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.     

Citric acid production by a novel Aspergillus niger isolate: II. Optimization of process parameters through statistical experimental designs

In this work, sequential optimization strategy, based on statistical designs, was employed to enhance the production of citric acid in submerged culture. For screening of fermentation medium composition significantly influencing citric acid production, the two-level Plackett-Burman design was used. Under our experimental conditions, beet molasses and corn steep liquor were found to be the major factors of the acid production. A near optimum medium formulation was obtained using this method with increased citric acid yield by five-folds. Response surface methodology (RSM) was adopted to acquire the best process conditions. In this respect, the three-level Box-Behnken design was applied. A polynomial model was created to correlate the relationship between the three variables (beet molasses, corn steep liquor and inoculum concentration) and citric acid yield. Estimated optimum composition for the production of citric acid is as follows pretreated beet molasses, 240.1g/l; corn steep liquor, 10.5g/l; and spores concentration, 10(8)spores/ml. The optimum citric acid yield was 87.81% which is 14 times than the basal medium. The five level central composite design was used for outlining the optimum values of the fermentation factors initial pH, aeration rate and temperature on citric acid production. Estimated optimum values for the production of citric acid are as follows initial pH 4.0; aeration rate, 6500ml/min and fermentation temperature, 31.5 degrees C.     

The utilization of beet molasses as a novel carbon source for cephalosporin C production by Acremonium chrysogenum: Optimization of process parameters through statistical experimental designs

In this work, cephalosporin C (CPC) production on pilot scale fermenters of 600l capacity with 350l working volume by Acremonium chrysogenum EMCC 904 was performed. The effects of fermentation medium composition, inoculum concentration, initial pH and aeration rate on CPC production by A. chrysogenum strain was investigated by using response surface methodology (RSM). The Plackett-Burman design which involves two concentrations of each nutrient was effective in searching for the major medium components promoting CPC production. Under our experimental conditions; Soya oil, beet molasses and corn steep liquor were found to be the major factors contributing to the antibiotic production. Subsequently, a Box-Behnken design was used for outlining the concentration of the most effective medium constituents. Estimated optimum composition for the production of CPC was as follows: soya oil, 40g/l; beet molasses, 180g/l; and corn steep liquor, 330g/l. The central composite design was used for outlining the optimum values of the fermentation parameters. Estimated optimum values for the production of CPC are as follows: inoculum level, 10(5.5)spores/ml; initial pH, 4.3; and aeration rate, 9364ml/min.     

Economical succinic acid production from cane molasses by Actinobacillus succinogenes

In this work, production of succinic acid by Actinobacillus succinogenes CGMCC1593 using cane molasses as a low cost carbon source was developed. In anaerobic bottles fermentation, succinic acid concentration of 50.6+/-0.9 g l(-1) was attained at 60 h using an optimum medium containing molasses pretreated with sulfuric acid, resulting in a succinic acid yield of 79.5+/-1.1% and sugar utilization of 97.1+/-0.6%. When batch fermentation was carried out in a 5-l stirred bioreactor with pretreated molasses, 46.4 g l(-1) of succinic acid was attained at 48 h and faster cells growth was also observed. Fed batch fermentation was performed to minimize the substrate (sugar) inhibition effect, giving 55.2 g l(-1) of succinic acid and 1.15 g l(-1)h(-1) of productivity at 48 h. The present study suggests that the inexpensive cane molasses could be utilized for the economical and efficient production of succinic acid by A. succinogenes.     

Production of bacterial cellulose from <Emphasis Type="Italic">Enterobacter amnigenus</Emphasis> GH-1 isolated from rotten apple

Bacterial cellulose finds novel applications in biomedical, biosensor, food, textile and other industries. The optimum fermentation conditions for the production of cellulose by newly isolated Enterobacter amnigenus GH-1 were investigated. The strain was able to produce cellulose at temperature 25–35°C with a maximum at 28°C. Cellulose production occurred at pH 4.0–7.0 with a maximum at 6.5. After 14 days of incubation, the strain produced 2.5 g cellulose/l in standard medium whereas cellulose yield in the improved medium was found to be 4.1 g/l. The improved medium consisted of 4% (w/v) fructose, 0.6% (w/v) casein hydrolysate, 0.5% (w/v) yeast extract, 0.4% (w/v) disodium phosphate, and 0.115% (w/v) citrate. Addition of metal ions like zinc, magnesium, and calcium and solvents like methanol and ethanol were found to be stimulatory for cellulose production by the strain. The strain used natural carbon sources like molasses, starch hydrolysate, sugar cane juice, coconut water, coconut milk, pineapple juice, orange juice, and pomegranate juice for growth and cellulose production. Fruit juices can play important role in commercial exploitation of bacterial cellulose by lowering the cost of the production medium.     

Ergosterol production from molasses by genetically modified <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Ergosterol is an economically important metabolite produced by fungi. Recombinant Saccharomyces cerevisiae YEH56(pHXA42) with increased capacity of ergosterol formation was constructed by combined overexpression of sterol C-24(28) reductase and sterol acyltransferase in the yeast strain YEH56. The production of ergosterol by this recombinant strain using cane molasses (CM) as an inexpensive carbon source was investigated. An ergosterol content of 52.6 mg/g was obtained with 6.1 g/l of biomass from CM medium containing 60 g/l of total sugar in 30 h in shake flask. The ergosterol yield was enhanced through the increasing cell biomass by supplementation of urea to a concentration of 6 g/l in molasses medium. Fermentation was performed in 5-l bioreactor using the optimized molasses medium. In batch fermentation, the effect of agitation velocity on ergosterol production was examined. The highest ergosterol yield was obtained at 400 rpm that increased 60.4 mg/l in comparison with the shake flask culture. In fed-batch fermentation, yeast cells were cultivated, firstly, in the starting medium containing molasses with 20 g/l of total sugar, 1.68 g/l of phosphate acid, and 6 g/l of urea (pH 5.4) for 5 h, then molasses containing 350 g/l of total sugar was fed exponentially into the bioreactor to keep the ethanol level in the broth below 0.5%. After 40 h of cultivation, the ergosterol yield reached 1,707 mg/l, which was 3.1-fold of that in the batch fermentation.     

Medium optimization for antifungal active substances production from a newly isolated Paenibacillus sp. using response surface methodology

Statistics based experimental designs were used to optimize the medium for antifungal active substances production from a newly isolated Paenibacillus polymyxa Cp-S316 in shaker flask cultivation. The medium components having significant effect on the production were first identified using a fractional factorial design. Then steepest ascent method was employed to approach the experimental design space, followed by an application of response surface methodology for further optimization. A quadratic model was found to fit the antifungal active substances production. Response surface analysis revealed that the optimum values of the tested variables for the production of active substances were 12.3 (g/l) lactose, 17.5 (g/l) peptone, 0.4 (g/l) sodium nitrate, 4.5 (g/l) magnesium sulfate and 100 (g/l) potato. A production of 4687.71mug/ml, which was in agreement with the prediction, was observed in verification experiment. In comparison to the production of basal medium, 3.05-fold increase had been obtained.     

L-亮氨酸发酵培养基优化试验

应用Plackett-Burman设计试验从L-亮氨酸基础发酵培养基的10种成分中筛选出5种重要成分,然应用响应面分析试验确定5种重要成分的最适用量。培养基优化后摇瓶分批发酵72h产L-亮氨酸18.05g/L     

Production of thuringiensin from Bacillus thuringiensis using a net-draft-tube,modified airlift reactor

A net-draft-tube, modified airlift reactor and a stirred-tank reactor were used for thuringiensin production by Bacillus thuringiensis subsp. darmstadiensis growing with various concentrations of molasses. The optimum concentration of molasses for thuringiensin production in both reactors was 15 g/l. There was a 6 h delay in sporulation in the modified airlift reactor compared with that in the stirred-tank reactor. Thuringiensin yield in the modified airlift reactor (2.2 g/l) was consequently higher than that in the stirred-tank reactor (1.1 g/l).     

ε-PolyLysine production from sugar cane molasses by a new isolates of Bacillus sp. and optimization of the fermentation condition

An attempt was made to use cane molasses as a culture medium for ε-PolyLysine (ε-PL) production by a natural bacterial isolate. The bacterium was identified as Bacillus sp., as confirmed by 16S rDNA sequence analysis. A BLAST result of the sequence indicated that the closest relative of this Bacillus BHU strain was B. thuringiensis, with 97 % homology. The molasses was found to be a better culture medium compared to commonly used culture media comprised of either glucose or glycerol as a carbon source. The various physicochemical parameters were studied for culture growth and polymer production, and were further optimized using response surface methodology (RSM). The correlation coefficient of the resulting model was found to be R ²?=?0.9828. The RSM predicted optimum conditions for ε-PL production (2.46 g/l) by the Bacillus strain was achieved by using molasses, 59.7 g/l; yeast extract, 15.2 mg/l; pH, 6.8 and fermentation time, 42 h at 30 °C. This study represents the first report on the potential application of cane molasses (a byproduct of sugarcane industries) as a culture medium for ε-PL production by Bacillus species. The specific Bacillus strain used in the present study can be exploited for developing a novel technology using inexpensive renewable resources for ε-PL production, a polymer of commercial interest.     

Optimization of lactic acid production from beet molasses by Lactobacillus delbrueckii NCIMB 8130

Production of lactic acid from beet molasses by Lactobacillus delbrueckii NCIMB 8130 in static and shake flask fermentation was investigated. Shake flasks proved to be a better fermentation system for this purpose. Substitution of yeast extract with other low cost protein sources did not improve lactic acid production. The maximum lactic acid concentration was achieved without treatment of molasses. A Central Composite Design was employed to determine the maximum lactic acid concentration at optimum values for the process variables (sucrose, yeast extract, CaCO₃). A satisfactory fit of the model was realized. Lactic acid production was significantly affected both by sucrose–yeast extract and sucrose–CaCO₃ interactions, as well as by the negative quadratic effects of these variables. Sucrose and yeast extract had a linear effect on lactic acid production while the CaCO₃ had no significant linear effect. The maximum lactic acid concentration (88.0 g/l) was obtained at concentrations for sucrose, yeast extract and CaCO₃ of 89.93, 45.71 and 59.95 g/l, respectively.     

Medium optimization for the production of avermectin B1a by Streptomyces avermitilis 14-12A using response surface methodology

Response surface methodology was employed to optimize the composition of medium for the production of avermectin B1a by Streptomyces avermitilis 14-12A in shaker flask cultivation. Corn starch and yeast extract were found to have significant effects on avermectin B1a production by the Plackett–Burman design. The steepest ascent method was used to access the optimal region of the medium composition, followed by an application of response surface. The analysis revealed that the optimum values of the tested variables were 149.57 g/l corn starch and 8.92 g/l yeast extract. A production of 5128 mg/l, which was in agreement with the prediction, was observed in verification experiment. In comparison to the production of original level (3528 mg/l), 1.45-fold increase had been obtained.     

Optimization of medium composition for actinorhodin production by Streptomyces coelicolor A3(2) with response surface methodology

Optimization of the fermentation medium for maximization of actinorhodin production by Streptomyces coelicolor A3(2) was carried out. Response surface methodology (RSM) was applied to optimize the medium constituents. A 2⁴ full-factorial central composite design (CCD) was chosen to explain the combined effects of the four medium constituents, viz. sucrose, glucose, yeast extract (YE) and peptone, and to design a minimum number of experiments. The P-values of the coefficients for linear, quadratic and cross-product effect of sucrose and glucose concentration were <0.0001, suggesting that these were critical variables having the greatest effect on the production of actinorhodin in the complex medium. The optimized medium consisting of 339 g/l sucrose, 1 g/l glucose, 1.95 g/l YE and 2.72 g/l peptone predicted 195 mg/l of actinorhodin which was 32% higher than that of the unoptimized medium. The amounts of glucose, YE and peptone required were also reduced with RSM.     

Production of ethanol from molasses at 45 °C using alginate-immobilized Kluyveromyces marxianus imb3

The thermotolerant, ethanol-producing yeast strain, Kluyveromyces marxianus IMB3, has been immobilized in calcium alginate matrices. The ability of the biocatalyst to produce ethanol from cane molasses originating in Guatemala, Honduras, Senegal, Guyana and the Philippines was examined. In each case the molasses was diluted to yield a sugar concentration of 140?g/l and fermentations were carried out in batch-fed mode at 45?°C. During the first 24 hours, the maximum ethanol concentrations obtained ranged from 43–57?g/l with optimum production on the molasses from Honduras. Ethanol production during subsequent re-feeding of the fermentations at 24-hour intervals over a 120-hour period, decreased steadily to concentrations ranging from 20–36?g/l and it was found that ethanol productivity remained highest in fermentations containing the molasses from Guyana. When each set of fermentations was re-fed at 120?h and allowed to continue for 48?h, ethanol production again increased to a maximum with concentrations ranging from 25–52?g/l. It was also found however, that increasing the time between re-feeding at this stage in fermentation had a detrimental effect on the functionality of the biocatalyst.     

Production of poly-b-hydroxybutyrate by Azotobacter vinelandii in a two-stage fermentation process

Poly-b-hydroxybutyrate (PHB) production in Azotobacter vinelandii UWD, a mutant that produces PHB constitutively, was suppressed by high aeration of beet molasses medium. Thus a two-stage process was designed using aeration to promote growth and suppress PHB production in the first phase, while lower aeration of raw sugar medium containing fish peptone was used to promote PHB formation in the second phase. A PHB yield of 36 g/l and productivity of > 1 g polymer l -1 .h was obtained by this approach.     

Optimization of pH,Temperature and Inoculum Ratio for the Production of β‐D‐Galactosidase by Kluyveromyces marxianus Using a Lactose‐free Medium

The pH, temperature and inoculum ratio for the production of β‐galactosidase by Kluyveromyces marxianus CDB 002 were optimized using sugar‐cane molasses (100 g/l) in a lactose‐free medium. The temperature optimum was evaluated in the range from 28–37 °C. Lactase production was initiated after substrate consumption indicating a reversible enzyme inhibition or catabolic repression. The specific enzyme activity after 45 h was between 456.3 U/g cell mass (37 °C) and 733.3 U/g (34 °C), whereas the highest volumetric activity was obtained at 30 °C: 21.8 U/ml. This is generally consistent with results from other authors that used whey as a carbon source. Ethanol as a by‐product reached its maximum concentration after 10–14 h (31.1–40.5 g/l), but was completely consumed afterwards. A pH of 5.5 without further control gave the best production rate for lactase (484.4 U/l × h). In this process, the pH was stable during cell growth at 5.5 and then went up to pH 7.2 after 45 h. At a fixed pH of 5.5 or 6.5, the production rates achieved 313.3 U/l × h and 233.3 U/ l × h, respectively. These results differed from those of other authors, who suggested a fixed pH at 7.0 using whey as a carbon source. There were no significant differences between inoculum ratios of 1% [v/v] and 10% [v/v] so that 1% is the preferable ratio as it is cheaper. Yeast extract (10 g/l) and peptone (20 g/l) were used as the vitamin and nitrogen source, respectively, for the studies of temperature and pH. These were substituted by corn steep liquor (100 g/l) for inoculum ratio experiments. Production of lactase using sugar cane molasses in a lactose‐free medium gave better enzyme productivity rates than obtained by other authors using whey. The optimum conditions for β‐galactosidase synthesis were a temperature of 30–34 °C and an inoculum ratio of 1% [v/v], an initial pH of 5.5 without any further control or a control of 5.5 during cell growth. Then the pH was raised up to 7.     

Production of bacterial cellulose by Acetobacter xylinum BPR2001 using molasses medium in a jar fermentor

Bacterial cellulose (BC) production by Acetobacter xylinum subsp. sucrofermentans BPR2001 using molasses medium was carried out in a jar fermentor. When molasses was subjected to H₂SO₄-heat treatment, the maximum BC concentration increased to 76% more than that achieved using untreated molasses, and the specific growth rate increased 2-fold. When the initial sugar concentrations in the H₂SO₄-heat treated molasses were varied from 23 g/l to 72 g/l, BC concentration, production rate, and yield were maximum at sugar concentrations of 23 g/l and 37 g/l, and production of by-products, such as polysaccharides and CO₂, was lower than at sugar concentrations of 48 g/l and 72 g/l, indicating that maintaining a lower molasses concentration is essential for efficient BC production in jar fermentors, this being due mainly to the complex nature of molasses. Molasses has a clear advantage over pure sugars as a carbon source from an economic viewpoint.     

STATISTICAL MEDIA OPTIMIZATION FOR THE BIOMASS PRODUCTION OF POSTHARVEST BIOCONTROL YEAST Rhodosporidium paludigenum

A cane molasses-based medium for the biomass production of biocontrol agent Rhodosporidium paludigenum was statistically optimized. Molasses concentration (after pretreatment), yeast extract, and initial pH were identified by the Plackett–Burman design to show significant influence on the biomass production. The three factors were further optimized by central composite design and response-surface methodology. The statistical analysis indicated the optimum values of the variables were 89.98 g/L for cane molasses, 2.35 g/L for yeast extract and an initial pH of 8.48. The biomass yield at the optimal culture achieved 15.89 g/L in flask fermentation, which was 2.1 times higher than that at the initial NYDB medium. In a 10-L fermenter, 18.97 g/L of biomass was obtained after 36 hr of cultivation. Moreover, the biocontrol efficacy of the yeast was investigated after culture optimization. The results showed the yeast harvested in the optimal medium maintained its initial biocontrol properties by reducing the percentage of decayed apples to below 20%.     

Use of a sequential strategy of experimental design to optimize the inulinase production in a batch bioreactor

A potential application of inulinase in the food industry is the production of fructoligosaccharides (FOS) by the transfructosilation of sucrose. The FOSs present many interesting functional properties besides their ability to increase the shelf-life and flavor of many products. The use of an industrial medium represents a good alternative to producing inulinase at low cost, since the activity may improve, or at least remain the same, as that obtained using a synthetic medium. This work was an optimization study of the inulinase production by Kluyveromyces marxianus NRRL Y-7571 using industrial pre-treated culture medium in a bioreactor employing a sequential strategy of experimental design. Initially, a Plackett–Burman (Screening Design) design was used, where the studied variables were molasses, corn steep liquor, yeast extract concentration, and agitation and aeration rates. After the analysis of the effects, a central composite rotational design (CCRD) was carried out. The optimized condition for the inulinase production was: 250 g/l of molasses, 80 g/l of corn steep liquor, 6 g/l of yeast extract, 300 rpm of agitation and 1.5 vvm aeration rate, which resulted in an enzymatic activity of 1,317 ± 65 U/ml.     

Isomaltulose production using free cells: optimisation of a culture medium containing agricultural wastes and conversion in repeated-batch processes

The enzyme glucosyltransferase is an industrially important enzyme since it produces non-cariogenic isomaltulose (6-O-alpha-D-glucopyronosyl-1-6-D-fructofuranose) from sucrose by intramolecular transglucosylation. The experimental designs and response surface methodology (RSM) were applied for the optimisation of the nutrient concentrations in the culture medium for the production of glucosyltransferase by Erwinia sp. D12 in shaken flasks at 200 rpm and 30 degrees C. A statistical analysis of the results showed that, in the range studied, the factors had a significant effect (P < 0.05) on glucosyltransferase production and the highest enzyme activity (10.84 U/ml) was observed in culture medium containing sugar cane molasses (150 g l(-1)), corn steep liquor (20 g l(-1)), yeast extract Prodex Lac SD (15 g l(-1)) and K2HPO4 (0.5 g l(-1)) after 8 h at 30 degrees C. The production of cell biomass by the strain of Erwinia sp. D12 was carried out in a 6.6-l fermenter with a mixing rate of 200 rpm and an aeration rate of 1 vvm. Fermentation time, cellular growth, medium pH and glucosyltransferase production were observed. The greatest glucosyltransferase activity was 22.49 U/ml, obtained after 8 h of fermentation. The isomaltulose production from sucrose was performed using free Erwinia sp. D12 cells in a batch process using an orbital shaker. The influence of the parameters sucrose concentration, temperature, pH, and cell concentration on the conversion of sucrose into isomaltulose was studied. The free cells showed a high conversion rate of sucrose into isomaltulose using batch fermentation, obtaining an isomaltulose yield of 72.11% from sucrose solution 35% at 35 degrees C.