Characterization of up-regulated proteases in an industrial recombinant Escherichia coli fermentation

Proteolytic degradation of recombinant proteins is an industry-wide challenge in host organisms such as Escherichia coli. These proteases have been linked to stresses, such as the stringent and heat-shock responses. This study reports the dramatic up-regulation of protease activity in an industrial recombinant E. coli fermentation upon induction. The objective of this project was to detect and characterize up-regulated proteases due to recombinant AXOKINE overexpression upon IPTG induction. AXOKINE is a 22-kDa protein currently in clinical trials as a therapeutic for obesity associated with diabetes. AXOKINE was expressed in both the soluble and inclusion body fractions in E. coli. Sodium dodecyl sulfate gelatin-polyacrylamide gel electrophoresis (SDS-GPAGE) was used to analyze the up-regulated protease activity. Western blot analysis showed degraded AXOKINE in both the soluble and insoluble fractions. Protease inhibitors were used to characterize the proteases. The proteases were ethylenediaminetetraacetic acid (EDTA) sensitive. The protease activity increased in the presence of phenyl-methyl sulfonyl-fluoride (PMSF), a serine protease inhibitor. The incubation buffer composition was varied with respect to Mg2+ and ATP, and the protease activity was ATP independent and Mg2+ dependent. A two-dimensional electrophoresis technique was used to estimate the pI of the proteases to be between 2.9 and 4.0.     

Production of poly(4-hydroxybutyric acid) by fed-batch cultures of recombinant strains of Escherichia coli

A recombinant strain of Escherichia coli was used to produce poly(4-hydroxybutyric acid), P(4HB), homopolyester by fed-batch culture in M9 mineral salts medium containing glucose and 4-hydroxybutyric acid as carbon sources. The final cell dry weight, P(4HB) concentration and P(4HB) content were 12.6 g/l, 4.4 g/l, and 36% of cell dry weight, respectively, in a 27-l stirred and aerated fermenter after 60 h of fed-batch fermentation at constant pH.     

重组大肠杆菌合成左旋多巴条件的优化

通过对合成体系各组分对产物形成的影响的研究。分别求得了底物邻苯二酚,丙酮酸及乙酸氨的表观米氏常数,表观底物抑制常数和最适底物浓度,并得出合成左旋多巴的最适反应体系为：1%丙酮酸,1.2%邻苯二酚,2%乙酸铵,0.1?TA,0.2%亚硫酸钠,用氨水调pH至8.0。加入从与合成体系等体积培养液中收获的重组大肠杆菌细胞,于15℃反应16h,L-DOPA的产量为15.36g/L。     

Preparation of recombinant six-histidine-tagged human LECT2, a chemotactic protein to neutrophils, in Escherichia coli

LECT2 is a chemotactic protein to neutrophils. A recombinant six-histidine-tagged human LECT2, (His)₆-LECT2, was expressed in E. coli using a pET21a(+) vector. The (His)₆-LECT2 was purified from the soluble fraction in E. coli as a single band in sodium dodesyl sulfate/polyacrylamide gel electrophoresis using three steps of column chromatography with Ni²⁺-charged nitrilo-triacetic acid (Ni-NTA) agarose, DEAE-Sepharose, and CM-Sepharose. The purified (His)₆-LECT2 was yielded with 96 μg from the soluble fraction of 1,500 ml culture of E. coli. The circular dichroism spectrum of (His)₆-LECT2 showed the folded structure, which is rich in β-sheet structure and rare in α-helix. This revised version was published online in June 2006 with corrections to the Cover Date.     

A single-cell assay of beta-galactosidase in recombinant Escherichia coli using flow cytometry

A flow cytometric method was developed for the assay of beta-galactosidase in single Escherichia coli cells. A new fluorogenic substrate for beta-galactosidase, C(12)FDG, contains a lipophilic group that allows the substrate to penetrate through cell membranes under normal conditions. When the substrate is hydrolyzed by intracellular beta-galactosidase, a green fluorescent product is formed and retained inside the cell. Consequently, the stained beta-galactosidase-positive cells exhibit fluorescence, which is detected by flow cytometry. This new assay was used to analyze the segregational instability caused by a reduction in specific growth rate of the plasmid-bearing cells in the T7 expression system. Induction results in a substantial accumulation of intracellular beta-galactosidase along with a rapid increase in the fraction of plasmid-free cells. Once the cells lose the plasmid, they no longer produce beta-galactosidase, which is reduced by at least half every generation; thus, after staining, the fluorescent, plasmid-bearing cells can be distinguished from the nonfluorescent, plasmid-free cells using flow cytometry. This article describes the feasibility of the flow cytometric assay for single E. coli cells and reports the optimal assay conditions. A direct relationship between beta-galactosidase activity and green fluorescence intensity was found, and the fractions of recombinant cells in batch cultures were analyzed after various levels of induction.     

Predictive tool for recombinant protein production in Escherichia coli shake-flask cultures using an on-line monitoring system

As Escherichia coli (E. coli) is well defined with respect to its genome and metabolism, it is a favored host organism for recombinant protein production. However, many processes for recombinant protein production run under suboptimal conditions caused by wrong or incomplete information from an improper screening procedure, because appropriate on-line monitoring systems are still lacking. In this study, the oxygen transfer rate (OTR), determined on-line in shake flasks by applying a respiration activity monitoring system (RAMOS) device, was used to characterize the metabolic state of the recombinant organisms. Sixteen clones of E. coli SCS1 with foreign gene sequences, encoding for different target proteins, were cultivated in an autoinduction medium, containing glucose, lactose, and glycerol, to identify relationships between respiration activity and target protein production. All 16 clones showed a remarkably different respiration activity, biomass, and protein formation under induced conditions. However, the clones could be classified into three distinct types, and correlations could be made between OTR patterns and target protein production. For two of the three types, a decrease of the target protein was observed, after the optimal harvest time had passed. The acquired knowledge was used to modify the autoinduction medium to increase the product yield. Additional 1.5 g/L glucose accelerated the production process for one clone, shifting the time point of the maximal product yield from 24 to 17 h. For another clone, lactose addition led to higher volumetric product yields, in fact 25 and 38% more recombinant protein for 2 and 6 g/L additional lactose, respectively.     

大肠杆菌高效表达重组蛋白策略

大肠杆菌表达系统是基因表达技术中发展最早和目前应用最广的经典表达系统。利用该系统表达重组蛋白具有许多优越性,但其表达效率受诸多因素的影响。本文综述国内外利用大肠杆菌表达系统高效表达外源蛋白的策略,主要包括选择合适的启动子、改变信号肽结构、提高mRNA稳定性、提高翻译效率、表达稀有密码子、降低包涵体形成及蛋白降解,利用融合蛋白与分子伴侣、调控发酵条件实现高密度培养等。     

Fed-batch operation of recombinant Escherichia coli containing trp promoter with controlled specific growth rate

A feb-batch operation for the production of bovine somatotropin (bST) under the control of tryptophan promoter in Escherichia coli was investigated. The plasmid used contains a two-cistron system and altered codon usage for higher expression of bST. Specific growth rate is an important parameter in the fermentation, because it affects the production of growth-inhibitory organic acids and the expression of recombinant protein. The feeding rate was adjusted to keep the specific growth rate constant in this study. The variable growth yield expressed as a function of time was used for the calculation of the feeding rate. The growth yield decreases during the fermentation as product expression is induced. The specific growth rate was well controlled; however, intracellular bST concentration decreased at high cell concentrations. This is considered to be due to degradation by proteases. The decrease was prevented by an exponential feeding of the yeast extract as an organic nitrogen source. (c) 1994 John Wiley & Sons, Inc.     

响应面分析法优化重组大肠杆菌生物合成谷胱甘肽的条件

通过响应面分析法和典型性分析得出重组大肠杆菌酶法合成谷胱甘肽的最优条件:菌体量249 mg/mL,磷酸钾缓冲液145 mmol/L,MgCl243 mmol/L和ATP 34 mmol/L,预测谷胱甘肽最大量为16.50 mmol/L。验证性实验证明在优化条件下,重组大肠杆菌酶法合成谷胱甘肽达16.42 mmol/L。响应面分析还表明,在重组大肠杆菌酶法合成谷胱甘肽各因素中,MgCl2和ATP,以及菌体量与磷酸钾缓冲液之间的交互作用较显著。     

重组大肠杆菌右旋糖酐蔗糖酶的纯化及其性质

[目的]研究工程菌E.coli BL21(DE3)/pET28-dexYG产右旋糖酐蔗糖酶的纯化和酶学性质.[方法]工程菌经过IPTG诱导后生产含His-tag融合蛋白的右旋糖酐蔗糖酶,通过硫酸铵沉淀、Ni-NTA亲和层析纯化,得到纯度较高的酶蛋白,并对纯酶进行了酶学性质及动力学研究.[结果]经过SDS-PAGE测得该酶的分子量约为170 kDa,与理论推测值基本相同.以蔗糖为底物,酶促反应的最适温度为25～30℃,最适pH值为5.4,动力学常数Km值为10.43 mmol/L;酶活在pH 5.0～8.0较为稳定,在室温(25 ℃)保藏4天仍有59%的酶活力,4℃保存7周酶活力仅下降一半,但在35℃以上失活很快;Ca2 对催化作用有较大的促进,Mg2 有微弱的促进作用,K 对催化反应无影响,Cu2 的抑制作用最强.其他试剂对重组酶的活性有不同程度的影响,其中SDS抑制作用很强.[结论]研究为重组右旋糖酐蔗糖酶纯酶的获取、得到稳定性好、活性高的酶反应体系及利用该酶进行催化反应和工业化应用提供了重要参数.     

重组大肠杆菌的高密度发酵和甘油生产条件的初步研究

在摇瓶中进行重组大肠杆菌菌株BL21高密度发酵条件的研究,考察了葡萄糖浓度、盐离子浓度、温度、接种量、发酵时间等对该菌株生产甘油的影响。初步确定底物浓度为2.5%,盐离子浓度0.2%,温度为37℃,接种量为2%,经24h的摇瓶发酵,甘油产量最高达6.8g/L。在30L发酵罐实验中、按初步确定的优化条件发酵26h,甘油产量可达46.67g/L,是LB/葡萄糖培养基中甘油产量的2.06倍。     

EDTA induced autolysis in Escherichia coli and isolation of resistant mutants

Abstract Autolysis of Escherichia coli induced by a shock treatment with 10⁻³M EDTA, pH 6.5 was investigated. Mutants presenting reduced rates of EDTA-induced autolysis were isolated. A remarkable feature of these mutants was their tolerance to penicillin G, cephaloridine and moenomycin. Furthermore, a reduced level of peptidoglycan endopeptidase or N -acetylmuramidase activity was observed. Penicillin-binding protein patterns were unaltered.     

温度调控大肠杆菌发酵合成L-丙氨酸

正L-丙氨酸是最小的手性分子之一,被用于医药和兽药行业,与其他L-型氨基酸共同用作手术前和手术后的营养剂[1]。由于L-丙氨酸具有甜味,也被用于食品添加剂[2]。目前,L-丙氨酸全球需求年增长率为20%,主要增长地区是亚洲、北美等。然而,L-丙氨酸产量和价格基本被日本垄断和控制。国内企业生产规模小,生产菌种陈旧低效,L-丙氨酸的供应量远低于市场需求量。     

大肠杆菌严谨型RNA聚合酶的筛选及体内转录活性测定

利用选择性培养基筛选大肠杆菌自然突变菌株,经噬菌体P1转导和蛋白质互补试验,发现一株突变体(LCH001)的突变基因发生在编码RNA聚合酶β′亚基的rpoC基因上,经DNA序列分析,发现突变位点发生在第3406个碱基上,由G变成了T,导致编码的氨基酸由甘氨酸(GGT)变成半胱氨酸(TGT)。体内转录试验表明该突变RNA聚合酶转录严谨型启动子控制基因的活性显著降低,其β-半乳糖苷酶的活性是野生型菌株的18%,而转录非严谨型启动子控制基因的活性显著提高,其β-半乳糖苷酶的活性约是野生型菌株的5倍。研究结果对探讨RNA聚合酶结构与功能的关系以及RNA聚合酶在细菌严谨反应过程中的作用具有重要意义。     

Tracking the acetate threshold using DO-transient control during medium and high cell density cultivation of recombinant Escherichia coli in complex media

DO-transient nutrient controllers use the dissolved oxygen signal to attempt acetate threshold tracking during fed-batch cultivation of recombinant E. coli. Here we apply DO-transient control to the production of Jembrana disease virus protein in complex Super Luria medium and compare performance against a high-limit pH-stat controller. For induction at medium cell density (harvest between 31 and 32.5 g dcw L) a total productivity of 0.27 g L h was achieved as compared to 0.24 g L h with the high-limit pH-stat. For induction at high cell density (harvest at 60 g dcw L), decreased productivity (0.12 g L h) was attributed to the effect of acetate accumulation on recombinant protein formation and a concomitant lowering of the critical growth rate. Our results suggest that complex media provides a difficult environment for the application of acetate threshold tracking DO-transient control because of difficulties in re-oxidizing acetate, and apparent localized production of acetate below the production threshold (as detected by the DO-transient controller as SPOUR(crit)). Configuring the DO-transient controller to avoid aggressive threshold probing is suggested as a means to improve performance and reduce acetate accumulation in complex media.     

产1，3-丙二醇重组大肠杆菌JM109（pEtac—dhaB—tac—yqhD）的构建

在生物柴油的生产过程中,最高可得到约10％的副产物甘油,副产物甘油的去向将成为生物柴油大规模产业化发展所面临的严峻问题。以生物柴油副产物甘油为原料耦合生产1,3-丙二醇,不仅解决了生物柴油副产物甘油的出路问题,同时降低了1,3-丙二醇的生产成本。本研究在前期工作的基础上,分别获得了来源于肺炎克雷伯氏茵的甘油脱水酶编码基因dhaB和来源于大肠杆菌的1,3-PD氧化还原酶同工酶编码基因yqhD,利用表达载体pEtac串联构建了重组质粒pEtac—dhaB—tac—yqhD,将其转化大肠杆菌得到产1,3-丙二醇重组大肠杆菌JM109（pEtac—dhaB-tac—yqhD）,降低了代谢中间产物3-羟基丙醛的积累,提高了1,3-丙二醇的产量。     

Genetic selection system for improving recombinant membrane protein expression in E. coli

A major barrier to the physical characterization and structure determination of membrane proteins is low yield in recombinant expression. To address this problem, we have designed a selection strategy to isolate mutant strains of Escherichia coli that improve the expression of a targeted membrane protein. In this method, the coding sequence of the membrane protein of interest is fused to a C‐terminal selectable marker, so that the production of the selectable marker and survival on selective media is linked to expression of the targeted membrane protein. Thus, mutant strains with improved expression properties can be directly selected. We also introduce a rapid method for curing isolated strains of the plasmids used during the selection process, in which the plasmids are removed by in vivo digestion with the homing endonuclease I‐CreI. We tested this selection system on a rhomboid family protein from Mycobacterium tuberculosis (Rv1337) and were able to isolate mutants, which we call EXP strains, with up to 75‐fold increased expression. The EXP strains also improve the expression of other membrane proteins that were not the target of selection, in one case roughly 90‐fold.     

Lactobacillus acidophilus expressing recombinant K99 adhesive fimbriae has an inhibitory effect on adhesion of enterotoxigenic Escherichia coli

The most common enteric colibacillosis in neonatal and newborns is caused by enterotoxigenic Escherichia coli(ETEC). Colonization of ETEC in the small intestine is associated with adhesions using fimbriae, which is known as a specific adhesion factor and provides highly specific means for anchoring and prerequisite for an infectious agent. In the present study we have engineered Lactobacillus acidophilus to produce recombinant K99 fimbriae, which is used for the colonization to the intestine of pigs. The expression of K99 fimbrial protein was confirmed using SDS-PAGE, immunoblot and agglutination analyses. To evaluate a function of the K99 fimbrial protein, inhibition and competition tests were performed on pre-screened intestinal brush border from pigs. The tests showed that recombinant L. acidophilus, not control L. acidophilus, had a significant inhibitory effect to and competition against K99+ E. coli in a dose dependent manner. In conclusion, we demonstrated that recombinant K99 fimbriae producing L. acidophilus was able to prevent E. coli binding to intestinal brush border.     

Increased phenotypic stability and ethanol tolerance of recombinant Escherichia coli KO11 when immobilized in continuous fluidized bed culture

The recombinant Escherichia coli B strain KO11, containing chromosomally-integrated genes for ethanol production, was developed for use in lignocellulose-to-ethanol bioconversion processes but suffers from instability in continuous culture and a low ethanol tolerance compared to yeast. Here we report the ability cell immobilization to improve its phenotypic stability and ethanol tolerance during continuous culture on a 50 g/L xylose feed. Experiments conducted in a vertical tubular fermentor operated as a liquid-fluidized bed with the cells immobilized on porous glass microspheres were compared to control experiments in the same reactor operated as a chemostat without the support particles. Without cell immobilization the ethanol yield fell sharply following start-up, declining to 60% of theoretical after only 8-9 days of continuous fermentation. While immobilizing the cells did not prevent this decline, it delayed its onset and slowed its rate. With immobilization, a stable high ethanol yield (>85%) was maintained for at least 10 days, thereafter declining slowly, but remaining above 70% even after up to 40 days of fermentation. The ethanol tolerance of E. coli KO11 cells was substantially increased by immobilization on the glass microspheres. In ethanol tolerance tests, immobilized cells released from the microspheres had survival rates 2.3- to 15-fold higher than those of free cells isolated from the same broth. Immobilization is concluded to be an effective means of increasing ethanol tolerance in E. coli KO11. While immobilization was only partially effective in combating its phenotypic instability, further improvements can be expected following optimization of the immobilization conditions.     

Process optimization for large-scale production of TGF-α-PE40 in recombinant Escherichia coli: effect of medium composition and induction timing on protein expression

The effects of medium composition and induction timing on expression of a chimeric fusion protein TGF-α -PE40 (TP-40) in Escherichia coli strain RR1 were examined using a complex medium at several fermentor scales. Two distinctive phases in E. coli catabolism were identified during fermentation based on preferential utilization between protein hydrolysate and glycerol. Maximum specific and volumetric productivities were achieved by inducing the culture when the cells were switching substrate utilization from protein hydrolysate to glycerol. By increasing the yeast extract concentration in the production medium, initiation of the catabolic switch was delayed until high cell mass was achieved. The final titer of TP-40 at the 15-L fermentation scale was doubled from 400 mg L⁻¹ to 850 mg L⁻¹ by increasing the yeast extract concentration from 1% to 4% (w/v) and delaying the time of induction. This fermentation process was rapidly scaled up in 180-L and 800-L fermentors, achieving TP-40 titers of 740 and 950 mg L⁻¹, respectively. Received 26 August 1996/ Accepted in revised form 10 December 1996