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。     

红酵母类胡萝卜素形成的生理学研究

从数株红酵母中选出 1株产类胡萝卜素能力较强的红酵母RY 98(生物量、类胡萝卜素含量和产量分别为19.9g/L ,334 .8μg/ g和 6 .7mg/L) ;研究了该菌株产类胡萝卜素的最适营养与环境条件 ,获得了最佳的发酵生理学条件 :葡萄糖 40 g/L ,(NH4 ) 2 SO4 10 g/L ,酵母膏 3g/L ,蕃茄汁 2mL/L ,花生油 0 .5mL/L ,接种量 30mL/L ,初始pH 6 .0和通气量 (培养基装量 ) 4 0mL/ 2 5 0mL。在此初步优化的培养条件下 ,红酵母RY 98经 72h摇瓶发酵其生物量、类胡萝卜素含量和产量分别可达 2 6 .8g/L ,386 .9μg/ g和 10 .4mg/L ,依次比初筛中提高了 34 .7% ,15 .6 %和 5 5 .2 %。     

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.     

前体及诱导子和发酵条件对烟曲霉TMS-26产紫杉醇发酵体系优化

紫杉醇是一种广谱的抗癌药物,因其具有独特的抗癌机制、良好的抗癌效果和供不应求的市场等特征而备受关注。紫杉醇具有重大经济效益,但产量受到制约,价格极为昂贵,通过内生真菌发酵法生产紫杉醇能在一定程度上缓解其来源困难的问题。在产紫杉醇内生真菌TMS-26发酵液中添加前体物质和诱导子,并通过对接种量、装液量、初始pH和发酵时间等条件进行优化研究。单因素及正交试验表明在PDB培养基中加入苯丙氨酸20mg/L、苯甲酸钠30mg/L、乙酸钠8g/L、甘氨酸15mg/L、CuSO₄ 0.05mg/L、H₂O₂ 6mmol/L、3,5-二硝基水杨酸15mg/L时能有效提高紫杉醇产量,比优化前增产46.64%,达到446.28µg/L,并且发现最适菌株TMS-26的发酵条件为pH7.5、接种量5%、装液量120mL/250mL、发酵时间为10d。     

红酵母类胡萝卜素高产菌株的筛选及其发酵生理学条件研究

从数株红酵母中选出了1株产类胡萝卜素能力较强的红酵母RY－98（生物量,类胡萝卜素含量和产量分别为19．9g/L,334.8ug/g和6．7mg/L);研究了该菌株产类胡萝卜素的最适营养与环境条件,获得了最佳的发酵生理学条件;葡萄糖40g/L,(NH4)2SO4 10g/L,酵母膏3g/L,蕃茄汁2mL/L,花生油0.5mL/L,接种量30mLL初始pH6.0和通气量（培养基装置040ml/250mL:,在此初步优化的培养条件下,红酵母RY－98经72小时摇瓶发酵其生物量,类胡萝卜素含量和产量分别可达26．8g/L,386.9ug/g和10．4mg/L,依次比初筛中提高了34．7％,15．6％,和55．2％。     

珍稀药用真菌——樟芝深层发酵培养条件的优化

对樟芝深层发酵培养基进行了筛选,并在此基础上对发酵条件进行了优化。以樟芝深层发酵菌丝体三萜产量为主要目标产物,确定发酵培养条件为:40g/L葡萄糖,6g/L豆饼粉,1g/L K_2HPO_4,0．5g/L MgSO4,VB_1 100mg/L,自然pH,接种量为20%,装液量为100mL/250mL三角瓶,转速100r/min,26℃恒温培养6d,胞内三萜产量达15．25mg/100mL发酵液。     

酸奶菌群发酵糖蜜产复合有机酸化剂的研究

【背景】开发安全、有效、稳定、适口性好、对环境无危害的无抗饲料添加剂是我国畜牧业的重中之重,酸化剂作为功能性饲料添加剂在众多替抗产品中有较大的优势。【目的】通过酸奶菌群发酵甜菜糖蜜制备低成本乳酸型复合液态酸化剂。【方法】以11种不同的新疆农牧民传统发酵酸奶菌群为出发菌,经MRS培养基富集乳酸菌群,选择产酸量高的菌群进行甜菜糖蜜发酵试验,并对菌群发酵时间、发酵条件、糖蜜浓度、氮源及中和剂进行优化。【结果】在糖蜜浓度为100 g/L、培养基未灭菌且37℃静置发酵48 h时,B2菌群发酵乳酸产量为34.52 g/L,总酸为83.42 g/L,加入中和剂Na₂CO₃后其乳酸产量达73.42 g/L,总酸达到169.37 g/L;B5菌群发酵乳酸产量可达61.12 g/L,总酸可达112.50 g/L,加入中和剂Ca（OH）₂后其乳酸产量达74.37 g/L,总酸为137.26 g/L。B2菌群发酵原液对沙门氏菌、金黄色葡萄球菌及产气荚膜杆菌均有较强的抑制作用;B5菌群发酵原液则对产气荚膜杆菌、沙门氏菌、金黄色葡萄球菌、大肠杆菌O...     

稀土元素对红霉素发酵的影响

通过对红霉素发酵培养基中添加稀土元素的研究,确定了几种能对发酵效价有提高作用的稀土元素及其浓度,当其中镧La^3＋、钕Nd^3＋和铈Ce^4＋离子浓度分别为50mg／L、50mg/L和100mg／L时对提高红霉素效价水平最显著,提高了32％、25％和25％,并且对改善红霉素组分也有明显作用,红霉素A组分相对百分含量分别提高18．9％、32．7％和34．4％,红霉素B组分分别减少24．1％、58．6％和62．1％。     

不同生境微生物转化H2/CO2产乙酸及其在合成气发酵中应用

【目的】合成气发酵对大力开发可再生资源和促进国家可持续发展具有重要意义,研究旨在探究不同生境微生物转化H2/CO2产乙酸及其合成气发酵的潜力。【方法】采集剩余污泥、牛粪、产甲烷污泥和河道底物样品在中温(37 °C)条件下生物转化H2/CO2气体,将来源于牛粪样品的H2/CO2转化富集物用于合成气发酵,通过454高通量技术和定量PCR技术分析复杂微生物群落的组成,GC气相色谱法检测气体转化产生的挥发性脂肪酸(VFAs)浓度。【结果】牛粪和剩余污泥微生物利用H2/CO2气体生成乙酸、乙醇和丁酸等,最高乙酸浓度分别为63 mmol/L和40 mmol/L,明显高于河道底物和产甲烷污泥样品的最高乙酸浓度3 mmol/L和16 mmol/L。牛粪和剩余污泥微生物中含有种类多样化的同型产乙酸菌,剩余污泥中同型产乙酸菌主要为Clostridium spp.、Sporomusa malonica和Acetoanaerobium noterae,牛粪中则为Clostridium spp.、Treponema azotonutricium和Oxobacter pfennigii。【结论】同型产乙酸菌的丰富度和数量两个因素都对复杂微生物群落转化H2/CO2产乙酸效率至关重要;转化H2/CO2得到的富集物可用于合成气发酵产乙酸和乙醇,这为基于混合培养技术的合成气发酵提供了依据。     

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％.     

黄孢原毛平革菌产絮凝剂营养条件优化

微生物絮凝剂与传统化学絮凝剂相比,安全无毒、无二次污染,具有开发潜力.黄孢原毛平革菌(Phanerochaete chrysosporium)能产生微生物絮凝剂,但目前缺少对其产絮凝剂营养条件的优化.使用高岭土并利用单因素法研究碳源、氮源、碳氮比、接种量对Phanerochaete chrysosporium产絮凝剂的...     

Production of ethanol by Clostridium thermosaccharolyticum: I. Effect of cell recycle and environmental parameters

The direct microbial conversion (DMC) process for the production of ethanol from lignocellulosic biomass is limited by low volumetric ethanol production rates due to the low cell densities of Clostridium thermosaccharolyticum which is a key organism for ethanol production in this process. Hence, this study focuses on the use of a continuous- culture cell recycle system to improve the volumetric ethanol productivity and yield of the fermentation of xylose by C. thermosaccharolyticum. Early experiments with the continuous-culture cell recycle system showed a two-fold improvement in volumetric ethanol productivity. However, the ethanol yield at the higher dilution rates suffered because of the large amount of lactate produced. The manipulation of two environmental parameters-iron concentration in the nutrient medium and the N(2) purge rate of the fermentor headspace-allowed a dramatic reduction in the lactate production and a simultaneous improvement in the ethanol titer and yield. Under the improved conditions of increased iron concentration (12.5 mg/L FeSO(4) . 7H(2)O) and decreased N(2) purge rate (0.1 L/min), a continuous culture of C. thermosaccharolyticum operating at a dilution rate of 0.24 h(-1) and 50% cell recycle produced 8.6 g/L ethanol and less than 1 g/L each of acetate and lactate. The volumetric ethanol productivity was 2.2 g/L/h, which is 8 times larger than obtained for a continuous culture operated with no cell recycle and the same specific growth rate.     

Efficient butanol production under aerobic conditions by coculture of Clostridium acetobutylicum and Nesterenkonia sp. strain F

Clostridium acetobutylicum is widely used for the microbial production of butanol in a process known as acetone–butanol–ethanol (ABE) fermentation. However, this process suffers from several disadvantages including high oxygen sensitivity of the bacterium which makes the process complicated and necessitate oxygen elimination in the culture medium. Nesterenkonia sp. strain F has attracted interests as the only known non-Clostridia microorganism with inherent capability of butanol production even in the presence of oxygen. This bacterium is not delimited by oxygen sensitivity, a challenge in butanol biosynthesis, but the butanol titer was far below Clostridia. In this study, Nesterenkonia sp. strain F was cocultivated with C. acetobutylicum to form a powerful “coculture” for butanol production thereby eliminating the need for oxygen removal before fermentation. The response surface method was used for obtaining optimal inoculation amount/time and media formulation. The highest yield, 0.31 g/g ABE (13.6 g/L butanol), was obtained by a coculture initiated with 1.5 mg/L Nesterenkonia sp. strain F and inoculated with 15 mg/L C. acetobutylicum after 1.5 hr in a medium containing 67 g/L glucose, 2.2 g/L yeast extract, 4 g/L peptone, and 1.4% (vol/vol) P2 solution. After butanol toxicity assessment, where Nesterenkonia sp. strain F showed no butanol toxicity, the coculture was implemented in a 2 L fermenter with continual aeration leading to 20 g/L ABE.     

Effective production of N-acetyl-β-D-glucosamine bySerratia marcescens using chitinaceous waste

The strain ofSerratia marcescens QM B1466 produces selectively large amount of chitinolytic enzymes (about 1mg/L medium). Enzymatic hydrolysis of chitin to N-acetyl-β-D-glucosamine (NAG) was performed with a system consisting of two hydrolases (chitinase and chitobiase) produced by optimization of a microbial host consuming chitin particles. For the development of Large-scale biological process for the production of NAG from chitinaceous waste, the selection and optimization of a microbial host, particle size of chitin and pretreatment of chitin source were investigated. Also, the effect of crab/shrimp chitin sources and initial induction time using chitin as a sole carbon source on chitinase/chitobiase production and NAG production were examined. Crab-shell chitin(1.5%) treated by dilute acid and, ball-milled with a nominal diameter less than 250m gave the highest chitinase activity over a 7 days culture. Crude chitinase/chitobiase solution obtained in a 10 L fed-batch fermentation showed a maximum activities of 23.6 U/mL and 5.1 U/mL, respectively with a feeding time of 3 hrs, near pH 8.5 at 30°C.     

适合飞虱虫疠霉菌丝生产的液体培养基组分及发酵条件

蚜虫、飞虱、叶蝉等是威胁农业生产的刺吸式口器害虫,长期以来依赖化学农药防治,严重影响农产品的安全性和农业生态环境.探讨这类害虫的生物防治途径,减轻农产品化学农药的残留污染,一直受到国内外学者的关注.虫霉(En-tomophthorales)的许多种类具有优异的诱病杀虫能力,尤其通过主动弹射孢子而在害虫种群中高强度流行的特征,可在短期内迅速压低虫口密度,是极其重要的杀虫微生物资源[1～3].     

甘蔗糖蜜酒精废液混菌发酵菌体蛋白的研究

本文报导利用甘蔗糖蜜酒精废液混菌发酵高质量菌体蛋白的研究,通过热带假丝酵母Ｃａｎｄｉｄａ ｔｒｏｐｉｃａｌｉｓ种合融合株Ｃｔ－３配伍其他菌株,混菌发酵时间缩短２￣４ｈ,生物量可达２０ｇ／Ｌ,粗蛋白质含量５０￣５３％,灰份≤１０％,水分为５￣８％,与Ｃｔ－３单菌发酵相比,蛋白质提高４￣６％。     

Optimization of bioconversion conditions for vitamin D3 to 25-hydroxyvitamin D using Pseudonocardia autotrophica CGMCC5098

The optimal culture conditions for bioconversion of vitamin D₃ to calcifediol (25(OH)D₃) were investigated by varying carbon and nitrogen sources, metal salt concentrations, initial pH, temperature, solvents, surfactants, and agitation speed. In the process of this microbial hydroxylation, the timing of the addition of vitamin D₃, which is dissolved in ethanol, is of critical importance. Besides, the concentration of ethanol in zymotic fluid is the key factor to get high conversion ratio of vitamin D₃. In particular, the optimal culture conditions were 1.5% glucose, 1.5% soybean cake meal, 0.5% yeast extract, 0.5% corn steep liquor, 0.3% CaCO₃, 0.1% NaCl, 0.2% KH₂PO₄, pH 7.2 at 27?°C and the timing of the addition of vitamin D₃ dissolved in 5% (v/v) ethanol was 48?h followed by the inoculation of seed culture broth. Under the optimized conditions, the conversion of vitamin D₃ (1?g/L) by Pseudonocardia autotrophica CGMCC5098 in 50?L fermenter resulted in about 61.31% bioconversion ratio (639?mg/L) of 25(OH)D₃ on the 5th day.     

Perfusion culture process plus H2O2 stimulation for efficient astaxanthin production by Xanthophyllomyces dendrorhous

A semicontinuous perfusion culture process (repeated medium renewal with cell retention) was evaluated together with batch and repeated fed-batch processes for astaxanthin production in shake-flask cultures of Xanthophyllomyces dendrorhous. The perfusion process with 25% medium renewal every 12 h for 10 days achieved a biomass density of 65.6 g/L, a volumetric astaxanthin yield of 52.5 mg/L, and an astaxanthin productivity of 4.38 mg/L-d, which were 8.4-fold, 5.6-fold, and 2.3-fold of those in the batch process, 7.8 g/L, 9.4 mg/L, and 1.88 mg/L-d, respectively. The incorporation of hydrogen peroxide (H(2)O(2)) stimulation of astaxanthin biosynthesis into the perfusion process further increased the astaxanthin yield to 58.3 mg/L and the productivity to 4.86 mg/L-d. The repeated fed-batch process with 8 g/L glucose and 4 g/L corn steep liquor fed every 12 h achieved 42.2 g/L biomass density, 36.5 mg/L astaxanthin yield, and 3.04 mg/L-d astaxanthin productivity. The lower biomass and astaxanthin productivity in the repeated fed-batch than in the perfusion process may be mostly attributed to the accumulation of inhibitory metabolites such as ethanol and acetic acid in the culture. The study shows that perfusion process plus H(2)O(2) stimulation is an effective strategy for enhanced astaxanthin production in X. dendrorhous cultures.