混菌发酵中不同分子量代谢产物对非酿酒酵母胞内蛋白及酒体有机酸的影响

本研究采用透析袋发酵法研究了酿酒酵母产生的不同分子量代谢产物对非酿酒酵母胞内蛋白和酒体有机酸的影响。当截留分子量为3.5 kD和10.0 kD时非酿酒酵母的存活时间分别延长至18 d和22 d,表明通过改变菌种之间物质的交换可以调节非酿酒酵母的存活时间。蛋白质解析发现共有65个蛋白质斑点表达出现差异,占蛋白质总数的13%,经质谱鉴定表明与这些蛋白同类固醇、赖氨酸、有机酸和ATP的生物合成有关。与截留分子量为10 kD的透析袋发酵相比,在截留分子量为3.5 kD的混菌发酵中,酒石酸含量升高5.1%、醋酸含量下降44.3%,说明通过限定菌体间代谢产物的沟通可以调整酒的滴定酸度和挥发酸度。     

高温α-淀粉酶基因突变体在大肠杆菌、毕赤酵母中的表达

对地衣芽孢杆菌(Bacillus licheniformis)高温α-淀粉酶(amyE)基因进行改造获得的基因突变体(amyEM),通过PCR扩增,将此基因分别克隆至大肠杆菌表达载体pBV220和毕赤酵母表达载体pPIC9K上,并分别转化大肠杆菌DH5α和毕赤酵母GS115感受态细胞,获得重组大肠杆菌和重组毕赤酵母。通过表达产物的酶活性检测和SDS-PAGE分析,证明突变α-淀粉酶(AmyEM)在大肠杆菌、毕赤酵母中获得有效表达。对重组大肠杆菌产生的α-淀粉酶的粗酶性质分析表明,此酶分子量约为55kDa。其最适反应温度为80℃~90℃,与野生型基因相比,其最适pH均为6.0,但不同的是突变体在pH 5.0~5.5时表现出较高的酶活力;在毕赤酵母细胞的表达产物可分泌至胞外。由于酵母可对蛋白进行糖基化,酶分子量增加到60kDa,最适pH也改变为5.5。此高温α-淀粉酶突变体所具有的在微酸性环境具有较高酶活力的性质,具有重要的潜在工业应用价值。     

乙酰氨基半乳糖转移酶14(GALNT14)在毕赤酵母中的表达纯化及活性鉴定

将GALNT14全长编码区克隆到分泌型酵母表达载体pPIC9K中,构建重组载体pPIC9K-T14,经电转至毕赤酵母GS115中表达,使用G418筛选高表达重组菌,并对诱导条件进行优化,表达产物使用SDS-PAGE分析、Western blot鉴定、Sephadex G-100纯化、最后经HPLC检测活性。结果显示,在提供更好的供氧量条件下,用0.75％甲醇诱导可提高目的蛋白的表达量而降低杂蛋白的表达。培养上清液经SDS-PAGE检测显示目的蛋白分子量约64 kDa;Western blot结果显示在相应分子量处有一条特异性条带;利用Sephadex G-100成功分离纯化了目的蛋白;活性测定结果显示所获得的目的蛋白具有催化活性,为深入研究GALNT14的结构与功能奠定了基础。     

猪β干扰素在毕赤酵母中的分泌表达及其对伪狂犬病毒的抑制作用

为了研制高活性的重组猪β干扰素,对PoIFN-β成熟蛋白第3、7和164位的3个氨基酸密码子进行毕赤酵母偏嗜性改造并构建了酵母表达载体pPICZαA-PIB。pPICZαA-PIB经SacⅠ酶切线性化后电转化导入毕赤酵母菌株X-33。多株PCR鉴定为阳性的酵母转化子经甲醇诱导发酵分泌表达了PoIFN-β,其中B1株酵母的PoIFN-β产量最高,约为2.5×105U/mL,其表达量约为60μg/mL,比活为4.17×106U/mg。将发酵上清液用PEG20000浓缩后进行SDS-PAGE和Western blot检测,结果表明表达产物是分子量约为28kDa和25kDa蛋白的混合物,两者均可与PoIFN-β阳性抗血清发生特异反应。表达产物比PoIFN-β理论推导分子量(约20.8kDa)大,推测可能是表达产物发生了不同程度的糖基化。重组PoIFN-β对伪狂犬病毒在细胞中增殖可呈现抑制作用,并且rPoIFN-β对伪狂犬病毒在MDBK细胞上早期增殖的抑制效果最为明显。     

甲醇/山梨醇共混流加控制溶氧改善毕赤酵母表达猪圆环病毒Cap蛋白的发酵性能

研究在重组毕赤酵母(GS115,Mut+)表达猪圆环病毒Cap蛋白的发酵过程中,甲醇毒害作用以及溶氧波动影响目的蛋白的正常表达。基于对甲醇和山梨醇代谢途径的分析,将C源流加的手动调节与反馈控制相结合,提出了1种新型的甲醇/山梨醇共混诱导策略,能够将溶氧稳定地控制于某一设定值,同时避免甲醇毒害作用。使用该策略将溶氧控制于20%的批次,C源(甲醇和山梨醇)添加过少,导致Cap蛋白表达量较低(54 mg/L);而将溶氧控制于10%的批次,C源流加速率适宜,Cap蛋白表达量达到198 mg/L,表达水平明显高于采用传统甲醇诱导策略(0 mg/L)和DO-stat诱导策略的批次(121 mg/L)。     

重组人kallistatin蛋白在毕赤酵母中的高效表达及生物活性分析

为了研究kallistatin(Kal)的生物活性,本实验构建了可分泌表达Kal的毕赤酵母菌株。首先通过PCR方法从pAAV-Kal中扩增出KalcDNA,并克隆至酵母表达载体pPIC9,得到甲醇酵母分泌型表达载体pPIC9-Kal,然后将载体线性化并电击转化毕赤酵母GS115(his4),通过MD平板筛选出阳性表达菌株。阳性表达菌株在BMMY培养基(pH7.0)中29℃培养,经2%甲醇诱导表达96h,摇瓶表达量可达14mg/L。表达上清经PhenylSuperose、Heparin SepharoseFF分离纯化,目的蛋白纯度达到98%,分子量为58kDa。生物活性实验显示,所得到的Kal蛋白具有较好的抗氧化活性,过氧化物酶活性达到(163±4)U/(mg·min),可有效降低H2O2对LX-2细胞的氧化损伤。另外,重组产生的Kal还能抑制HUVEC细胞的增殖。本研究首次成功地利用毕赤酵母表达系统分泌表达了有生物活性的Kal,为继续开展其抗肿瘤活性奠定了基础。     

人微小纤溶酶原基因的克隆和表达

用PCR方法扩增人微小纤溶酶原(Microplasmingen,mPlg)基因,再与表达载体重组．构造mPlg原核表达质粒并转化大肠杆菌。阳性克隆pSSE-mPlg经温度诱导表达,SDS-PAGE等方法证明表达产物的分子量约为29kDa。占全菌总蛋白的24％左右,并在菌内形成包涵体。经半胱氨酸再氧化法和空气氧化法复性。表达产物r-mPlg经SK作用后显示纤溶活性。同时对蛋白质浓度、复性时间等因素对复性的影响进行了初步探讨。     

产HSA—CP融合蛋白毕赤酵母的发酵条件优化

为提高重组毕赤酵母生产人血清白蛋白-C肽融合蛋白（HSA—CP）的产量和生产强度,在摇瓶条件下考察了甲醇诱导时间和浓度对目的蛋白产量的影响。结果表明,质量浓度10g/L的甲醇诱导72h最适于产物表达。通过对7L发酵罐中各因素的优化,得到最佳条件为：初始甘油质量浓度10g/L,30℃培养,菌体生长期和诱导期的pH及溶氧分别控制在pH5．0、30％溶解O2或pH6．0、15％的溶解O2。10g/L的甲醇诱导72h,最终使干细胞质量浓度达到56．43g/L,目的蛋白产量达368．45mg／L。生产强度为3．920mg/（L·h）,目标蛋白的比生产速率为5．12mg/（L·h）。     

人肺表面活性相关蛋白Al在酿酒酵母中表达、纯化及活性分析

将编码正常人肺表面活性物质相关蛋白A1基因的cDNA克隆至酿酒酵母的分泌表达载体pVT102U/α中,构建了重组质粒pVT102U/α-SP-A1,转化酵母宿主菌S-78,通过改变培养基的pH值水平,经摇瓶培养,SDS-PAGE结果显示,培养上清中SP-A1表达量达400mg/L以上,表达产物分子量为62kD和32kD.分别以二聚体和单体形式出现.ELISA和Western blot实验表明表达产物能被抗体特异性识别.生物学活性检测证实其具有调理肺巨噬细胞吞噬E.coli的功能.     

玉米赤霉烯酮降解酶毕赤酵母表达载体的构建及其表达

目的构建毕赤酵母表达载体pPIC9-ZEN-jjm,筛选高效分泌表达活性目的蛋白的菌株。方法克隆ZEN-jjm基因,经EcoRⅠ和NotⅠ双酶切连接至pPIC9中,电转化至毕赤酵母GS115。利用RDB培养基和甲醇诱导表达进行筛选。HPLC检测表达蛋白降解玉米赤霉烯酮的活性。结果测序表明ZEN-jjm成功插入pPIC9中,SDS-PAGE表明获得1株高效表达目的蛋白的重组酵母,其分子量约29 kDa。HPLC表明其能有效地降解玉米赤霉烯酮。结论玉米赤霉烯酮降解酶在毕赤酵母中获得了高效分泌表达。     

1株抑制土传病原菌且产纤维素酶芽胞杆菌筛选及产酶条件的研究

通过刚果红染色法和DNS分光光度法对6种芽胞杆菌分泌胞外纤维素酶进行筛选,再通过管碟法测试对5种病原菌的抑菌作用,得到1株芽胞杆菌（菌株编号为X-02）酶活达182.5 U/mL,而且对几种土传病害有抑制作用。并对其产酶发酵培养基碳源、氮源及初始pH、发酵温度、接种量、摇瓶转速和时间进行优化,结果显示该菌株最佳碳源是2%CMC-Na,其次是葡萄糖,二者产酶之差只为21 U/mL。考虑大量生产的成本和方便性（CMC-Na溶解慢）,选择葡萄糖为碳源,氮源为2.0%蛋白胨与酵母膏复合氮源,在pH值为8.0、温度37℃、接种量为2%、转速为180 r/m in、时间48 h条件下酶活达到391.0 U/mL酶液,比优化前提高了2.1倍。     

青霉F10-2固态发酵植物农药残渣产纤维素酶

采用单因素试验观察了不同C、N源、植物提取残渣与麦麸比例、初始pH和水料比对青霉F10-2菌株产纤维素酶的影响;在此基础上根据Box-w ilson的中心组合试验设计原理,选取蛋白胨、初始pH和水料比等影响因素,采用三因素五水平的响应面分析方法,对瓦克青霉F10-2的固态产纤维素酶条件进行了优化。其优化后的产酶条件为m(川楝树皮残渣)∶m(麦麸)∶m(蛋白胨)∶m(KH2PO4)=80∶20∶1.4∶0.4、初始pH 6.2、水料比2∶1、26℃发酵8 d,在此条件下纤维素酶比酶活可达6.47 U/g,较原始培养条件提高了46.38%。     

Ethanol fermentation characteristics of Thermoanaerobacter ethanolicus

Thermoanaerobacter ethanolicus is an extreme thermophilic non-spore forming ethanol-producing anaerobic bacterium. Minimum nutrient requirements and optimum growth conditions have been established. An optimum yeast extract-glucose ratio for ethanol yield has also been determined. Initial medium pH, optimally 7.5–8.0, significantly affected the amount of ethanol formed. Maximum specific growth rate was found to be 0.22 h^?1at pH 7.5 and 69°C. Ethanol concentration up to 11 g l^?1at pH 7.5 and 69°C was used to characterize ethanol inhibition. The growth kinetics of T. ethanolicus were characterized in terms of environmental parameters. Substrate utilization, ethanol formation and inhibition by both sugar and ethanol were also quantified.     

灰树花发酵工艺及培养基研究

详细、系统地研究了碳源、氮源、无机盐、维生素以及种龄、接种量、摇床转速、摇瓶装液量和培养基 pH值等因素对灰树花液体深层发酵菌丝体产量的影响 ,结果表明 :玉米粉、葡萄糖为最佳碳源 ,豆饼粉为最佳氮源 ,KH2 PO4 ,MgSO4 以及少量VB1的添加均使菌丝体产量明显增加     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

Implication of <Emphasis Type="Italic">Bacillus</Emphasis> sp. in the production of pectinolytic enzymes during cocoa fermentation

The role of bacilli in cocoa fermentation is not well known. Their potential of production of pectinolytic enzymes during this process was evaluated. Bacillus growth was monitored and pectinolytic strains were screened for their use of pectin as sole carbon source. Effects of cocoa fermentation parameters susceptible to influence on enzyme production were analysed. Among 98 strains isolated, 90 were positive for pectin degradation and 80% of them presented detectable pectinolytic activities in submerged fermentation. Forty-eight strains produced polygalacturonase (PG), 47 yielded pectin lyase (PL) and 23 strains produced both enzymes. Bacilli growth was not significantly affected during fermentation. PL production was favoured by galactose, lactose, glucose as sugars, and arginine, glutamine, cysteine and ammonium sulphate as nitrogen compounds. Pectin at low concentration (0.05%) and iron stimulated PL production. It was strongly repressed by galacturonic acid (1%), and negatively affected by nitrogen starvation, zinc and temperatures above 45°C. PL yield was very weak below pH 4.0 and in anaerobic conditions. PG production was weakened by sucrose and cation depletion. It was increased slightly by cysteine, ammonium nitrate and nitrogen starvation and significantly above 40°C. PG synthesis was not affected by acidic pH (3.0–6.0) or oxygen availability. As fermentation products, lactate and acetate lowered the production of both enzymes while ethanol had no effect. The high proportion of pectinolytic producers among the strains studied and analysis of factors influencing pectinolytic enzymes production, suggest that Bacillus sp. is liable to produce at least one enzyme during cocoa fermentation.     

Fermentation of glycerol by Clostridium pasteurianum--batch and continuous culture studies

The fermentation of glycerol by Clostridium pasteurianum was studied with respect to product formation as influenced by the culture conditions. In the majority of batch cultures, butanol was the main fermentation product, but a varying fraction of glycerol was also converted to 1,3-propanediol, butyric and acetic acids and ethanol. More than 60 g/l glycerol was utilized, and up to 17 g/l butanol was produced. Fed-batch cultures did not offer an advantage. When molecular nitrogen was used as a nitrogen source, the fermentation time was prolonged by a factor of 1.5. Fermentations at constant pH values between 4.5 and 7.5 did not reveal significant differences in product formation except for an increase in the ethanol content starting at pH 6.5. Chemostat cultures also yielded predominantly n-butanol, but in some fermentations, the 1,3-propanediol fraction was relatively high. The pH auxostat cultures, which were operated at a glycerol excess, contained 1,3-propanediol as the main product. As a whole, the fermentations were characterized by a certain variability in product formation under seemingly equal or slightly varied conditions. It appears that the regulation of the numerous fermentation pathways occurring in this organism is not very strict. Journal of Industrial Microbiology & Biotechnology (2001) 27, 18–26. Received 25 September 2000/ Accepted in revised form 07 April 2001     

Optimization of process variables for minimization of byproduct formation during fermentation of blackstrap molasses to ethanol at industrial scale

Aims: To investigate the effect of molasses concentration, initial pH of molasses medium, and inoculum’s size to maximize ethanol and minimize methanol, fusel alcohols, acetic acid and aldehydes in the fermentation mash in industrial fermentors. Methods and Results: Initial studies to optimize temperature, nitrogen source, phosphorous source, sulfur supplement and minerals were performed. The essential nutrients were urea (2 kg in 60 m³), 0·5 l each of commercial phosphoric acid and sulfuric acid (for pH control) added at the inoculum preparation stage only. Yields of ethanol, methanol, fusel alcohols, total acids and aldehydes per 100‐l fermentation broth were monitored. Molasses at 29°Brix (degree of dissolved sugars in water), initial pH 4·5, inoculum size 30% (v/v) and anaerobic fermentation supported maximum ethanol (7·8%) with Y_P/S = 238 l ethanol per tonne molasses (96·5% yield) (8·2% increase in yield), and had significantly lower values of byproducts than those in control experiments. Conclusions: Optimization of process variables resulted in higher ethanol yield (8·2%) and reduced yield of methanol, fusel alcohols, acids and aldehydes. Significance and Impact of the Study: More than 5% substrate is converted into byproducts. Eliminating or reducing their formation can increase ethanol yield by Saccharomyces cerevisiae, decrease the overall cost of fermentation process and improve the quality of ethanol.     

Effect of L-amino acids on Mucor rouxii dimorphism.

Mucor rouxii organisms growing aerobically and exponentially on a well-defined minimal medium are able to differentiate as yeasts or as mycelia, depending on the amino acid as the nitrogen source. When certain amino acids were used as the nitrogen source, spores differentiated only as hyphae, whereas other amino acids gave rise to other morphological forms having different ratios of yeasts to hyphae. In both hyphal and yeast cultures, an aerobic metabolism was predominant, as shown by determining several metabolic parameters such as oxygen tension, glucose consumption, ethanol production, and CO2 release. A complete conversion of yeasts to hyphae was obtained by the appropriate change in the amino acid used as nitrogen source. By preparing spheroplasts from mycelial cultures and transferring them to media with amino acids that induce yeast formation, a 50% yield in the reverse transformation was achieved. A correlation between the change in pH of the medium and cell morphology was observed in different growth conditions. Decrease in the pH of the medium preceded the appearance of hyphae. Also, when the initial pH of the medium was increased, aspartate-containing cultures developed mainly as mycelia, instead of yeasts, with a corresponding decrease in the final pH.     

氮源种类及溶氧水平对锁掷酵母产类胡萝卜素组分的影响

在锁掷酵母（Sporidioboluspararoseus）发酵产类胡萝卜紊的过程中,发酵产物中类胡萝卜紊种类繁多,而且性质相似,加大了不同色素分离纯化的难度。为定向积累不同种类的类胡萝卜素,以本实验室保藏锁挪酵母JD-2为出发菌,研究了氮源种类和浓度及溶氧对锁掷酵母产类胡萝卜素的影响,并在7L发酵罐中进行了补料分批发酵试验。发现培养基中同时添加有机氮源和无机氮源且溶氧控制较低（5％）时有利于β-胡萝卜素的大量积累,最佳有机氮源和无机氮源分别为玉米浆（20g／L）、硫酸铵（5g／L）。补料分批发酵时β-胡萝卜素产量达到31．28mg／L,红酵母烯12．38mg／L。培养基中只添加有机氮源且相对溶氧控制相对较高（30％）时有利于红酵母烯的大量积累,最佳有机氮源为酵母膏（20g／L）。补料分批发酵时红酵母烯产量达到38．96mg／L,8．胡萝卜素12．36mg／L。