培养条件对凝结芽孢杆菌芽孢形成的影响

目的:提高凝结芽孢杆菌芽孢形成率及芽孢数量,为凝结芽孢杆菌芽孢制剂的产业化生产提供理论依据.方法:在摇瓶、15L自动发酵罐中考察了碳源、氮源、无机盐、微量元素Mn2+、pH、温度、接种量、溶氧水平对凝结芽孢杆菌液体培养形成芽孢的影响.结果:芽孢形成的最适培养基组成为:麸皮20g/L,酵母膏5g/L,豆粕粉10g/L,NaCl 5g/L,K2HPO4 3g/L,MnSO4.3g/L;最适培养条件为:初始pH7.0,接种后最适起始芽孢浓度为106CFU/mL,培养温度为40℃,180r/min摇瓶培养,250mL三角瓶中最适装液体积为15mL.在15L自动发酵罐中扩大培养,控制溶氧在30%以上,培养20h,芽孢数量可达5.8×109CFU/mL,芽孢率达96.7%.结论:试验获得的最佳培养条件可进一步应用于生产.     

蔗渣发酵菌剂培养基的筛选及发酵条件的优化

采用单因素和正交试验研究了蔗渣高效发酵菌剂(芽孢杆菌B-A、曲霉菌F-A、链霉菌A-B)的摇瓶发酵最佳工艺条件.结果表明:芽孢杆菌B-A的最佳培养基配方:牛肉膏0.3%、蛋白胨1%、葡萄糖1%、NaCl 0.5%、可溶性淀粉0.5%、3.08%浓度的MnSO4溶液0.1;最适发酵条件为pH7、装液量100 ml(250 ml三角瓶)、36℃培养27 h.曲霉F-A的最佳培养基配方:葡萄糖3%、豆饼粉3%、蛋白胨1.2%、酵母膏0.3%、K2HPO4 0.05%、KH2PO40.05%、CaCl20.08%、MgSO40.04%、MnSO40.04%、ZnSO40.02%;最适发酵条件为pH6、装液量50 ml、30℃培养3 d.链霉菌A-B的最佳培养基配方:可溶性淀粉4.5%、蔗糖1%、豆饼粉3%、NaNO30.2%、ZnSO40.01%、KH2PO40.001%;最适发酵条件为pH7、装液量50 ml、30℃培养3 d.     

链霉菌FIM-0916产安福霉素的发酵条件优化

本文采用单因素和正交试验设计,对链霉菌 Streptomyces canus sp. FIM-0916产安福霉素的发酵培养基配方及发酵条件进行了优化。优化后的最佳培养基配方为：蔗糖1.5%,黄豆粉1.0%,组氨酸0.1%,KNO3 0.1%, CaCO3 0.1%。最佳发酵条件为：种子菌龄54 h,装液量120 mL/500 mL,接种量2%,发酵温度28℃,摇床转速250 r/min;最佳发酵时间为5 d。在该优化条件下,安福霉素的发酵效价比对照提高248%,为安福霉素的后续开发奠定了基础。     

蜡样芽孢杆菌CP-1对Cr(Ⅵ)还原效果研究

为了提高蜡样芽孢杆菌CP-1菌株对Cr(Ⅵ)的还原效果,采用单因素和正交试验,通过摇瓶发酵培养,对影响蜡样芽孢杆菌CP-1菌株还原Cr(Ⅵ)的发酵培养基成分和培养条件进行了优化,并研究了最佳发酵条件下的蜡样芽孢杆菌CP-1对Cr(Ⅵ)的还原效果。结果表明,蜡样芽孢杆菌CP-1菌株还原Cr(Ⅵ)的最佳培养基组成为:1%甘露醇, 3%的大豆蛋白胨, 0.05%KCl, 0.1%CuSO4,在此基础上的最佳培养条件为:pH7.0、6%接种量、45℃培养3 d,在此条件下,Cr(Ⅵ)初始浓度为100mg·L^-1时,对Cr(Ⅵ)的还原率达99.75%。在Cr(Ⅵ)污染的土壤中添加蜡样芽孢杆菌CP-190d后,土壤中的Cr(Ⅵ)含量降低55.15%左右。     

芽孢乳杆菌发酵葡萄糖制备D(-)-乳酸的研究

在国内首次报道了发酵法制备D(-)-乳酸,采用芽孢乳杆菌(Sporolactobacillus sp．)从葡萄糖发酵制备D-乳酸。该发酵为微需氧,发酵培养基组成(g/L):葡萄糖60,酵母膏6,玉米浆5,NH4NO3l,麸皮2,NaH2PO4 4,CaCO340。发酵液的初始pH为7．0.在最佳条件下,37℃发酵72h可产40．7g/L的D-乳酸,葡萄糖转化率67．83％。通过离子配位色谱分析,产物的D-乳酸光学纯度为96．04％e．e．。     

重组大肠杆菌产γ-环糊精葡萄糖基转移酶的摇瓶发酵优化

为了实现来源于碱性芽孢杆菌Alkalophilic Bacillus clarkii 7364的γ-环糊精葡萄糖基转移酶的高效胞外表达,对OmpA信号肽介导的E.coli BL21(DE3)/pET20b(+)-γcgt基因工程菌进行发酵培养基及发酵条件的优化,并进行正交试验,获得最优培养基:甘油5g/L、蛋白胨6g/L、酵母膏24g/L、钙离子6mmol/L、镁离子2mmol/L、甘氨酸0.75%、PO₄^3- 0.1mol/L;在此基础上最适发酵条件:pH6.5、25℃培养、装液量30ml/250ml、转速220r/min、0.02%SDS、在发酵10h时利用5g/L乳糖进行诱导,使得酶活从初始的5189.2U/ml提高到20268.8U/ml。研究结果得到高效表达的培养条件,为实现该酶的工业化应用打下了基础。     

酵母产γ-氨基丁酸发酵培养基的优化

目的:提高酵母产γ-氨基丁酸的能力。方法:采用单因素及正交设计实验对酵母产γ-氨基丁酸(GABA)的培养基进行优化。结果:确定最适碳源为葡萄糖,最佳氮源为蛋白胨和硫酸铵复合氮源,合适的无机盐为KH2PO4;最佳发酵培养基为3%葡萄糖,3%蛋白胨,0.3%(NH4)2SO4和0.1%KH2PO4。在此培养条件下,摇瓶发酵可以获得1.690g.L-1的GABA产量。结论:发酵培养基的优化,提高了菌株产γ-氨基丁酸的能力。     

酵母产γ-氨基丁酸发酵培养基的优化

目的：提高酵母产γ-氨基丁酸的能力。方法：采用单因素及正交设计实验对酵母产γ-氨基丁酸（GABA）的培养基进行优化。结果：确定最适碳源为葡萄糖,最佳氮源为蛋白胨和硫酸铵复合氮源,合适的无机盐为KH2PO4;最佳发酵培养基为3%葡萄糖,3%蛋白胨,0.3%（NH4）2SO4和0.1%KH2PO4。在此培养条件下,摇瓶发酵可以获得1.690g.L-1的GABA产量。结论：发酵培养基的优化,提高了菌株产γ-氨基丁酸的能力。     

嗜线虫致病杆菌产生抗生素的培养基及条件

本对嗜线虫致病杆菌（Xenorhadbus nematophilus）产生抗生素的发酵培养基和发酵条件进行了研究,同时对该菌代谢过程pH值、还原糖、总糖、氨基氮与抗生素产量的关系进行了分析,通过筛选该菌对碳源和氮源的要求,用正交试验初步确定了该菌产素的最佳发酵培养基和条件为：玉米粉1％,大豆粉3％,蔗糖1％,蛋白胨1.5％,KH2PO40.02％,MgSO40.2％,活化剂T0.1％;发酵培养基的起始pH值在6.0－8.0,种龄16h,接种量4％,500mL摇瓶装量15－150mL的条件下培养72h可获得较高的抗生素产量;产素量与菌代谢过程中pH、还原糖、总糖和氨基氮的变化有一定关系,通过培养基和培养条件的研究使该菌的产抗生素能力提高了56.3％。     

响应面法优化提高萎缩芽孢杆菌E20303抑制马铃薯干腐病病原菌活性的研究

【背景】萎缩芽孢杆菌E20303可以有效地抑制马铃薯干腐病病原菌的活性,而响应面法可在较少的试验次数下优化生防菌发酵培养基配方与发酵条件,获得的最优组合将为马铃薯干腐病生防菌剂的制备与应用提供参考。【目的】以分离自青海察尔汗盐湖湖泥中且对马铃薯干腐病病原菌具有较高抑菌活性的萎缩芽孢杆菌E20303为研究对象,利用响应面法对其培养基配方和发酵条件进行优化,以期提高其对马铃薯干腐病病原菌的抑菌活性。【方法】采用单因素试验、中心组合设计试验及响应面法设计优化萎缩芽孢杆菌E20303发酵培养基配方及发酵条件。【结果】培养基最优发酵配方(g/L):淀粉10.72、酵母粉23.60、七水合硫酸镁16.00、碳酸钙1.14、磷酸二氢钾8.00和磷酸氢二钾16.00,优化后抑菌率由46.51%提高至62.00%;最优发酵条件为装液量102.89 mL、pH 8.64、温度28.73℃、转速200 r/min、培养时间3 d、接种量2%,优化后抑菌率由51.15%提高至72.51%。【结论】实验获得了对马铃薯干腐病病原菌的抑菌活性明显提高的萎缩芽孢杆菌E20303发酵配方及发酵条件,为马铃薯干腐病生防制...     

响应面法优化甘蔗糖蜜发酵产丁醇

以甘蔗糖蜜为底物,用响应面法对高丁醇比突变菌株拜氏梭菌(Clostridium beijerinckii)ART124发酵生产丁醇的培养条件进行优化.首先利用Plackett - Burman试验设计筛选出影响丁醇生产的3个重要因素CaCO3和NH4 HCO3和K2HPO4的用量,再通过最陡爬坡路径逼近最大向应区域,最后根据响应面中心组合设计理论,确定主要影响因素的最佳条件:CaCO3、NH4HCO3和K2HPO4的质量浓度分别为2.65、2.16和0.43 g/L.利用数学模型分析预测得甘蔗糖蜜质量浓度为30 g/L时,最佳的丁醇产量为8.10 g/L,比优化前提高了53.14％.在最佳工艺条件下得到的实验结果与模型预测值很吻合,说明所建立的模型是有效的.     

米根霉利用纯糖和不同预处理玉米秸秆酶解糖生产L-乳酸

通过单因素实验设计,优化米根霉摇瓶发酵产L-乳酸。在此基础上,以蒸气爆破和碱处理玉米秸秆酶解液为混合C源,与纯糖对比,研究不同预处理玉米秸秆混合C源对米根霉发酵产L-乳酸的影响。结果显示:在初始葡萄糖质量浓度100g/L、(NH4)2SO4质量浓度2g/L、接种量6%(体积分数)、转速170r/min、发酵12h后添加30g/LCaCO3的条件下,米根霉发酵产L-乳酸质量浓度为69.15g/L。米根霉发酵不同预处理玉米秸秆酶解混合C源,木糖的存在影响了米根霉的C代谢网络,降低L乳酸的产量。     

一株拜氏梭菌利用甘蔗废糖蜜发酵生产丙酮丁醇

以甘蔗废糖蜜作为原料,利用Clostridium beijerinckii DSM 6422菌株进行丙酮丁醇发酵的初步研究.结果表明:采用H2SO4预处理糖蜜,初糖质量浓度60 g/L,(NH4)2SO4 2g/L,CaCO3 10 g/L,温度30℃,pH 5.5～7.0,接种量6％(体积分数),在5L发酵罐中发酵培养96 h,总溶剂产量为16.17 g/L,其中丁醇质量浓度为10.07 g/L,总溶剂产率为30.2％,糖利用率为89.3％.     

Gluconic acid production byPenicillium puberulum

Twenty-five Penicillium species isolated from Egyptian soil were examined for their ability to produce gluconic acid in surface culture. Of the eight species capable of producing gluconic acid, Penicillium puberulum gave the maximum yield (91% gluconic acid from glucose after 7 days of fermentation with 3% CaCO3). Peptone was the best nitrogen source for acid fermentation and glucose was superior to sucrose. Addition of low concentrations of KH2PO4 and MgSO4 - 7 H2O stimulated acid production. An initial pH of 6.1 was most favourable for acid accumulation and addition of CaCO3 was necessary for maximum acid production.     

Production of rosamicin: improvement of synthetic medium

Rosamicin is one of the important macrolide antibiotics that has clinical efficacy and broad-spectrum antibacterial activity. Using a mutant strain of Micromonospora rosaria (NRRL 3718), a chemically defined medium was developed, and some fermentation conditions that are important to rosamicin biosynthesis were optimized to achieve rosamicin productivity of 230 mug/ml. Soluble starch and l-asparagine were found to be the best carbon and nitrogen sources, and a stimulative effect of magnesium and zinc ions was also found. The medium developed contains: soluble starch, 4%; l-asparagine, 0.15%; K(2)HPO(4), 0.075%; CaCO(3), 0.6%; MgSO(4) . 7H(2)O, 0.05%; FeSO(4) . 7H(2)O, 10 M; CuSO(4) . 5H(2)O, 10 M; ZnSO(4) . 7H(2)O, 10 M; and MnSO(4) . (4-6)H(2)O, 10 M. The required air supply was about 40 mmol of O(2) liter . h . atm, and the favorable culture temperature was 28 to 29 degrees C.     

Optimization of fermentation medium for xylanase-producing strain Xw2

To improve the fermentation yield of xylanase by optimizing the fermentation conditions for strain Xw2, a Plackett-Burman design was used to evaluate the effects of eight variables on xylanase production by strain Xw2. The steepest ascent （descent） method was used to approach the optimal response surface experimental area. The optimal fermentation conditions were obtained by central composite design and response surface analysis. The results showed that the composition of the optimal fermentation medium was corn cob ＋ 1.5% wheat bran （1：1）, 0.04% MnSO4, 0.04% K2HPO4. 3H2O, and an inoculum size of 6% in 50 mL liquid volume （pH = 6.0）. The optimal culture conditions were 28oc at 150 r/min for 54.23 h. The results of this study can serve as the basis for the industrial production and application of xylanase.     

Production of acetone butanol ethanol (ABE) by a hyper-producing mutant strain of Clostridium beijerinckii BA101 and recovery by pervaporation.

A silicone membrane was used to study butanol separation from model butanol solutions and fermentation broth. Depending upon the butanol feed concentration in the model solution and pervaporation conditions, butanol selectivities of 20.88-68.32 and flux values of 158.7-215.4 g m(-)(2) h(-)(1) were achieved. Higher flux values (400 g m(-)(2) h(-)(1)) were obtained at higher butanol concentrations using air as sweep gas. In an integrated process of butanol fermentation-recovery, solvent productivities were improved to 200% of the control batch fermentation productivities. In a batch reactor the hyper-butanol-producing mutant strain C. beijerinckii BA101 utilized 57.3 g/L glucose and produced 24.2 g/L total solvents, while in the integrated process it produced 51.5 g/L (culture volume) total solvents. Concentrated glucose medium was also fermented. The C. beijerinckii BA101 mutant strain was not negatively affected by the pervaporative conditions. In the integrated experiment, acids were not produced. With the active fermentation broth, butanol selectivity was reduced by a factor of 2-3. However, the membrane flux was not affected by the active fermentation broth. The butanol permeate concentration ranged from 26.4 to 95.4 g/L, depending upon butanol concentration in the fermentation broth. Since the permeate of most membranes contains acetone, butanol, and ethanol (and small concentrations of acids), it is suggested that distillation be used for further purification.     

产木聚糖酶芽胞菌Y-12的筛选及产酶条件的研究

利用透明圈平板培养和木聚糖发酵试验,筛选出1株高产木聚糖酶的芽胞杆菌,并对该菌株的酶学特性和适宜发酵条件进行研究。结果表明,此菌对秸秆和麦麸的分解率分别为43.3%和63.4%。产酶较高的最适培养条件,即大豆蛋白胨2%、胰蛋白胨3%、酵母粉0.1%和葡萄糖2%。适宜反应温度和pH分别为37℃和7。采用10 L发酵罐发酵,培养48 h后,酶活达3024 U/m l,比三角瓶发酵(酶活达2185 U/m l)提高了38%。     

重组谷氨酸棒杆菌发酵L-苯丙氨酸培养基的优化

【目的】提高重组谷氨酸棒杆菌发酵L-苯丙氨酸(L-phenylalanine,L-Phe)的产量。【方法】使用正交试验设计以及响应面优化法分别对种子培养基及发酵培养基进行优化,确定了重组谷氨酸棒杆菌发酵L-Phe的最佳种子培养基及最佳发酵培养基。【结果】重组谷氨酸棒杆菌发酵L-Phe最佳种子培养基(g/L):葡萄糖25.0,玉米浆25.0,硫酸铵15.0,硫酸镁1.0,磷酸二氢钾2.0,尿素2.0,p H 6.8-7.0;最佳发酵培养基(g/L):葡萄糖110.0,玉米浆7.0,硫酸铵25.0,硫酸镁1.0,磷酸二氢钾1.0,柠檬酸钠2.0,谷氨酸1.0,碳酸钙25.0,p H 6.8-7.0;在最佳培养基条件下L-Phe产量最高达到9.14 g/L,较优化前的7.46 g/L提高了22.5%。【结论】通过正交试验和响应面分析对重组谷氨酸棒杆菌发酵L-Phe培养基进行优化,明显提高了L-Phe的产量,并确定了葡萄糖、玉米浆和硫酸铵为发酵培养基中影响L-Phe产量的3个关键因子。研究结果为L-Phe的发酵放大提供了依据。     

苏云金杆菌ZLL13晶体蛋白分析及其菌糠液态培养基的优化

食用菌栽培废料,简称菌糠(spent mushroom substrate, SMS)是食用菌栽培和生产的残留物,其含有丰富的甲壳素、木质纤维和蛋白质等,可为苏云金芽孢杆菌(Bacillus thuringiensis, Bt)的生长提供所需的营养物质。本研究以优化后的前处理条件制备的菌糠浸提液(2%硫酸, 121℃, 1 h)作为主要碳源,通过单因素试验、Plackett-Burman设计、最陡爬坡和响应面分析等方法来优化最佳培养基组分,结果表明,54%SMS浸提液,31.9 g/L大豆饼粉、0.88 g/L CaCO3、0.4 g/L MnSO4、0.5 g/L K2HPO4和0.4 g/L吐温100为最佳培养基配方,且优化后培养基(1.8×108/mL)产生的孢子数是原始SMS培养基(0.065×108/mL)的27倍,这不仅为菌糠的二次利用提供一种新的有效方法,而且也可以大大降低生产Bt所需要的发酵成本,具有良好的应用前景。