丝状真菌Glarea lozoyensis SIIA-F1108产纽莫康定B0发酵条件的研究

【目的】采用响应面法优化丝状真菌Glarea lozoyensis SIIA-F1108发酵生产纽莫康定B_0培养基,提高发酵产量;通过氮源优化,降低发酵液菌体浓度,改善发酵过程的溶氧水平。【方法】采用Plackett-Burman设计和响应面法进行培养基优化,筛选出对纽莫康定B_0产量具有显著影响的因素;通过最陡爬坡实验及Box-Behnken设计,并利用Design-Expert软件对实验数据进行回归分析,得到优化的发酵培养基配方;通过对优化培养基中氮源组分进行全因子实验,最终得到高产量和低菌体浓度发酵培养基。【结果】实验数据表明:甘露醇、脯氨酸和葡萄糖对纽莫康定B_0产量影响最大;最佳浓度分别为甘露醇167.3 g/L、脯氨酸26.1 g/L、葡萄糖28.5 g/L。采用优化后的培养基进行摇瓶发酵,纽莫康定B_0产量达到了1 840 mg/L,较优化前提高了42%,与预测结果一致。用硫酸铵部分替换棉籽饼粉后,发酵液菌体浓度降低,在100 L发酵罐上对优化后的结果做了进一步的验证,纽莫康定B_0产量达到1 980 mg/L。【结论】模型预测值与实验值有较高吻合度,具备较高可信度和显著性,发酵产量提高了42%,响应面实验设计和分析方法能够有效地用于丝状真菌Glarea lozoyensis SIIA-F1108产纽莫康定B_0发酵培养基进行优化。通过调整培养基中的氮源组成,降低了发酵液菌体浓度,改善了发酵过程的溶氧水平。     

裂殖壶菌Schizochytrium sp. 20888产DHA培养条件优化

【目的】为了优化裂殖壶菌产DHA的培养条件,提高油脂中DHA含量。【方法】采用单因素试验和正交设计试验方案,针对分批培养时间、培养基碳、氮源的种类和浓度以及培养温度开展试验,采用重量法测定生物量、采用索氏提取法测定油脂总量,采用气相色谱法测定油脂DHA含量,考察培养条件对细胞油脂DHA含量的影响。【结果】最适培养时间为4 d,培养温度23°C,最优碳氮源组成为(g/L):葡萄糖65、甘油80、蛋白胨6、酵母粉4和谷氨酸钠8。【结论】裂殖壶菌Schizochytrium sp.20888在葡萄糖和甘油组成的复合碳源和由蛋白胨、酵母粉和谷氨酸钠组成的复合氮源的培养基中可以得到最优的DHA产量,细胞DHA含量能达到33.68%。     

圆红冬孢酵母利用生物乙醇废水-木薯粉水解液发酵产油

【目的】获得能够高效降解生物乙醇废水化学需氧量(COD)的圆红冬孢酵母菌株,评估废水初始COD浓度对驯化菌株生长的影响,将木薯粉生产微生物油脂和高浓度有机废水降解过程整合,以生物乙醇废水为水源制备生物乙醇废水-木薯粉水解液培养基,明确产油效率高、生物乙醇废水COD降解率高的初始还原糖浓度。【方法】采用在高浓度的生物乙醇废水中进行多次驯化的方法,获得能够适应废水环境的圆红冬孢酵母菌株;采用双酶水解法对加入乙醇废水中的木薯粉进行水解;采用重量法监测生物量浓度变化,采用酸热法提取油脂,重铬酸钾法监测COD,DNS法测定废水还原糖浓度,凯氏定氮法测定总氮,钼酸铵比色法测定总磷。【结果】通过驯化筛选得到一株能耐受高浓度生物乙醇废水的优势菌株Rhodosporidium toruloides D5。以未稀释的废水为培养基,驯化菌株的最终生物量浓度和COD降解率分别为3.8 g/L和75.0%。采用生物乙醇废水-木薯粉水解液发酵时,控制初始还原糖浓度低于30 g/L时,生物量浓度和油脂浓度随初始还原糖浓度的升高而升高,均在120 h时达到最高COD降解率,初始还原糖浓度对达到的最大COD降解率无明显影响,废水N、P去除率分别达到99%和92%以上。【结论】在未经稀释的高浓度生物乙醇废水中可获得较高的生物量浓度;采用高浓度生物乙醇废水-木薯粉水解液培养基发酵产油,初始还原糖浓度为30 g/L,可在保证高油脂产量的同时,实现废水COD的高效降解,有效回收利用废水中残余的N、P源,从而降低微生物油脂生产和废水处理成本,研究结果可为开发廉价微生物油脂生产技术提供有用的参考。     

高山被孢霉发酵产花生四烯酸油脂的补料工艺

为了缩短高山被孢霉(Mortierella alpina)产花生四烯酸(ARA)油脂发酵周期,以提高ARA油脂生产强度,主要研究了不同底物流加方式对M.alpina产ARA油脂的影响。考察分批发酵、残糖反馈补料分批发酵对ARA油脂发酵的影响,并进一步在残糖反馈补料发酵的基础上建立了一种反复补料分批发酵工艺。结果表明:与分批发酵相比,虽然细胞干质量和油脂浓度变化不显著,但是残糖反馈补料方式ARA生产强度从0.93提高至1.33g/(L·d)。在残糖反馈补料基础上反复补料分批发酵一共进行了4批,细胞干质量稳定在30 g/L左右,油脂含量稳定在50%左右,ARA含量分别达到42.81%、43.17%、42.30%和39.71%。     

木薯粉同步糖化发酵(SSF)产丁二酸

【目的】通过优化产琥珀酸放线杆菌GXAS137同步糖化发酵木薯粉产丁二酸的发酵培养基,提高丁二酸产量,降低生产成本。【方法】在单因素试验的基础上,先利用Plackett-Burman试验设计筛选出影响丁二酸发酵的重要参数,再采用正交试验确定重要参数的最佳水平。【结果】价格低廉玉米浆可用作氮源,影响丁二酸产量的重要参数是木薯粉、玉米浆、碱式碳酸镁和糖化酶浓度。最佳条件为(g/L):木薯粉100,玉米浆14,糖化酶2.0 AGU/g底物,碱式碳酸镁75。优化后丁二酸产量达到69.31 g/L,丁二酸得率为90.01%,生产强度为1.44 g/(L·h)。与初始条件(52.34 g/L)相比,丁二酸浓度提高了32.42%。并利用1.3 L发酵罐对SSF与SHF两种发酵工艺进行了比较,SSF丁二酸产量(72.21 g/L)远高于SHF(56.86 g/L)。【结论】产琥珀酸放线杆菌同步糖化发酵木薯粉丁二酸产量高,生产成本低,具有较好的工业化应用前景。     

产花生四烯酸油脂高山被孢霉干法造粒提油及菌粕的重复利用

对高产花生四烯酸油脂高山被孢霉干法造粒提油工艺中3个参数及菌粕重复利用进行研究。设计三因素四水平L16(43)正交试验,考察造粒直径、正己烷与菌粕的比例、萃取时间对提油效率及正己烷回收率的影响。结果表明:当含水率20%~25%、造粒直径1.2mm、正己烷的体积与颗粒的质量比20∶1L/g、萃取时间5h时,每克干菌体油脂得率0.5594g,正己烷的回收率达90%。与均质湿法提油相比,分别提高了17.35%和83.67%。用碱性蛋白酶及复合酶(纤维素酶、果胶酶和碱性蛋白酶)处理菌粕,以50%替代氮源(酵母膏)添加到培养基中,发酵周期分别为10d和7d。此时,生物量、油脂产量、花生四烯酸产量都达到了最大值,分别为30.33g/L、16.25g/L、8.59g/L(碱性蛋白酶处理);29.77g/L、16.89g/L、7.12g/L(复合酶处理)。其中,复合酶处理菌粕的生产强度可达4.253g/(L·d)、2.413g/(L·d)和1.017g/(L·d),与碱性蛋白酶处理相比,其生产强度分别提高了40.22%、48.49%和18.39%。干法造粒提油是有效的,且酶法处理菌粕的方法有应用前景。     

抗肿瘤银杏内生真菌Aspergillus oryzae YX-5发酵 培养基的优化

【目的】对一株具有抗肿瘤活性的银杏内生真菌Aspergillus oryzae YX-5的发酵培养基进行优化。【方法】以发酵后的菌体干重、粗提物质量和粗提物抗肿瘤活性为指标,通过单因素实验选出合适的碳源和氮源,再以选出的碳源、氮源以及K2HPO4、MgSO4·7H2O、KCl共5个因素进行正交实验,确定出最适宜的发酵培养基配方。【结果】YX-5的最佳发酵培养基配方为葡萄糖45 g/L,蛋白胨8 g/L,K2HPO4 0.5 g/L,MgSO4·7H2O 0.2 g/L,KCl 1 g/L,FeSO40.01 g/L。优化后菌体干重、代谢物的产量和抗肿瘤活性分别提高了41.88%、226.52%和19.31%。【结论】通过对米曲霉菌(Aspergillus oryzae)YX-5的发酵培养基进行优化,明显提高了粗提物产量和抗肿瘤活性,这对后期规模化发酵中减小发酵规模和降低工作量十分有利。     

柳枝稷青贮用乳酸菌复合系的组成多样性及其代谢特性

摘要:【目的】筛选一组乳酸产量高、组成稳定的柳枝稷青贮用乳酸菌复合系。【方法】通过连续限制性培养方法获得乳酸菌复合系SGL,使用变性梯度凝胶电泳(DGGE)和高通量测序技术分别分析其群落结构的稳定性和组成多样性。在培养基中添加不同氮源,测定氮源对SGL菌体生长和代谢产酸的影响。【结果】连续限制性培养8代,SGL的菌群结构趋于稳定,主要菌种为同型发酵乳酸菌,包括Lactobacillus nantensis (78.78%)、Lactobacillus plantarum(7.92%)、Lactobacillus pantheris(5.27%)、Bacillus coagulans(4.41%)和Lactococcus lactics(3.31%),是现有唯一的同时包含Lactobacillus、Lactococcus和Bacillus的乳酸菌复合系。酵母浸粉是促进SGL菌体生长和产乳酸的最好氮源,最适添加量为20 g/L。当(NH4)2SO4和酵母浸粉中N的比例为1:4时,菌体生长量和乳酸产量与20 g/L 酵母浸粉等同。【结论】乳酸菌复合系SGL 多样性高、组成稳定、可利用无机氮源,作为青贮饲料添加剂,具有很大的应用潜力,本研究为SGL的培养和应用提供了理论依据。     

小球藻高密度培养及油脂提取条件的优化

【目的】高密度培养小球藻及优化油脂提取条件。【方法】通过进行单因素实验研究不同培养基组成及环境因子对其细胞生长影响,并采用超声波提取法进行正交实验对藻粉油脂提取条件进行研究。【结果】对椭圆小球藻Y4进行异养培养,最适培养条件为:葡萄糖50 g/L,硝酸钾2 g/L,适宜的培养温度、摇床转速和接种量分别为29°C、180 r/min和20%。在此基础上,进行了1 L发酵罐培养实验,获得了干重18.25 g/L的生物量。通过对油脂提取条件进行优化,Y4的油脂提取率由优化前的25.0%提高到60.2%,提高了35.2%。【结论】优化了小球藻的培养条件及油脂提取条件,促进了小球藻的开发和利用。     

高山被孢霉发酵生产花生四烯酸的宏观形态

采用图像处理技术对高山被孢霉(Mortierella alpina)发酵过程中的不同形态进行分析,并对其产花生四烯酸(ARA)能力进行了比较。研究发现:复合N源中蛋白胨与酵母粉比例是影响高山被孢霉宏观形态的重要因素,球形形态生长的菌体中ARA产量较分散,菌丝体中ARA产量高;在球形形态中,空心球的菌体生物量低,ARA比例低,蓬松球可以兼顾菌体高生物量、高油脂比例及高ARA比例。产ARA能力由生物量、油脂比例及油脂中ARA比例共同决定。结果表明:直径大约4 mm、成核区域面积大约为43.6%、紧密度为71.36的蓬松球形态,是高山被孢霉一种相对较佳的发酵形态,其菌体产ARA能力分别是空心球和分散丝状菌体产ARA能力的2.01和2.70倍。     

利用甘蔗糖蜜发酵生产花生四烯酸的研究

通过培养高山被孢霉利用糖蜜来发酵生产花生四烯酸(ARA),研究了不同甘蔗糖蜜预处理方法对ARA发酵生产的影响。研究表明:H2SO4法是最利于ARA发酵生产的糖蜜预处理方法。利用预处理的甘蔗糖蜜发酵生产ARA,通过单因素实验设计,确定了最优的培养条件,包括初始还原糖80 g/L,N源6 g/L,接种量20%,初始pH6.0和培养温度25℃,在此条件下发酵,干细胞质量、油脂含量、ARA产量和糖利用率分别达到28.5 g/L、11.7g/L、3.68 g/L和94.5%。     

花生四烯酸油脂高产菌株的选育

以高山被孢霉为出发菌株,抗氧化剂——没食子酸辛酯为筛选剂,经过紫外-LiCl复合诱变处理,筛选出抗脂肪酸脱氢酶抑制剂的菌株。将筛选出的菌株经过摇瓶发酵复筛,筛选到1株生产性能优于出发菌株的突变株R807。与原始菌株相比,该菌株的油脂组成脂肪酸分布中C18系列脂肪酸相对较少,花生四烯酸(ARA)占总脂肪酸的含量保持在40%(质量分数)以上。其菌体生物量达到39.2 g/L,油脂产量达到16.3 g/L,ARA占总脂肪酸含量为41.72%(质量分数),ARA产量达6.81 g/L。各数值比原始菌株分别提高了22.9%、3.2%、35.1%和39.8%。连续传代多次,其产量性状无显著变化。     

Growth-coupled lipid synthesis in Mortierella alpina LPM 301, a producer of arachidonic acid

Mortierella alpina LPM 301, a producer of arachidonic acid (ARA), was found to possess a unique property of intense lipid synthesis in the period of active mycelium growth. Under batch cultivation of this strain in glucose-containing media with potassium nitrate or urea, the bulk of lipids (28-35% of dry biomass) was produced at the end of the exponential growth phase and remained almost unaltered in the stationary phase. The ARA content of lipids comprised 42-50% at the beginning of the stationary phase and increased continuously after glucose depletion in the medium due to the turnover of intracellular fatty acids; by the end of fermentation (189-210 h), the amount of ARA reached 46-60% of the total fatty acids (16-19% of dry mycelium). Plausible regulatory mechanisms of the growth-coupled lipid synthesis in microorganisms are discussed.     

高山被孢霉三阶段培养法生产花生四烯酸油脂

为提高高山被孢霉（Mortierella alpina）生物合成花生四烯酸油脂的生产效率,基于花生四烯酸油脂的积累机制,建立了一种三阶段培养法：第一阶段在全培养基中培养促进菌体生物量的快速积累,确定了60 g/L糖初始质量浓度时,最有利于生物量的快速积累;第二阶段在C源丰富而其他营养缺乏的条件下培养,促进油脂快速积累,对糖最佳初始浓度、接种时间、pH和培养时间进行了优化;第三阶段培养诱导油脂中花生四烯酸的高效积累,并确定此阶段培养时间为36 h时为最佳时间。实验结果表明：三阶段培养工艺条件下,菌体生物量、油脂量、花生四烯酸量分别为41.6、26.6和11.4 g/L,本研究相比传统分批发酵工艺在产率和花生四烯酸最终产量方面都有了显著提高。     

被孢霉γ-亚麻酸高产菌株选育

利用紫外线复合氯化锂诱变高山被孢霉SM96,筛选出一株高产γ-亚麻酸的菌株TM11,产量比出发菌株(25mg/L)提高了近3倍。对影响其多不饱和脂肪酸产生的因子Mg2+,VB6,营养盐溶液,磷源,碳源,氮源酵母膏进行了正交试验,选出TM11最佳的培养基配方:MgSO4·7H2O1.0g,VB6150mg/L,酵母膏6g/L,葡萄糖100g/L,营养盐溶液1mL/L,K2HPO42g/L。在上述最佳培养基中TM11的生物量达18.0213g/L,总脂达10.8128g/L,GLA量达668mg/L。     

离子注入花生四烯酸产生菌诱变选育

利用离子束注入生物技术对花生四烯酸产生菌(Mortierella alpina)进行诱变高产菌筛选。筛选到高产菌I₄₉N₁₈,该菌每升培养液可得生物量30.80g(约4%的含水量),干菌体油脂含量为25.8%,其中花生四烯酸的含量占总.脂的45.37%。30L和250L发酵罐发酵试验,该高产菌的花生.四烯酸得率为4.0g/L。     

Spore germination in <Emphasis Type="Italic">Mortierella alpina</Emphasis> is associated with a transient depletion of arachidonic acid and induction of fatty acid desaturase gene expression

Mortierella alpina is an oleaginous filamentous fungus whose vegetative mycelium is known to accumulate triglyceride oil containing large amounts of arachidonic acid (ARA 20:4, n − 6). We report that the spores of Mortierella alpina also contain a large proportion of ARA, comprising 50% of total fatty acid. Fatty acid desaturase genes were not expressed in dormant spores but were induced during germination, following a significant drop in the level of ARA (down from 50% of total fatty acid to 12%) prior to germ-tube emergence. We propose that ARA serves as a reserve supply of carbon and energy that is utilised during the early stages of spore germination in Mortierella alpina.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Arachidonic acid-rich oil production by Mortierella alpina with different gas distributors

Arachidonic acid (ARA)-rich oil production by Mortierella alpina is a high oxygen demand and shear-sensitive process. In the aerobic fermentation process, oxygen supply is usually a limiting factor owing to the low solubility of oxygen in the fermentation broth. Two kinds of perforated ring gas distributors and a novel microporous ceramic membrane gas distributor were designed and applied to improve oxygen supply. With the decrease of the orifice diameter of perforated ring gas distributors, dry cell weight (DCW), lipids concentration, and ARA content in total fatty acid increased from 17.86 g/L, 7.08 g/L, and 28.08 % to 25.67 g/L, 11.94 g/L, and 36.99 %, respectively. Furthermore, the effect of different dissolved oxygen (DO) on ARA-rich oil production with membrane gas distributor was also studied. The maximum DCW, lipid concentration, and ARA content using membrane gas distributor with DO controlled at 40 % reached 29.67 g/L, 16.74 g/L, and 49.53 %, respectively. The ARA titer increased from 1.99 to 8.29 g/L using the membrane gas distributor to substitute the perforated ring gas distributor. In the further experiment, a novel tubular titanium metal membrane gas distributor was successfully applied in a 7,000 L bioreactor and the results demonstrated that membrane gas distributor was industrially practical.