利用扁桃斑鸠菊叶发酵生产蛹虫草胞外多糖的条件及其抗氧化活性

蛹虫草胞外多糖具有增强免疫力、抗疲劳等药理活性,有极高的保健价值。为高效地获取蛹虫草胞外多糖,本研究通过向发酵培养基中添加适量的扁桃斑鸠菊叶粉末,来提高蛹虫草发酵液中胞外多糖的产量,并对优化得到的胞外多糖红外吸收光谱和化学抗氧化活性进行了研究。实验结果表明,液体发酵最优条件为:扁桃斑鸠菊叶粉末添加量8 g/L、发酵时间9 d、pH 6.5、接种量5.0 mL,在此条件下,蛹虫草胞外多糖的产量可达(5.24±0.28) mg/mL,与未添加扁桃斑鸠菊叶的空白组相比,胞外多糖产量提高了约205.20%;红外分析与抗氧化活性实验结果显示,扁桃斑鸠菊叶对蛹虫草生产的胞外多糖结构和活性影响较小。该研究结果表明扁桃斑鸠菊叶能够有效地提高蛹虫草胞外多糖的产量,为蛹虫草胞外多糖的高效生产提供了新思路。     

蛹虫草多糖发酵工程研究

报道了蛹虫草(Gordyceps militaris)多糖发酵工程中的关键因子对菌丝体生物量和多糖产量影响的研究结果.对蛹虫草液体发酵培养基中的碳源、氮源和温度进行了正交试验,考察了三因子对蛹虫草生物量以及多糖的综合效应.实验结果表明:各因素不同水平间的组合对蛹虫草生物量、胞外多糖、胞内多糖以及总多糖的影响不同.其中.在6%的碳源和1%的氮源以及25℃的条件下.能获得蛹虫草的最大生物量以及总多糖和胞外多糖的最大产量;碳源为6%、氮源为1%、温度为22℃时.胞内多糖的产量达到最高.     

短梗霉胞外多糖发酵及其发酵动力学

对短梗霉（Aureobasidiumpullulans)胞外多糖（EPS）的发酵及其发酵动力学进行了研究。短梗霉菌体前期生长速度较快,到48b生长趋于稳定期,其胞外多糖合成随菌体生长的不断上升,到84b多糖的产量达到最高,为14.24(g/L)发酵实验基于Logitic方程和Luedeking-Piret方程,得到了描述发酵过程的动力学数学模型和模型参数,同时对实验数据与模型进行了验证比较。     

响应面法优化蛹虫草与厚朴双向液体发酵工艺

为提高蛹虫草液体发酵胞外多糖含量和菌丝体生物量,以厚朴为药性基质,对蛹虫草进行双向液体发酵。在单因素实验的基础上,应用Box-Behnken实验设计,对发酵过程关键影响因素进行优化。结果表明,在厚朴添加量5g、接种量15.5mL、发酵温度25℃的条件下发酵9d,蛹虫草双向液体发酵产物中胞外多糖含量为3.11mg/mL,菌丝体生物量为18.81mg/mL。各发酵因素中,发酵液胞外多糖含量受接种量影响最大,菌丝体生物量则主要受发酵温度影响。优化所得发酵工艺可行性高、周期短、生产过程可控,为进一步提高人工培育蛹虫草质量、增加其关键活性产物的产量提供了参考。     

滇重楼寄生菌的研究

从滇重楼(Paris polyphylla var.yunnanensis)地下茎中分离和鉴定出两种细菌——蜡状芽孢杆菌(Bacillus cereus)和产碱假单胞菌(Pseudomonas alcaligenes),以及三种真菌——黑团孢霉(Periconia sp.)、白色厚顶孢霉(Pachnocybe albida)和重楼索霉(Hormomyces paridiphilus)。对蜡状芽孢杆菌、产碱假单胞菌和重楼索霉进行了液体培养并测定了胞外多糖含量,结果表明重楼索霉可分泌大量胞外多糖,这可能是导致滇重楼地下茎胶质化和多糖含量增加的原因。     

蛹虫草多糖和D-甘露醇深层发酵的非结构动力学模型

多糖和D-甘露醇是蛹虫草的重要药理活性成分。本文开展了蛹虫草在分批发酵过程中同时生产多糖和D-甘露醇的发酵动力学研究。利用Sigmoid函数构建了蛹虫草菌丝生长、糖基质消耗、多糖和D-甘露醇的非结构动力学模型,并根据Boltzmann方程拟合求解出各模型参数。结果显示,各模型的实测值和预测值拟合度较好。蛹虫草比生长速率在第1.0天达到最大值（μ_max）1.244d^-1;底物葡萄糖的比消耗速率在第0.6天达到最大值（q_{S, max}）2.163d^-1;多糖比合成速率在第2.0天达到最大值（q_{P, max}）51.852mg/(g·d);D-甘露醇比合成速率在第0.99天左右达到最大值（q_{D, max}）37.963mg/(g·d)。蛹虫草多糖的形成与菌丝细胞的生长呈现部分生长关联型,而D-甘露醇的形成与细胞生长呈现生长关联型关系。研究结果为利用分批发酵规模化同时发酵生产蛹虫草多糖和D-甘露醇提供了理论依据。     

放射形土壤杆菌Q9415发酵产胞外多糖动力学研究

放射形土壤杆菌Q9415产胞外多糖PS-9415的发酵为混合型发酵。应用logistic方程和L-P方程对PS-9415发酵过程的菌体生长,多糖合成以及底物消耗的动力学进行了讨论。研究发现：logistic方程和L-P方程建立的动力学模型较好地拟合了实验数据。     

放射形土壤杆菌Q9415发酵产胞外多糖动力学研究*

放射形土壤杆菌Q941 5产胞外多糖PS 941 5的发酵为混合型发酵。应用logistic方程和L P方程对PS 941 5发酵过程的菌体生长 ,多糖合成以及底物消耗的动力学进行了讨论。研究发现 :logistic方程和L P方程建立的动力学模型较好地拟合了实验数据。     

忍冬桑黄和蛹虫草共发酵联产真菌多糖初步研究

忍冬桑黄和蛹虫草两种药用真菌均可产活性多糖,共发酵模式是产生新化合物或提高化合物含量或药效的潜在方式。本研究尝试用忍冬桑黄和蛹虫草共发酵联产真菌多糖,并对其共发酵所得的菌丝体多糖开展抗氧化活性试验。结果表明,当忍冬桑黄和蛹虫草预先分别发酵3d和1d后再同时接种共发酵,两菌可以较好地进行共生长,菌体总量和总多糖得率显著高于两菌单独进行发酵时的相应量。进一步对适宜两菌共发酵的培养基进行了优化,获得适宜两菌共发酵高产多糖的培养基组成为：可溶性淀粉30g/L、牛肉粉12g/L、磷酸氢二钾和硫酸镁各1.5g/L。共发酵菌丝体中多糖和黄酮含量均高于两菌单个菌体中的相应含量,但三萜含量和桑黄菌体中的三萜含量没有显著差异。抗氧化活性试验表明,共发酵菌体多糖、忍冬桑黄菌体多糖和蛹虫草菌体多糖对DPPH·自由基、羟基自由基、超氧阴离子自由基均具有清除作用,其中共发酵菌体多糖对3种自由基的清除作用显著强于两菌单个菌体多糖的清除效果。本研究表明忍冬桑黄和蛹虫草共发酵联产真菌多糖具有可行性。     

发酵虫草菌质与天然虫草主要活性成分含量比较研究

用大米作为固体发酵基质,通过蛹虫草菌种发酵后制成虫草菌质,测定菌质中腺苷、虫草素、多糖等成分含量.比较人工发酵虫草菌质与天然虫草腺苷、虫草素、多糖等主要活性成分的含量.结果表明,虫草菌质中虫草素、多糖含量分别超过天然虫草的40倍和3倍.因此.人工发酵虫草菌质可以替代天然虫草应用.     

微生物法生产二羟基丙酮的研究进展

以下综述了微生物发酵法制备二羟基丙酮的研究进展。利用微生物发酵法生产二羟基丙酮比化学合成法具有更大的优势,氧化葡萄糖酸杆菌是二羟基丙酮工业发酵生产中最有应用价值的菌株。发酵过程中底物、产物、氧气、菌体量等各种因素都会对二羟基丙酮产量产生影响,在各种发酵方式中反复流加工艺和固定化发酵工艺最有前途。重组菌株的构建和发酵工艺的优化是将来微生物发酵生产二羟基丙酮的发展方向。     

Study of mycelial growth and bioactive polysaccharide production in batch and fed-batch culture of Grifola frondosa

The fermentation of Grifola frondosa was investigated in the shake flasks and a 5-L jar fermenter in batch and fed-batch modes. In the shake-flask experiments, the preferable mycelial growth and exopolysaccharide (EPS) production was observed at relatively low pH; maltose and glucose were preferred carbon sources for high mycelial production. The EPS was doubled after 13 d of cultivation when glucose was increased from 2% to 4%. Yeast extract (YE) (0.4%) in combination with corn steep powder (CSP) (0.6%) and YE (0.8%) in combination with CSP (1.2%) were preferred nitrogen sources for high mycelial production and EPS production, respectively. All plant oils tested significantly stimulate cell growth of G. frondosa but they failed to enhance EPS production. The EPS products usually consisted of two fractions of different molecular sizes varied by the plant oils used. The fed-batch fermentation by glucose feeding was performed when the glucose concentration in the medium was lower than 0.5% (5g/L), which greatly enhanced the accumulation of mycelial biomass and EPS; the mycelial biomass and EPS were 3.97g/L and 1.04g/L before glucose feeding, which reached 8.23g/L and 3.88g/L at 13 d of cultivation. In contrast, the mycelial biomass and EPS in the batch fermentation were 6.7g/L and 3.3g/L at 13 d of cultivation.     

Quantitative analysis for the effect of plant oil and fatty acid on Tuber melanosporum culture by uniform design combined with partial least squares regression

Uniform design and partial least squares regression were adopted to quantitatively analyze the effects of plant oil and fatty acid as well as their addition amount and addition time on the performance of Tuber melanosporum submerged fermentation. The regression models showed the optimal scheme was the addition of 1.2 mL soybean oil on day 9, which was validated by experiment. The maximal biomass of 25.89 ± 1.01 g/L and extracellular polysaccharides (EPS) production of 6.51 ± 0.68 g/L were obtained, which were enhanced by 18.5% and 86%, respectively. Palmitic acid was identified to be the key component to stimulate the cell growth and EPS biosynthesis, and stearic acid was beneficial for the production of intracellular polysaccharides. Not only the biomass but also EPS production obtained in this work are the highest reported in the batch fermentation of truffle.     

Comparison of the kinetics of lipopeptide production by Bacillus amyloliquefaciens XZ-173 in solid-state fermentation under isothermal and non-isothermal conditions

This study aimed to compare the kinetics of lipopeptide production in solid-state fermentation (SSF) under isothermal and non-isothermal conditions. Models based on the logistic, modified Gompertz and Luedeking–Piret-like equations were developed to describe the time course of fermentation under different conditions. The experiments were conducted in 250 mL flasks and a 50 L fermenter. The results showed that the non-isothermal process had higher levels of product formation rate and substrate utilization rate compared to the isothermal process. The part of substrate carbon to meet microbial maintenance—energy, biomass and lipopeptides formation requirements got increased using the non-isothermal technique. In addition, fermenter conditions positively influenced the lipopeptides formation rate with significantly higher levels of substrate for the microbial growth and product formation, though the product productivity and biomass both decreased as compared to flask. This is the first report that investigates the effects of temperature changing on the kinetics of lipopeptide production by Bacillus amyloliquefaciens strain under SSF condition using soybean flour and rice straw as major substrates in flask and in fermenter.     

Effects of carbon sources on growth and extracellular polysaccharide production of Nostoc flagelliforme under heterotrophic high-cell-density fed-batch cultures

Dissociated cells separated from a natural colony of Nostoc flagelliforme were cultivated heterotrophically in the darkness on glucose under fed-batch culture conditions. The effects of carbon sources (glucose, fructose, xylose, and sucrose) and concentrations on cell growth and extracellular polysaccharide (EPS) production were investigated. At harvest, the culture contained 1.325 g L^?1 of biomass and 117.2 mg L^?1 of EPS, respectively. The gravimetric EPS production rate was 16.7 mg g^?1 cell dry weight day^?1, which was 2.1 times higher than previously reported. Using sigmoid model, batch fermentation of N. flagelliforme was kinetically simulated to obtain equations including substrate consumption, biomass growth, and EPS accumulation. Results from a simulation correlated well with the experimental ones, indicating that this method could be useful in studying EPS production from batch and fed-batch cultures.     

利用扁桃斑鸠菊叶发酵高产粗毛纤孔菌胞外多糖的条件优化及其抗氧化活性研究

粗毛纤孔菌胞外多糖是粗毛纤孔菌液体发酵的重要活性代谢产物,但采用常规的发酵方法,粗毛纤孔菌胞外多糖的产量较低。为更好地获取粗毛纤孔菌胞外多糖,本文采用双向液体发酵的方法,通过向发酵培养基中添加适量的扁桃斑鸠菊叶粉末,来提高粗毛纤孔菌胞外多糖的产量,并对优化得到的胞外多糖抗氧化活性进行了研究。以发酵液中胞外多糖含量为指标,采用单因素实验和正交实验优化发酵条件;采用红外光谱对胞外多糖的结构特征进行分析;通过测定胞外多糖对ABTS、DPPH和羟基自由基的清除率来了解其抗氧化活性。结果表明,最优发酵条件为:扁桃斑鸠菊叶粉末添加量0.5g/L、发酵时间10d、pH 6.5、接种量5.0mL,在此条件下,粗毛纤孔菌胞外多糖的产量达到(2.34±0.25)mg/mL,与未添加扁桃斑鸠菊叶的空白组相比,其胞外多糖产量提高了约216.22%;红外分析与抗氧化活性实验结果表明,添加扁桃斑鸠菊叶后的胞外多糖与未添加扁桃斑鸠菊叶的胞外多糖红外主要吸收峰一致,并且对ABTS、DPPH以及羟基自由基清除能力相近。本研究结果表明扁桃斑鸠菊叶能够有效地提高粗毛纤孔菌胞外多糖的产量,为其他珍稀食药用菌胞外多糖的高效生产提供了新思路。     

聚唾液酸的发酵动力学研究

对以大肠杆菌K235发酵法生产聚唾液酸的动力学特性进行了研究,提出了细胞生长动力学,基质消耗动力学,聚唾液酸生成动力学模型,通过对实验数据的计算,模型的模拟结果较好地和实验值吻合,正确地分析 聚唾液酸的发酵过程及其动力学机制。     

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.     

Enhanced production of exopolysaccharides by fed-batch culture of Ganoderma resinaceum DG-6556

The objectives of this study were to optimize submerged culture conditions of a new fungal isolate, Ganorderma resinaceum, and to enhance the production of bioactive mycelial biomass and exopolysaccharides (EPS) by fed-batch culture. The maximum mycelial growth and EPS production in batch culture were achieved in a medium containing 10 g/l glucose, 8 g/l soy peptone, and 5 mM MnCl(2) at an initial pH 6.0 and temperature 31 degrees C. After optimization of culture medium and environmental conditions in batch cultures, a fed-batch culture strategy was employed to enhance production of mycelial biomass and EPS. Five different EPS with molecular weights ranging from 53,000 to 5,257,000 g/mole were obtained from either top or bottom fractions of ethanol precipitate of culture filtrate. A fed-batch culture of G. resinaceum led to enhanced production of both mycelial biomass and EPS. The maximum concentrations of mycelial biomass (42.2 g/l) and EPS (4.6 g/l) were obtained when 50 g/l of glucose was fed at day 6 into an initial 10 g/l of glucose medium. It may be worth attempting with other mushroom fermentation processes for enhanced production of mushroom polysaccharides, particularly those with industrial potential.