灵芝胞外多糖分批发酵非结构动力学模型

在２Ｌ搅拌发酵罐上提出了描述了灵芝胞外多糖分批发酵过程中菌球生长、底物消耗和胞外多糖形成的非结构动力学模型。首先研究了灵芝分批发酵特性,结果表明该发酵过程属菌体生长和产物形成相偶联型。然后在总结文献的基础上,运用动力学模型,经过非线性回归,得到了模型中的参数值。通过计算机模拟,证明模型预测值与实际实验值具有良好的拟合性。     

药用昆虫蜣螂对灵芝多糖生物合成的影响

采用液体深层发酵方式,研究了几种药用昆虫对灵芝多糖生物合成的影响。结果表明,药用昆虫蜣螂在添加量为5g/L时能显著促进灵芝胞内多糖(IPS)和胞外多糖(EPS)的形成(P<0.05)。胞内多糖和胞外多糖的产量分别由对照的(1.93±0.09)g/L和(520.3±20.2)mg/L提高到(2.41±0.12)g/L和(608.9±20.2)mg/L。灵芝胞内多糖和胞外多糖在DEAE纤维素柱上都可分离得到5种主要组分,其中IPS-1和EPS-1分别为2类多糖的主要组分。进一步用凝胶柱分离显示,IPS-1由3个单个的组分组成,EPS-1由2个单个的组分组成。添加蜣螂发酵后,灵芝胞内多糖和胞外多糖中没有出现新的组分,且各组分的相对含量也没有显著变化(P>0.05),提示添加蜣螂发酵后,灵芝胞内多糖和胞外多糖主要组分的合成途径并未改变。     

金针菇菌丝体的深层培养及多糖制取

从２０株金针菇菌株中筛选出适于液体发酵的９４Ｂ２株。该菌种适宜的摇瓶培养条件：培养温度２３～２４℃,ｐＨ６．５,接液体种量１０％,装液量≤５０ｍｌ／５００ｍｌ瓶;不同的间歇振荡形式对菌丝球产量和形态有显著影响。深层发酵工艺相似于抗生素发酵。发酵期间发酵液ｐＨ变化幅度很小,总糖、还原糖、氨基氮与菌丝生长量有一定的相关性。发酵酵的菌丝产量可达４７．５ｇ（湿重）／１００ｍｌ、胞外多糖达１７４．７ｋｇ／１００ｍｌ发酵液上清、胞内多糖达３３８．１ｍｇ／１００ｇ湿菌丝体。     

糖质溶液中发酵生产灰树花胞外多糖的研究

研究了葡萄糖浓度和pH值调控对糖质溶液中发酵生产灰树花胞外多糖的影响。葡萄糖浓度为5％时胞外多糖产量最高;发酵液pH控制为3．5－4．0时有利于胞外多糖的合成;并守试了重复使用菌丝体在糖质溶液中发酵生产灰树花胞外多糖的新方法。     

灵芝液态发酵胞内外多糖结构特征及其活性研究进展

灵芝是一味传统的中药材,具有很高的药用价值,多糖是其主要的活性成分之一,可从其子实体、孢子粉、发酵菌丝体和胞外液中获得。近年来,从灵芝菌丝体和胞外液中发现的多糖越来越得到研究者们的关注。本文从发酵培养基成分及发酵条件对灵芝胞内外多糖的影响、灵芝胞内外多糖的结构、灵芝胞内外多糖生物活性3个方面进行综述,为发酵来源灵芝多糖的开发利用提供科学理论依据。     

产灵芝胞外多糖培养基的优化及发酵指标变化

经单因素和正交试验优化,灵芝胞外多糖最佳发酵培养基各成分质量分数为:麦芽糖2%,黄豆粉1%,FeSO4·7H2O0.02%,KH2PO40.1%,土豆汁体积分数30%,pH自然,产量可达到86.36g·L-1(湿重)。灵芝胞外多糖产量受发酵过程各因素的影响,发酵过程中pH、总糖、还原糖和氨基氮有一定的相关性。灵芝多糖整个发酵过程需要144h左右,第6d达到发酵终点。     

灵芝胞外多糖的分离纯化及生物活性

目前,灵芝多糖的抗肿瘤及免疫活性已得到人们的广泛关注[1]。灵芝子实体多糖和发酵过程中产生的胞内和胞外多糖已被国内外的研究者证实都是有效多糖[2]。因此利用深层发酵来大规模地生产生物活性多糖是目前灵芝开发利用技术的热点。国内对灵芝培养基的组成、培养方法等已?..     

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。     

灵芝胞外多糖分批发酵动力学模型

利用分批发酵研究了灵芝(Ganoderma lucidum)胞外多糖的合成特性,结果表明Ganodermalucidum多糖合成和菌体生长呈部分生长关联型。菌体干重、胞外多糖分别达到15.56g·L-1、3.02g·L-1,胞外多糖对细胞干重得率系数(Yp/x)为0.19。根据分批发酵试验结果采用Logistic方程、Luedeking-Piret方程和类似Luedeking-Piret方程,得到了描述灵芝生长、胞外多糖以及葡萄糖底物消耗分批发酵动力学模型。同时在初始葡萄糖变化较大范围内,试验数据与模型预测值进行了比较拟合,平均相对误差小于5%,表现出很好的适用性。表明该动力学模型对指导灵芝胞外多糖的发酵生产具有实际意义。     

灵芝胞外多糖分批发酵动力学模型

利用分批发酵研究了灵芝（Ganoderma lucidum）胞外多糖的合成特性,结果表明Ganoderma lucidum多糖合成和菌体生长呈部分生长关联型。菌体干重、胞外多糖分别达到15.56g·L^-1<、3.02g·L^-1<,胞外多糖对细胞干重得率系数(Y_p/x）为0.19。根据分批发酵试验结果采用Logistic方程、Luedeking-Piret方程和类似Luedeking-Piret方程,得到了描述灵芝生长、胞外多糖以及葡萄糖底物消耗分批发酵动力学模型。同时在初始葡萄糖变化较大范围内,试验数据与模型预测值进行了比较拟合,平均相对误差小于5％,表现出很好的适用性。表明该动力学模型对指导灵芝胞外多糖的发酵生产具有实际意义。     

调控pH提高分批发酵赤霉素GA3产量

为高效率发酵生产GA₃,对藤仓赤霉菌发酵过程pH进行优化调控研究。采用5L全自动发酵罐,在pH 3.0-5.0条件下,对藤仓赤霉菌菌丝生长及GA₃产量的影响进行了考察,实验数据表明：在pH 4.0条件下,菌比生长速率可获最大值,为0.395/h;而pH 3.0条件下,GA₃比生成速率最大,达到4.43mg/(g?h)。基于不同pH条件下,对菌比生长速率、得率、GA₃比生成速率的影响,提出GA₃分批发酵过程中的pH调控策略,即：0-20h,pH自然;20-50h,pH 4.0;50-80h,pH 3.0-3.5;80h后控制pH为3.5-4.0。在此控制模式下,经过196h发酵GA₃的终产量达到2 224mg/L,GA₃产率44.5mg/g,GA₃生产强度0.242mg/(L?h),分别比不控制pH条件下发酵的数值增长了7.75%、7.74%、8.04%,表明该pH控制策略能增进GA₃发酵生产效率。     

茴香酸产生菌发酵条件的优化

为提高微生物降解反式茴脑获得茴香酸的产量,对假单胞菌Pseudomonas sp.NT2的发酵参数进行优化,以提高降解过程的转化率。利用单因素试验考察碳氮源种类及浓度、反式茴脑添加量、发酵温度、接种量、初始pH以及装液量对茴香酸生成量、反式茴脑降解率的影响,通过Plackett-Burman试验和最陡爬坡试验确定影响茴香酸生成量的显著因素并获取中心点,最后采用Box-Behnken模型进行响应面优化得到最佳发酵条件并验证。结果表明氯化铵浓度、初始pH和装液量是显著影响因素,最佳发酵条件为:柠檬酸钠10 g/L,氯化铵1.26 g/L,反式茴脑添加量1%,发酵温度30℃,接种量4%,初始pH 7.9,装液量42 mL/250 mL。优化后茴香酸生成量为7.24 g/L,为优化前的3.5倍,茴香酸摩尔生成率为80.72%,反式茴脑降解率为89.81%,分别比优化前提高了270.28%和97.78%。综上,假单胞菌NT2是生物转化生产茴香酸的潜力菌株。响应面优化可以显著提高反式茴脑的降解率和茴香酸产量,这为大规模生产茴香酸奠定了基础。     

Exopolysaccharide production by free and immobilized microbial cultures

The batch production of different exopolysaccharides (alginate, xanthan, pullulan, dextran) by free and immobilized microbial cultures was investigated. First, conventional free-cell cultures were performed to obtain control fermentation parameters and macromolecular characteristics of exopolysaccharides. Then microbial cultures were immobilized in composite agar layer/microporous membrane structures and tested for polysaccharide production. The immobilized-cell system proved unsuitable for xanthan and pullulan production. Owing to the fouling of the microporous membrane by the polysaccharide, dextran production by immobilized Leuconostoc mesenteroides also was inefficient. More promising results have been obtained with immobilized Azotobacter vinelandii cultures. The amount of alginate produced by immobilized A. vinelandii represented about 60% of that recovered from a free-cell culture, whereas the polysaccharide yield reached 35% instead of 9% for the free counterpart. These results are compared to the macromolecular characteristics of exopolysaccharides.     

Improvement of mannitol production by Lactobacillus brevis mutant 3-A5 based on dual-stage pH control and fed-batch fermentations

Lactobacillus brevis 3-A5 was isolated and expected to produce mannitol efficiently by regulating pH in batch and fed-batch fermentations. In 48 h batch fermentations with free and constant pH, the optimal pH for cell growth and mannitol production in the first 24 h of incubation was 5.5, whereas that for mannitol production in the second 24 h of incubation was 4.5. To achieve high cell density and mannitol yield simultaneously, a dual-stage pH control strategy was proposed based on the kinetic analysis of mannitol production. The pH value was controlled at 5.5 for the first 12 h of fermentation and subsequently shifted to 4.5 until the fermentation was completed. Under dual-stage pH control fermentation, a 103 g/L yield of mannitol with a volumetric production rate of 3.7 g/L/h was achieved after 28 h. The dual-stage pH control fed-batch fermentation strategy was further developed to improve mannitol yield, wherein the yield increased by 109 % to 215 g/L after 98 h of fermentation. This value is the highest yield of mannitol ever reported using L. brevis.     

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。     

响应面分析法优化黑根霉胞外多糖发酵工艺

实验以商品化的马铃薯葡萄糖液体培养基为基础培养基,以胞外粗多糖产量为考察指标,运用响应面分析法考察玉米浆浓度、KH₂PO₄浓度和发酵时间3个因素对胞外多糖发酵产量的影响,以获得黑根霉胞外多糖发酵最优工艺,建立高产、稳定、可控的胞外多糖发酵生产工艺技术方案。经响应面分析,各因素按照对响应值的影响顺序为：玉米浆浓度>发酵时间> KH₂PO₄浓度,且玉米浆浓度、发酵时间对胞外多糖产量的影响极显著,KH₂PO₄浓度对胞外多糖产量的影响不显著。胞外多糖发酵最优工艺为：玉米浆3.2mg/mL、KH₂PO₄ 1.5mg/mL和发酵时间132h,在此条件下胞外多糖的最大预测产量为0.824mg/mL。实验重复性好,是一个高产、稳定、可控的胞外多糖发酵生产工艺技术方案,可以指导黑根霉胞外多糖发酵。     

营养及环境因素对黄色短杆菌发酵生产L-亮氨酸的影响

目的:研究葡萄糖、玉米浆、蛋氨酸等主要营养物质以及环境因素对发酵生产L-亮氨酸的影响。方法:应用单因素实验确定发酵条件,采用高效液相色谱法测定产量。结果:在最优发酵条件下,以种龄36h、接种量为10%,摇瓶产L-亮氨酸的量可达19.4g/L,采用10L罐分批补料发酵64h可积累29.47g/L的亮氨酸。结论:营养及环境因素对发酵生产L-亮氨酸具有重要影响。     

基因组改组技术选育耐酸性琥珀酸放线杆菌

以琥珀酸产生菌Actinobacillus succinogenes CGMCC 1593为出发菌,分别经过紫外线-甲基磺酸乙酯(UV-EMS)和紫外线-硫酸二乙酯(UV-DES)诱变处理,得到7株耐酸性有所提高的突变株.以此作为候选菌库,经3轮原生质体递进融合,筛选获得4株可以在pH 5.6下生长的改组菌株.其中改组菌株F3-21在pH 5.6的完全液体培养基中生长的OD值是原始菌的7倍,在pH 5.2条件下仍能生长;其摇瓶发酵48h琥珀酸产量较原始菌株提高48%.在5L发酵罐中进行分批发酵,当控制pH在较低值(5.6～6.0)时,F3-21厌氧发酵48h积累琥珀酸38.1g/L,较出发菌株提高了45%;当控制pH在6.5～7.0时,F3-21厌氧发酵32h积累琥珀酸40.7g/L.F3-21在5L发酵罐中进行补料分批发酵,厌氧发酵72h,产琥珀酸达67.4g/L.结果说明基因组改组技术能够改进琥珀酸放线菌的耐酸性能及其琥珀酸的产量.     

Extractive fermentation for butyric acid production from glucose by Clostridium tyrobutyricum

A novel extractive fermentation for butyric acid production from glucose, using immobilized cells of Clostridium tyrobutyricum in a fibrous bed bioreactor, was developed by using 10% (v/v) Alamine 336 in oleyl alcohol as the extractant contained in a hollow-fiber membrane extractor for selective removal of butyric acid from the fermentation broth. The extractant was simultaneously regenerated by stripping with NaOH in a second membrane extractor. The fermentation pH was self-regulated by a balance between acid production and removal by extraction, and was kept at approximately pH 5.5 throughout the study. Compared with conventional fermentation, extractive fermentation resulted in a much higher product concentration (>300 g/L) and product purity (91%). It also resulted in higher reactor productivity (7.37 g/L. h) and butyric acid yield (0.45 g/g). Without on-line extraction to remove the acid products, at the optimal pH of 6.0, the final butyric acid concentration was only approximately 43.4 g/L, butyric acid yield was 0.423 g/g, and reactor productivity was 6.77 g/L. h. These values were much lower at pH 5.5: 20.4 g/L, 0.38 g/g, and 5.11 g/L. h, respectively. The improved performance for extractive fermentation can be attributed to the reduced product inhibition by selective removal of butyric acid from the fermentation broth. The solvent was found to be toxic to free cells in suspension, but not harmful to cells immobilized in the fibrous bed. The process was stable and provided consistent long-term performance for the entire 2-week period of study.     

一株高产Monacolin K紫红曲霉菌株筛选、鉴定及发酵条件优化

为从天然发酵红曲米中分离的30株红曲霉菌株中筛选高产MonacolinK的菌株,并对其产MonacolinK的发酵条件进行优化。实验采用高效液相色谱法(HPLC)筛选到9株具有产MonacolinK能力的红曲霉菌株,其中以编号ZX26的菌株产MonacolinK能力最高,发酵液中Monacolin K产量达到107.6mg/L,并且产MonacolinK能力具有良好的稳定性。微生物形态学结合ITS基因同源性分析结果表明,编号ZX26菌株为紫红曲霉。进一步采用单因素试验和正交试验法优化紫红曲霉ZX26产MonacolinK的发酵条件,结果表明在培养基组分为葡萄糖70g/L,牛肉膏15g/L,NaNO32g/L,MgSO4·7H2O0.5g/L,KH2PO41.5g/L时,其最优发酵条件为:发酵初始pH4.0,接种量为7%,培养温度30℃,发酵10天,在此条件下,紫红曲霉ZX26发酵液中MonacolinK产量达到271.36mg/L,相对于培养条件优化前MonacolinK产量提高152.19%,经验证此培养条件下MonacolinK产量最佳。