鸡腿菇液体深层发酵工艺条件的研究

目的：研究碳源、氮源、接种量、初始pH值、温度等对鸡腿菇深层发酵的生物量和多糖产量的影响。方法：通过摇瓶培养确定了该菌株的发酵优化条件,在此条件下,获得了较高的多糖产量。结论：结果表明葡萄糖、酵母浸粉有利于鸡腿菇菌体生长和胞外多糖的形成,在初始pH值6、接种量10％、温度26℃、250ml摇瓶装液量l00ml的条件下,鸡腿菇深层发酵结果最佳,在此基础上进行摇瓶发酵曲线测定,确定了鸡腿菇适宜发酵周期为144h,胞外多糖最高可达1．98g/L。     

出芽短梗霉色素变异菌株R45的普鲁蓝糖发酵研究

用正交实验确定了出芽短梗霉（Aureobasidiumpullulans）色素变异菌株R45的发酵优化条件。在此条件下,摇瓶培养的普鲁蓝糖产量最高可达82．4g／L,转化率为54．9％。实验表明,CaCO3是多糖发酵的重要影响因素,多糖的合成与发酵pH值及细胞形态密切相关。     

法夫酵母生产虾青素发酵条件的研究

方法：分别进行了接种时间、摇床转速、接种量和装液量对法夫酵母细胞生产虾青素摇瓶发酵过程影响的实验,比较了DMSO法、酸热法、碱法和自溶法等破壁方法和提取溶剂之间的差别,测定了法夫酵母生长过程中的生物量、类胡萝卜素产量和培养基中的残糖。结果：确定了最佳的摇瓶发酵条件为：种瓶至发酵摇瓶的接种时间为40h,摇床转速为160r/min,接种量为10%,装液量为50mL;DMSO法和丙酮分别为合适的破壁方法和提取溶剂。结论：初步确定发酵的基本条件,为进行法夫酵母高产虾青素菌种的筛选以及发酵培养基的优化奠定了基础。     

茁霉多糖生物合成的研究进展

本文综述了茁霉多糖的生物合成,简单探讨了其生物合成的机理,并从发酵工艺入手,对通过各种发酵条件的对比,分析并讨论了生物合成的一系列优化结果。同时,简要介绍了茁霉多糖的一些理化性质以及它在工业上的生产应用,并讨论了其应用前景。     

几株出芽短梗霉在不同发酵条件下产生多糖的比较

将已有的４株出芽短梗霉在摇瓶中于不同发酵条件下进行比较,考察了它们的生长情况,不同的碳源、氮源、磷酸盐、初始ｐＨ和通气量等对短梗霉多糖合成的影响,获得一株产短梗霉多糖的高产菌株,为以后工作打下良好基础。     

多拷贝毕赤酵母重组菌表达GCL摇瓶优化和高密度发酵

目的:构建高效表达白地霉脂肪酶的毕赤酵母重组菌株,并对筛选得到的菌株进行摇瓶发酵条件优化和分批补料高密度发酵工艺研究。方法:将诱导型表达载体pPIC9K-gcl电转化至毕赤酵母GS115。通过橄榄油-罗丹明B平板和摇瓶发酵筛选高脂肪酶活力的重组菌株,运用基于TaqMan探针的实时荧光定量PCR 法确定其拷贝数,并对菌株进行摇瓶发酵条件优化。在此基础上,研究重组菌在3L 发酵罐中的高密度发酵工艺。结果:筛选得到一株具有3 个白地霉脂肪酶基因拷贝的菌株GS115/pPIC9K-gcl 78#,初始酶活力为220 U/ml。当摇瓶发酵条件为甲醇诱导96 h,每24 h甲醇添加量1 %,接种量2 %,培养基初始pH 7.0,500 ml摇瓶装液量50 ml,甲醇诱导温度25℃ 时酶活力达735 U/ml。3L 发酵罐高密度发酵176.5 h,酶活力达到3360 U/ml,总蛋白含量达到4.30 g/L,且发酵过程中细胞活性一直保持在96 % 以上。结论:基因拷贝数与重组菌株的产酶水平呈正相关,摇瓶优化可显著提高重组菌株的产酶能力,为白地霉脂肪酶的工业化生产奠定了技术基础。     

高山被孢霉产花生四烯酸发酵条件的研究

通过一株高山被孢霉M_(20)(Mortierella alpina)产花生四烯酸的摇瓶发酵研究,确定了其最佳发酵培养基组成及最适摇瓶发酵工艺条件。摇瓶实验确定的最佳培养基组成为(g/L):玉米粉水解液葡萄糖150,酵母粉15,KH_2PO_4 3.0,NaNO_3 3.0,MgSO_4·7H_2O 0.5。最佳发酵工艺条件为:初始pH6.5,装液量为50ml/500ml摇瓶,摇床转速150r/min,温度在菌体生长前三天控制在25℃培养,以后调至20℃培养。在此条件下,发酵培养被孢霉的生物量、菌体总油脂及花生四烯酸分别高达35.5g/L、13.2g/L及2.2g/L,在15L及1000L自动机械搅拌罐进行发酵试验,AA产量分别高达1.86g/L及1.70g/L。     

一株产几丁质酶菌株的筛选及其产酶条件的研究

采用平板透明圈法从土壤中分离筛选到一株产几丁质酶放线菌株L12,用250mL摇瓶发酵初筛和复筛,酶活力为0.63U/mL。通过产酶条件实验,初步确定了该菌株较适产酶培养基和摇瓶发酵条件。条件优化后,30℃、250mL摇瓶发酵48h,几丁质酶活力达到1.06U/mL。     

出芽短梗霉在三种不同氮源的培养基中多糖积累以及形态变化

本研究旨在阐明出芽短梗霉在不同氮源培养基中形态和胞外多糖的积累及化学成分变化。采用摇瓶法培养出芽短梗霉。三种培养基的氮源分别为硝酸钠(培养基1,M1)、硫酸氨、酵母膏(培养基2,M2)和硫酸氨、蛋白胨和酵母膏(培养基3,M3)。M1培养基中,菌丝体和单细胞的生物量积累均比M2、M3低,但胞外多糖的产量则等于甚至略超过M2和M3。在指数生长的前期,白色菌丝体和酵母状细胞状态占优势。指数生长的后期,以厚垣孢子、肿大细胞和黑色菌丝体占优势。胞外多糖都能为茁霉多糖酶水解为麦芽糖和麦芽三糖,说明这些多糖的化学组成都具有(1→4,1→6)-α结构的茁霉多糖。但M1中产生的茁霉多糖结构单元为麦芽糖和麦芽三糖,且二者比例相当。M2中茁霉多糖的麦芽糖结构单元明显减少,而M3中144h后麦芽糖结构单元完全消失。这似乎表明氧化性的氮源和低溶解氧水平可能是造成茁霉多糖结构单元同时具有麦芽糖和麦芽三糖的原因。     

一株产生L-乳酸的米根霉

为获得理想的L-乳酸产生菌,选择适合根霉属微生物生长的土样,利用溴甲酚绿平板结合摇瓶复筛的方法得到了一株有一定L-乳酸积累能力的米根霉Rhizopus oryzae CS323。摇瓶发酵试验显示,在未优化发酵条件的情况下发酵48h,米根霉CS323L-乳酸积累量达到50.1g/L,是一株有良好改造潜力的L-乳酸产生菌,适合作为进一步诱变育种的出发菌株。     

Production of pullulan from xylose and hemicellulose hydrolysate by Aureobasidium pullulans AY82 with pH control and DL-dithiothreitol addition

Xylose, the second most abundant sugar in lignocellulosic materials, is not efficiently utilized in current lignocellulose biotransformation processes, such as cellulosic ethanol production. The bioconversion of xylose to value-added products, such as pullulan, is an alternative strategy for efficient lignocellulose biotransformation. This paper reports the production of pullulan from xylose and hemicellulose hydrolysate by Aureobasidium pullulans AY82. The effects of DL-dithiothreitol (DTT) and pH on pullulan production from xylose were also intensively investigated. A maximal increase of 17.55% of pullulan production was observed in flasks added with 1.0 mM DTT. Batch fermentations with controlled pH were also conducted, and the optimal pH for cell growth and pullulan synthesis was 3.0 and 5.0, respectively. Based on these findings, two-stage pH control fermentations were performed, in which the pH of the medium was first adjusted to 3.0 for cell growth, and then changed to 5.0 for pullulan synthesis. However, the earlier the pH was changed to 5.0, the more pullulan was produced. Fermentation with controlled pH of 5.0 acquired the highest pullulan production. Under the optimized conditions (with the addition of 1.0 mM DTT and controlled pH of 5.0), the maximal pullulan production obtained from xylose was 17.63 g/L. A. pullulans AY82 also readily fermented hemicellulose hydrolysate under these optimized conditions, but with lower pullulan production (12.65 g/L). Fourier transform infrared spectroscopy and high-performance liquid chromatography showed that the structure of the pullulan obtained in this study was identical to that of the pullulan standard.     

短梗霉多糖发酵条件的研究

在摇瓶发酵条件研究的基础上。于16L自控发酵罐上进行了罐上发酵条件优化研究。发现以10％淀粉水解物为碳源时,淀粉水解物的最适DE值为40－50,发酵培养基中的硫酸铵最适用量不同于摇瓶发酵时的量,种龄和接种量、通气量、罐压、搅拌速度和搅拌叶轮挡数等均对多糖的产生有较大的影响。另外还进行了发酵过程的动力学的研究。     

Optimization of physico‐chemical and nutritional parameters for a novel pullulan‐producing fungus,Eurotium chevalieri

Aims: To isolate the novel nonmelanin pullulan‐producing fungi from soil and to optimize the physico‐chemical and nutritional parameters for pullulan production. Methods and Results: A selective enrichment method was followed for the isolation, along with development of a suitable medium for pullulan production, using shake flask experiments. Pullulan content was confirmed using pure pullulan and pullulanase hydrolysate. Eurotium chevalieri was able to produce maximum pullulan (38 ± 1·0 g l^?1) at 35°C, pH 5·5, 2·5% sucrose, 0·3% ammonium sulfate and 0·2% yeast extract in a shake flash culture medium with an agitation rate of 30 rev min^?1 for 65 h. Conclusions: The novel pullulan‐producing fungus was identified as E. chevalieri (MTCC no. 9614), which was able to produce nonmelanin pullulan at from poorer carbon and nitrogen sources than Aureobasidium pullulans and may therefore be useful for the commercial production of pullulan. Significance and Impact of the Study: Eurotium chevalieri could produce pullulan in similar amounts to A. pullulans. Therefore, in future, this fungus could also be used for commercial pullulan production, because it is neither polymorphic nor melanin producing, hence its handling during pullulan fermentation will be easier and more economical.     

Isolation of New Aureobasidium Strains That Produce High-Molecular-Weight Pullulan with Reduced Pigmentation

New isolates of Aureobasidium pullulans were obtained from plant leaf surfaces gathered in San Diego County. The new fungal isolates were identified as A. pullulans on the basis of the appearance of polymorphic colonies formed on agar plates, the electrophoretic profiles of repeated genomic DNA sequences, and the production of pullulan in shake flask cultures. The isolates showed different degrees of pigmentation. One of the natural isolates was nonpigmented under mock production conditions in liquid culture, but was still able to synthesize a reduced amount of pigment on agar plates at late times. A mutagenic treatment with ethidium bromide produced derivatives of normally pigmented natural isolates that exhibited an increased tendency toward yeastlike growth and reduced pigmentation. Additionally, some of the new isolates and mutant derivatives accumulated pullulan of relatively high molecular weight in the culture broths.     

Effect of carbon source and dissolved oxygen level on cell growth and pullulanase production byBacillus stearothermophilus G-82

Cell growth and extracellular pullulanase production ofBacillus stearothermophilus G-82 were investigated in batch culture using a defined medium with glucose, maltose, pullulan or amylopectin as carbon source. Maximum enzyme activity was with pullulan or amylopectin. Cell growth in batch culture was better under oxygen unlimited conditions, while higher total and specific enzyme activities, using pullulan or amylopectin, were obtained in oxygen-limited conditions. Enzyme accumulation took place in the late growth phase. The highest enzyme production of 300 U/I was reached when pullulan was used as carbon source in conditions of oxygen limitation.     

Affinity purification of recombinant interferon-alpha on a mimetic ligand adsorbent

A method for improved refolding and purification of recombinant human interferon-alpha (rh-IFN-alpha) from inclusion bodies is described. The optimal conditions of refolding were obtained by the addition of 0.5 M l-arginine to the refolding buffer. The rh-IFN-alpha was purified to near homogeneity utilizing a single-step chromatography on a mimetic dye-ligand matrix. Improved refolding, coupled to a single-column affinity purification strategy, resulted in a 10-fold increase in the yield of rh-IFN-alpha. This single-step purification protocol yielded approximately 50 mg of purified rh-IFN-alpha from 1 liter of shake flask culture. The rh-IFN-alpha prepared by this protocol was found to be essentially monomeric based on HPLC gel filtration and nonreducing SDS-PAGE. It had a specific activity of approximately 2.8 x 10(8) IU/mg, measured as inhibition of cytopathic effect of encephalomyocarditis virus on A549 human lung carcinoma cells.     

Pullulan production and physiological characteristics of Aureobasidium pullulans under acid stress

In this study, batch processes of pullulan production by Aureobasidium pullulans CCTCC M 2012259 under different pH environments were evaluated. The pH of the medium decreased quickly to an acid stress condition under batch fermentation without pH control. A higher pullulan production was always obtained with a lower biomass under a given glucose concentration with constant pH control, and vice versa. Based on the nonlinear regression analysis of the results obtained from diverse pH control modes, a constant controlled pH of 3.8 was predicted as an optimum pH for efficient pullulan production using a one-element cubic equation. A maximum pullulan concentration of 26.8 g/L and a minimum biomass of 8.1 g/L were achieved under the optimal pH of 3.8, which were in good agreement with the results predicted by the mathematical model. Further information on the physiological characteristics of A. pullulans CCTCC M 2012259 such as intracellular pH, NADH/NAD⁺, ATP/ADP, and glutathione generation under moderate or severe acidic conditions were investigated, and the results presented more evidence on why pullulan biosynthesized with high efficiency under moderate acid stress (e.g., pH 3.8), which would also help us to better understand the response of the cells to acid stress.     

Downstream processing and characterization of pullulan from a novel colour variant strain of Aureobasidium pullulans FB-1

Exopolysaccharide produced by a new novel colour variant strain of Aureobasidium pullulans FB-1 was purified by cell harvesting and precipitation of the polymer. Various organic solvents were screened for pullulan precipitation. Isolation and purification of pullulan from fermentation broth was carried out using single-step purification strategy by isopropyl alcohol precipitation. Ratio of culture supernatant to isopropyl alcohol and time of precipitation were optimized for pullulan precipitation. Maximum yield (4.47%, w/v) of polysaccharide was obtained when two volumes of ice-cold isopropyl alcohol were added to one volume of supernatant with precipitation time of 12 h. IR spectra as well as carbon-13 and proton NMR spectra in aqueous solution of intact polysaccharide obtained from A. pullulans FB-1 and commercially available pullulan (Sigma, USA) revealed solely α-(1 → 6) linked maltosyl units, in accord with the generally accepted structure of pullulan. Maximum hydrolysis (94.25%) of purified pullulan at 50 °C by pullulanase was achieved under agitation (150 rpm) after 360 min.     

灵芝液体浅层静置培养高效生产三萜的研究

三萜是灵芝Ganoderma lingzhi中重要的活性物质.本研究采用液体浅层静置培养方式(LSSC)提高灵芝三萜的产量.结果表明,在T25细胞培养瓶中的最佳培养条件为初始培养体积2mL,接种量7.0g(菌体湿重/L),在48h补加2mL培养液,发酵7d,三萜产量可达(32.95±0.51)mg/g,为摇瓶培养最高产...     

Real encoded genetic algorithm and response surface methodology to optimize production of an indolizidine alkaloid, swainsonine, from Metarhizium anisopliae

Response surface methodology (RSM) and artificial neural network-real encoded genetic algorithm (ANN-REGA) were employed to develop a process for fermentative swainsonine production from Metarhizium anisopliae (ARSEF 1724). The effect of finally screened process variables viz. inoculum size, oatmeal extract, glucose, and CaCl₂ were investigated through central composite design and were further utilized for training sets in ANN with training and test R values of 0.99 and 0.94, respectively. ANN-REGA was finally employed to simulate the predictive swainsonine production with best evolved media composition. ANN-REGA predicted a more precise fermentation model with 103 % (shake flask) increase in alkaloid production compared to 75.62 % (shake flask) obtained with RSM model upon validation.