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。     

通气量对灵芝菌丝体液态深层发酵合成灵芝三萜的影响

采用5 L搅拌式发酵罐研究灵芝菌丝体液态深层发酵合成灵芝三萜的扩大培养条件,考察了不同条件下的通气量对灵芝菌丝体生长、比生长速率、灵芝三萜合成、比合成速率、还原糖消耗、还原糖比消耗速率、铵根离子消耗以及铵根离子比消耗速率的影响。研究结果表明,通气量能够显著影响菌丝体的生长以及灵芝三萜的合成,当通气量为8 L/min时,菌丝体合成灵芝三萜得率和生产强度最高,分别为0.204 g/L和0.00131 g/(L·h),最大菌丝体得率达到8.77 g/L。发酵过程中菌丝体最大比生长速率为0.0704 1/h,灵芝三萜最大比合成速率为0.0256 1/h,还原糖和铵根离子最大比消耗速率分别为0.562 1/h和0.0171 1/h。     

乙酸镁对桑黄液态发酵合成黄酮类物质的促进研究

本文探究了桑黄菌丝体黄酮类物质合成中的关键影响因素。在添加乙酸镁单因素实验基础上,运用Plackett-Burman设计筛选出对黄酮产量影响显著的3个因素:接种量、乙酸镁添加、基质中的葡萄糖;通过中心组合设计确定了合成黄酮类物质的最优发酵工艺:基质营养因子葡萄糖23.41g/L、酵母自溶粉10g/L、桑树粉10g/L、KH_2PO_4 1g/L、MgSO_4?7H_2O 1g/L,接种量10%,乙酸镁添加量1.16g/L,在上述条件下,桑黄黄酮产量为0.75g/L,较未优化对照组提高了1.43倍。通过添加乙酸镁,较大幅度地提高了桑黄菌丝体中黄酮类物质的合成,为桑黄规模化发酵产黄酮类物质提供了参考价值。     

云芝糖肽的液体发酵培养基的研究

通过液体发酵的摇瓶实验,考察碳源、氮源、碳氮比和乙醇浓度对云芝糖肽的产率影响,确定葡萄糖和玉米淀粉为适宜碳源,蛋白胨和黄豆饼粉为适宜氮源,合适的碳氮比为20∶1,适宜的乙醇体积分数为1.5%。采用以上的培养基进行70 L发酵罐进行扩大实验和10 t工业生产规模试验。发酵周期32 h,最终生物量达到13.0 g/L,云芝糖肽产率平均为2.21 g/L,与摇瓶发酵水平相当。此外工业实验还确定了云芝液体发酵的pH值、残糖浓度以及菌丝体形态等终点指标。     

猴头菌高产麦角甾醇液体发酵工艺优化

以菌丝体中麦角甾醇产量为考察指标,在单因素实验的基础上用响应面分析法考察碳源、氮源和无机盐3个因素对麦角甾醇发酵产量的影响,以获得猴头菌液体发酵产麦角甾醇最优工艺,建立高产、稳定的猴头菌液体发酵产麦角甾醇生产工艺。经响应面分析,各因素按照对响应值的影响顺序为：氮源>碳源>无机盐,且氮源对麦角甾醇产量的影响极显著,碳源和无机盐对麦角甾醇产量的影响不显著。猴头菌液体发酵产麦角甾醇最优工艺为：发酵培养基为酵母自溶粉18g/L、复合碳源14g/L（葡萄糖:麦芽浸粉,7.4:6.6,M/M）、无机盐3.9g/L（KH₂PO₄:K₂S₂O₈,2.6:1.3,M/M）;接种量为10%,培养时间为7d,在此条件下菌丝体生物量干重达11.24g/L,麦角甾醇的产量达69.79mg/L,比优化前分别提高了71.08%和81.56%。该发酵工艺重复性好,效率高,成本低,是一个稳定且可控的猴头菌液体发酵产麦角甾醇生产工艺技术方案;通过该发酵工艺得到的猴头菌发酵菌丝体麦角甾醇含量高,为相关功能营养食品的开发提供了优质资源。     

变转速策略调控灵芝菌丝体发酵高产三萜

灵芝发酵过程中,采用变转速调控策略,对振荡发酵阶段进行优化,以期达到高产三萜的目的。振荡阶段最佳条件为转速由150r/min变为100r/min,该策略与液体静置培养相结合,最终菌丝体三萜产量高达678.0g/L,比优化前提高了21%。振荡发酵阶段的变转速策略有效地提高了三萜的产量。     

瑞士乳杆菌LH-G51冻干菌粉生产工艺研究

目的：对瑞士乳杆菌LH-G51菌粉生产工艺进行优化。方法：通过单因素及正交实验设计,确定适合LH-G51生长的发酵培养基、冻干保护剂配方及生产工艺。结果：发酵时间、碳氮源及微量元素等添加量均对LH-G51生长有明显影响。最终确定LH-G51培养基碳氮源及微量元素为：葡萄糖20 g/L,大豆蛋白胨10 g/L,酵母膏15 g/L,MgSO4·7H2O为250 mg/L,MnSO4·H2O为50 mg/L,发酵时间10 h,保护剂为B。结论：根据优化工艺,LH-G51冻干菌粉活菌数可达到4.21×1011 CFU/g。     

珍稀药用真菌——樟芝深层发酵培养条件的优化

对樟芝深层发酵培养基进行了筛选,并在此基础上对发酵条件进行了优化。以樟芝深层发酵菌丝体三萜产量为主要目标产物,确定发酵培养条件为:40g/L葡萄糖,6g/L豆饼粉,1g/L K_2HPO_4,0．5g/L MgSO4,VB_1 100mg/L,自然pH,接种量为20%,装液量为100mL/250mL三角瓶,转速100r/min,26℃恒温培养6d,胞内三萜产量达15．25mg/100mL发酵液。     

发酵性丝孢酵母(Trichosporon fermentans)发酵产油脂的研究

通过摇瓶发酵,考察了碳源浓度、氮源种类和浓度对发酵性丝孢酵母(Trichosporonfermentans)发酵产油脂的影响,对发酵产油脂条件的初步优化结果为:在葡萄糖100 g/L、蛋白胨1.8 g/L、初始pH 7.0的培养基中,以10%的接种量,于33℃、190 r/min的摇床上发酵120 h,可得菌体生物量为18.2 g/L,干细胞的油脂含量为68.5%。     

pH对灵芝液态发酵代谢物及抗氧化活性的影响

已有研究报道灵芝栽培生长的最适pH在中性偏酸环境,在碱性范围的生长及代谢情况鲜见报道。本研究主要探究广泛pH对灵芝液态发酵代谢物及其抗氧化活性的影响。采用摇瓶液态培养后分析代谢物中灵芝三萜、胞内外多糖、菌丝体蛋白及抗氧化活性等指标,系统比较灵芝菌丝体在pH值2-11的生长和代谢情况。研究结果表明,灵芝菌丝体生长、合成灵芝三萜、胞内多糖、30E胞外多糖、菌丝体蛋白和菌丝体水解氨基酸的最适pH值分别为10、3、2、7、2和2。对应结果分别为17.13 g/L、33.86 mg/g、72.73 mg/g、7.86 g/L、71.42 mg/g和107.10 mg/g。比对照分别提高28.5%、77.3%、22.4%、96.5%、97.1%和70.8%。胞内多糖组分1和组分2最高分子量均在初始pH 4,分别为1.016×10⁸ g/mol和9.280×10⁴ g/mol,胞外多糖组分1最高分子量在初始pH 10,为4.946×10⁶ g/mol;对菌丝体的总抗氧化能力、1,1-二苯基-2-三硝基苯肼(1,1-diphenyl-2- picrylhydrazyl,DPPH)自由基清除能力、羟自由基清除能力分析结果表明最佳的初始pH分别为3、7、9。本研究为液态发酵方式下灵芝生长及其代谢物定向调控发酵的工艺优化提供参考依据,同时发现灵芝菌丝体中优质蛋白及抗氧化活性可在功能性食品和化妆品领域推广应用。     

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%。     

Study of fermentation behavior and formulation of a semidefined nutrient medium based on acid-production measurements in Z. mobilis cultures

Batch fermentations of glucose to ethanol by Z. Mobilis.(ATCC 10988) were examined in several semidefined nutrient media. The measurement of acid produced by the microorganism was used to study its transient fermentation characteristics. Limitation of nitrogen source in the semidefined medium of Rogers and coworkers(2) was found to limit the growth of this microorganism in the late stages of batch fermentations, when the initial glucose concentration was 75 g/L and higher. The microorganism exhibits a preference for inorganic nitrogen over preformed organic nitrogen provided by yeast extract. The microbial growth occurs exponentially in the presence of ammonium sulfate and yeast extract. However, in the absence of ammonium sulfate, the growth occurs in a linear fashion. The "linear" growth phase is characterized by poor cell-mass yields, and during this phase, growth and ethanol production are decoupled. An improved semi-defined growth medium is established which supports better growth rate and cellular yield, without affecting the ethanol yield.     

Effect of nitrogen limitation on the ergosterol production by fed-batch culture of Saccharomyces cerevisiae

The diversity and content of available nitrogen sources in the growth medium both are very important in the accumulation of ergosterol in the yeast cell membrane. Growth on the good nitrogen sources such as ammonia can harvest more yeast cells than on poor ones, but ergosterol content in those yeast cells is relatively lower. Ergosterol content, one of the most variable parameters in ergosterol production by yeast cultivation, is greatly influenced by nitrogen limitation. The aim of our work was to study how the nitrogen sources affected the membrane ergosterol content and increase the total ergosterol yield. On the premise of keeping high ergosterol content in yeast cell, the ergosterol yield was enhanced by increasing the yeast biomass. Direct feed back control of glucose using an on-line ethanol concentration monitor was introduced to achieve high cell density. Ammonia, which acted as nitrogen source, was added to adjust pH during fermentation process, but its addition needed careful control. Cultivation in 5 L bioreactor was carried out under following conditions: culture temperature 30+/-1 degrees C, pH 5.5+/-0.1, agitation speed 600 rpm, controlling ethanol concentration below 1% and controlling ammonium ion concentration below 0.1 mol/L. Under these conditions the yeast dry weight reached 95.0+/-2.6 g/L and the ergosterol yield reached 1981+/-34 mg/L.     

A novel Ganoderma lucidum G0119 fermentation strategy for enhanced triterpenes production by statistical process optimization and addition of oleic acid

A novel enhanced triterpenes fermentation production process by Ganoderma lucidum G0119 with the addition of oleic acid in the medium has been developed and optimized. All of the six exogenous additives tested were found to exhibit stimulatory effect on mycelial growth and triterpenes biosynthesis by G. lucidum. The results show that oleic acid addition had significant role in promoting triterpenes production. The optimal concentration and time of oleic acid addition were determined to be 30 mL/L and 0 h, respectively. Furthermore, three significant factors influencing triterpenes production were identified as glucose, magnesium sulfate and temperature using the Plackett–Burman design. The optimized conditions by central composite design were 27.83 g/L glucose, 1.32 g/L magnesium sulfate, 26.2°C temperature. The triterpenes fermentation yield with the optimized medium based on actual confirmatory experimental data in 6 L fermentor was 1.076 g/L versus the statistical model predicted value of 1.080 g/L. Our innovatively developed triterpenes fermentation production technology and process has been proven to produce high triterpenes productivity and yield conceivably useful for industrial production.     

樟芝产生三萜类化合物的液体培养条件的响应面法优化

樟芝(Antrodia cinnamomea)是一种非褶菌目、多孔菌科的多年生蕈菌类,樟芝子实体中含有多种生理活性物质包括三萜类化合物,但野生樟芝只生长在台湾特有的牛樟树树干腐朽的心材内壁和枯死倒伏的牛樟树表面,生长极其缓慢,很难获得,价格昂贵。本研究的目的是通过液体培养樟芝的菌丝体以产生三萜类化合物,用响应面法优化了樟芝产生三萜类化合物的液体发酵条件。首先对樟芝的液体发酵的培养基成分及培养条件进行了单因素优化,研究发现樟芝液体发酵产生三萜类化合物的最佳碳源和氮源分别为葡萄糖和酵母提取物,最佳浓度分别为100 g/L和9 g/L,优化的培养基配方为(g/L):葡萄糖100.0,酵母提取物9.0,Mg SO4·7H2O 0.5,KH2PO41.0。优化的培养条件为:初始pH值6.0,温度28℃,接种量10%(v/v),摇床转速180 r/min。在此基础上,用响应面法对樟芝液体发酵产生三萜类化合物影响最大的三个因素即碳源、氮源和培养温度进行了优化,结果优化的三种因素条件为:葡萄糖104.71 g/L,酵母提取物9.93 g/L,温度28.42℃。用优化的培养条件液体培养樟芝,其三萜类化合物的产量达到391.45 mg/L,比优化前的产量223.39 mg/L提高了75.23%,为进一步研究液体培养樟芝产生三萜类化合物奠定了基础。     

发酵产丁二酸过程中废弃细胞的循环利用

对厌氧发酵产丁二酸后的废弃细胞进行破壁处理,考察了以细胞水解液作为有机氮源重新用于丁二酸发酵的可行性。比较了超声破碎、盐溶、酶解3种方法破碎细胞获得的水解液作为氮源发酵产丁二酸的效果,结果表明酶解制得的细胞水解液效果最佳。以总氮含量为1.11g/L的酶解液(相当于10g/L酵母膏)作为氮源发酵,丁二酸产量可达42.0g/L,继续增大酶解液用量对耗糖、产酸能力没有显著提高。将细胞酶解液与5g/L酵母膏联用发酵36h后,丁二酸产量达75.5g/L,且丁二酸生产强度为2.10g/(L·h),比使用10g/L酵母膏时提高了66.7%。因此,厌氧发酵产丁二酸结束后的废弃细胞酶解液可以替代原培养基中50%的酵母膏用于发酵。     

树干毕赤酵母和酿酒酵母混合糖发酵产乙醇

以树干毕赤酵母和酿酒酵母为发酵菌株,酸性蒸汽爆破玉米秸秆预水解液和纯糖模拟液为C源,采用固定化酵母细胞的方法,研究了酸爆玉米秸秆预水解液初始pH、N源种类及其浓度、3种发酵模式对树干毕赤酵母戊糖发酵的影响。结果表明:玉米秸秆预水解液适合发酵的初始pH范围为6.0～7.0;1.0 g/L的(NH4)2SO4作为N源,在40 g/L葡萄糖和25 g/L木糖培养基中发酵24 h,糖利用率达到99.47%,乙醇质量浓度为24.72 g/L,优于尿素和蛋白胨作为N源;3种模式的发酵体系中,以游离树干毕赤酵母和固定化酿酒酵母发酵性能最好,糖利用率和乙醇得率分别为99.43%和96.39%。     

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.