重组巴氏毕赤酵母高密度发酵表达rHSA

对基因工程菌Pichiapastoris的摇瓶发酵条件进行了试验 ,并根据摇瓶发酵的优化结果进行了补料分批高密度发酵。在摇瓶发酵时 ,甲醇诱导基因工程菌P .pastoris表达重组人血清白蛋白的发酵周期为 96h ;甲醇的最佳诱导浓度为 1 0g L ;发酵pH范围为 5 72～ 6 5 9;在摇瓶培养时 ,随着接种量的增加 ,虽然目的蛋白表达量缓慢增加 ,但单位细胞光密度的蛋白产率却明显下降 ,符合y =1 2 941x- 0 50 59方程 (线性相关系数r=0 9789) ,其限制性因子很可能为溶氧。在分批发酵 ,接种量为 1 0 %且种子细胞光密度 (OD60 0 )为 2 0左右时 ,细胞生长的延迟期为 2 1 1h左右 ,细胞生长光密度与培养时间的关系模型为 :y =0 7841e0 .2 3 19t(线性相关系数r=0 .993 6 ) ;在补料发酵时细胞干重浓度可达到 1 1 5g L— 1 6 0g L ,在 1 2 0h重组人血清白蛋白表达量最大达到 3 6g L。     

两次诱导实现重组大肠杆菌高密度、高表达研究

通过不同温度诱导模式对大肠杆菌高密度,高表达的研究,确定两次升温诱导模式实现大肠杆菌高密度、高表达重组人载脂蛋白的目的。实验证实两次诱导成功的避免了乙酸对高密度、高表达的影响,最终发酵的细胞密度OD600达150,蛋白表达量4.8g·L-1,证明两次升温诱导的发酵方法在高密度、高表达外源蛋白上是成功的,从而为基因工程菌规模化生产奠定了基础。     

两次诱导实现重组大肠杆菌高密度、高表达研究*

通过不同温度诱导模式对大肠杆菌高密度,高表达的研究,确定两次升温诱导模式实现大肠杆菌高密度、高表达重组人载脂蛋白的目的。实验证实两次诱导成功的避免了乙酸对高密度、高表达的影响,最终发酵的细胞密度OD₆₀₀达150,蛋白表达量4.8g·L^-1,证明两次升温诱导的发酵方法在高密度、高表达外源蛋白上是成功的,从而为基因工程菌规模化生产奠定了基础。     

乳糖诱导的重组人血管内皮抑素(rhEndostatin)蛋白的表达

研究用乳糖替代IPTG作为诱导剂进行重组蛋白的表达,观察乳糖对乳糖操纵子调控的基因工程菌发酵及重组血管内皮抑素表达的影响,从而选取最佳诱导表达条件。以重组人血管内皮抑素表达工程菌pETrhEN/BL21(DE3)作为研究对象,分别用IPTG和乳糖作为诱导剂,在摇瓶中进行表达实验。并对重组蛋白质表达量进行分析。然后在5 L发酵罐中进行验证。在摇瓶培养条件下,乳糖浓度大于0.5 g/L即可以诱导目的蛋白的表达。乳糖浓度1 g/L时诱导目的蛋白表达量与1 mmol/L的IPTG相当,当乳糖浓度为10 g/L,目的蛋白表达量达到最大。在发酵罐培养条件下,补料4 h后葡萄糖浓度基本耗尽,此时开始加入乳糖。诱导后1 h,即有重组蛋白表达,在诱导后4 h达到高峰(占菌体可溶性蛋白的56%),与此同时,诱导后5 h菌体浓度也达到最高值。在以乳糖操纵子为调控手段的工程菌表达系统中,可以使用乳糖作为诱导剂,诱导应在葡萄糖消耗完后进行。     

重组尿酸氧化酶发酵工艺优化

目的:优化并获得重组尿酸氧化酶(rUOX)基因工程大肠杆菌BL21(DE3)/pET-32a-uox高密度发酵的工艺参数。方法:在三角摇瓶中进行培养条件的优化实验,分别考察了pH值、接种量、无机盐、碳源、诱导强度等对工程菌生长和重组蛋白表达的影响,得到了优化的发酵条件;在此基础上放大至NBS BIOFLO 110 14 L发酵罐,通过对诱导时机的优化,利用分批补料发酵的方式,使rUOX在高密度培养的条件下得到高表达。结果:在优化的发酵条件下,菌体密度(D600nm)最终达到50以上,相当于20 g/L干重;可溶性rUOX占菌体总蛋白量的45%,其含量达到3.45 g/L。结论:为规模化制备重组黄曲霉尿酸氧化酶奠定了基础。     

高密度发酵重组大肠杆菌产海藻糖合成酶

酶法催化是目前生产海藻糖的主要手段。本文中,笔者通过高密度发酵重组大肠杆菌产海藻糖合成酶,进而以麦芽糖为底物,催化生产海藻糖。首先根据大肠杆菌高密度发酵条件要求,在揺瓶中对基因工程菌进行了培养基、发酵条件和诱导条件的逐一优化;然后在5 L和50 L发酵罐中进行批次补料发酵的放大实验;最后采用变指数-恒pH法的策略发酵重组大肠杆菌,结果OD_(600)达到97,海藻糖合成酶酶活达到(24 000±350) U/mL,实现了海藻糖合成酶的重组大肠杆菌高密度发酵生产,极大提高了海藻糖的生产效率。     

乳糖作为诱导剂对重组目的蛋白表达的影响

将重组粒细胞-巨噬细胞集落刺激因子/白细胞介素3(GM-CSF/IL-3)融合蛋白表达菌BL21(DE3)(pFu)作为研究对象,对于以乳糖作为诱导剂时重组目的产物的诱导表达规律进行了深入的研究。分析比较了不同培养基中,不同生长阶段进行诱导对于产物表达的影响。对诱导所需的乳糖浓度、诱导持续时间长短等因素亦进行了研究。实验结果表明,在对诱导条件进行优化控制的前提下,利用乳糖作为诱导剂可以达到与IPTG类似的诱导效果。随后的研究中,将乳糖作为诱导剂应用于高密度发酵过程。这些研究结果为乳糖作为诱导剂最终应用于重组基因工程药物的工业化生产提供了有益的参考和借鉴。     

基因工程菌高密度发酵工艺研究进展

阐述了基因工程菌高密度发酵工艺的几个主要影响因素,包括重组菌构建、培养条件、生长抑制因子以及它们的控制技术。通过高密度发酵可以提高细胞生长密度、目的蛋白的表达含量。在高密度发酵过程中,会产生一些有害抑制代谢副产物,但通过分批补料可以降低影响。     

重组戊型肝炎病毒衣壳蛋白工程菌的高密度培养

在10L发酵罐中对戊型肝炎病毒衣壳蛋白在重组大肠杆菌中表达发酵工艺进行了研究,用分批培养方法探讨了不同培养基、培养基中磷酸盐浓度和Mg^2＋浓度等因素对菌体生长与重组蛋白表达的影响;用分批补料培养研究了不同的补料工艺对菌体生长与重组蛋白表达的影响,同时对重组菌诱导时期、诱导持续时间以及不同诱导温度表达包含体在尿素溶液中的溶解性进行了研究。结果表明,在优化后的培养基中,磷酸盐浓度、Mg^2＋浓度分别为80mmol/L 与20mmol/L时菌体生长与表达效果较好;分批补料培养中,37℃培养9h菌体达到对数期中期(约45OD600)为适宜诱导时期,加入终浓度为10mmol/L IPTG后诱导5h,OD600达到80以上,重组蛋白表达量达到29.74％,为最适收获菌体时间;37℃表达的包含体80％以上溶解在4mol/L的尿素溶液中,最终浓度达到14mg/mL; 10L发酵罐中确定的发酵工艺参数在30L发酵罐中进行了放大培养,10L发酵罐中确定的发酵工艺参数在30L发酵罐上具有可放大性与重复性, 可以应用于工业生产。     

基因工程菌Pichia pastoris高密度培养条件研究

基因工程菌pichiapastoris最佳种子培养基为添加4mL/LPTMl的BMGY培养基;全合成高密度摇瓶培养基是甘油4%,(NH4)2SO410g/L,CaSO40.93g/L,K2SO418.2g/L,MgSO4@7H2O14.9g/L,0.1mol/L磷酸缓冲液(pH=6.0)配制,培养26h后细胞密度OD600可达到65。经SDS-PAGE电泳图谱分析,甲醇诱导培养72h结果12h有重组人血清白蛋白表达,24h达到最大。此全合成摇瓶培养基与批补料发酵培养基相类似,有利于指导发酵罐上发酵培养。     

High-cell-density fermentation of recombinant Saccharomyces cerevisiae using glycerol

To obtain a high cell density of recombinant Saccharomyces cerevisiae (INVSc 1 strain bearing a 2 microm plasmid, pYES2 containing a GAL1 promoter for expression of the beta-galactosidase gene), the yeast was grown with glycerol as the substrate by fed-batch fermentation. The feeding strategy was based on an on-line response of the medium pH to the consumption of glycerol. The approach was to feed excess carbon into the medium to create a benign environment for rapid biomass buildup. During cell growth in the presence of glycerol, the release of protons in the medium caused a decrease in pH and the consumption rate of ammonium phosphate served as an on-line indicator for the metabolic rate of the organism. The extent of glycerol feeding in a fed-batch mode with pH control at 5.0 +/- 0.1 was ascertained from the automatic addition of ammonium phosphate to the medium. The glycerol feeding to ammonium phosphate addition ratio was found to be 2.5-3.0. On the basis of the experiments, a maximum dry cell biomass of 140 g per liter and a productivity of 5.5 g DCW/L/h were achieved. The high cell density of S. cerevisiae obtained with good plasmid stability suggested a simple and efficient fermentation protocol for recombinant protein production.     

Production of poly(3-hydroxybutyrate) by high cell density fed-batch culture of Alcaligenes eutrophus with phospate limitation

High cell density fed-batch fermentation of Alcaligenes eutrophus was carried out for the production of poly(3-hydroxybutyrate) (PHB) in a 60-L fermentor. During the fermentation, pH was controlled with NH(4)OH solution and PHB accumulation was induced by phosphate limitation instead of nitrogen limitation. The glucose feeding was controlled by monitoring dissolved oxygen (DO) concentration and glucose concentration in the culture broth. The glucose concentration fluctuated within the range of 0-20 g/L. We have investigated the effect of initial phosphate concentration on the PHB production when the initial volume was fixed. Using an initial phosphate concentration of 5.5 g/L, the fed-batch fermentation resulted in a final cell concentration of 281 g/L, a PHB concentration of 232 g/L, and a PHB productivity of 3.14 g/L . h, which are the highest values ever reported to date. In this case, PHB content, cell yield from glucose, and PHB yield from glucose were 80, 0.46, and 0.38% (w/w), respectively. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 28-32, 1997.     

过表达carAB和pyrBI对大肠杆菌发酵胞苷的影响

为了考察氨甲酰磷酸合成酶和天冬氨酸氨甲酰转移酶对大肠杆菌发酵生产胞苷的影响,以E. coli A39 (△cdd)基因组为模板克隆carAB和pyrBI并与载体pSTV28连接构建出重组质粒pSTV28-carAB和pSTV28-pyrBI,将这两个重组质粒分别转入出发菌株A39 (△cdd)后,通过摇瓶发酵研究重组质粒对菌体的生长、胞苷和尿苷产量及副产物乙酸积累的影响。结果显示,工程菌E. coli A39-AB和A39-BI的胞苷产量分别为583.5 mg/L、408.4 mg/L,与出发菌株相比,分别提高了85.3%、29.7%。这说明过表达操纵子基因carAB和pyrBI均可促进胞苷的积累。     

Extractive lactic acid fermentation in poly (ethyleneimine)-based aqueous two-phase system

The potential of an aqueous two-phase system composed of a polycation, poly(ethyleneimine) (PEI), and an uncharged polymer, (hydroxyethyl) cellulose (HEC), for extractive lactic acid fermentation was tested. Batch fermentation with 20 g/L glucose in two-phase medium using Lactococcus lactis without external pH control resulted in 3-4 times higher amount of lactate and biomass produced as compared to that in a conventional one-phase medium. Lactic acid was preferentially partitioned to the PEI-rich bottom phase. However, the cells which favored the HEC-rich top phase in a fresh two-phase medium were partitioned to a significant extent to the bottom phase after fermentation. Addition of phosphate buffer or pH adjustment to 6.5 after fermentation caused fewer cells to move to the bottom phase. With external pH control, fermentation in normal and two-phase medium showed no marked differences in glucose consumption and lactic acid yield, except that about 1.3 times higher cell density was obtained in the two-phase broth, especially at initial glucose concentrations of 50-100 g/L. Use of higher concentration of phosphate during batch fermentation in the two-phase medium with 50 g/L sugar provided a 15% higher yield of lactic acid, but the growth rate of cells was nearly half of the normal, thus affecting the productivity. Continuous fermentation with twice the normal phosphate concentration resulted in higher cell density, product yield, and productivity in two-phase medium than in monophasic medium. (c) 1996 John Wiley & Sons, Inc.     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

重组毕赤酵母高密度发酵表达H5N1禽流感病毒糖蛋白

在10L发酵罐中,对高致病性禽流感病毒H5N1糖蛋白HA1在重组毕赤酵母中的表达发酵工艺进行了研究。通过分批补料培养方法探讨不同培养温度、诱导温度、补料方式、微量元素等因素对菌体的生长以及重组蛋白表达和活性的影响。结果表明,菌种培养和诱导温度均为25oC时,菌体的生长、分泌表达量和与广谱中和抗体的反应活性较好;微量元素是影响重组HA1蛋白生物活性的重要因素;通过优化高密度发酵工艺,H5N1病毒糖蛋白HA1在发酵罐中的表达量比摇瓶培养提高10.5倍,达到约120mg/L,为大规模制备高致病性禽流感病毒的HA1蛋白奠定了基础。     

过量表达自身hemA基因的重组大肠杆菌发酵生产5-氨基乙酰丙酸的研究

研究了优化重组大肠杆菌产5-氨基乙酰丙酸（ALA）的条件,提高大肠杆菌发酵生产AL气的产量。在测定重组大肠杆菌GT48的生长曲线的基础上,确定诱导时间,优化摇瓶发酵条件。然后,进一步在5L发酵罐上进行间歇和流加发酵研究。摇瓶实验表明,细胞培养最佳初始pH为6．5,最佳诱导时间为稳定期前期,最佳接种量为2％,过高的葡萄糖浓度对细胞生长和产物合成均有一定的抑制作用。在5L发酵罐间歇发酵中,重组菌产ALA能力达到47．8mg／L。采用流加发酵可以进一步将产物产量提高到63．8mg／L。构建的过量表达自身的hemA基因的大肠杆菌具有较高的产ALA能力,通过发酵条件优化和采用流加发酵可以提高AL气产量。     

Medium optimization for the production of recombinant nattokinase by Bacillus subtilis using response surface methodology

Nattokinase is a potent fibrinolytic enzyme with the potential for fighting cardiovascular diseases. Most recently, a new Bacillus subtilis/Escherichia coli (B. subtilis/E. coli) shuttle vector has been developed to achieve stable production of recombinant nattokinase in B. subtilis (Chen; et al. 2007, 23, 808-813). With this developed B. subtilis strain, the design of an optimum but cost-effective medium for high-level production of recombinant nattokinase was attempted by using response surface methodology. On the basis of the Plackett-Burman design, three critical medium components were selected. Subsequently, the optimum combination of selected factors was investigated by the Box-Behnken design. As a result, it gave the predicted maximum production of recombinant nattokinase with 71 500 CU/mL for shake-flask cultures when the concentrations of soybean hydrolysate, potassium phosphate, and calcium chloride in medium were at 6.100, 0.415, and 0.015%, respectively. This was further verified by a duplicated experiment. Moreover, the production scheme based on the optimum medium was scaled up in a fermenter. The batch fermentation of 3 L was carried out by controlling the condition at 37 degrees C and dissolved oxygen reaching 20% of air saturation level while the fermentation pH was initially set at 8.5. Without the need for controlling the broth pH, recombinant nattokinase production with a yield of 77 400 CU/mL (corresponding to 560 mg/L) could be obtained in the culture broth within 24 h. In particular, the recombinant B. subtilis strain was found fully stable at the end of fermentation when grown on the optimum medium. Overall, it indicates the success of this experimental design approach in formulating a simple and cost-effective medium, which provides the developed strain with sufficient nutrient supplements for stable and high-level production of recombinant nattokinase in a fermenter.