蝉拟青霉液体培养条件优化

[目的]建立能够有效提高蝉拟青霉液体培养效率的培养体系,增加其生物量。[方法]以蝉拟青霉生物量作为响应值,通过Plackett-Burman实验设计从8个试验影响因素中筛选出3个主要影响因素,基于3因素3水平的BoxBehnken设计法以及响应面分析法研究影响蝉拟青霉液体培养各因素之间的交互作用。[结果]通过Plackett-Burman设计法确定影响最为显著的因素为接种量、p H和温度,利用最陡爬坡试验确定最佳范围在接种量7%、p H 6.00、温度25℃附近,借助Box-Behnken设计法最终确定最佳液体培养条件为:葡萄糖20 g/L、蛋白胨3 g/L、酵母膏2 g/L、KH2PO41 g/L、MgSO40.5 g/L、接种量6.65%、p H 6.00、温度24.01℃。优化后的培养体系所培养的蝉拟青霉其生物量从优化前的147.106 0 g/L提高到239.475 3 g/L,提高了62.79%。[结论]优化后的培养体系能够有效提高蝉拟青霉生物量,该方法对于优化蝉拟青霉生物量发酵条件是一种有效、可行的方法。     

葡萄糖流加策略对基因工程FR-008／杀念菌素衍生物CS103补料分批发酵过程的影响

以组合生物合成技术得到的链霉菌FR-008突变株CS103为研究对象,研究了3．7L发酵罐上维持一定葡萄糖浓度对其次级代谢产物脱羧FR-008／candicidin衍生聚酮抗生素CS103生物合成的影响。当初始葡萄糖浓度20g／L,发酵过程还原糖浓度维持在10g/L时,抗生素CS103最高产量较分批发酵最高产量相比提高30％。研究了3．7L罐上补料分批发酵生产CS103的工艺,主要考察了脉冲补料、间歇流加补料和连续流加补料三种补料分批发酵工艺,并与分批发酵进行了比较。连续流加补料维持糖浓度的效果明显,最高产量达到126．9μg/mL,与分批发酵相比提高了44％左右。     

氮源对L-苏氨酸发酵的影响

以L-苏氨酸生产菌TRFC为供试菌株,研究了氮源对L-苏氨酸发酵的产量和糖酸转化率的影响。首先通过摇瓶实验确定发酵的最佳无机氮源和有机氮源分别为硫酸铵和酵母粉,进一步利用10L罐补料分批发酵确定硫酸铵和酵母粉的最佳用量,继续优化培养条件,采用发酵中后期流加硫酸铵和糖氨混合补料等措施,L-苏氨酸产量得到进一步的提高。在最优发酵条件下,通过10L罐补料分批发酵36h,产酸可达118.9g/L,糖酸转化率为47.6%。     

采用玉米秸秆水解糖和玉米浆发酵生产丁二酸

研究了以玉米秸秆水解糖为碳源,不同氮源条件下琥珀酸放线杆菌Actinobacillus succinogenesSF-9的丁二酸发酵产酸能力。结果表明玉米浆可以替代酵母膏作为丁二酸发酵的廉价氮源。厌氧摇瓶丁二酸发酵单因素试验,得到在初糖浓度50 g/L时,玉米浆的较佳用量为20 g/L。在5 L搅拌罐上,考察了不同初始玉米秸秆水解糖浓度对A.succinogenes SF-9发酵生产丁二酸的影响,结果显示高初始秸秆糖浓度对琥珀酸放线杆菌的生长有抑制作用。采用补料分批发酵,发酵60 h丁二酸的产量达到42.7g/L,丁二酸产率82.7%,生产强度0.81 g/(L·h)。丁二酸的产量和生产强度较分批发酵有明显提高。     

L-谷氨酸补料分批发酵的研究

对谷氨酸棒杆菌(Corynebacteriuin glutamicum)HCJ46产L-谷氨酸的补料分批发酵条件进行研究.结果表明:最适初糖质量浓度和最佳残糖维持质量浓度分别为100和(10～20)g/L;对发酵控温方式进行研究,确定了最佳温度控制策略为0～8h维持32℃,8～16h维持34℃、16～32h维持36℃,同时发现相对溶氧控制在30%左右时产酸最高.在以上的优化条件下,L-谷氨酸产量从72g/L提高到95g/L,提高了31.9%.     

基于动力学模型的法夫酵母发酵生产虾青素的补料策略优化

对法夫酵母的不同补料发酵方式进行了研究.基于底物抑制模型,提出了一种优化的两阶段补料策略,用于法夫酵母产虾青素的高密度发酵.在发酵的延迟期和对数生长期早期,糖浓度控制在25 g/L左右,在此条件下,生物量可以达到最大,且时间缩短.在对数生长期后期及稳定期,糖浓度控制在5 g/L,虾青素的合成时间可以有效延长.与传统的补料方式相比,采用此补料策略取得了较好的发酵效果.发酵终点细胞干重达到23.8g/L,虾青素产量达到29.05 mg/L,分别比分批发酵提高了52.8%和109%.     

大球盖菇产胞外多糖液体优化培养条件初探

以菌丝生物量及胞外多糖(exopolysaccharides,EPS)含量为指标对大球盖菇产胞外多糖液体培养基组成和发酵条件进行了优化。结果表明,最适碳源是麦芽糖,最适氮源是酵母膏,正交试验确定最佳培养基组成为马铃薯150 g/L,麦芽糖20 g/L,酵母膏1 g/L,KH2PO41 g/L,MgSO4.7H2O 2.5 g/L。最佳发酵条件为28℃,摇床转速160 r/min,起始pH值6.5,装液量100 mL/250 mL、接种量10%,发酵时间6 d。在此条件下,大球盖菇菌丝生物量及EPS含量分别比对照增加了31.8%和51.6%。     

灵芝多糖液体发酵条件的研究

液体发酵灵芝是目前灵芝多糖开发的有效途径。以灵芝的生物量和胞外多糖为指标,对影响灵芝发酵的条件进行了研究。单因素实验表明灵芝发酵的最佳碳源、(?)源和生长因子分别是葡萄糖、酵母膏和维生素B1,最适温度、起始pH值和摇床转速分别是28℃、5．5和160 rpm。最佳培养方式是接种后静置4 h再振荡培养,其生物量和胞外多糖的产量最高,分别为7．743g/L和0．907g/L。     

根瘤菌N613胞外多糖发酵条件及抗肿瘤作用研究

用摇瓶正交试验研究了根瘤菌Rhizobium sp.N613合成根瘤菌胞外多糖(rhizobium exopolysaccharide,REPS)的最佳培养基配方和最适培养条件。采用10L自动控制罐进行了分批发酵试验,获得了合成REPS的发酵动力学参数。经40h的补料分批发酵与代谢调控,REPS产量达到11.31g/L。此外,抗肿瘤实验表明,当REPS剂量为5mg/kg时,其抑瘤率可达53.40%。结果表明,REPS的发酵周期短,产量高,成本低,且具有良好的免疫活性与增稠性,有着极高的开发应用价值。     

补料工艺对两株法夫酵母菌株产虾青素的影响

【目的】考察不同补料工艺对法夫酵母菌株生长和虾青素合成的影响。【方法】对法夫酵母JMU-VDL668和JMU-MVP14菌株在7 L罐中进行分批及分批补料培养; 同时, 测定发酵过程中生物量、虾青素和葡萄糖含量的变化。【结果】采用恒DO补料, 法夫酵母JMU-VDL668菌株获得的生物量最大(64.6 g/L), 是分批培养的2.2倍; 采用恒pH补料发酵, 虾青素的产量最高(20.6 mg/L), 是分批培养的1.5倍。与JMU-VDL668菌株不同, 虾青素高产菌株JMU-MVP14菌株采用恒pH补料, 获得生物量最大(48.5 g/L), 但虾青素产量大大降低(仅17.5 mg/L); 采用脉冲补料, 虾青素产量最高, 达到414.1 mg/L, 与分批发酵相比提高了200.2%; 采用恒DO补料, 生物量(38.5 g/L)和虾青素产量(403.2?mg/L)增加显著, 与分批发酵相比分别提高了133.1%和192.3%。【结论】不同补料工艺对法夫酵母菌株生产虾青素影响很大。其中, 采用恒pH补料工艺, 法夫酵母JMU-VDL668菌株可以获得最高的虾青素产量, 而采用脉冲补料工艺, 最适于法夫酵母JMU-MVP14菌株发酵生产虾青素。     

香菇液体发酵高产多糖菌株筛选

通过评价香菇野生菌株发酵产多糖性能,筛选高产香菇多糖菌株.以采自长白山野生香菇通过组织分离获得的6株菌株和2株人工栽培菌株为出发菌株,对不同发酵培养时间菌丝体生物量、胞内多糖含量、胞外多糖含量等进行测试分析,结果表明,8株菌株随着培养时间的延长,菌丝体生物量均有不同程度的增加,但胞内多糖含量和胞外多糖得率变化趋势不同,...     

The scale-up cultivation of Candida utilis in waste potato juice water with glycerol affects biomass and β(1,3)/(1,6)-glucan characteristic and yield

New ideas on production of yeast origin β-glucan preparations for industrial application are attracting interest considering market development of that high-value functional polysaccharide. Sellecting an efficient yeast producer and designing culture conditions are a prerequisite for obtaining high yield of β-glucan. The aim of this study was to describe at the first time the influence of the mode of cultivation (shake-flasks and batch fermentation) and time of culture on characteristic and yield of biomass and β(1,3)/(1,6)-glucan preparations of Candida utilis ATCC 9950 after cultivation in medium based on waste potato juice water supplemented with 10% of glycerol. After shake-flask culture, the biomass was characterized by higher protein content (app. 26.5%) compared to 19% after batch fermentation while the cultivation on a biofermentor scale promoted polysaccharides biosynthesis. The highest output of purified β(1,3)/(1,6)-glucan preparation (5.3 g_d.w./L), containing app. 85% of that polysaccharide, was found after 48 h cultivation in biofermentor. Batch fermentation promoted biosynthesis of alkali-insoluble β(1,3)/(1,6)-glucan fraction, decreasing the content of β(1,6)-glucan. The yield of β(1,3)/(1,6)-glucan synthesis was 0.063 (g/g glycerol), while the productivity of that polysaccharide reached 0.094 (g/L/h). Longer batch fermentation (72 h) resulted in reduction of production efficiency of β-glucan preparation under studied conditions. The results of the study provide a new efficient biotechnological solution to produce high-value β-glucan preparations of C. utilis origin based on valorization of agro-waste potato juice water with glycerol.

     

出芽短梗霉Aureobasidium sp. SRF的菌株特性分析及胞外多糖结构鉴定

菌株SRF是1株从意大利树莓(Rubus corchorifolius)果实表面分离、可产胞外多糖的新菌株。在鉴定其分类归属的基础上,对其产生的胞外多糖进行了结构分析和发酵条件优化,为寻找微生物多糖提供新的菌株,为开发利用资源微生物提供借鉴。通过形态学和ITS序列对比分析进行菌株鉴定;通过薄层层析和红外光谱分析,确定胞外多糖结构;通过单因素检测试验,确定影响产糖量的主要因素;响应面Plackett-Burman和Box-Behnken设计筛选发酵产胞外多糖的最优条件。结果表明,出发菌株SRF隶属于出芽短梗霉属,命名为Aureobasidium sp. SRF;SRF所产胞外多糖为普鲁兰多糖;单因素检测表明,对多糖产量影响最大的因素为碳源浓度、氮源浓度、无机离子浓度,其次是碳源、氮源、无机离子、pH值;根据响应面结果确定最优发酵条件为麦芽糖8%(质量分数)、酵母提取物3%(质量分数)、钙离子0.3 g/L、pH 6,产糖量达5.93 g/L。SRF是1株来源于树莓浆果表面,可产胞外普鲁兰多糖的出芽短梗霉新菌株,是1株产微生物多糖的候选菌株。     

虎掌菌菌丝富硒培养的研究

为生产合适的硒源提供一种思路,以菌丝体生物量、含硒量、还原糖、氨态氮和蛋白质为指标,采用四因素三水平正交设计法优化虎掌菌的富硒发酵条件,探讨不同浓度的硒对虎掌菌固体培养菌丝生长和液体培养产生的生物组分的影响。结果表明,高浓度的硒抑制虎掌菌菌丝体生长;正交试验选择不同的衡量指标,由极差分析得出各因素的影响程度大小,结合证实试验得到以还原糖为指标的最优组合为葡萄糖6%(质量分数)、酵母浸膏3%(质量分数)、KH_2PO_4 0.1%(质量分数)、Na_2SeO_3 0.6 mmol/L,其菌丝体生物量和氨态氮含量较高。与对照相比,加硒后虎掌菌发酵液中氨态氮、还原糖和总糖含量显著增加(P0.05);当硒浓度为0.5 mmol/L时,氨态氮、还原糖和总糖含量均达到最高值。菌丝体生物量和可溶性蛋白质分别在硒浓度为0.2 mmol/L和0.4 mmol/L时达到最大值。虎掌菌富硒培养后,发酵液的营养成分含量会发生变化。     

响应面法优化杀鱼假交替单胞菌2515发酵培养基

杀鱼假交替单胞菌(Pseudoalteromonas piscicida)2515是一株具有广谱抗弧菌性能的菌株，为提升菌株2515的培养生物量，通过单因素优化方法，研究碳源、氮源、无机盐等营养成分对菌株2515的发酵产量的影响，确定关键营养因子，利用响应面分析法对影响菌株2515生物量的关键营养因子进行优化。结果显示，菌株2515的最佳发酵培养基配方为麦芽糖2.85 g/L、CaCl₂ 0.65 g/L、MnCl₂ 0.10 g/L、酵母膏3.85 g/L、胰蛋白胨10 g/L、NaCl 10 g/L。优化后的培养基使菌株2515在锥形瓶和发酵罐中发酵的OD₆₀₀值分别为1.416和1.866,生物量分别提高了36.4%和40.4%,其发酵上清液和细胞内容物的抑菌活性分别提高了28.2%和27.2%。表明响应面法优化后的培养基有利于提高菌株2515的发酵生物量及抗菌效果，研究结果为菌株2515的后续开发应用提供了参考。     

Optimum conditions for the biological production of lactic acid by a newly isolated lactic acid bacterium,Lactobacillus sp. RKY2

Lactic acid is a green chemical that can be used as a raw material for biodegradable polymer. To produce lactic acid through microbial fermentation, we previously screened a novel lactic acid bacterium. In this work, we optimized lactic acid fermentation using a newly isolated and homofermentative lactic acid bacterium. The optimum medium components were found to be glucose, yeast extract, (NH₄)₂HPO₄, and MnSO₄. The optimum pH and temperature for a batch culture ofLactobacillus sp. RKY2 was found to be 6.0 and 36°C, respectively. Under the optimized culture conditions, the maximum lactic acid concentration (153.9 g/L) was obtained from 200 g/L of glucose and 15 g/L of yeast extract, and maximum lactic acid productivity (6.21 gL⁻¹h⁻¹) was obtained from 100 g/L of glucose and 20 g/L of yeast extract. In all cases, the lactic acid yields were found to be above 0.91 g/g. This article provides the optimized conditions for a batch culture ofLactobacillus sp. RKY2, which resulted in highest productivity of lactic acid.     

Optimization and characterization of pullulan production by a newly isolated high-yielding strain Aureobasidium melanogenum

Abstract

Pullulan is an extracellular water-soluble polysaccharide with wide applications. In this study, we screened strains that could selectively produce high molecular weight pullulan for application in industrial pullulan production. A new fungus strain A4 was isolated from soil and identified as Aureobasidium melanogenum based on colony characteristics, morphology, and internally transcribed spacer analysis. Thin-layer chromatography, Fourier-transform infrared spectroscopy, and nuclear magnetic resonance analysis suggested that the dominant exopolysaccharide produced by this strain, which presented a molecular weight of 1.384?×?10⁶ Dalton in in-gel permeation chromatography, was pullulan. The culture conditions for A. melanogenum A4 were optimized at 30?°C and 180?rpm: carbon source, 50?g/L maltose; initial pH 7; and 8?g/L Tween 80. Subsequently, batch fermentation was performed under the optimized conditions in a 5-L stirred-tank fermentor with a working volume of 3?L. The fermentation broth contained 303?g/L maltose, which produced 122.34?g/L pullulan with an average productivity of 1.0195?g/L/h and 82.32?g/L dry biomass within 120?h. The conversion efficiency of maltose to pullulan (Y%) and specific production rate (g/h/g dry cells) (Qs) reached 40.3% and 0.0251?g/L/g dry cells, respectively. The results showed strain A4 could be a good candidate for industrial production.     

β‐poly(l‐malic acid) production by fed‐batch culture of Aureobasidium pullulans ipe‐1 with mixed sugars

β‐poly(l ‐malic acid) (PMLA) is a biopolyester, which has attracted growing attention due to its potential applications in medicine and other industries. In this study, the biosynthetic pathway of PMLA and the fermentation strategies with mixed sugars were both investigated to enhance PMLA production by Aureobasidium pullulans ipe‐1. Metabolic intermediates and inhibitors were used to study the biosynthetic pathway of PMLA. It showed that exogenous addition of l ‐malic acid, succinic acid, TFA, and avidin had negligible effect on PMLA production, while pyruvic acid and biotin were the inhibitors, indicating that PMLA biosynthesis was probably related to phosphoenolpyruvate via oxaloacetate catalyzed by phosphoenolpyruvate carboxylase. Sucrose was suitable for achieving the highest PMLA concentration, while fructose generated a higher yield of PMLA (PMLA produced per biomass). Furthermore, the fed‐batch culture using fed solution with different sugar mixture for PMLA production was implemented. During the fed‐batch culture with mixed solution, fructose could increase PMLA production. Compared with the batch culture, the feeding with mixed sugar (sucrose and glucose) increased PMLA concentration by 23.9%, up to 63.2 g/L, and the final volume of the broth was increased by 25%. These results provide a good reference for process development and optimization of PMLA production.     

Fed-batch fermentation of Tuber melanosporum for the hyperproduction of mycelia and bioactive Tuber polysaccharides

For the first time, a fed-batch fermentation process of Tuber melanosporum was developed for the efficient production of bioactive mycelia and Tuber polysaccharides. Each 1.67 g/L of peptone and 8.33 g/L of yeast extract were added on day 3, 6, and 9, respectively, and sucrose was fed to maintain its concentration around 35–5 g/L when its residual level decreased to 10–5 g/L. Then, the maximal biomass, the production of extracellular polysaccharides (EPS) and intracellular polysaccharides (IPS) reached 53.72 ± 2.57 g DW/L, 7.09 ± 0.62 and 4.43 ± 0.21 g/L, respectively. Compared with the batch culture conducted in the enriched medium, the biomass, the production of EPS and IPS were enhanced by 55.8%, 222.3% and 103.2%, respectively. Not only the cell density but also the production of EPS and IPS were the highest ever reported in truffle fermentation, and the biomass was also the highest as ever reported in mushroom fermentation.     

Improved algal oil production from Botryococcus braunii by feeding nitrate and phosphate in an airlift bioreactor

To improve biomass and microalgal oil production of Botryococcus braunii, fed‐batch culture was investigated in an airlift photobioreactor. The optimal feeding time of the fed‐batch culture was after 15 days of cultivation, where 1.82 g/L of the microalgal biomass was obtained in the batch culture. Nitrate nutrient was the restrictive factor for the fed‐batch cultivation while phosphate nutrient with high concentration did not affect the microalgal growth. The optimal mole ratio of nitrate to phosphate was 34.7:1, where nitrate concentration reached the initial level and phosphate concentration was one quarter of its initial level. With one feeding, the biomass of B. braunii reached 2.56 g/L after 18 days. Two feedings in 2‐day interval enhanced the biomass production up to 2.87 g/L after 19 days of cultivation. The hydrocarbon content in dry biomass of B. braunii kept at high level of 64.3% w/w. Compared with the batch culture, biomass production and hydrocarbon productivity of B. braunii were greatly improved by the strategic fed‐batch cultivation.