重组大肠杆菌高密度发酵研究进展

重组大肠杆菌的高密度发酵是提高基因工程产品产量的一个非常有铲的手段,是现代发酵工程研究的一个热点。本文就高密度发酵中影响重组大肠杆菌发酵产率的几个因素,包括宿主菌、培养基、培养条件、补料方法以及高密度发酵过程中存在的问题和对策加以讨论,着重探讨了高密度下大肠杆菌产生的有害代副产物－－乙酸的产生机制、抑制作用机理,以及控制乙酸机累的技术方法。     

重组大肠杆菌高密度发酵研究进展

重组大肠杆菌的高密度发酵是提高基因工程产品产量的一个非常有效的手段,是现代发酵工程研究的一个热点。本文就高密度发酵中影响重组大肠杆菌发酵产率的几个因素,包括宿主菌、培养基、培养条件、补料方法以及高密度发酵过程中存在的问题和对策加以讨论,着重探讨了高密度下大肠杆菌产生的有害代谢副产物———乙酸的产生机制、抑制作用机理,以及控制乙酸积累的技术方法 。     

重组大肠杆菌高密度培养

重组大肠杆菌的高密度培养是增加单位时间,体积重组蛋白产率的最有效途径之一。如何在获得高密度的同时取得较高的单位时间／体积目的蛋白产率,是高密度培养（过程中亟待解决的问题,这与所选用的菌体、构建的表达系统、发酵时pH、溶氧、培养基成分及培养温度、质粒稳定性、代谢副产物的限制及时比生长速率的控制等因素有关。试从这些方面加以综述,分析这些条件对重组蛋白生产的影响,介绍大肠杆菌高密度培养领域的一些研究进展。     

代谢工程与重组大肠杆菌的发酵

利用代谢工程可以在重组大肠杆菌的改良中减少代谢副产物乙酸的累积,优化代谢系统,利于重组蛋白质的高表达以及重组菌的高密度发酵。应用代谢工程改良重组大肠杆菌主要包括阻断乙酸产生的主要途径、限制糖酵解途径上的碳代谢流、将过量的丙酮酸转化为其它低毒的副产物以及对碳代谢流进行分流等几个方面的工作。     

重组大肠杆菌的分批补料培养方法

在重组大肠杆菌的培养过程中,存在着菌体的高浓度与外源蛋白的高表达这一矛盾,使得重组菌的比生长速率通常远远低于宿主菌,限制了基因工程菌由实验室规模向工业化规模的转变。要实现重组大肠杆菌的高密度培养,最常用和最有效的方法就是分批补料流加培养。     

重组大肠杆菌高表达高密度发酵研究

大肠杆菌高密度高表达发酵技术是现代发酵工程的重要研究课题,此项技术可以有效地提高大肠杆菌的产量和外源重组蛋白的表达量,该文就影响大肠杆菌高密度发酵的主要因素如宿主菌类型、培养基组成、培养条件、生长抑制物质、补料调控等进行了阐述和讨论。     

重组大肠杆菌高密度、高表达研究进展

高密度发酵因其节约、高效等诸多优点而成为近年来发酵工业重要的研究热点之一。要实现重组大肠杆菌高密度发酵,不仅要考虑工程菌自身的表达性能,还必须兼顾能促进基因工程菌生长和产物表达的最适培养条件,包括较佳的培养基组成、适宜的补料策略、培养温度、pH值、溶解氧等。该文就影响大肠杆菌高密度发酵的影响因子、工艺条件等进行综述,并探讨了大肠杆菌高密度发酵的工艺改进方向。     

重组大肠杆菌高密度培养研究进展

大肠杆菌是基因工程中常用的宿主菌,许多有价值的多肽和蛋白在大肠杆菌中已成功地进行了表达,表达水平有些高达细胞总蛋白的３０％以上,为了提高单位体积设备产物的产量,除了提高表达水平外,还需提高重组大肠杆菌的培养密度。大肠杆菌高密度培养的早期工作主要是以宿主菌为模型进行研究的,而近年来,重组大肠杆菌高密度高表达的研究已经有了较大进展。本文着重综述了培养基成分、溶氧、比生长速率和代谢副产物乙酸等因素对工程菌生长和表达的影响,及提高菌密度和表达水平的培养方法。     

重组大肠杆菌产普鲁兰酶的高密度发酵工艺研究

以表达普鲁兰酶的重组大肠杆菌作为出发菌株,在摇瓶培养的基础上,建立了大肠杆菌工程菌产普鲁兰酶的高密度发酵工艺。通过测定细胞密度、细胞干重、分离菌体可溶性成分与不溶性成分及SDS-PAGE电泳,分析重组大肠杆菌的生长和普鲁兰酶的表达情况。摇瓶试验使用合成培养基和LB培养基,重组大肠杆菌在合成培养基生长较慢,诱导5 h的普鲁兰酶表达量高于LB培养基,包涵体比例低于LB培养基。重组大肠杆菌的高密度发酵使用合成培养基,补料阶段采用指数流加的工艺,在设定细胞的比生长速率为0.12的前提下,限制补料中碳源的供应,以阻止乙酸的产生。当细胞密度OD600达到70.0开始诱导,最终细胞密度为每升53.3 g细胞干重,细胞内可溶性普鲁兰酶为每升1.35 g。     

重组大肠杆菌YK537/pSB┐TK高密度培养过程中有机酸的RP┐HPLC快速分析

采用高压液相色谱法（ＨＰＬＣ）,利用Ｃ１８反相柱快速检测重组大肠杆菌ＹＫ５３７／ｐＳＢ－ＴＫ高密度发酵过程中细菌代谢产生的各种有机酸。分析表明,经乙醚和水两次萃取处理后能去除样品中大部分的干扰峰,可获得理想的分离效果,并能定量测出发酵过程中各种有机酸的积累。不同培养方式的结果表明用甘油代替葡萄糖作为细菌生长的碳源可减少乙酸的积累,降低其对细菌生长和外源蛋白表达的抑制作用,从而更易实现重组大肠杆菌的高表达、高密度培养。     

High cell density cultivation of recombinant Escherichia coli for hirudin variant 1 production

A synthetic medium, TK-25, for high cell density cultivation (HCDC) of Escherichia coli K-12 was modified to support HCDC of strain JM109. By optimizing the culture conditions, the cell concentration of 65 g/l in 14 h was obtained in the optimized medium, namely TK-10, with glucose-fed batch cultivation. When these conditions were further applied for HCDC of E. coli JM109 harboring pUC-based recombinant plasmid which expresses a hirudin variant, HV-1-fused protein under the control of trp promoter, it grew to 24 g/l of dried cells expressed as an inclusion body as 15.9% of the total protein, corresponding to 1908 mg/l hirudin-fused protein.     

Comparison of the extracellular proteomes of Escherichia coli B and K-12 strains during high cell density cultivation

Escherichia coli BL21 (DE3) and W3110 strains, belonging to the family B and K-12, respectively, have been most widely employed for recombinant protein production. During the excretory production of recombinant proteins by high cell density cultivation (HCDC) of these strains, other native E. coli proteins were also released. Thus, we analyzed the extracellular proteomes of E. coli BL21 (DE3) and W3110 during HCDC. E. coli BL21 (DE3) released more than twice the amount of protein compared with W3110 during HCDC. A total of 204 protein spots including 83 nonredundant proteins were unambiguously identified by 2-DE and MS. Of these, 32 proteins were conserved in the two strains, while 20 and 33 strain-specific proteins were identified for E. coli BL21 (DE3) and W3110, respectively. More than 70% of identified proteins were found to be of periplasmic origin. The outer membrane proteins, OmpA and OmpF, were most abundant. Two strains showed much different patterns in their released proteins. Also, cell density-dependent variations in the released proteins were observed in both strains. These findings summarized as reference proteome maps will be useful for studying protein release in further detail, and provide new strategies for enhanced excretory production of recombinant proteins.     

High cell density culture of metabolically engineered Escherichia coli for the production of poly(3-hydroxybutyrate) in a defined medium

A recombinant Escherichia coli strain XL1-Blue harboring a stable high-copy-number plasmid pSYL107 containing the Alcaligenes eutrophus polyhydroxyalkanoate biosynthesis genes and the Escherichia coli ftsZ gene was employed for the production of poly(3-hydroxybutyrate) (PHB) by fed-batch culture in a defined medium. Suppression of filamentation by overexpressing the cell division protein FtsZ allowed production of PHB to a high concentration (77 g/L) with high productivity (2 g/L/h) in a defined medium, which was not possible with the recombinant E. coli that underwent filamentation. Further optimization of fed-batch culture condition resulted in PHB concentration of 104 g/L in a defined medium, which was the highest value reported to date by employing recombinant E. coli.     

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。     

Extracellular production of phospholipase A2 from Streptomyces violaceoruber by recombinant Escherichia coli

Phospholipase A(2) (PLA(2)) from Streptomyces violaceoruber was successfully produced extracellularly in an active form by using a recombinant strain of Escherichia coli. The PLA(2) gene, which was artificially synthesized with optimized codons for E. coli and fused with pelB signal sequence, was expressed in E. coli using pET system. Most of the enzyme activity was detected in the culture supernatant with negligible activity in the cells. The recombinant enzyme was purified to homogeneity from the culture supernatant simply by ammonium sulfate precipitation and an anion exchange chromatography. The purified enzyme showed a specific activity comparable to that of the authentic enzyme. The recombinant enzyme had the same N-terminal amino acid sequence to that of the mature protein, indicating the correct removal of the signal peptide. An inactive PLA(2) with a mutation at the catalytic center was also secreted to the culture medium, suggesting that the observed secretion was not dependent on enzymatic activity. A simple screening method for the PLA(2)-producing colonies was established by detecting clear zone formation around the colonies on agar media containing lecithin. This is the first example of direct extracellular production of active PLA(2) by recombinant E. coli.     

High-level expression of complementary DNA encoding rat calmodulin in Escherichia coli

We report the production and characterization of a rat calmodulin made in Escherichia coli. To express the rat calmodulin cDNA in E. coli, we have employed an expression vector containing the E. coli trp promoter and trpA terminator. The cDNA was modified so as to delete the 5' nontranslated sequence and to incorporate a consensus sequence for the E. coli ribosome-binding site. Several codons for the N-terminal amino acids were selected to fit the E. coli consensus nucleotide sequence around the translational initiation codon. After induction of expression in E. coli, rat calmodulin accounted for over 30% of total cellular proteins. About 100 mg of recombinant rat calmodulin, purified to over 90% homogeneity by extraction from bacterial lysate followed by phenyl-Sepharose column chromatography, was obtained from 1 liter of E. coli culture. This recombinant calmodulin activated rat brain cyclic AMP phosphodiesterase to the same extent as the native calmodulin purified from rat brain. These results indicate that the overproduction system of the recombinant calmodulin in E. coli facilitates the study of the structure-function relationship by site-specific mutagenesis.     

乳糖诱导木聚糖酶基因在大肠杆菌中的可溶性表达

以构建好的大肠杆菌工程菌BL21(DE3)/xylanase为研究对象,研究了以IPTG和乳糖作为诱导剂时重组蛋白的表达规律。在摇瓶发酵条件下研究了诱导剂浓度、诱导时机、诱导培养时间和诱导培养温度对目标蛋白表达的影响。实验结果表明,乳糖作为诱导剂时,重组菌产酶活力33.9 U/mg略高于IPTG作为诱导剂时重组菌产酶活力28.10 U/mg,这为乳糖作为诱导剂应用于重组大肠杆菌生产木聚糖酶提供了参考依据。     

Preparation of recombinant glycoprotease of Pasteurella haemolytica A1 utilizing the Escherichia coliα-hemolysin secretion system

Abstract Three murine monoclonal antibodies were prepared against the recombinant glycoprotease of Pasteurella haemolytica A1 expressed in Escherichia coli . These monoclonal antibodies were able to recognize the authentic glycoprotease from P. haemolytica A1 culture supernatant. A recombinant plasmid which contained most of the glycoprotease gene of P. haemolytica A1 fused with the secretion signal sequence from hlyA of the E. coli α-hemolysin determinant was constructed. This recombinant plasmid expressed a fusion protein (Gcp-F) which was secreted into the culture supernantant by E. coli cells when the α-hemolysin secretion functions HlyB and HlyD are supplied in trans. Gcp-F could be readily recovered from the supernatant free from other cellular materials and is suitable for use in vaccine trials and challenge experiments in animals.     

Participation of beta-carotene in antioxidant defense of bacterial cells

The effect of recombinant beta-carotene on the resistance of E. coli culture to menadione and paraquat was studied. The presence of beta-carotene in the E. coli cell significantly prevented an increase in the activity of superoxide dismutase induced by redox mediators but had no effect on the culture growth. The findings suggested the involvement of beta-carotene in the cell defense against oxidative stress.