氮源对灵芝菌丝体液态深层发酵合成灵芝三萜的影响

以沪农灵芝1号为供试菌株,葡萄糖作为碳源,用硫酸铵、氯化铵、鱼粉蛋白胨、胰蛋白胨和酵母粉作为氮源,研究不同种类氮源对灵芝菌丝体液态深层发酵过程的影响。首先,确定了N-10酵母自溶粉作为发酵的氮源,降低了发酵的复杂性和不确定性;其次,考察N-10酵母自溶粉不同浓度对灵芝菌丝体发酵合成灵芝三萜过程中菌丝体的生物量、葡萄糖消耗、灵芝三萜产量等方面的影响,确定了N-10酵母自溶粉的适宜添加浓度。在此基础上,采用响应面中心组合设计,对4因素最佳水平范围进行研究,结果表明,葡萄糖、N-10酵母自溶粉、磷酸二氢钾和七水硫酸镁的含量分别为31.06g/L、2.76g/L、1.77g/L和1.99g/L时,灵芝三萜的理论产量为21.166g/kg干菌丝体,实际发酵产量提高到21.153g/kg干菌丝体。与原工艺相比,新工艺的灵芝三萜产量提高了6.22%。     

Screening of Ganoderma strains with high polysaccharides and ganoderic acid contents and optimization of the fermentation medium by statistical methods

Polysaccharides and ganoderic acids (GAs) are the major bioactive constituents of Ganoderma species. However, the commercialization of their production was limited by low yield in the submerged culture of Ganoderma despite improvement made in recent years. In this work, twelve Ganoderma strains were screened to efficiently produce polysaccharides and GAs, and Ganoderma lucidum 5.26 (GL 5.26) that had been never reported in fermentation process was found to be most efficient among the tested stains. Then, the fermentation medium was optimized for GL 5.26 by statistical method. Firstly, glucose and yeast extract were found to be the optimum carbon source and nitrogen source according to the single-factor tests. Ferric sulfate was found to have significant effect on GL 5.26 biomass production according to the results of Plackett–Burman design. The concentrations of glucose, yeast extract and ferric sulfate were further optimized by response surface methodology. The optimum medium composition was 55 g/L of glucose, 14 g/L of yeast extract, 0.3 g/L of ferric acid, with other medium components unchanged. The optimized medium was testified in the 10-L bioreactor, and the production of biomass, IPS, total GAs and GA-T enhanced by 85, 27, 49 and 93 %, respectively, compared to the initial medium. The fermentation process was scaled up to 300-L bioreactor; it showed good IPS (3.6 g/L) and GAs (670 mg/L) production. The biomass was 23.9 g/L in 300-L bioreactor, which was the highest biomass production in pilot scale. According to this study, the strain GL 5.26 showed good fermentation property by optimizing the medium. It might be a candidate industrial strain by further process optimization and scale-up study.     

油酸促进灵芝三萜液态深层发酵的工艺研究及规模化验证

灵芝三萜是灵芝中主要的活性成分之一,前期研究发现油酸可以促进灵芝三萜液态深层发酵下的发酵合成。本研究主要对油酸促进灵芝三萜液态深层发酵的工艺进行优化,并进行3L发酵罐规模的验证。通过单因素实验考察油酸的添加方式、添加时间和添加浓度对灵芝三萜的影响,结合响应面实验,获得最优工艺条件并进行验证：在发酵第32h添加1.21%高温灭菌油酸,最高灵芝三萜含量为42.69mg/g;在发酵第7h添加1.35%过滤除菌油酸,最高三萜含量为43.38mg/g,分别比对照提高2.04倍和2.08倍。在1 000mL摇瓶中添加高温灭菌油酸和过滤除菌油酸,灵芝三萜含量分别为32.18和32.48mg/g,为对照的1.96倍和1.95倍;在3L发酵罐规模下灵芝三萜含量分别为28.66和25.13mg/g,为对照的1.62倍和1.42倍。本研究系统优化了油酸促进灵芝三萜液态深层发酵的工艺条件,并在与工业生产相对应的3L发酵罐上进行验证。该研究可为灵芝三萜的规模化发酵提供重要参考和借鉴。     

OPTIMIZATION OF FERMENTATION MEDIUM FOR ACETOIN PRODUCTION BY Bacillus subtilis SF4-3 USING STATISTICAL METHODS

To improve the acetoin-producing ability of Bacillus subtilis SF4-3, isolated from “natto,” a Japanese traditional food, the fermentation medium was optimized in shake-flask fermentation by statistically designed methods. Based on results of the single-factor experiment, orthogonal experiment, and Plackett–Burman design, yeast extract, corn steep liquor, and urea were identified as showing significant influence on the acetoin production. Subsequently, the optimum combination of the three factors was investigated by the Box–Behnken design (BBD) of response surface methodology (RSM) in order to further enhance the acetoin production. The maximum acetoin yield of 45.4 g/L was predicted when the concentrations of yeast extract, corn steep liquor, and urea were 8.5 g/L, 14.6 g/L, and 3.8 g/L, respectively. The results were further confirmed in triplicate experiments using the optimized medium (glucose 160 g/L, yeast extract 8.5 g/L, corn steep liquor 14.6 g/L, urea 3.8 g/L, manganese sulfate 0.05 g/L, ferrous sulfate 0.05 g/L), and an acetoin yield of 46.2 g/L was obtained in the validation experiment, which was in agreement with the prediction. After the optimization of medium components, an increase of 36.28% in acetoin production was achieved in comparison to that at the initial medium levels.     

响应面法优化褐藻胶降解菌Cobetia sp.20发酵培养基

为了提高褐藻胶降解菌株Cobetia sp.20产褐藻胶裂解酶的能力,利用响应面法优化其发酵产褐藻胶裂解酶的培养基。首先利用单因素法分别对发酵培养基中的不同碳源、碳源添加量、不同氮源、氮源添加量以及氯化钠添加量、磷酸二氢钾添加量、硫酸镁添加量和pH进行探究,研究各因素对产酶的影响。在单因素实验的基础上,通过Plackett-Burman试验确定Cobetia sp.20发酵培养基中影响产酶的主要因素。通过响应面试验建立回归方程。研究结果表明,Cobetia sp.20最优发酵培养基配方为褐藻胶15.00 g/L、硫酸铵7.50 g/L、氯化钠15.00 g/L、硫酸镁0.50 g/L、磷酸二氢钾5.30 g/L、硫酸亚铁0.01 g/L、pH值7.58。优化后酶活为142.79 U/mL,比优化前提高了26.36%。褐藻胶裂解酶活的提高,为褐藻胶裂解酶的工业化生产提供了参考。     

出芽短梗霉产聚苹果酸发酵条件的优化

【背景】出芽短梗霉可发酵葡萄糖生成聚苹果酸,但存在转化率和转化效率低等瓶颈,阻碍其实现商业化生产。【目的】通过优化发酵培养条件,提高出芽短梗霉的聚苹果酸产量、糖酸转化率和生产强度。【方法】采用单因素试验优化适宜出芽短梗霉BK-10菌株产生聚苹果酸的培养条件,通过Plackett-Burman法对培养基组分筛选显著性影响因素,并对其培养基中无机盐进行正交试验优化,最后进行5 L发酵罐验证。【结果】最优培养基配方和培养条件:100 g/L葡萄糖,1.5 g/L尿素,0.20 g/L KH_2PO_4,0.20 g/L ZnSO_4,0.05 g/L MgSO_4,0.75 g/L KCl,30 g/L CaCO_3,0.01%吐温-80,发酵温度26°C,250 mL摇瓶装液量50 mL。【结论】通过优化,聚苹果酸的糖酸转化率达到0.71 g/g,生产强度达到0.89 g/(L·h),较优化前分别提高了18.33%和71.15%,为发酵葡萄糖合成聚苹果酸进而生产L-苹果酸工艺的工业化生产奠定经济性基础。     

复合有机氮源对灵芝三萜液态深层发酵的影响

以灵芝为材料,在前期研究基础上,以不同酵母粉作为氮源,研究复合有机氮源对灵芝三萜液态深层发酵的影响。首先,由单因素实验考察3种不同的酵母粉对灵芝菌丝体合成灵芝三萜的影响,确定酵母粉的最适宜浓度范围。在此基础上,根据中心组合实验设计,对3种酵母粉分别采用2种复合和3种复合的方式,优化复合有机氮源的最佳组合配比。结果表明：当基础培养基中添加6.6g/L的酵母粉N-1与6.6g/L的酵母粉N-2时,灵芝三萜产量可达0.478g/L（理论产量为0.485g/L）,比添加单一酵母粉N-1、N-2、N-3分别提高了21%、139%、103%,其氮源用量为两种组合时最低。当基础培养基中酵母粉N-1、N-2与N-3添加量分别为5.07g/L、3.78g/L、7.63g/L时,灵芝三萜产量达0.514g/L（理论产量为0.510g/L）,比单因素对照组分别提高了30%、157%和74%。本研究优化的复合氮源添加方式可明显提高灵芝菌丝体液态深层发酵生产灵芝三萜的产量,为其规模化液态深层发酵的生产提供科学数据。     

Box-Behnken响应面法优化司替霉素B产生菌发酵条件

【背景】粗糙链霉菌(Streptomyces scabrisporus) HBERC-53204是本中心自主分离的一株链霉菌,经鉴定,其产生一种活性化合物司替霉素B (steffimycin B,SMB),对多种动植物重要病原菌具有良好生物活性。【目的】提高SMB发酵水平,拓宽放线菌活性天然产物在农牧业领域的研究及应用。【方法】以本实验室筛选出的一株产SMB的粗糙链霉菌HBERC-53204为研究对象,运用单因素试验筛选培养基的主效碳源、氮源、无机盐及各营养成分最适浓度,并基于单因素试验结果,通过Plackett-Burman (PB)试验设计筛选出显著影响因素,再结合最陡爬坡试验、Box-Behnken (BB)响应面法拟合显著因子与产量的非线性方程求解,进一步优化菌株产SMB的最佳发酵培养基配方。【结果】优化后最佳培养基配方为：葡萄糖36.22 g/L,蛋白胨8.00 g/L,酵母粉8.51 g/L,酸水解酪蛋白1.50 g/L,MgSO₄ 0.68 g/L,KNO₃ 1.00 g/L。经摇瓶验证,优化后SMB效价达到477.26 mg/L,比初始配方产量提高1 773.08%。在20 L发酵罐培养120 h,目标化合物产量达到214.48 mg/L。【结论】通过对菌株HBERC-53204发酵培养基优化,显著提高了SMB产量,并在20 L发酵罐中得到验证,在此基础上获得了克级纯品。     

不同发酵条件下产甘油假丝酵母有机酸代谢的研究

产甘油假丝酵母 (Candidaglycerolgenesis)发酵产生的有机酸对丙三醇产品质量和产率均有影响。发现在发酵其它条件恒定 ,装液比和玉米浆浓度增加时 ,发酵液总酸是递增的。在装液比为 0 2和玉米浆浓度为 8g L时 ,丙酮酸和乳酸在细胞生长期可分别积累达 4 1g L和 1 0g L ,比正常发酵时增加 2倍以上 ,丙三醇产率也低 ;然而 ,装液比为 0 0 8和玉米浆浓度为 4g L时 ,丙酮酸和乳酸产生较低 ,丙三醇产率较高 ,但乙酸积累比供氧不足时高 ,可达 2 6g L。发酵过程中有机酸被细胞代谢 ,含量逐渐下降 ,如在初糖浓度为 1 0 0g L时 ,有机酸在细胞生长期积累至高峰后 ,丙三醇和有机酸随之均降低至较低含量 ,并且丙酮酸或乳酸可以转化为乙酸。此外 ,在外加一些添加剂时对其产生有机酸也有影响 ,如添加 1 %油酸和VB1时可以降低乙酸的积累 ,同时增加丙酮酸的含量 ,丙三醇产量也有所增加 ;而丙酮酸结构类似物氟代丙酮酸和亚硫酸盐促进乙酸的产生 ,使酮戊二酸合成减少 ,丙三醇产量约增加 2 0 %。     

基于稳健性设计优化L-赖氨酸发酵过程

目的:选择发酵系统中各可控因素的最佳水平组合,从而减少各种干扰的影响,以获得稳健的赖氨酸产量。方法:利用田口法的内外表与Box性能规则优化赖氨酸发酵条件。结果:通过实验得知,转速、硫酸铵和葡萄糖浓度对发酵影响较大;结果稳定的最优发酵条件为初始葡萄糖浓度为80g/L、硫酸铵浓度为42g/L、转速为225r/min、初始pH值为6.7、接种量为8%。经实验验证,最优化发酵条件是低灵敏度的,最优目标值比较稳健。在10L自动发酵罐上培养65h,L-赖氨酸盐酸盐的产量为165.68g/L,比优化前提高了12.4%。结论:基于稳健性设计所得的最优发酵条件参数,可使目的产物产量稳定,便于生产操作。     

影响灵芝三萜类物质液态发酵合成的关键因素研究进展

灵芝是我国名贵的食药两用型菌类,具有广泛的药用价值,其三萜类物质为灵芝中最主要的药理活性物质之一。灵芝液态发酵因具有生长周期短、环境条件可控、目标产物质量稳定及易实现规模化制备等特点而成为获得灵芝三萜类物质最有前景的方式。灵芝三萜代谢途径、发酵工艺及参数、溶解氧控制等是影响灵芝三萜类物质液态发酵合成的关键因素。本文总结了灵芝三萜生物合成的代谢途径和相关的酶(基因)、液态发酵方式和发酵参数调节的溶解氧控制这3个层面对灵芝三萜类物质生物合成的影响,并对今后的研究方向进行了展望,为液态培养灵芝三萜类物质调控及高产提供参考,也为下一步研究提供借鉴。     

Improved production of citric acid by Yarrowia lipolytica using oleic acid as the oxygen‐vector and co‐substrate

Yarrowia lipolytica is able to secrete large amounts of citric acid (CA), which is greatly affected by the dissolved oxygen concentration (DOC) in the fermentation medium. In this study, oleic acid was selected as oxygen‐vector to improve DOC during CA fermentation. When 2% (v/v) of oleic acid was added to the culture broth, higher DOC (>42.1%) was determined throughout the CA synthesis phase. The yield of CA reached a maximum of 32.1 g/L (25.4% higher than the control) and the biomass was 8.8 g/L. The substrate uptake rate, products formation rate and key enzyme activities were also determined, and the results indicated that CA synthesis was strengthened with oleic acid addition. Furthermore, it was detected that oleic acid could be assimilated by the cells, which means that oleic acid could be served both as oxygen‐vector and co‐substrate for CA synthesis by Y. lipolytica. In a bioreactor with working volume of 3 L, the highest concentration of CA reached to 36. 4 g/L in the presence of 2% (v/v) oleic acid after 192 h of fermentation. These results confirmed that oleic acid could be applied in the large‐scale production of CA by Y. lipolytica.     

植物乳杆菌ZJ316生产细菌素

[目的]研究植物乳杆菌ZJ316生长和产细菌素的最佳培养基成分和发酵条件,以提高该菌产plantaricin ZJ316的能力.[方法]改变培养基成份和发酵条件,考察不同氮源、碳源等培养基成分和不同的发酵温度等条件对ZJ316生长和产细菌素的影响.[结果]最佳培养基为MRS培养基;优化后的培养基配方为葡萄糖10 g/L,麦芽糖10 g/L,酵母提取物10 g/L,蛋白胨10 g/L,柠檬酸三铵2 g/L,吐温80为1 Ml/L,K2HPO4·3H2O 6 g/L,乙酸钠5 g/L,硫酸镁0.2 g/L,硫酸锰0.05 g/L.培养基初始Ph6.5,30℃静置培养24 h.[结论]通过培养基成分和发酵条件的优化,细菌素产量提高了2.3倍,为进一步研究和规模化生产奠定基础.     

Optimization of culture medium for enhanced production of exopolysaccharide from Aureobasidium pullulans

Polysaccharides produced by microorganisms are utilized for a variety of purposes, including the use in cosmetics and as food additives. More recently, polysaccharides have been exploited by the medical and pharmaceutical industries, and those originated from many species of mushrooms have been especially useful in industrial applications; however, the production and synthesis of these compounds is costly and time consuming. In this study, we developed a method for low-cost production of exopolysaccharide (EPS) that effectively screens components and optimizes medium composition using statistical methods (Plackett-Burman and Box-Behnken design). As a result, we obtained the following optimized medium: sucrose 165.73 g/L, sodium nitrate 3.08 g/L, dipotassium phosphate 1.00 g/L, potassium chloride 0.50 g/L, magnesium sulfate 0.50 g/L, ferrous sulfate 0.01 g/L, and 0.71 g/L of Ashbya gossypii extract. The maximum production of about 29 g/L EPS was achieved in the optimized medium during 84 h batch fermentation.     

An unstructured kinetic model for the improvement of triterpenes production by Ganoderma lucidum G0119 based on nitrogen source effect

The kinetics of cell growth and triterpenes production for liquid submerged fermentation of the medicinal mushroom Ganoderma lucidum were investigated. A kinetic model was developed based on the Logistic and Luedeking-Piret equations for cell growth, substrate consumption and triterpene formation. The kinetic parameters of the model were optimized by specifically designed Runge-Kutta genetic algorithms. The mathematical model simulated the experimental data well and was capable of explaining the behavior of triterpenes production. The predictions of the kinetics from this model are very good both for normal fermentation kinetics under nitrogen limitation as well as for predictions of transitions to sluggish fermentations. The resulting model is very useful for scaling up liquid submerged fermentation of the mushroom G. lucidum and its application to the industrial production of triterpene.     

Statistical optimization of the medium composition by response surface methodology to enhance schizophyllan production by Schizophyllum commune

The response surface methodology (RSM) involving central composite design (CCD) was employed to optimize the fermentation medium for the cell growth and schizophllan production by Schizophyllum commune CGMCC 5.113 in submerged culture at pH 6.5 and 26 degrees C. The four variables involved in this study were glucose, yeast extract, ammonium nitrate, and magnesium sulfate. The statistical analysis of the results showed that, in the range studied, glucose and yeast extract had a highly significant effect on schizophyllan production. The optimal medium for schizophyllan production calculated from the regression model of RSM was as follows: glucose, 18 g/l; yeast extract, 0.5 g/l; NH4NO3, 0.48 g/l; and MgSO4, 0.05 g/l, with a predicted maximum schizophyllan production of 11.74 g/l. These predicted values were experimentally validated. The excellent correlation between predicted and measured values justifies the validity of the response model. The results of bioreactor fermentation also show that the optimized medium enhanced schizophyllan production (12.80 g/l) by S. commune in a 5-1 fermenter.     

Optimization of a liquid medium for beauvericin production in <Emphasis Type="Italic">Fusarium redolens</Emphasis> Dzf2 mycelial culture

Beauvericin (BEA) is a proven and potent antibiotic compound useful for bio-control and a potential antifungal and anticancer agent for human. This study was to evaluate and optimize the nutrient medium for BEA production in mycelial liquid culture of a high BEA-producing fungus Fusarium redolens Dzf2 isolated from a medicinal plant. Among various organic and inorganic carbon and nitrogen sources, glucose and peptone were found the most favorable for the F. redolens Dzf2 mycelial growth and BEA production. Through a Plackett-Burman screening test on a basal medium, glucose, peptone, and medium pH were identified as the significant factors for mycelial growth and BEA production. These factors were optimized through central composite design of experiments and response surface methodology, as 49.0 g/L glucose, 13.0 g/L peptone and pH 6.6, yielding 198 mg/L BEA (versus 156 mg/L in the basal medium). The BEA yield was further increased to 234 mg/L by feeding 10 g/L glucose to the culture during exponential phase. The results show that F. redolens Dzf2 mycelial fermentation is a feasible and promising process for production of BEA.     

Gluconate production by spores of Aspergillus niger

Spores of Aspergillus niger obtained by solid state fermentation on buckwheat seeds produced gluconic acid from glucose with a high yield, near 1.06 g gluconic acid/g glucose, close to the stoichiometric value. The reaction itself could be carried out either with purified biocatalyst or with the whole buckwheat medium resulting from spore production process. 200 g gluconic acid/L were obtained in 200 h with sequential feedings of glucose up to 190 g/L.     

Bioethanol from fermentation of cassava pulp in a fibrous-bed bioreactor using immobilized Δldh, a genetically engineered Thermoanaerobacterium aotearoense

There is an increasing worldwide interest in bioethanol production from agricultural, industrial, and urban residues for both ecological and economic reasons. The acid hydrolysis of cassava pulp to reducing sugars and their fermentation to ethanol were evaluated in a fibrousbed bioreactor with immobilized Δldh, a genetically engineered Thermoanaerobacterium aotearoense. A maximum yield of total reducing sugars of 53.5% was obtained after 8 h of hydrolysis at 85oC in 0.4 mol/L hydrochloric acid with a solid-to-liquid ratio of 1:20, which was optimized by using an orthogonal design based on preliminary experiments. In the FBB, the fed-batch fermentation, using glucose as the sole carbon source, gave a maximum ethanol production of 38.3 g/L with a yield of 0.364 g/g in 100 h; whereas the fed-batch fermentation, using xylose as the sole carbon source, gave 34.1 g/L ethanol with a yield of 0.342 g/g in 135 h. When cassava pulp hydrolysate was used as a carbon source, 39.1 g/L ethanol with a yield of 0.123 g/g cassava pulp in185 h was observed, using the fed-batch fermentation model. In addition, for repeated batch fermentation of cassava pulp hydrolysate carried out in the fibrous-bed bioreactor, long-term operation with high ethanol yield and volumetric productivity were achieved. The above results show that the acid hydrolysate of cassava pulp can be used for ethanol production in a fibrous-bed bioreactor, although some inhibition phenomena were observed during the process of fermentation.     

提高蛋白激发子产量的培养基及发酵条件的优化

为了进一步提高极细链格孢菌产蛋白激发子的产量,通过单因子和多因子试验与分析,筛选优化了适于极细链格孢菌产生蛋白激发子的培养基和培养条件,并检测了发酵过程中pH、还原糖、氨基氮和菌丝量变化以及与蛋白激发子产量的关系。结果表明,土豆淀粉和黄豆粉对蛋白激发子产量影响最大,其次是蛋白胨和无机盐。优化的发酵培养基主要成分（g／L）：碳源I 15、葡萄糖5、玉米淀粉5、土豆淀粉20、谷氨酸10、氮源I5、黄豆粉10、硫酸铵5。确定了优化的培养条件,调整培养基起始pH为7．0～7．5,将18h菌龄的种子培养液按10％接种量接种到装液量为75mL的500mL摇瓶中,在温度（28±1）℃、摇床转速180r／min下培养可获得理想的蛋白产量。在优化的培养基和培养条件下,发酵12～48h该菌进入对数生长期,48h进入稳定生长期,60h菌丝扣蛋白激发子产量达最高。蛋白产量与菌体生物量呈正相关,当还原糖、总糖量消耗到最低水平时,菌丝产量和蛋白激发子产量达最高。优化的培养基菌丝干重收率迭3．9g／100mL,蛋白激发子产量达到5．17g／L,比普通的土豆液体培养基提高近4倍。