少根根霉菌株发酵生产纤溶酶条件的研究

发酵条件优化可提高少根根霉菌株8B所产纤溶酶的活性。使用单因素试验和正交试验确定该茵发酵产酶的最佳条件。试验确定最优化发酵条件,培养基：麸皮水5g／L,尿素5g／L,胰蛋白胨0．5g／L,K2HPO4·3H2O 0．3g／L,MgSO4·7H2O 0.15g／L,pH5.5,摇床转速160r／min,30℃发酵56h。在此优化条件下培养,8B产纤溶酶活力达到345．41U／mL,是初始培养基发酵产酶活力的7．52倍。     

血栓溶解酶产生菌及其培养条件的研究

通过对根霉１２号发酵液的分析及发酵条件的研究,发现其发酵液中含有能溶解血栓的物质,但不能分解血细胞。它在麸皮胰蛋白胨培养基（ｐＨ５．１）上３０℃振荡培养４８～６０ｈ,ｐＨ值达到７．４左右时产生血栓溶解酶的活力最高。     

根霉12号固体发酵产生纤溶酶工艺条件的研究

研究了根霉12号固体发酵产生纤溶酶的工艺条件。采用单因素试验、均匀设计方法对固体发酵培养基的碳源、氮源、碳氮比、初始pH、加水量、无机盐加量进行了优化;采用正交试验对发酵时间、接种量进行了研究。结果表明,实验范围内根霉12固体发酵产纤溶酶的适宜培养基组成为：麸皮：豆粕=1:2,初始pH5.0,加水量0.75ml／g物料,MnSO4-H2O 和 (NH4)2SO4加量分别为0.25％和1.42％(对物料)。适宜培养条件为接种量10^7个孢子/g 物料,培养时间 72h。优化条件下的纤溶酶产量平均达 791.81u／g物料。     

一株具有纤溶活性的枯草杆菌(Bacillus Subtilis)的研究——液体发酵条件的选择

本文主要报告了,以ＢａｃｉｌｕｓＳｕｂｔｉｌｉｓＨＷ－１２为试验菌株,在液体发酵中,所确定的发酵条件为：碳源是木糖,氮源是大豆胰蛋白胨,发酵液ｐＨ７．０,培养温度３７℃,培养时间９６小时。在这样的发酵条件下,该菌产酶活力为２００尿激酶单位／毫升发酵液 。     

黑曲霉产木聚糖酶发酵条件的研究

正交设计试验结果表明,黑曲霉（Ａｓｐｅｒｇｉｌｌｕｓ ｎｉｇｅｒ ｍ１２）产木聚糖酶活力达７６．６０ｕ／ｍｌ,合适的产酶发酵条件如下,培养基（ｇ／Ｌ）：麸皮４０,尿素６．６７,ＫＨ２ＰＯ４ １．０,ＭｇＳＯ４．７Ｈ２Ｏ０．５,ＮａＣｌ０．３,Ｔｗｅｅｎ－８０ ３．０,ＣａＣＯ３ ２．０,２８℃,１２０ｒ／ｍｉｎ水浴振荡培养５．５ｄ。     

嗜碱芽孢杆菌NTT33产碱性β-甘露聚糖酶发酵条件的研究及高产菌株选育

研究了嗜碱芽孢杆菌（ａｌｋａｌｏｐｈｉｌｉｃＢａｃｌｕｓｓｐ．）ＮＴＴ３３发酵产生胞外碱性β－甘露聚糖酶的条件,其最佳碳源为１％槐豆角,最佳氮源为１％蛋白胨＋０．２％酵母膏,发酵培养３６ｈ产酶量最高（达６１．３υ／ｍＬ）。甘油,葡萄糖,甘露糖等对产酶有强的阻遏作用。该菌株经紫外诱变处理后,采用透明圈法初步筛选出在含葡萄糖和不含葡萄糖的槐豆胶培养基上同时产生透明圈的菌株,进一步测定其产酶进程曲线,最后筛选到一株（ＮＴＴ３３－ｒ６）部分消除葡萄糖代谢阻遏高产β－甘露聚糖酶的菌株,其酶活力比出发菌株提高５０％,,达到９６．３Ｕ／ｍｌ;。     

根霉cw-1产纤溶酶的发酵条件优化

目的:确定根霉cw-1高产纤溶酶的液体发酵培养基组成及培养条件,使纤溶酶产量得到明显提高。方法和结果:采用响应面法对该菌种产纤溶酶的发酵条件进行优化。首先利用Plackett Burman试验设计筛选出影响产酶量的3个主要因素,即麸皮的浓度、豆粕的浓度和初始p H。在此基础上使用Design-Expert软件进行Box-Behnken试验设计,通过响应面分析得出菌株cw-1发酵产酶的最佳条件为:麸皮28.67g/L、豆粕46.28g/L、初始p H 5.8。经过试验验证,优化后粗酶液酶活达到243.22 U/m L(尿激酶单位),与响应面预测结果一致,较优化前酶活提高41倍。     

华根霉产纤溶酶液体发酵条件的研究

研究了华根霉TCCC 41014产纤溶酶液态发酵的工艺条件,采用单因素实验对液态发酵培养基的碳源、氮源、初始pH值、温度和装液量进行了优化.结果表明,实验范围内华根霉TCCC41014液态发酵产纤溶酶的适宜培养基组成(g桙L):糊精80,蛋白胨60,豆粕60,初始pH为4.5.适宜培养条件:培养温度为29℃,装液量为5...     

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。     

一株根霉产脂肪酶发酵条件的研究

通过对筛选出的一株根梅ＲｈｉｚｏｐｕｓＹ－９２产旨肪肪酶发酵２基组成（Ｃ,Ｎ,无机盐）及工艺条件的探索,并经正交实验,得到较优培养基配方为：蛋白胨６％,豆饼粉４％,葡萄糖１％,ＭｇＳＯ４·７Ｈ２Ｏ０．１％,ＫＨ２ＰＯ４０．３％,起始ＰＨ８．０,在此条件下,发酵液酶活可达９９．１５ｕ／ｍｌ,是初始酶活的１７８％。     

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。     

海洋来源链霉菌MY0504产纤溶酶的发酵条件优化

【目的】以发酵液纤溶酶活力为指标,优化海洋来源的链霉菌菌株MY0504的发酵条件。【方法】在菌株生长曲线及单因素试验基础上,采用Plackett-Burman设计筛选影响纤溶酶活性的主要因素,进一步用最陡爬坡试验及Box-Behnken中心组合设计法优化发酵条件。【结果】纤溶酶活性最高的发酵条件为:葡萄糖21.68 g/L,酵母粉25.31 g/L,NaCl5.0 g/L,K_2HPO_4·3H_2O3.0 g/L,MgSO_4·7H_2O 0.5 g/L,FeSO_4·7H_2O 0.02 g/L,装液量50 mL(250 mL摇瓶),接种量10%(体积比),初始pH 7.5,温度24°C,转速200 r/min,培养时间4.5 d。发酵液纤溶酶活性可达2 190.6 U/mL。【结论】确定了MY0504菌株产纤溶酶的最优发酵条件,为该酶的进一步分离纯化及性质研究奠定基础。     

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.     

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.     

纳豆激酶液态发酵条件的研究

考察纳豆杆菌在7.5 L发酵罐中分批发酵产纳豆激酶的条件,纳豆激酶酶活采用四肽底物测定。结果表明:纳豆杆菌生长和产酶的适宜条件不一致。发酵过程中发酵罐搅拌转速控制为500 r/min不变,0～12 h时控制pH为8.0、温度为37℃;12～36 h调整pH为7.0、温度为30℃;16 h时补加外源C源,连续发酵36 h。该过程中发酵液中比酶活最高达到3 232 U/mL,与摇瓶发酵相比,比酶活提高了58%。     

一株脂肪酶产生菌的筛选及产酶条件优化研究

通过利用溴甲酚紫显色培养基初筛和酶活测定法复筛得到产脂肪酶的一株细菌HP2,经形态学观察和生理生化测定初步鉴定该菌株为不动杆菌属。并对该菌株的摇床培养产酶条件进行了初步研究,采用正交试验对HP2菌株发酵产脂肪酶的条件进行了优化,得到最佳发酵条件为初始pH为7.7,培养温度为35℃,接种量(V/V)为1.5%,发酵周期为48 h,酶活力达到129.7 U/mL。     

根霉12号固体发酵产生纤溶酶工艺条件的研究*

研究了根霉12号固体发酵产生纤溶酶的工艺条件。采用单因素试验、均匀设计方法对固体发酵培养基的碳源、氮源、碳氮比、初始pH、加水量、无机盐加量进行了优化;采用正交试验对发酵时间、接种量进行了研究。结果表明,实验范围内根霉12固体发酵产纤溶酶的适宜培养基组成为:麸皮∶豆粕=1∶2,初始pH5.0,加水量0.75ml/g物料, MnSO4H2O和 (NH4)2SO4加量分别为0.25%和 1.42%(对物料)。适宜培养条件为接种量107个孢子/g物料,培养时间72h。优化条件下的纤溶酶产量平均达791.81u/g物料。