Application of factorial designs for optimization of cyclodextrin glycosyltransferase production from Klebsiella pneumoniae pneumoniae AS-22.

Production of cyclodextrin glycosyltransferase (CGTase) from Klebsiella pneumoniae pneumoniae AS-22 was optimized in shake flasks using a statistical experimental design approach. Effect of various components in the basal medium, like carbon, nitrogen, phosphorus, and mineral sources as well as initial pH and temperature, were tested on enzyme production. The optimum concentrations of the selected media components were determined using statistical experimental designs. Two level fractional factorial designs in five variables, namely, dextrin, peptone, yeast extract, ammonium dihydrogen orthophosphate, and magnesium sulphate concentrations were constructed. The optimum medium composition thus found consisted of 49.3 g/L dextrin, 20.6 g/L peptone, 18.3 g/L yeast extract, 6.7 g/L ammonium dihydrogen orthophosphate, and 0.5 g/L magnesium sulphate. The maximum CGTase activity obtained was 21.4 U/mL in 28 h of incubation. The cell growth and CGTase production profiles were studied with the optimized medium in shake flasks and in 1-L fermenters. It was observed that the enzyme production was growth associated both in shake flask and in fermenter, although it was slower in shake flask. The maximum CGTase activity obtained in the fermenter was 32.5 U/mL in 16 h. The optimized medium resulted in about 9-fold increase in the enzyme activity as compared to that obtained in the basal medium in shake flask as well as in fermenter.     

重组Bacillus subtilis产B.stearothermophilus环糊精葡萄糖基转移酶的发酵优化

利用本研究室已构建的重组菌Bacillus subtilis/pBSMuL3-α/β-CGTase对产B.stearothermophilus环糊精葡萄糖基转移酶的发酵产酶进行了优化,考察了培养基中重要成分:碳源、有机氮源、无机氮源、有机与无机氮源质量比、碳源与氮质量比、金属离子种类等单因素对该重组菌产α/β-CGTase的影响,并采用正交实验对发酵培养基进行优化,对优化结果分析可知,重组菌B.subtilis/pBSMuL3-α/β-CGTase发酵产α/β-CGTase的最优培养基成本为:葡萄糖5 g/L,氮源(鱼骨蛋白胨∶NH4Cl=3∶1)25 g/L,1 mmol/L Mg^2+。在最优条件下发酵培养,α/β-CGTase的酶活由原来TB发酵培养基的9.20 U/mL提高至20.32 U/mL,是优化前酶活的2.2倍,为α/β-环糊精葡萄糖基转移酶的工业应用提供了理论支持。     

Mixed carbon source control strategy for enhancing alginate lyase production by marine Vibrio sp. QY102

Medium and culture conditions for alginate lyase production by marine Vibrio sp. QY102 were first optimized using statistical methods including Plackett–Burman design and central composite design. Then, fermentation in 5-L bioreactor showed that alginate acted as easily used carbohydrate for Vibrio sp. QY102, while starch extended its growth phase and stabilized pH variations. Thus, a novel strategy using mixed carbon sources was proposed that starch supported growth while enzyme synthesis was induced by pulse feedings of solid alginate. The optimized process followed that Vibrio sp. QY102 grew on starch until the end of the logarithmic growth phase, and then solid alginate was added as 1 g/L every 3 h. Meanwhile, initial pH 5.0 and natural pH during fermentation was favorable for alginate lyase production. After optimization, the highest alginate lyase production reached 52.8 U/mL, which was 329 % higher than the control. Finally, fermentation scale-up was performed in 30-L bioreactor and the maximum alginate lyase production was obtained as 46.8 U/mL.     

一株产环糊精葡萄糖基转移酶的地衣芽孢杆菌的选育、产酶条件及酶学特性

从土壤分离物中筛选到一株环糊精葡萄糖基转移酶 (CGTase)产生菌 4 0 3,96h发酵酶活为 0 95U mL。经紫外辐射和硫酸二乙酯复合诱变而获得突变株CLS4 0 3,96h发酵酶活达 1 36U mL ,提高 4 3%。该突变菌株被鉴定为地衣芽孢杆菌 (Bacilluslicheniformis) ,产CGTase的最佳碳源为可溶性淀粉 ,最佳氮源为硝酸铵 ,最适初始pH为 6 5 ,最适培养温度为 35℃ ,发酵期间CGTase的产生高峰 (第 96h)滞后于菌体生物量高峰 (第 4 8h) 2d。菌株所产CGTase的最适反应pH为 6 0 ,最适温度为 5 5℃ ,在pH 6 0～ 7 5间和 5 0℃下保持 1h后的剩余酶活均达 90 %以上 ;酶液中适量添加Ca2 能大幅提高CGTase在 5 5℃下的稳定性。经高效液相色谱分析 ,CGTase作用于淀粉后的产物以α 环糊精为主 ,β 环糊精为次 ,二者比例为 2 4 7∶1,环糊精总产率达 2 9 8% ,但产物中不含γ 环糊精     

Secretion of cyclodextrin glucanotransferase in E. coli using Bacillus subtilis lipase signal peptide and optimization of culture medium

The cyclodextrin glycosyltransferase (CGTase) of Paenibacillus pabuli US132 was fused to the secretive lipase signal peptide of B. subtilis. This leads to an efficient secretion of the recombinant enzyme into the culture medium of E. coli as an active and soluble form contrasting with the native construction leading to a periplasmic production. In order to enhance the yield of CGTase production, an experimental design methodology was applied for the optimization of the culture composition. Hence, the media components were submitted to preliminary screening using a Plakett-Burman design. The concentrations of the major operating ones were then optimized to enhance the secretion of CGTase using response surface methodology. The findings revealed that concentrations of 0.5% potato starch, 3% yeast extract, 3% tryptone, 1.5% casein hydrolysate, 0.5% NaCl, 0.2% KH2PO4, and 0.02% MgSO4 were the optimal conditions for CGTase production. The experimental value (9.43 U/mL) obtained for CGTase activity was very close to the predicted value (9.27 U/mL).     

Enzymatic production of cyclodextrins from milled corn starch in an ultrafiltration membrane bioreactor

Cyclodextrin glycosyltransferase (CGTase) was found to be severely inhibited by cyclodextrins. In order to increase the conversion yield by reducing product inhibition and reuse the CGTase in the production of cyclodextrins from milled corn starch, an ultrafiltration membrane bioreactor system was employed. In a batch operation with ultrafiltration, the conversion yield was increased 57% compared with that without ultrafiltration. Operating conditions for the continuous production of cyclodextrins in the membrane bioreactor were optimized by taking into consideration the filtration rate and the conversion yield as follows: initial starch concentration, 7% (w/v); starch feeding rate, 240 mg/h; CGTase loading, 350 units/initial gram starch. When cyclodextrins were continuously produced in the membrane bioreactor under optimized conditions, 340 units of CGTase was require to produce 1 g of cyclodextrins for 48 h, while in the case of conventional batch operation, 1 g of cyclodextrins was produced for 24 h by 1410 units of CGTase. (c) 1993 John Wiley & Sons, Inc.     

Optimisation of growth medium for the production of cyclodextrin glucanotransferase from Bacillus stearothermophilus HR1 using response surface methodology

Cyclodextrin glucanotransferase (CGTase) activity was observed when the bacterium was grown in the medium at various initial pH values, containing carbon, nitrogen, phosphorus and mineral salt sources at 50 °C for 24 h in the shake flasks. The optimisation of this growth medium was carried out using response surface methodology. The design contains a total of 32 experimental trials involving 10 star points and 6 replicates at the centre points. The design was employed by selecting sago starch, peptone from casein, K₂HPO₄, CaCl₂ and initial pH as five independent variables in this study. The optimal calculated values of tested variables for maximal production of CGTase were found to be comprised of: sago starch, 16.02 g/l; peptone from casein, 20 g/l; K₂HPO₄, 1.4 g/l; CaCl₂, 0.2 g/l and initial pH, 7.54 with a predicted CGTase activity of 14.20 U/ml. These predicted optimal parameters were tested in the laboratory and the final CGTase activity obtained was very close to the predicted value at 14.80 U/ml.     

Cyclodextrin glycosyltransferase from Bacillus circulans DF 9R: Activity and kinetic studies

Activity characteristics and kinetic aspects of a cyclodextrin glycosyltransferase (CGTase) from Bacillus circulans DF 9R were studied. A mixture of α-, β- and γ-cyclodextrins (CDs), glucose, maltose and negligible amounts of longer linear dextrins were produced from gelatinized amylose, amylopectin and starch from different sources. In the coupling reaction, CDs were the substrates in the presence of acceptors such as maltose and/or longer oligosaccharides. From oligosaccharides formed by three or more glucose units, this enzyme produced linear chains of several lengths which were then cyclized. CGTase catalytic efficiency was compared employing an analytical grade starch and cassava starch for food use. Since the results obtained were similar for both starches, the use of an economic starch is an advantage. CGTase was inhibited by the substrate and its own products. Starch concentrations over 20 mg/mL inhibited the cyclizing activity. CDs behaved as competitive inhibitors and maltose as an uncompetitive inhibitor while maltotriose showed a mixed inhibition pattern. Limit dextrins showed a scarce inhibitory effect on enzyme activity. CD production could be improved with an ultrafiltration membrane reactor for continuous removal of the products; the starch concentration should be maintained below an inhibitory concentration and limit dextrins would remain in the reactor without affecting enzyme activity.     

重组青霉素G酰化酶拆分制备（S）-邻氯苯甘氨酸

对产青霉素G酰化酶的重组枯草芽胞杆菌发酵产酶条件进行优化,确定优化后的发酵条件：可溶性淀粉10g/L、蛋白胨12g/L、酵母粉3g/L、NaCl10g,／L;pH7．5、培养温度37℃、装液量80mL（500mL三角瓶）、培养28h,青霉素G酰化酶的表达水平由最初的7．34U／mL提高至18．23U／mL。以表达青霉素G酰化酶的枯草芽胞杆菌发酵液为酶源,在水相中对映选择性催化N-苯乙酰-（R,S）-邻氯苯甘氨酸制备（S）-邻氯苯甘氨酸,当底物浓度为100mol／L时转化4h,转化率达44．2％。对底物浓度为80mmoL／L反应液中的（S）-邻氯苯甘氨酸进行分离,达到理论收率的94．29％（以N-苯乙酰-（R,S）-邻氯苯甘氨酸的0．5倍摩尔量为理论产率）,e．e．值大于99．9％。170℃条件下,N-苯乙酰-（R）-邻氯苯甘氨酸与苯乙酸共熔消旋为N-苯乙酰-（R,S）-邻氯苯甘氨酸可用于循环拆分。     

Optimization of nutrients for the production of RNase by <Emphasis Type="Italic">Bacillus firmus</Emphasis> VKPACU1 using response surface methodology

Medium optimization for the nuclease (RNase) production by Bacillus firmus VKPACU-1 was studied using the one-factor-at-a-time method and Response Surface Methodology (RSM). One-factor-at-a-time methodology was used to study the effects of carbon, nitrogen, phosphorus sources, and physical conditions such as pH and temperature, on nuclease (RNase) production. After optimizing the carbon (glucose) and nitrogen (tryptone) sources in the culture medium the physical conditions, pH (6.5) and temperature (35°C) were also optimized. Later these conditions were chosen as the main factors and used in the experimental design. The central composite design (CCD) of the RSM was employed to evaluate the interactive effects of these four variables. The optimized values obtained by the statistical analysis showed that glucose 5.95 g/L, tryptone 22.5 g/L, pH 6.5, and temperature 35°C affected maximum nuclease (RNase) production. When utilizing these proposed optimized conditions, the model predicted nuclease (RNase) production of 43.6 U/mL and in the validation experiments, the nuclease production obtained was 46.5 U/mL. The nuclease production in medium optimized by RSM was 26% higher, than in the non-optimized medium.     

Coexpression of folding accessory proteins for production of active cyclodextrin glycosyltransferase of Bacillus macerans in recombinant Escherichia coli

Coexpression of folding accessory proteins, molecular chaperones, and human peptidyl-prolyl cis-trans isomerase (PPIase) increased production of active cyclodextrin glycosyltransferase (CGTase) of Bacillus macerans, which is otherwise mainly expressed as inclusion body in recombinant Escherichia coli. The best partner for soluble expression of CGTase was found to be human PPIase followed by coexpression of DnaK-DnaJ-GrpE together with GroEL-GroES. Such a significant enhancement by human PPIase coexpression seemed to be due to dual functions of chaperone and peptidyl-prolyl cis-trans isomerization. Coexpression of GroEL-GroES or minichaperone alone did not influence the specific CGTase activity. For production of active CGTase in large amounts, a high cell density culture was achieved using a pH-stat fed-batch strategy. The optimized fed-batch fermentation resulted in dry cell weight of 103.4 g/L and CGTase activity of 1200 U/mL. Combination of human PPIase expression at a gene level and cell culture optimization at a process scale exerted a synergistic effect on the product yield of soluble CGTase expression in recombinant E. coli.     

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.     

Optimization of cyclodextrin production from sago starch

Cyclodextrin (CD) is synthesized by bacterial cyclodextrin glycosyltransferase (CGTase) and is widely used in food, pharmaceutical, cosmetic, and agricultural industries. In this study, Bacillus circulans CGTase was partially purified by ammonium sulfate precipitation at 50-70% saturation. The optimum pH and temperature for CD production from sago starch were found to be in the ranges of 4.5-5.0 and 55-60 degrees C, respectively. beta-CD was the predominant product, constituting 65% of all CD products. The beta-CD produced using partially purified and crude CGTase were compared and found to have no significant difference in yield and productivity. The appropriate proportion of CGTase to sago starch for beta-CD production was determined by response surface methodology. The most appropriate enzyme:substrate ratio was 50 U g sago starch(-1) CGTase and 60 g l(-1) sago starch.     

Ethanol production from seaweed (Undaria pinnatifida) using yeast acclimated to specific sugars

Ethanol production from Undaria pinnatifida (Sea mustard, Miyuk) was performed using yeast acclimated to specific sugars. Pretreatment conditions were optimized by thermal acid hydrolysis and enzyme treatment to increase the monosaccharide yield. Pretreatment by thermal acid hydrolysis was carried out using seaweed powder at 8 ～ 17% (w/v) solid content with a treatment time of 30 ～ 60 min. Enzyme treatment was carried out with 1% (v/v) Viscozyme L (1.2 FGU/mL), 1% (v/v) Celluclast 1.5 L (8.5 EGU/mL), 1% (v/v) AMG 300 L (3.0 AGU/mL), and 1% (v/v) Termamyl 120 L (0.72 KNU/mL). All enzymes except Termamyl 120 L, which was applied during pretreatment, were treated at 45°C for 24 h following pretreatment. Optimal pretreatment and enzyme conditions were determined to be 75 mM H₂SO₄, 13% (w/v) slurry, and 2.88 KNU/mL Termamyl 120 L at 121°C for 60 min. A maximum monosaccharide concentration of 33.1 g/L with 50.1% theoretical yield was obtained. To increase the ethanol yield, Pichia angophorae KCTC 17574 was acclimated to a high concentration (120 g/L) of galactose and mannitol at 30oC for 24 h. Ethanol production of 12.98 g/L with 40.12% theoretical yield was obtained from U. pinnatifida through fermentation with 0.35 g dry cell weight/L P. angophorae KCTC 17574 acclimated to mannitol and galactose.     

Effect of culture medium on hydrogen production by sulfur-deprived marine green algae Platymonas subcordiformis

To study the effect of culture medium on hydrogen production by the marine green algae, Platymonas subcordiformis under sulfur deprivation, cell growth, hydrogen production, and starch and protein catabolism was investigated in the work. Algae cells cultured only in optimized medium required 6～8 days to reach the late logarithmic at the approximate density of (2.00 ± 0.18) × 10⁶ cells/mL, which in traditional medium needed 18～22 days to reach (1.85 ± 0.20) × 10⁶ cells/mL. Increased levels of Chlorophyll (10.74 ± 0.20 μg/mL), starch (149.50 ± 6.15 μg/mL), and protein (213.00 ± 7.36 μg/mL) were accumulated in optimized medium, which were 1.06, 1.47, and 1.87-fold of the algae cells cultured in traditional medium, respectively. The sealed culture of algae cells in sulfur-deprived optimized medium shifted to anaerobic conditions after 96 h of light illumination and produced 0.45 ± 0.12 mL H₂, but in traditional medium maintained aerobic condition and no hydrogen was produced. In addition, changes in starch and protein content during continuous light illumination indicated that more endogenous substrate was consumed in the sulfur-deprived optimized medium than that in the sulfur-deprived traditional medium.     

Optimization of alkaline protease production by <Emphasis Type="Italic">Aspergillus clavatus</Emphasis> ES1 in <Emphasis Type="Italic">Mirabilis jalapa</Emphasis> tuber powder using statistical experimental design

Medium composition and culture conditions for the bleaching stable alkaline protease production by Aspergillus clavatus ES1 were optimized. Two statistical methods were used. Plackett-Burman design was applied to find the key ingredients and conditions for the best yield. Response surface methodology (RSM) including full factorial design was used to determine the optimal concentrations and conditions. Results indicated that Mirabilis jalapa tubers powder (MJTP), culture temperature, and initial medium pH had significant effects on the production. Under the proposed optimized conditions, the protease experimental yield (770.66 U/ml) closely matched the yield predicted by the statistical model (749.94 U/ml) with R (2)=0.98. The optimum operating conditions obtained from the RSM were MJTP concentration of 10 g/l, pH 8.0, and temperature of 30 degrees C, Sardinella heads and viscera flour (SHVF) and other salts were used at low level. The medium optimization contributed an about 14.0-fold higher yield than that of the unoptimized medium (starch 5 g/l, yeast extract 2 g/l, temperature 30 degrees C, and pH 6.0; 56 U/ml). More interestingly, the optimization was carried out with the by-product sources, which may result in cost-effective production of alkaline protease by the strain.     

Co-fermentation of carbon sources by Enterobacter aerogenes ATCC 29007 to enhance the production of bioethanol

We investigated the enhancement of bioethanol production in Enterobacter aerogenes ATCC 29007 by co-fermentation of carbon sources such as glycerol, glucose, galactose, sucrose, fructose, xylose, starch, mannitol and citric acid. Biofuel production increases with increasing growth rate of microorganisms; that is why we investigated the optimal growth rate of E. aerogenes ATCC 29007, using mixtures of different carbon sources with glycerol. E. aerogenes ATCC 29007 was incubated in media containing each carbon source and glycerol; growth rate and bioethanol production improved in all cases compared to those in medium containing glycerol alone. The growth rate and bioethanol production were highest with mannitol. Fermentation was carried out at 37 °C for 18 h, pH 7, using 50 mL defined production medium in 100 mL serum bottles at 200 rpm. Bioethanol production under optimized conditions in medium containing 16 g/L mannitol and 20 g/L glycerol increased sixfold (32.10 g/L) than that containing glycerol alone (5.23 g/L) as the carbon source in anaerobic conditions. Similarly, bioethanol production using free cells in continuous co-fermentation also improved (27.28 g/L) when 90.37 % of 16 g/L mannitol and 67.15 % of 20 g/L glycerol were used. Although naturally existing or engineered microorganisms can ferment mixed sugars sequentially, the preferential utilization of glucose to non-glucose sugars often results in lower overall yield and productivity of ethanol. Here, we present new findings in E. aerogenes ATCC 29007 that can be used to improve bioethanol production by simultaneous co-fermentation of glycerol and mannitol.     

Immobilization of cyclodextrin glucanotransferase on amberlite IRA-900 for biosynthesis of transglycosylated xylitol

Cyclodextrin glucanotransferase (CGTase) fromThermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH 6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of the amount ratio of the adsorbed enzyme to the initial amount in the solution. Immobilization of CGTase shifted the optimum temperature for the enzyme to produce transglycosylated xylitol from 70°C to 90°C and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuously produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10% (w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10% (w/v) xylitol as the glycosyl acceptor, 20 mL/h of medium flow rate, and 60°C. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g·L⁻¹·h⁻¹, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.     

内切中性纤维素酶EGⅡ的发酵条件优化

对毕赤酵母基因工程菌EIM-50-eg2产内切中性纤维素酶的主要影响因子进行研究,考察氮源、pH、温度、微量元素PTM1和甲醇浓度等对工程菌产酶的影响。单因素实验和正交实验结果表明,优化后的培养基组成及培养条件:磷酸氢二铵40 g/L,甲醇15 mL/L,硫酸镁10 g/L,磷酸二氢钾9 g/L,初始pH 6.0,培养温度28℃,PTM1添加量0.02%,甲醇诱导浓度1.5%。优化后内切葡聚糖酶活力可达4 158 U/(mL.min)是优化前1 449 U/(mL.min)的2.86倍。     

Substrate complexation and aggregation influence the cyclodextrin glycosyltransferase (CGTase) catalyzed synthesis of alkyl glycosides

Bacillus macerans cyclodextrin glycosyltransferase (CGTase) was used to convert dodecyl-β-maltoside (DDM) to dodecyl-β-maltooctaoside (DDMO) using α-cyclodextrin (α-CD) or starch as glycosyl donors. At 300 mM α-CD, varied DDM concentration and 60 °C, the reaction obeyed Michaelis-Menten kinetics with a K_m value of 18 mM and a V_max value of 100 U/mg enzyme. However, at 25 mM α-CD the reaction rate decreased with increasing DDM concentration (5-50 mM), and when the α-CD concentration was varied at fixed DDM concentration an S shaped curve was obtained. The deviations from Michaelis-Menten kinetics were interpreted as being caused by formation of inclusion complexes between α-CD and DDM and by micellation of DDM. To achieve a high reaction rate, a high concentration of free α-CD is necessary, since α-CD in the form of a complex has low reactivity. When starch is used as glycosyl donor in the CGTase catalyzed alkyl glycoside elongation reaction, it is thus important to choose reaction conditions under which the cyclization of starch to α-CD is efficient.