Optimization of fibrinolytic enzyme production by Bacillus subtilis DC-2 in aqueous two-phase system (poly-ethylene glycol 4000 and sodium sulfate)

The central composite rotable design (CCRD) was used to determine optimal conditions for fibrinolytic enzyme production by Bacillus subtilis DC-2 in poly-ethylene glycol 4000 (PEG 4000) and sodium sulfate (Na(2)SO(4)) aqueous two-phase system (ATPS). PEG 4000 and Na(2)SO(4) concentration, fermentation time and temperature, and pH were selected as variables to evaluate the fibrinolytic activity in PEG phase. Using response surface methodology (RSM), a second-order polynomial equation was obtained by multiple regression analysis. The predicted maximal fibrinolytic activity in PEG phase was 1241.02 IU/ml with 9.05% PEG 4000 concentration, 5.06% Na(2)SO(4) concentration, 118.77 h fermentation time, 37.57 degrees C fermentation temperature and pH 6.52. The validity of the response model was verified by a good agreement between predicted and experimental results. The fibrinolytic activity obtained from experimental results in PEG phase (1223.61 IU/ml) was higher than that produced in homogeneous fermentation (1165.58 IU/ml).     

Solid state fermentation of rice chaff for fibrinolytic enzyme production by Fusarium oxysporum

Rice chaff was used as the substrate for the production of fibrinolytic enzyme by Fusarium oxysporum in solid state fermentation. The optimized moisture content of the medium was 30 - 50% (v/w). An inoculum of 5 - 10% (v/v) and an average particle size of 400 μm for the substrate were optimum for productivity and enzyme activity of 80 IU per ml filtrate was achieved after 96 hours of fermentation. This revised version was published online in November 2006 with corrections to the Cover Date.     

根霉液态发酵产生纤溶酶的培养条件优化

目的:目前临床使用的溶栓药物疗效肯定,但还存在许多缺陷,而且价格昂贵,因此研制新型溶栓药物的需求迫切。方法:研究了根霉Rhizopus chinensisYY-15液体摇瓶发酵产生纤溶酶的工艺条件。采用单因素试验对液体发酵培养基的碳源、氮源、碳氮比、初始pH进行了优化;采用正交试验对发酵时间、接种量进行了研究。结果:实验范围内菌株液体发酵产纤溶酶的适宜培养基组成为:麸皮水浓度3%(w/v),豆粕浓度5%(w/v),初始培养基pH5.0。适宜培养条件为接种量6%,培养时间72h。优化条件下的摇瓶液体发酵纤溶酶产量平均达98.31 U/ml。     

Chitinolytic and chitosanolytic activities from crude cellulase extract produced by A. niger grown on apple pomace through Koji fermentation

Enzyme extracts of cellulase [filter paper cellulase (FPase) and carboxymethyl cellulase (CMCase)], chitinase, and chitosanase produced by Aspergillus niger NRRL-567 were evaluated. The interactive effects of initial moisture and different inducers for FP cellulase and CMCase production were optimized using response surface methodology. Higher enzyme activities [FPase 79.24+/- 4.22 IU/gram fermented substrate (gfs) and CMCase 124.04+/-7.78 IU/gfs] were achieved after 48 h fermentation in solid-state medium containing apple pomace supplemented with rice husk [1% (w/w)] under optimized conditions [pH 4.5, moisture 55% (v/w), and inducers veratryl alcohol (2 mM/kg), copper sulfate (1.5 mM/kg), and lactose 2% (w/w)] (p<0.05). Koji fermentation in trays was carried out and higher enzyme activities (FPase 96.67+/-4.18 IU/gfs and CMCase 146.50+/-11.92 IU/gfs) were achieved. The nonspecific chitinase and chitosanase activities of cellulase enzyme extract were analyzed using chitin and chitosan substrates with different physicochemical characteristics, such as degree of deacetylation, molecular weight, and viscosity. Higher chitinase and chitosanase activities of 70.28+/-3.34 IU/gfs and 60.18+/-3.82 to 64.20+/-4.12 IU/gfs, respectively, were achieved. Moreover, the enzyme was stable and retained 92-94% activity even after one month. Cellulase enzyme extract obtained from A. niger with chitinolytic and chitosanolytic activities could be potentially used for making low-molecular-weight chitin and chitosan oligomers, having promising applications in biomedicine, pharmaceuticals, food, and agricultural industries, and in biocontrol formulations.     

Solid-State Fermentation with Trichoderma reesei for Cellulase Production

Cellulase yields of 250 to 430 IU/g of cellulose were recorded in a new approach to solid-state fermentation of wheat straw with Trichoderma reesei QMY-1. This is an increase of ca. 72% compared with the yields (160 to 250 IU/g of cellulose) in liquid-state fermentation reported in the literature. High cellulase activity (16 to 17 IU/ml) per unit volume of enzyme broth and high yields of cellulases were attributed to the growth of T. reesei on a hemicellulose fraction during its first phase and then on a cellulose fraction of wheat straw during its later phase for cellulase production, as well as to the close contact of hyphae with the substrate in solid-state fermentation. The cellulase system obtained by the solid-state fermentation of wheat straw contained cellulases (17.2 IU/ml), β-glucosidase (21.2 IU/ml), and xylanases (540 IU/ml). This cellulase system was capable of hydrolyzing 78 to 90% of delignified wheat straw (10% concentration) in 96 h, without the addition of complementary enzymes, β-glucosidase, and xylanases.     

高产纤溶酶菌株CNY16发酵条件优化及其酶学特性初步研究

【目的】通过响应面试验对产纤溶酶菌株CNY16发酵条件进行优化,并对其酶学特性进行初步研究。【方法】采用Plackett-Burman设计得出酵母膏、氯化钠、转速3个最重要影响因素,通过最陡爬坡实验逼近酶活的最高区域,然后根据Box-Behnken中心组合设计实验对显著因素进行优化分析,最后对该酶学性质进行初步分析。【结果】最终得到3个因素的最优组合:酵母膏3.28%,氯化钠1.14%,转速166 r/min,在此培养条件下,纤溶酶活达到875.932 U/mL,比优化前提高了46%;该菌株产纤溶酶最适温度为30°C,最适pH为6.5。【结论】确定了高产纤溶酶菌株CNY16的最优发酵条件及其部分酶学性质,为该酶的进一步深入研究及中试实验奠定基础。     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

Optimization of medium and process parameters for the production of inulinase from a newly isolated Kluyveromyces marxianus YS-1

A newly isolated strain of Kluyveromyces marxianus YS-1 was used for the production of extra cellular inulinase in a medium containing inulin, meat extract, CaCl2 and sodium dodecyl sulphate (SDS). Fermentation medium pH 6.5, cultivation temperature 30 degrees C and 5% (v/v) inoculum of 12 h-old culture were optimal for enzyme production (30.8 IU/ml) with a fermentation time of 72 h at shake flask level. Raw inulin (2%, w/v) extracted from dahlia tubers by processing at 15 kg/cm2 for 10 min was optimum for bioreactor studies. Maximum enzyme production (55.4 IU/ml) was obtained at an agitation rate of 200 rpm and aeration of 0.75 vvm in a stirred tank reactor with a fermentation time of 60 h.     

Enhancement of fibrinolytic enzyme production from Bacillus subtilis via immobilization process onto radiation synthesized starch/dimethylaminoethyl methacrylate hydrogel

Hydrogel matrices based on starch and dimethylaminoethyl methacrylate (Starch/DMAEMA) were synthesized including γ-irradiation as a clean initiator. The prepared hydrogels were characterized in terms of their gel fraction yield, degree of equilibrium swelling. The prepared hydrogels were examined as carriers for immobilization of Bacillus subtilis that has the ability to secrete an extracellular fibrinolytic enzyme that degrades fibrin. Scanning electron microscope (SEM) analysis showed proliferation of the bacterial cells entrapped inside the polymeric matrix. The immobilization process increases the production time of fibrinolytic enzyme up to 120 h instead of 96 h for the free cells. The optimum temperature of activity broadened and a significant shift in the pH optima was observed upon immobilization. The reusability of immobilized cells under repeated batch fermentation conditions was also investigated. At the optimum production conditions, immobilization of B. subtilis cells onto Starch/DMAEMA resulted in a four fold increase in enzyme activity.     

Optimization of a pseudo-affinity process for penicillin acylase purification

A pseudo-affinity process for penicillin acylase (EC 3.5.1.11) purification using an affinity ligand (Ampicillin) attached on Sepharose 4B-CNBr was optimized. The enzyme adsorption on this affiant (Amp-Seph) is independent of pH between 5.5 and 8.8, in 100?mM phosphate containing 22% (w/v) ammonium sulphate. The desorption of the penicillin acylase from the affinity gels was carried out, the best desorption results being obtained through a non specific eluent, 100?mM phosphate pH 4.6 with 15% (w/v) ammonium sulphate. The best purification results were obtained with an enzymatic extract, produced through osmotic shock of Escherichia coli cells (3.7?IU/mg prot). With this extract and an affinity gel of Sepharose 4B-CNBr derivatized with ampicillin (3.8?μmol/cm³?gel), a maximum activity capacity adsorbed of 20?IU/cm³?gel was obtained for initial values of activity and protein concentration of 1.7?IU/cm³ and 0.4?mg prot/cm³, respectively. With the optimized eluent it was possible to obtain penicillin acylase in only one purification step with a desorption yield of enzyme activity higher than 90%. The penicillin acylase produced with this process was characterized by a maximum purity of 34?IU/mg prot, corresponding to a purification degree higher than 150 in relation to the lowest pure enzymatic extract. The enzyme purity of the eluted fractions was certified by SDS gel electrophoresis and liquid chromatography through a Mono Q column in a FPLC apparatus. The gel electrophoresis presented 4 main stained bands with 2 corresponding to α and β subunits of the penicillin acylase with equivalent molecular weights of 27 and 63?kDa. No external diffusion resistance on penicillin acylase and total protein adsorption on this affiant (Amp-Seph 3.8?μmol/cm³?gel) were observed for continuous adsorption processes performed at two different agitation speeds (120 and 400?rpm).     

豆豉纤溶酶基因在大肠杆菌中的可溶性表达及纯化(英文)

豆豉纤溶酶是从豆豉中发现的新型纤溶酶.从枯草杆菌DC-12中提取总DNA,PCR法扩增pro-DFE基因.将pro-DFE基因插入载体pET-32a,构建表达质粒pET-pro-DFE,转化大肠杆菌BL21(DE3),对重组菌株进行变温诱导表达,重组菌株于37℃培养至OD600为0.6时,加入终浓度为0.4mmol/L的IPTG于24℃进行诱导,SDS-PAGE显示可溶性重组融合蛋白约占重组蛋白的60%.且少量融合重组蛋白发生自切割,形成成熟的豆豉纤溶酶,破菌上清中含有成熟的豆豉溶栓酶,纤溶活性为200IU/mL.重组酶经纯化后比酶活为1280IU/mg.     

Fermentation Kinetics and Continuous Process of L-Asparaginase Production

For the purpose of obtaining L-asparaginase in quantities from Erwinia aroideae, cell growth and enzyme formation were investigated in both batch and continuous fermentation. Using yeast extract as a growth-limiting substrate, the relationship between specific growth rate and substrate concentration was found to fit the Monod equation. The optimum temperature for enzyme production was 24 C, although cell growth was higher at 28 C. The enzyme yield reached its maximum of 4 IU/ml during the negative acceleration growth phase which occurs just prior to stationary growth. Compared to batch fermentations, the continuous fermentation process gave a lower enzyme yield except when the fermentation was conducted at a dilution rate of 0.1 hr(-1). The graphical method frequently used for prediction of continuous fermentation does not apply to L-asparaginase production by E. aroideae. The optimum temperature for enzyme production in continuous process was 24 C, which was the same as in batch process. Increasing the temperature from 24 to 28 C resulted in a 20% loss of enzyme yield.     

Production of cyclodextrin glucanotransferase from alkalophilic Bacillus sp. TS1-1: Optimization of carbon and nitrogen concentration in the feed medium using central composite design

Optimisation of nutrient feeding was developed to overcome the limitation in batch fermentation and to increase the CGTase production from Bacillus sp. TS1-1 in fed batch fermentation. Optimisation of the C/N ratio in the feed stream was conducted in a 5 l fermenter, where feeding was initiated at constant rate of 0.02 h⁻¹. In our initial screening process, the addition of nitrogen source boosted the growth of the microbes, but on the other hand reduced the CGTase production. The amount of tapioca starch and yeast extract was optimised in order to obtain a sufficient growth and thus, increased the CGTase production. Results were analysed using three-dimensional response surface plot, and the optimised values of carbon and nitrogen concentration of 3.30% (w/v) and 0.13% (w/v) were obtained, respectively. CGTase activity increased up to 80.12 U/ml, which is 13.94% higher as compared to batch fermentation (70.32 U/ml). This also led to 14.54% increment of CGTase production in fed batch culture as compared to the production before the optimisation. The CGTase activity obtained was close to the predicted value, which is 78.05 U/ml.     

High gravity fermentation of sugarcane molasses to produce ethanol: Effect of nutrients

Fermentation efficiency of more than 85% was obtained by high gravity fermentation of 33–34°Bx (spec. gravity ≈1.134) molasses medium with certain nutrients, instead of generally employed medium containing ≈16% (w/v) total sugar (spec. gravity ≈1.090) for ethanol fermentation in distilleries to get maximum 80–85% conversion. The fermenting yeast, Saccharomyces, has varied capabilities, depending on the species and nutrition for fermenting the high solids medium. The fermentation period was reduced to 48 h; and the byproducts obtained were less in concentration, upon supplementation with nutrients (or osmoprotectants) like soy flour/wheat bran to the medium in the existing batch fermentation technology. This has been found partly due to improved yeast cell viability during fermentation.     

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.     

Rice straw fermentation by Schizophyllum commune ARC-11 to produce high level of xylanase for its application in pre-bleaching

Rice straw is valuable resource that has been used as substrate for cost effective production of xylanase under solid-state fermentation by a newly isolated white rot fungi, S. commune ARC-11. Out of eleven carbon sources tested, rice straw was found most effective for the induction of xylanase that produced 4288.3?IU/gds of xylanase by S. commune ARC-11. Maximum xylanase production (6721.9?IU/gds) was observed on 8^th day of incubation at temperature (30?°C), initial pH (7.0) and initial moisture content (70.0%). The supplementation of ammonium sulphate (0.08% N, as available nitrogen) enhanced the xylanase production up to 8591.4?IU/gds. The xylanase production by S. commune ARC-11 was further improved by the addition of 0.10%, (w/v) of Tween-20 as surfactant. The maximum xylanase activities were found at pH 5.0 and temperature 55?°C with a longer stability (180?min) at temperature 45, 50 and 55?°C. This xylanase preparation was also evaluated for the pre-bleaching of ethanol-soda pulp from Eulaliopsis binata. An enzyme dosage of 10?IU/g of xylanase resulted maximum decrease in kappa number (14.51%) with a maximum improvement 2.9% in ISO brightness compared to control.     

Crude glycerol from biodiesel as a carbon source for production of a recombinant highly thermostable β-mannanase by <Emphasis Type="Italic">Pichia pastoris</Emphasis>

Objective

To explore an efficient use of crude glycerol for the production of a highly thermostable β-mannanase (ReTMan26) by Pichia pastoris X33.

Results

Cell growth was significantly inhibited by 4 and 6% (w/v) crude glycerol in 250 ml shake-flasks and in 5 l bioreactor batch cultures, respectively, but not affected by pure glycerol at the same concentrations. For further study, the impact of various impurities in crude glycerol on the cell growth of, and ReTMan26 production by, Pichia pastoris was investigated. Salts and methanol did not exert an inhibitory effect, but ≥ 0.2% and 0.3% (w/v) soap in shake-flask and bioreactor cultures, respectively, inhibited fermentation. Under identical conditions, the biomass and ReTMan26 activity produced by high-cell-density fermentation using 5% crude glycerol (glycerol at 80%, w/w) were slightly higher than those using 4% (w/v) pure glycerol.

Conclusions

Non-pretreated ≤ 5% (w/v) crude glycerol could be effectively utilized for industrial production of ReTMan26, and the total production costs using crude glycerol were ~ 4.2% lower than those using pure glycerol.

     

Membrane-integrated fermentation system for improving the optical purity of D-lactic acid produced during continuous fermentation

This report describes the production of highly optically pure D-lactic acid by the continuous fermentation of Sporolactobacillus laevolacticus and S. inulinus, using a membrane-integrated fermentation (MFR) system. The optical purity of D-lactic acid produced by the continuous fermentation system was greater than that produced by batch fermentation; the maximum value for the optical purity of D-lactic acid reached 99.8% enantiomeric excess by continuous fermentation when S. leavolacticus was used. The volumetric productivity of the optically pure D-lactic acid was about 12 g/L/h, this being approximately 11-fold higher than that obtained by batch fermentation. An enzymatic analysis indicated that both S. laevolacticus and S. inulinus could convert L-lactic acid to D-lactic acid by isomerization after the late-log phase. These results provide evidence for an effective bio-process to produce D-lactic acid of greater optical purity than has conventionally been achieved to date.     

α-amylase production in aqueous two-phase systems with Bacillus subtilis

The production of α-amylase (1,4-α-d-glucan glucanohydrolase, EC 3.2.1.1) by Bacillus subtilis has been studied in repeated batch fermentations in aqueous two-phase systems. In a phase system composed of PEG 600, 8% (w/w), PEG 3350, 5% (w/w)/Dextran T 500, 2% (w/w), 82% of the enzyme partitioned to the top phase. The enzyme concentration in the top phase reached 0.85–1.35 U ml^?1 during the fermentations compared with 0.58 U ml^?1 in the reference fermentation. In the phase system composed of PEG 3350, 9% (w/w)/Dextran T 500, 2% (w/w), 73% of the enzyme partitioned to the top phase. However, the enzyme concentration in this phase system reached only 0.35 U ml^?1 in the top phase. The bacterial cells were microscopically observed to partition totally to the bottom phase in the aqueous two-phase system used. The results are discussed in relation to recirculation of cells by immobilizing to a solid matrix. Extraction of the product to the top phase and the effect of the phase polymers, especially PEG, on the production are also discussed.     

里氏木霉液体发酵产纤维素酶的研究

在摇瓶试验基础上,采用里氏木霉(Trichoderma reesei)HC-415菌株进行5L自控罐产纤维素酶深层发酵试验。在通气量为 0.2—0.6vvm、搅拌速度为 400r/min、发酵液pH控制在5.8—6.1的条件下,发酵液的羧甲基纤维素(CMC)酶酶活最高为325.0mg糖/ml,滤纸糖酶(FPA)酶活最高达17.9mg糖/ml。发酵周期为108h。所得冻干纤维素酶粉CMC酶活最高3111IU/g,FPA最高135IU/g ,对发酵液得率平均6.7g/L。酶活总收率CMC酶活平均78.2％,FPA酶活平均73.5％。