D-核糖发酵条件研究

对枯草芽孢杆菌Bacillus subtilis ptn15-1的发酵条件进行优化。采用优化后的培养基对发酵液的pH、发酵温度、摇床转速、接种量、装液量等进行单因素实验。确定发酵最适发酵条件为：pH7.0,发酵温度37℃;摇床转速180r/min,接种量10%,300mL三角瓶装30mL发酵液,发酵时间为68h。在此条件下,该菌的D-核糖产量从31.7g/L提高到43.1g/L,提高了35.9%。     

纳他霉素发酵培养基及发酵条件的优化

采用Plackett-Burman法、最陡爬坡实验和响应面实验(Box-Behnken设计法)相结合的方法对褐黄孢链霉菌合成纳他霉素的发酵培养基及发酵条件进行优化。结果表明,培养基中的蛋白胨、pH和摇瓶装液量是影响纳他霉素产量的主要因素。优化后的培养基组成为葡萄糖50 g/L、蛋白胨19.5 g/L、酵母粉7 g/L、pH 7.4~7.5;发酵条件为装液量60 mL/500 mL、接种量15%、发酵温度29℃、摇床转速200 r/min、发酵周期96 h。此条件下,纳他霉素的产量较优化前提高了94%,达到2.19 g/L。     

药用真菌桑黄液体深层发酵条件的优化

以菌丝体生物量和多糖产量为主要指标,对桑黄(鲍氏层孔菌)的深层发酵条件进行了优化,通过单因素试验和四因素三水平正交试验筛选出了桑黄液体发酵的培养基,结果表明,最适培养基为:葡萄糖5g/L,玉米粉40g/L,豆饼粉20g/L,KH2PO41.5g/L,MgSO41g/L。进一步通过培养条件的优化,得到最适菌丝体生长的液体发酵条件为:培养温度28℃,摇床转速140r/min,pH值自然,接种量10%,装液量100mL(250mL三角瓶),发酵周期132h。     

响应面法优化短短芽胞杆菌ch2-22的发酵工艺

在摇瓶发酵条件下,优化提高短短芽胞杆菌ch2-22芽胞浓度和抑菌活性的发酵培养基和培养条件。首先在单因素试验基础上进行响应面设计对ch2-22的发酵培养基进行优化,然后使用单因素试验方法确定最佳发酵条件,得到优化发酵培养基为淀粉35.05 g/L,豆饼粉26.08 g/L,蔗糖10 g/L,鱼粉5 g/L,Na Cl 1 g/L,Mg SO40.3 g/L,(NH4)2SO43 g/L,Mn SO40.1 g/L,K2HPO43 g/L,酵母膏1 g/L,Ca CO32 g/L。培养条件为温度32℃,转速180 r/min,装液量100 m L/500 m L,接种量4%,初始pH为7.0,发酵时间45 h。优化后的芽胞数量达到8.1×109cfu/m L,与优化前的芽胞数量(1.6×109cfu/m L)相比,提高了3.7倍,优化后发酵液效价达到3 350 IU/m L,提高了109%,高于同类菌株的2 000 IU/m L。     

一株苝产醌类光敏剂丝状真菌AL18的液体发酵工艺研究

为研究一株丝状真菌AL18产苝醌类光敏剂的液体发酵工艺.以马铃薯综合培养基为发酵培养基,采用单次单因素实验法,研究了液体摇瓶培养条件对苝醌类光敏剂产量的影响.实验结果表明液体摇瓶最适培养条件为250ml三角瓶装液量40ml,接种量7.5%,接种种龄40h,初始pH5.75,摇床转数180r/min,30℃振荡培养48h.在此培养条件下,采用单因素法筛选了发酵培养基中的碳源、氮源和无机离子,选用L9(34)对筛选到的绵白糖(A)、蛋白胨(B)、蚕蛹粉(C)、CuSO4·5H2O(D)进行了正交试验.经优化后的发酵培养基配方为马铃薯200g/L,绵白糖30g/L,蛋白胨3g/L,蚕蛹粉12.5g/L,磷酸二氢钾1g/L,硫酸镁0.5g/L,硫酸铜0.05g/L,VB1 100mg/L.对此发酵培养基配方进行了5次验证实验,苝醌类光敏剂的平均产量为1.21g/L.     

重组大肠杆菌Bgl2238的发酵优化

本研究对前期实验室从黑龙江玉米土壤中筛选并构建的β-葡萄糖苷酶Bgl2238的重组大肠杆菌(E.coliBL21(DE3)-pET32a-bgl2238)采用响应面(Box-Behnken)优化的方法进行摇瓶发酵,优化培养基组分,而培养条件即温度、pH值、接种量及装液量则采用单因素法优化。结果显示最佳培养基配比为:甘油9.32g/L、酵母提取粉12g/L、胰蛋白胨19.13g/L、NaCl8g/L、K_2HPO_4·3H_2O 19.13g/L、KH_2PO_42g/L、柠檬酸高铁胺0.2g/L和微量元素母液6mL/L。重组大肠杆菌Bgl2238最佳的发酵条件为:发酵温度37℃、起始pH8.0、3%接种量、25mL装液量、IPTG终浓度为0.25mmol/L。在250mL锥形瓶对重组子Bgl2238进行发酵,在最优化的发酵培养基成分和培养条件下,Bgl2238的酶活力可以达到2910U/L,比起始培养基中的酶活提高了61.77%。     

解淀粉芽孢杆菌M1摇瓶发酵条件优化及脱氮性能评价

旨在提高解淀粉芽孢杆菌M1液体发酵产芽孢量,并考察其对实际废水的反硝化脱氮效果。首先采用单因子实验研究了碳源、氮源、初始pH值、温度、转速和装液量等因子对M1液体发酵产芽孢量的影响。然后对其中显著性因子:氮源浓度、接种量、装液量、温度4个因素进行正交试验,进一步优化发酵条件。结果显示,优化后的培养基成分为:5 g/L碳源(可溶性淀粉)、10 g/L氮源(酵母粉∶蛋白胨=2∶1)、1 g/L NaCl;最佳培养条件为:初始pH6.5、发酵温度34℃、摇床转速180 r/min、培养瓶装液量30%、接种量7%。在此条件下,芽孢杆菌M1芽孢数可达到6.8×108 CFU/mL,高于优化前的2.08×108 CFU/mL。将芽孢杆菌M1投加于反应器中,与不加菌种相比,反硝化脱氮效果提升15%-34%。     

一株产苝醌类光敏剂丝状真菌AL18的液体发酵工艺研究

为研究一株丝状真菌AL18产艹北醌类光敏剂的液体发酵工艺。以马铃薯综合培养基为发酵培养基,采用单次单因素实验法,研究了液体摇瓶培养条件对艹北醌类光敏剂产量的影响。实验结果表明:液体摇瓶最适培养条件为250ml三角瓶装液量40ml,接种量7.5%,接种种龄40h,初始pH5.75,摇床转数180r/min,30℃振荡培养48h。在此培养条件下,采用单因素法筛选了发酵培养基中的碳源、氮源和无机离子,选用L9(34)对筛选到的绵白糖(A)、蛋白胨(B)、蚕蛹粉(C)、CuSO4.5H2O(D)进行了正交试验。经优化后的发酵培养基配方为:马铃薯200g/L,绵白糖30g/L,蛋白胨3g/L,蚕蛹粉12.5g/L,磷酸二氢钾1g/L,硫酸镁0.5g/L,硫酸铜0.05g/L,VB1100mg/L。对此发酵培养基配方进行了5次验证实验,艹北醌类光敏剂的平均产量为1.21g/L。     

产紫杉醇内生真菌枝状枝孢霉MD2的发酵条件优化

[目的]通过优化内生真菌枝状枝孢霉MD2的发酵条件,提高10-去乙酰巴卡亭Ⅲ (10-DAB)和紫杉醇(Taxol)的产量.[方法]采用单因素试验分析不同的培养基初始pH值、培养温度、摇床转速和培养时间对10-DAB和紫杉醇产量的影响,优化枝状枝孢霉MD2的培养条件;以YES为基本培养基,采用单因素试验和正交试验分析添加苯甲酸钠、苯丙氨酸、丝氨酸和甘氨酸4种前体物对10-DAB和紫杉醇产量的影响,优化枝状枝孢霉MD2的培养基组分.[结果]优化后发酵条件为:在初始pH为5.0的300 mL YES培养基中,添加15 mg/L苯甲酸钠、25 mg/L苯丙氨酸、5 mg/L丝氨酸、15 mg/L甘氨酸,接种1 mL枝状枝孢霉MD2的孢子悬液(107-10s个孢子/mL),28.0℃、220 r/min发酵培养12d.在此条件下,枝状枝孢霉MD2的生物量、10-DAB和紫杉醇的产量分别为15.5 g/L、471.5 μg/L和569.5 μg/L,与初始发酵条件相比,分别提高了1.3、3.6和3.4倍.[结论]首次获得了枝状枝孢霉MD2生产10-DAB和紫杉醇的较适摇瓶发酵条件,可为进一步放大发酵培养提供参考.     

啤酒糟固态发酵产β-葡萄糖苷酶的研究

利用啤酒糟为培养基对黑曲霉固态发酵产β-葡萄糖苷酶的工艺条件进行了优化和动力学研究。单因素试验表明,最适产酶温度、料液比和接种量分别为30℃、1∶5(啤酒糟∶水,g∶mL)和10%(mL/g);利用L9(34)正交试验优化反应条件,结果表明,在25℃,初始料水比为1:5,接种量10%的条件下,培养4d,β-葡萄糖苷酶的酶活可达10.85U/g。动力学研究表明,β-葡萄糖苷酶在96h进入产酶的高峰期,120h达到酶活最大值。     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。     

Optimization of bio-hydrogen production from biodiesel wastes by Klebsiella pneumoniae

Biodiesel wastes containing glycerol were utilized by Klebsiella pneumoniae DSM 2026 to produce hydrogen. The optimization of medium components was performed using both Plackett-Burman and uniform design methods. Using the Plackett-Burman design, glycerol, yeast extract, NH(4)Cl, KCl and CaCl2 were found to be the most important components, which were further investigated by uniform design and second-order polynomial stepwise regression analysis. The optimized medium containing 20.4 g.L(-1) glycerol, 5.7 g.L(-1) KCl, 13.8 g.L(-1) NH(4)Cl, 1.5 g.L(-1) CaCl(2) and 3.0 g.L(-1) yeast extract resulted in 5.0-fold increased level of hydrogen (57.6 mL/50 mL medium) production compared to initial level (11.6 mL/50 mL medium) after 24 h of fermentation The optimization of fermentation condition (pH, temperature and inoculum) was also conducted. When the strain grew in the optimized medium under optimal fermentation condition in a 5-L stirred tank bioreactor for batch production, hydrogen yield and production reached 0.53 mol/mol and 117.8 mmol/L, respectively. The maximum hydrogen evolution rate was 17.8 mmol/(L.h). Furthermore, 1,3-propanediol (6.7 g.L(-1)) was also obtained from the liquid medium as a by-product.     

Chemiluminescence of daphnia cultivating medium and optimization of conditions for its determination

The article deals with the optimization of conditions for the chemiluminescence determination. The Daphnia habitat was shown to have no spontaneous chemiluminescence. This was revealed using hydrogen peroxide and luminol, the optimal concentrations of which were 23 and 1.6 x 10(-2) mmol/L. p-Iodphenol at low concentrations (4 x 10(-5)-2 x 10(-3) mmol/L) did not render its effect chemiluminescence signal while at high concentrations (4 x 10(-2) mmol/L) an inhibition of chemiluminescence was observed. To obtain the needed intensity of chemiluminescence no more than 5 daphnia persons is required to incubate in volume of 10 mL of sample for analyzing. The intensity of chemiluminescence of daphnia cultivating medium and the sensitivity of this organism to potassium chromate increased at the temperature increasing from 24 to 32 degrees C. Daphnia cultivating medium can be preserved in refrigerator for several hours without lost of chemiluminescence signal.     

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。     

液化沙雷氏菌磷脂酶A1的克隆表达及乳糖自诱导发酵

为了利用大肠杆菌高效生产重组磷脂酶,克隆了液化沙雷氏菌磷脂酶A1的编码基因pla,分别使用pET-28a(+)和pET-20b(+)载体,实现了磷脂酶A1在大肠杆菌BL21(DE3)中的功能表达.重组菌利用载体pET-28a(+)在原始信号肽的介导下胞外PLA1酶活达40.8 U/mL,占总酶活的91％.重组菌转接至优化后的发酵诱导培养基:蛋白胨10 g/L,酵母粉5g/L,葡萄糖0.8 g/L,乳糖5 g/L,25 mmol/L Na2HPO4,25 mmol/L KH2PO4和1 mmol/L MgSO4;菌体生长6h后,添加7.5 g/L的甘氨酸,37℃恒温发酵24 h,重组菌胞外PLA1酶活达到128.7 U/mL.     

Optimization of fermentation medium and conditions for mycelial growth and water-soluble exo-polysaccharides production by Isaria farinosa B05

The optimal fermentation medium and conditions for mycelial growth and water-soluble exo-polysaccharides production by Isaria farinosa B05 were investigated. The medium components and fermentation conditions were optimized according to the one at a time method, while the concentration of medium components was determined by the orthogonal matrix method. The results showed that the optimal fermentation medium was as follows: sucrose 3.5% (w/v), peptone 0.5%, yeast extract 0.2%, K(2)HPO(4) 0.1%, and MgSO(4) 0.05%. The suitable fermentation conditions were as follows: initial pH 7.0, temperature 25 degrees C, medium volume 75 mL/250 mL, inoculum volume 5% (v/v), time 5d. In such optimal nutrition and environmental conditions, the maximal mycelial yield was 2.124 g/100 mL after 4 day's fermentation, while maximal water-soluble exo-polysaccharides production reached 2.144 g/L after 5 day's fermentation.     

杂色云芝产漆酶的发酵条件研究*

本文对杂色云芝（Coriolus versicolor）产漆酶的发酵条件作了研究。结果表明摇瓶实验产漆酶（Laccase）的最佳培养基成分为：可溶性淀粉 2g/L, NH4Cl 24mmol/L, 微量元素混合液 7ml/L, pH3.0柠檬酸—Na2HPO4缓冲溶液 0.01mol/L, KH2PO4 1.4×10-2 mol/L, MgSO4·7H2O 2.03×10-3mol/L, CaCl2·2H2O 6.8×10-4 mol/L, VB1 2.97×10-6 mol/L, 吐温80 4.0g/L, 愈创木酚0.01mmol/L, CuSO4 ·5H2O 0.005mmol/L,最佳发酵条件为培养基初始pH3.0, 菌体生长6d,培养基装量为250ml三角瓶中25ml培养液,25℃条件下振荡培养(150r/min)9d。     

Production of probiotic cabbage juice by lactic acid bacteria

Research was undertaken to determine the suitability of cabbage as a raw material for production of probiotic cabbage juice by lactic acid bacteria (Lactobacillus plantarum C3, Lactobacillus casei A4, and Lactobacillus delbrueckii D7). Cabbage juice was inoculated with a 24-h-old lactic culture and incubated at 30 degrees C. Changes in pH, acidity, sugar content, and viable cell counts during fermentation under controlled conditions were monitored. L. casei, L. delbrueckii, and L. plantarum grew well on cabbage juice and reached nearly 10x10(8) CFU/mL after 48 h of fermentation at 30 degrees C. L. casei, however, produced a smaller amount of titratable acidity expressed as lactic acid than L. delbrueckii or L. plantarum. After 4 weeks of cold storage at 4 degrees C, the viable cell counts of L. plantarum and L. delbrueckii were still 4.1x10(7) and 4.5x10(5) mL(-1), respectively. L. casei did not survive the low pH and high acidity conditions in fermented cabbage juice and lost cell viability completely after 2 weeks of cold storage at 4 degrees C. Fermented cabbage juice could serve as a healthy beverage for vegetarians and lactose-allergic consumers.     

Fermentation and recovery of glutamic acid from palm waste hydrolysate by Ion-exchange resin column

Glutamic acid produced from palm waste hydrolysate by fermentation with Brevibacterium lactofermentum ATCC 13869 is produced with a remarkably high yield compared with that produced from pure glucose as a carbon source. The produce yield is 70 g/L with glucose, wherease, when palm waste hydrolysate is the fermentation medium in the same bioreactor under same conditions, it is 88 g/L. The higher yield may be attributed to the fact that this organism has the ability to convert sugars other than only glucose present in the hydrolysate. Bioreactor conditions most conducive for maximum production are pH 7.5, temperature of 30 degrees rmentation period of 48 h, inoculum size 6%, substrate concentration of 10 g per 100 mL, yeast extract 0.5 g per 100 mL as a suitable N source, and biotin at a concentration of 10 pg/L. Palm waste hydrolysate used in this study was prepared by enzymic saccharification of treated palm press fiber under conditions that yielded a maximum of 30 g/L total reducing sugars. Glutamic acid from fermentation broth was recovered by using a chromatographic column (5cm x 60 cm) packed with a strong ion-exchange resin. The filtered broth containing glutamic acid and other inorganic ions was fed to the fully charged column. The broth was continuously recycled at a flow rate of 50 mL/min (retention time of 55 min) until glutamic acid was fully adsorbed on the column leaving other ions in the effluent. Recovery was done by eluting with urea and sodium hydroxide for total displacement of glutamic acid from the resin. The eluent containing 88 g/L of glutamic acid was concentrated by evaporation to obtain solid crystals of the product. (c) 1995 John Wiley & Sons, Inc.     

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。