experimental design and analysis. The optimal composition of the fermentation medium for maximum butyric acid yield, as determined on the basis of a three-level four-factor Box-Behnken design (BBD), was obtained by response surface methodology (RSM). The high correlation between the predicted and observed values indicated the validity of the model. A maximum butyric acid yield of 12.05 g/l was obtained at K₂HPO₄ 7.2 g/l, 34.9 g/l glucose, 20 g/l yeast extract, and 15 g/l acetate, which compared well to the predicated production of 12.13 g/l.     

Enhanced production of amidase from <Emphasis Type="Italic">Rhodococcus erythropolis</Emphasis> MTCC 1526 by medium optimisation using a statistical experimental design

In the present work, statistical experimental methodology was used to enhance the production of amidase from Rhodococcus erythropolis MTCC 1526. R. erythropolis MTCC 1526 was selected through screening of seven strains of Rhodococcus species. The Placket–Burman screening experiments suggested that sorbitol as carbon source, yeast extract and meat peptone as nitrogen sources, and acetamide as amidase inducer are the most influential media components. The concentrations of these four media components were optimised using a face-centred design of response surface methodology (RSM). The optimum medium composition for amidase production was found to contain sorbitol (5 g/L), yeast extract (4 g/L), meat peptone (2.5 g/L), and acetamide (12.25 mM). Amidase activities before and after optimisation were 157.85 units/g dry cells and 1,086.57 units/g dry cells, respectively. Thus, use of RSM increased production of amidase from R. erythropolis MTCC 1526 by 6.88-fold.     

Statistical optimization of medium components and growth conditions by response surface methodology to enhance lipase production by Aspergillus carneus

A response surface approach has been used to study the production of an extracellular lipase from Aspergillus carneus, which has the property of immense industrial importance. Interactions were studied for five different variables (sunflower oil, glucose, peptone, agitation rate and incubation period), which were found influential for lipase production by one-at a time method. We report a 1.8-fold increase in production, with the final yield of 12.7 IU/ml in comparison to 7.2 U/ml obtained by one-at-a-time method. Using the statistical approach (response surface methodology (RSM)) the optimum values of these most influential parameters were as follows: sunflower oil (1%), glucose (0.8%), peptone (0.8%), agitation rate (200 rpm) and incubation period (96 h) at 37 °C. The subsequent verification experiment confirmed the validity of the model.     

Monacolin K production by citrinin‐free Monascus pilosus MS‐1 and fermentation process monitoring

Monacolin K (MK) is a naturally occurring hypocholesterolemic agent that specifically inhibits HMG‐CoA reductase. As a natural source of MK, Monascus‐fermented products are of special interest; however, some Monascus strains could produce citrinin, which is a nephrotoxin, as a contaminant in Monascus‐derived products. A Monascus pilosus strain (MS‐1) that produces high amounts of MK, but no citrinin, was screened in previous investigations. Herein, liquid‐state fermentation parameters of the MS‐1 strain were optimized using statistical methods to maximize the MK yield with potato juice as a basic medium. The maximum MK yield (326.74 μg/mL) was predicted with 50 mL of medium in a 250‐mL conical flask containing 30 g/L sucrose, 38.75 g/L soybean flour, 0.00105 mol/L Mg²⁺ at pH 5.48, and 8% v/v seed inoculum precultured for 42 h at 30°C, incubated at 30°C for 3 days, followed by further incubation for 11 days at 24.7°C. The verified MK yield was 390.68 μg/mL and the MK yield increased to 565.64 μg/mL after 21 days of fermentation. No citrinin was detected in MS‐1‐fermented products. The results suggest that citrinin‐free MK can be obtained from natural medium through liquid‐state fermentation in an economical way. This method will be of practical value to the industrial production of MK.     

Paecilomyces sp. ZB is a cell factory for the production of gibberellic acid using a cheap substrate in solid state fermentation

Gibberellic acid from the fungi has been widely used in agriculture. In this study, more than 20 fungal isolates were screened and Paecilomyces sp. ZB shown to produce more gibberellic acid than other fungal isolates. Cow dung was used as low cost substrate for gibberellic acid production in solid state fermentation (SSF). Carbon, nitrogen and ionic sources stimulated gibberellic acid production in SSF. Lactose emerged as the significant carbon source supporting more gibberellic acid production (731 µg/g). Among the nitrogen sources, glycine appeared to influence the production of more gibberellic acid (803 µg/g). The process parameters were optimized to enhance gibberellic acid production using a two-level full factorial design and response surface methodology. The amount of gibberellic acid production was influenced mainly by moisture and pH of the substrate. Gibberellic acid production was 1312 µg/g under the optimized conditions and the predicted response was 1339 µg/g. The gibberellic acid yield increased twofolds after medium optimization. The extracted gibberellic acid was sprayed on the growing Mung bean plant and it stimulated the growth of the plant effectively. To conclude, cow dung is a new alternative to produce gibberellic acid in SSF.     

Optimization of culture conditions for production of yeast biomass using bamboo wastewater by response surface methodology

Response surface methodology (RSM) was applied to optimize culture conditions for the growth of Candida utilis with bamboo wastewater. A significant influence of initial pH, fermentation time and yeast extract on biomass of C. utilis was evaluated by Plackett–Burman design (PBD). These factors were further optimized using a central composite design (CCD) and RSM. A combination of initial pH 6.1, fermentation time 69 h and yeast extract 1.17 g/L was optimum for maximum biomass of C. utilis. A 1.7-fold enhancement of biomass of C. utilis was gained after optimization in shake-flask cultivation. The biomass of C. utilis reached 19.17 g/L in 3 L fermentor.     

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.     

Response surface methodology for optimization of medium components in submerged culture of Aspergillus flavus for enhanced heparinase production

Aims: Aim of the study was to develop a medium for optimal heparinase production with a strain of Aspergillus flavus (MTCC‐8654) by using a multidimensional statistical approach. Methods and Results: Statistical optimization of intracellular heparinase production by A. flavus, a new isolate, was investigated. Plackett–Burman design was used to evaluate the affect of medium constituents on heparinase yield. The experimental results showed that the production of heparinase was dependent upon heparin, the inducer; chitin, structurally similar to heparin and NH₄NO_3, the nitrogen source. A central composite design was applied to derive a statistical model for optimizing the composition of the fermentation medium for the production of heparinase enzyme. The optimum fermentation medium consisted of (g l^?1) Mannitol, 8·0; NH₄NO₃, 2·5; K₂HPO₄, 2·5; Na₂HPO₄, 2·5; MgSO₄.7H₂O, 0·5; Chitin, 17·1; Heparin, 0·6; trace salt solution (NaMoO₄.2H₂O, CoCl₂.6H₂O, CuSO₄.5H₂O, FeSO₄.7H₂O, CaCl₂), 10^?4 mol l^?1. Conclusions: A 2·37‐fold increase in heparinase production was achieved in economic and effective manner by the application of statistical designs in medium optimization. Significance and Impact of the Study: Heparinase production was doubled by statistical optimization in a cost‐effective manner. This heparinase can find application in pharmaceutical industry and for the generation of low‐molecular‐weight heparins, active as antithrombotic and antitumour agents.     

Use of wood vinegar to enhance 5-aminolevulinic acid production by selected Rhodopseudomonas palustris in rubber sheet wastewater for agricultural use

This study aimed to produce inexpensive 5-aminolevulinic acid (ALA) in a non-sterile latex rubber sheet wastewater (RSW) by Rhodopseudomonas palustris TN114 and PP803 for the possibility to use in agricultural purposes by investigating the optimum conditions, and applying of wood vinegar (WV) as an economical source of levulinic acid to enhance ALA content. The Box–Behnken Design experiment was conducted under microaerobic-light conditions for 96 h with TN114, PP803 and their mixed culture (1:1) by varying initial pH, inoculum size (% v/v) and initial chemical oxygen demand (COD, mg/L). Results showed that the optimal condition (pH, % inoculum size, COD) of each set to produce extracellular ALA was found at 7.50, 6.00, 2000 for TN114; 7.50, 7.00, 3000 for PP803; and 7.50, 6.00, 4000 for a mixed culture; and each set achieved COD reduction as high as 63%, 71% and 75%, respectively. Addition of the optimal concentration of WV at mid log phase at 0.63% for TN114, and 1.25% for PP803 and the mixed culture significantly increased the ALA content by 3.7–4.2 times (128, 90 and 131 μM, respectively) compared to their controls. ALA production cost could be reduced approximately 31 times with WV on the basis of the amount of levulinic acid used. Effluent containing ALA for using in agriculture could be achieved by treating the RSW with the selected ALA producer R. palustris strains under the optimized condition with a little WV additive.