Optimization of probiotic and lactic acid production by Lactobacillus plantarum in submerged bioreactor systems

Biomass and lactic acid production by a Lactobacillus plantarum strain isolated from Serrano cheese, a microorganism traditionally used in foods and recognized as a potent probiotic, was optimized. Optimization procedures were carried out in submerged batch bioreactors using cheese whey as the main carbon source. Sequential experimental Plackett–Burman designs followed by central composite design (CCD) were used to assess the influence of temperature, pH, stirring, aeration rate, and concentrations of lactose, peptone, and yeast extract on biomass and lactic acid production. Results showed that temperature, pH, aeration rate, lactose, and peptone were the most influential variables for biomass formation. Under optimized conditions, the CCD for temperature and aeration rate showed that the model predicted maximal biomass production of 14.30 g l⁻¹ (dw) of L. plantarum. At the central point of the CCD, a biomass of 10.2 g l⁻¹ (dw), with conversion rates of 0.10 g of cell g⁻¹ lactose and 1.08 g lactic acid g⁻¹ lactose (w/w), was obtained. These results provide useful information about the optimal cultivation conditions for growing L. plantarum in batch bioreactors in order to boost biomass to be used as industrial probiotic and to obtain high yields of conversion of lactose to lactic acid.     

Improved xylanase production using apple pomace waste by Aspergillus niger in koji fermentation

Xylanase production by Aspergillus niger NRRL‐567 in solid‐state fermentation (koji fermentation) was optimized using 2⁴ factorial design and response surface methodology. The evaluated variables were the initial moisture level and concentration of inducers [veratryl alcohol (VA), copper sulphate (CS), and lactose (LAC)], leading to the response of xylanase production. Initial moisture level and LAC were found to be the most significant variable for xylanase production (p<0.05). The highest xylanase production was observed with 3578.8 ± 65.3 IU/gds (gram dry substrate) under optimal conditions using initial moisture of 85% (v/w), pH 5.0 and inducers VA (2 mM/kg), LAC 2% (w/w), and CS (1.5 mM/kg) after 48 h of incubation time. Higher xylanase activity of 3952 ± 78.3 IU/gds was attained during scale‐up of the process in solid‐state tray fermentation under optimum conditions after 72 h of incubation time. The present study demonstrates that A. niger NRRL‐567 can efficiently be used to achieve xylanase production with an economical and environmental benefit in solid‐state tray fermentation. The developed process can be used to develop an effective process for commercially feasible bioproduction of xylanases for speciality applications, such as conversion of lignocellulosic biomass to biofuels and other value‐added products.     

Optimization of Cultivating Conditions for Triterpenoids Production from Antrodia cinnmomea

The submerged cultivating conditions for triterpenoids production from Antrodia cinnamomea were optimized using uniform design method and the one-factor-at-a-time method was adopted to investigate the effect of plants oils and glucose supply on triterpenoids production and mycelia growth. Corn starch and culturing time were identified as more significant variables for triterpenoids production. The optimal conditions for triterpenoids production was 20.0 g/L corn starch, 20.0 g/L wheat bran, 1.85 g/L MgSO4, initial pH 3 and 16 days of cultivation. In addition, investigation of plant oils and glucose supply showed that 0.3 % (v/v) olive oil supply at the beginning of fermentation stimulated mycelia growth and significantly increased triterpenoids production; 0.2 % (w/v) glucose supplement at 10th day enhanced production of triterpenoids with slight effect on biomass, which is reported for the first time. The triterpenoids production experimentally obtained under the optimal conditions was 7.23 % (w/w). The uniform design method may be used to optimize many environmental and genetic factors such as temperature and agitation that can also affect the triterpenoids production from A. cinnamomea.     

Breeding of high ergosterol-producing yeast strains

High ergosterol-producing yeast strains YEH-28 and YEH-56 were constructed by hybridization of two haploids with opposite mating types from different species. The fermentation conditions of hybrid strain YEH-56 were studied. The highest level of ergosterol was obtained in 30 h at 28°C and 200 rpm, when 60 ml of culture in 250-ml shake flasks was grown in fermentation medium that consisted of (per liter): 100 g glucose; 10 g peptone and 10 g yeast extract. The initial pH was adjusted to 6.0. The optimal inoculum volume was 10% (v/v). Under optimal conditions, the yield of ergosterol of YEH-28 strain is 1.96 and 1.56 times that of the parental strains YE39 and YE244, whereas that of YEH-56 is 1.98 and 1.57 times that of the parental strains YE39 and YE244, respectively. Analysis of genetic stability showed that hybrid strains YEH-28 and YEH-56 are stable genetically. Journal of Industrial Microbiology & Biotechnology (2000) 25, 39–44. Received 13 November 1999/ Accepted in revised form 09 March 2000     

Response Surface Optimization of Lyoprotectant for Lactobacillus bulgaricus During Vacuum Freeze-Drying

The individual and interactive effects of skimmed milk powder, lactose, and sodium ascorbate on the number of viable cells and freeze-drying survival for vacuum freeze-dried powder formulation of Lactobacillus bulgaricus were studied by response surface methodology, and the optimal compound lyoprotectant formulations were gained. It is shown that skim milk powder, lactose, and sodium ascorbate had a significant impact on variables and survival of cultures after freeze-drying. Also, their protective abilities could be enhanced significantly when using them as a mixture of 28% w/v skim milk, 24% w/v lactose, and 4.8% w/v sodium ascorbate. The optimal freeze-drying survival rate and the number of viable cells of Lactobacillus bulgaricus were observed to be (64.41 ± 0.02)% and (3.22 ± 0.02) × 10¹¹ colony-forming units (CFU)/g using the optimal compound protectants, which were very close to the expected values 64.47% and 3.28 × 10¹¹ CFU/g.     

Lactosucrose bioconversion from lactose and sucrose by whole cells of Paenibacillus polymyxa harboring levansucrase activity

Lactosucrose, a functional trisaccharide, was produced from lactose as an acceptor and sucrose as a fructosyl donor by whole cells harboring transfructosylation activity of levansucrase. Levansucrase-induced cells of Paenibacillus polymyxa were obtained in the medium containing sucrose, and the transfructosylation activity in the whole cell was optimized for lactosucrose production. The optimal cell concentration, substrates ratio, temperature, and pH were 2.0% (w/v), 22.5% (w/v) lactose and 22.5% (w/v) sucrose, 55 degrees C, and 6.0, respectively. Under these conditions, the whole cells produced approximately 17.0% (w/v) lactosucrose in 6 h of reaction time with a productivity of 2.8% (w/v)/h.     

Statistical Optimization of Alkaline Protease Production from Penicillium citrinum YL-1 Under Solid-State Fermentation

Proteases from halotolerant and halophilic microorganisms were found in traditional Chinese fish sauce. In this study, 30 fungi were isolated from fermented fish sauce in five growth media based on their morphology. However, only one strain, YL-1, which was identified as Penicillium citrinum by internal transcribed spacer (ITS) sequence analysis, can produce alkaline protease. This study is the first to report that a protease-producing fungus strain was isolated and identified in traditional Chinese fish sauce. Furthermore, the culture conditions of alkaline protease production by P. citrinum YL-1 in solid-state fermentation were optimized by response surface methodology. First, three variables including peptone, initial pH, and moisture content were selected by Plackett–Burman design as the significant variables for alkaline protease production. The Box–Behnken design was then adopted to further investigate the interaction effects between the three variables on alkaline protease production and determine the optimal values of the variables. The maximal production (94.30 U/mL) of alkaline protease by P. citrinum YL-1 took place under the optimal conditions of peptone, initial pH, and moisture content (v/w) of 35.5 g/L, 7.73, and 136%, respectively.     

Bioproduction of hydrolytic enzymes using apple pomace waste by A. niger: applications in biocontrol formulations and hydrolysis of chitin/chitosan

Studies were carried out for β-glucosidase production using apple pomace (AP) in solid-state fermentation using 2⁴ factorial design and response surface methodology. The influence of four independent variables including initial moisture level and inducers [veratryl alcohol (VA), lactose (LAC) and copper sulfate (CS)] was studied. The experimental design showed that initial moisture level had significant negative effect on the response. Higher β-glucosidase activity of 64.18 IU/gram fermented substrate (gfs) was achieved in solid-state tray fermentation with optimum conditions having initial moisture level 55% (v/w), pH 4.5, 2 mM/kg VA, 2% (w/w) LAC and 1.5 mM/kg CS concentration, respectively,. The non-specific chitinase 70.28 ± 6.34 IU/gfs and chitosanase activities 60.18 ± 6.82 to 64.20 ± 7.12 IU/gfs were observed. The study demonstrated that AP can be potentially used for the β-glucosidase production by Aspergillus niger. Moreover, β-glucosidase can be used for the hydrolysis of chitin/chitosan to depolymerized products and in the formulation of biocontrol agents for enhanced entomotoxicity levels.     

Improvement of covalent immobilization procedure of β‐galactosidase from Kluyveromyces lactis for galactooligosaccharides production: Modeling and kinetic study

Galactooligosaccharides (GOS) are prebiotics produced from lactose through an enzymatic reaction. Employing an immobilized enzyme may result in cost reductions; however, the changes in its kinetics due to immobilization has not been studied. This study experimentally determined the optimal reaction conditions for the production of GOS from lactose by β‐galactosidase (EC 3.2.1.23) from Kluyveromyces lactis covalently immobilized to a polysiloxane‐polyvinyl alcohol (POS‐PVA) polymer activated with glutaraldehyde (GA), and to study the transgalactosylation kinetics. Yield immobilization was 99 ± 1.1% with 78.5 ± 2.4% enzyme activity recovery. An experimental design 24 with 1 center point and 2 replicates was used. Factors were lactose [L], enzyme concentration [E], pH and temperature (T). Response variables were glucose and galactose as monosaccharides [G1], residual lactose [Lac]r and GOS as disaccharides [G2] and trisaccharides [G3]. Best conditions were pH 7.1, 40 °C, 270 gL^?1 initial lactose concentration and 6 U mL^?1 enzyme concentration, obtaining 25.46 ± 0.01 gL^?1 yield of trisaccharides. Although below the HPLC‐IR detection limit, tetrasaccharides were also identified after 115 min of reaction. The immobilization protocol was then optimized by diminishing total reactant volumes : support ratio, resulting in improved enzyme activity synthesizing 43.53 ± 0.02 gL^?1 of trisaccharides and 13.79 ± 0.21 gL^?1 of tetrasaccharides, and after four cycles remaining relative activity was 94%. A reaction mechanism was proposed through which a mathematical model was developed and rate constants were estimated, considering a pseudo steady‐state hypothesis for two concomitant reactions, and from this simplified analysis, the reaction yield could eventually be improved. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1568–1578, 2017     

Medium optimization of a hydrophilic solvent‐stable protease from Serratia sp. SYBC H

Two statistical methods were used for medium optimization for a hydrophilic solvent‐stable protease production by Serratia sp. SYBC H with duckweed as the nitrogen source. Orthogonal design was applied to find the significant variables, then response surface methodology (RSM), including Box–Behnken central composite experiments, was used to determine the optimal concentrations and interaction of the significant variables. Results demonstrated that duckweed powder, wheat flour, Tween 80, sodium chloride had significant effects on the solvent‐stable protease production. The interaction between duckweed and wheat flour was significant. The optimal level of the variables for the maximum protease production was duckweed 43.9 g/L, wheat flour 20 g/L, sodium chloride 0.08 M, Tween 80 1% v/v, initial pH 11.0, and inoculum size 7% v/v. The maximum protease activity reached 1922.8 U/mL in the optimized medium, with about 18.3‐fold higher than that in the unoptimized medium. Most importantly, the protease from Serratia sp. SYBC H has successfully catalyzed the specific acylation of sucrose in a two‐solvent medium consisting of pyridine and n‐hexane (1:1, v/v), and non‐specific acylation of sucrose in anhydrous DMSO. These results demonstrated that the protease from Serratia sp. SYBC H is a solvent‐stable protease and it could be an ideal biocatalyst for sugar esters syntheses in non‐aqueous media.     

Microencapsulation of alpha-tocopherol using sodium alginate and its controlled release properties

Response surface methodology (RSM) was used to optimize microencapsulation yield (MY) using three independent variables; the ratio of coating material to core material (w/w, X1), the emulsifier concentration (%, v/v, X2), and the CaCl2 concentration (%, w/v, X3). In the preparation of sodium alginate (SA) microcapsule, the regression model equation for the MY was predicted as follows; MY(%) = 56.02 + 3.64X2 + 3.18X1X2 - 3.74X2(2). The optimal conditions for the SA microcapsule were obtained at the [SA]/[alpha-TP] ratio of 6.6:3.4 (w/w), [emulsifier] of 1.35% (v/v), and [CaCl2] of 4.3% (w/v), and the predicted MY in this condition was of 57.2%. In vitro alpha-TP releasing test of the SA-based microcapsules was performed. The SA microcapsule released 28.8% of alpha-TP when exposed in the simulated gastric fluid (SGF, pH 1.2) for 24 h. In the simulated intestinal fluid (SIF, pH 7.4), the amount of released alpha-TP (81.5%) was significantly greater than that in the SGF. The duration time required for releasing 50 (T50%) and 70% (T70%) of alpha-TP from the SA-microcapsule were calculated to be 3.8 and 12.3 h, respectively. From these results, it was suggested that SA microcapsule would be structurally resistant against acidic environment, and it would rapidly release core material under mild alkali condition.     

Batch fermentation of whey ultrafiltrate by Lactobacillus helveticus for lactic acid production

Summary Cheese whey ultrafiltrate (WU) was used as the carbon source for the production of lactic acid by batch fermentation with Lactobacillus helveticus strain milano. The fermentation was conducted in a 400 ml fermentor at an agitation rate of 200 rpm and under conditions of controlled temperature (42° C) and pH. In the whey ultrafiltrate-corn steep liquor (WU-CSL) medium, the optimal pH for fermentation was 5.9. Inoculum propagated in skim milk (SM) medium or in lactose synthetic (LS) medium resulted in the best performance in fermentation (in terms of growth, lactic acid production, lactic acid yield and maximum productivity of lactic acid), as compared to that propagated in glucose synthetic (GS) medium. The yeast extract ultrafiltrate (YEU) used as the nitrogen/growth factor source in the WU medium at 1.5% (w/v) gave the highest maximum productivity of lactic acid of 2.70 g/l-h, as compared to the CSL and the tryptone ultrafiltrate (TU). L. helveticus is more advantageous than Streptococcus thermophilus and Lactobacillus delbrueckii for the production of lactic acid from WU. The L. helveticus process will provide an alternative solution to the phage contamination in dairy industries using Lactobacillus bulgaricus.     

Pilot-scale production of carboxymethylcellulase from rice hull by Bacillus amyloliquefaciens DL-3

Optimal conditions for pilot-scale production of the carboxymethylcellulase (CMCase) by Bacillus amyloliquefaciens DL-3 were investigated. The best carbon and nitrogen sources for the production of CMCase by B. amyloliquefaciens DL-3 were found to be rice hull and peptone and their optimal concentrations were 5.0 and 0.20% (w/v), respectively. Optimal temperature and initial pH for the production of CMCase were 37°C and 6.8. Optimal agitation speed and aeration rate for the production of CMCase were 300 rpm and 1.0 vvm in a 7 L bioreactor, which were different from those for the cell growth of B. amyloliquefaciens DL-3. The highest productions of CMCase by B. amyloliquefaciens DL-3 from 5.0% (w/v) rice hull as a carbon source under optimal conditions in a 7 or 100 L bioreactor were 220 and 367 U/mL, respectively.     

Optimization of fermentation conditions and rheological properties of exopolysaccharide produced by deep-sea bacterium Zunongwangia profunda SM-A87

Zunongwangia profunda SM-A87 isolated from deep-sea sediment can secrete large quantity of exopolysaccharide (EPS). Response surface methodology was applied to optimize the culture conditions for EPS production. Single-factor experiment showed that lactose was the best carbon source. Based on the Plackett–Burman design, lactose, peptone and temperature were selected as significant variables, which were further optimized by the steepest ascent (descent) method and central composite design. The optimal culture conditions for EPS production and broth viscosity were determined as 32.21 g/L lactose, 8.87 g/L peptone and an incubation temperature of 9.8°C. Under these conditions, the maximum EPS yield and broth viscosity were 8.90 g/L and 6551 mPa•s, respectively, which is the first report of such high yield of EPS from a marine bacterium. The aqueous solution of the EPS displayed high viscosity, interesting shearing thinning property and great tolerance to high temperature, a wide range of pH, and high salinity.     

出芽短梗霉Aureobasidium sp. SRF的菌株特性分析及胞外多糖结构鉴定

菌株SRF是1株从意大利树莓(Rubus corchorifolius)果实表面分离、可产胞外多糖的新菌株。在鉴定其分类归属的基础上,对其产生的胞外多糖进行了结构分析和发酵条件优化,为寻找微生物多糖提供新的菌株,为开发利用资源微生物提供借鉴。通过形态学和ITS序列对比分析进行菌株鉴定;通过薄层层析和红外光谱分析,确定胞外多糖结构;通过单因素检测试验,确定影响产糖量的主要因素;响应面Plackett-Burman和Box-Behnken设计筛选发酵产胞外多糖的最优条件。结果表明,出发菌株SRF隶属于出芽短梗霉属,命名为Aureobasidium sp. SRF;SRF所产胞外多糖为普鲁兰多糖;单因素检测表明,对多糖产量影响最大的因素为碳源浓度、氮源浓度、无机离子浓度,其次是碳源、氮源、无机离子、pH值;根据响应面结果确定最优发酵条件为麦芽糖8%(质量分数)、酵母提取物3%(质量分数)、钙离子0.3 g/L、pH 6,产糖量达5.93 g/L。SRF是1株来源于树莓浆果表面,可产胞外普鲁兰多糖的出芽短梗霉新菌株,是1株产微生物多糖的候选菌株。     

Production of β-carotene from deproteinized waste whey filtrate using Mucor azygosporus MTCC 414 in submerged fermentation

The cheese whey, a by-product of dairy industry proved to be an attractive substrate for production of β-carotene. The β-carotene production from Mucor azygosporus MTCC 414 by using deproteinized waste whey filtrate under submerged fermentation was investigated. Various fermentation variables, such as lactose content in whey, initial pH, production temperature, incubation time, and carbon and nitrogen sources played significant role on β-carotene production. Maximum β-carotene production (385 μg/g dcw) was obtained with the whey (pH 5.5) containing 3.5% (w/v) lactose supplemented with soluble starch at (1.0%, w/v) at 30°C after a 5 days incubation. Moreover, unlike other microorganisms which utilize pre-hydrolyzed lactose, this Mucor azygosporus MTCC 414 was found to be capable of utilizing unhydrolyzed lactose present in the whey.     

Enhancement of extracellular bispecific anti‐MUC1 nanobody expression in E. coli BL21 (DE3) by optimization of temperature and carbon sources through an autoinduction condition

Escherichia coli is one of the most suitable hosts for production of antibodies and antibody fragments. Antibody fragment secretion to the culture medium improves product purity in cell culture and diminishes downstream costs. In this study, E. coli strain BL21 (DE3) harboring gene encoding bispecific anti‐MUC1 nanobody was selected, and the autoinduction methodology for expression of bispecific anti‐MUC1 nanobody was investigated. Due to the replacement of IPTG by lactose as inducer, less impurity and toxicity in the final product were observed. To increase both intracellular and extracellular nanobody production, initially, the experiments were performed for the key factors including temperature and duration of protein expression. The highest amount of nanobody was produced after 21 h at 33°C. The effect of different carbon sources, glycerol, glucose, lactose, and glycine as a medium additive at optimum temperature and time were also assessed by using response surface methodology. The optimized concentrations of carbon sources were obtained as 0.75% (w/v), 0.03% (w/v), 0.1% (w/v), and 0.75% (w/v) for glycerol, glucose, lactose, and glycine, respectively. Finally, the production of nanobody in 2 L fermenter under the optimized autoinduction conditions was evaluated. The results show that the total titer of 87.66 µg/mL anti‐MUC1 nanobody, which is approximately seven times more than the total titer of nanobody produced in LB culture medium, is 12.23 µg/L .     

Enhancement of carotenoids and lipids production by oleaginous red yeast Sporidiobolus pararoseus KM281507

Bioconversion of biodiesel-derived crude glycerol into carotenoids and lipids was investigated by a microbial conversion of an oleaginous red yeast Sporidiobolus pararoseus KM281507. The methanol content in crude glycerol (0.5%, w/v) did not show a significant effect on biomass production by strain KM281507. However, demethanolized crude glycerol significantly supported the production of biomass (8.64?±?0.13?g/L), lipids (2.92?±?0.03?g/L), β-carotene (15.76?±?0.85?mg/L), and total carotenoids (33.67?±?1.28?mg/L). The optimal conditions suggested by central composite design were crude glycerol concentration (55.04?g/L), initial pH of medium (pH 5.63) and cultivation temperature (24.01°C). Under these conditions, the production of biomass, lipids, β-carotene, and total carotenoids were elevated up to 8.83?±?0.05, 4.00?±?0.06?g/L, 27.41?±?0.20, and 53.70?±?0.48?mg/L, respectively. Moreover, an addition of olive oil (0.5???2.0%) dramatically increased the production of biomass (14.47?±?0.15?g/L), lipids (6.40?±?0.09?g/L), β-carotene (54.43?±?0.95?mg/L), and total carotenoids (70.92?±?0.51?mg/L). The oleic acid content in lipids was also increased to 75.1% (w/w) of total fatty acids, indicating a good potential to be an alternative biodiesel feedstock. Meanwhile, the β-carotene content in total carotenoids was increased to 76.7% (w/w). Hence, strain KM281507 could be a good potential source of renewable biodiesel feedstock and natural carotenoids.     

Effective enhancement of polylactic acid-degrading enzyme production by Amycolatopsis sp. strain SCM_MK2-4 using statistical and one-factor-at-a-time approaches

This study aims to find the optimal medium and conditions for polylactic acid (PLA)-degrading enzyme production by Amycolatopsis sp. SCM_MK2-4. Screening of the most effective components in the enzyme production medium by Plackett–Burman design revealed that the silk cocoon and PLA film were the most significant variables enhancing the PLA-degrading enzyme production. After an response surface methodology, a maximum amount of PLA-degrading enzyme activity at 0.74?U?mL^?1 was predicted and successfully validated at 95% after 0.39% (w/v) silk cocoon and 1.62% (w/v) PLA film were applied to the basal medium. The optimal initial pH value, temperature, and inoculum size were evaluated by a method considering one-factor-at-a-time. The values were recorded at an initial pH in the range of 7.5–9.0, a temperature of 30–32°C, and an inoculum size of 4–10%. The highest activity of approximately 0.95?U?mL^?1 was achieved after 4 days of cultivation using the optimized medium and under optimized conditions in a shake flask. Upscaling to the use of a 3-L stirred tank fermenter was found to be successful with a PLA-degrading activity of 5.53?U?mL^?1; which represents a 51-fold increase in the activity compared with that obtained from the nonoptimized medium and conditions in the shake flask.     

Production of Extracellular Halo-alkaline Protease from a Newly Isolated Haloalkaliphilic Bacillus sp. Isolated from Seawater in Western India

Summary Haloalkaliphilic, gram positive, aerobic, coccoid Bacillus sp. Po2 was isolated from a seawater sample in Gujarat, India. On the basis of 16s rRNA gene homology, Po2 was 95% related to Bacillus pseudofirmus. A substantial level of extracellular alkaline protease was produced by Po2, which corresponded with the growth and reached a maximum level (264 U/ml) during the stationary phase at 24 h. The production thereafter remained nearly static at optimal level till 36 h. Po2 could grow in the range of 0–20% NaCl (w/v) and pH 7–9, optimally at 10% NaCl (w/v) and pH 8. The protease production was salt-dependent and optimum production required 15% NaCl (w/v) and pH 8. Among the organic nitrogen sources, optimum growth and protease production (260 U/ml) were supported by the combination of peptone and yeast extract. However, growth and protease production were highly suppressed by the inorganic nitrogen sources used; with the exception of potassium nitrate, which supported both growth and protease production to limited extent (24 U/ml). Strong inhibition of enzyme production was observed at above 1% glucose (w/v). Wheat flour served as both carbon and nitrogen source supporting growth and protease production.