Galactose can be an inducer for production of therapeutic proteins by auto-induction using E. coli BL21 strains

Recently lactose mediated auto-induction in Escherichia coli has gained a lot of interest because higher protein titer could be achieved without the need to monitor growth and add inducer at the proper time. In this study a high level therapeutic protein production by auto-induction was observed in E. coli BL21 using either T7 or tac promoters in the modified Luria Bertani (mLB) medium containing soy peptone instead of tryptone in Luria Bertani (LB) medium. Based on medium analysis and spiking experiments it was found that 0.4 mM galactose from the soy peptone caused the auto-induction. E. coli cultures induced by galactose can saturate at considerably higher density than cultures induced by IPTG. Galactose is not consumed by E. coli BL21. Finally it has been demonstrated that auto-induction can be effectively used in fed-batch fermentation for the industrial production of a therapeutic protein. The principle of galactose mediated auto-induction should be able to apply to high throughput microplates, shake flasks and fed-batch fermentors for clone screening and therapeutic protein expression in E. coli gal(-) strains such as most commonly used BL21.     

组合代谢调控提高大肠杆菌对氨基苯甲酸产量

对氨基苯甲酸是一种重要的有机合成中间体,广泛应用于医药、染料等行业。近年来对氨基苯甲酸作为一种潜在的高强度共聚物单体越来越受到重视。对氨基苯甲酸作为叶酸合成的前体之一,其合成在大肠杆菌体内由叶酸合成途径的pabA、pabB和pabC三个基因负责,催化分支酸合成对氨基苯甲酸。本研究以实验室构建的酪氨酸高产工程菌TYR002作为出发菌株,首先弱化双功能分支酸突变酶/预苯酸脱氢酶TyrA的表达,以减少酪氨酸积累,然后利用3种不同强度的组成型启动子分别调控pabA、pabB和pabC的表达。摇瓶发酵表明不同的组合调控模式下大肠杆菌发酵培养基中的对氨基苯甲酸积累量存在显著差异,最高可获得0.67 g/L的摇瓶发酵产量。进一步通过发酵条件优化和分批补料发酵,在5L发酵罐中获得了6.4g/L的对氨基苯甲酸产量。本研究为改善对氨基苯甲酸生物合成效率提供了重要理论参考。     

Engineering Escherichia coli for xylitol production from glucose-xylose mixtures

The range of value-added chemicals produced by Escherichia coli from simple sugars has been expanded to include xylitol. This was accomplished by screening the in vivo activity of a number of heterologous xylitol-producing enzymes. Xylose reductases from Candida boidinii (CbXR), Candida tenuis (CtXR), Pichia stipitis (PsXR), and Saccharmoyces cerivisiae (ScXR), and xylitol dehydrogenases from Gluconobacter oxydans (GoXDH) and Pichia stipitis (PsXDH) were all functional in E. coli to varying extents. Replacement of E. coli's native cyclic AMP receptor protein (CRP) with a cyclic AMP-independent mutant (CRP*) facilitated xylose uptake and xylitol production from mixtures of glucose and xylose, with glucose serving as the growth substrate and source of reducing equivalents. Of the enzymes tested, overexpression of NADPH-dependent CbXR produced the highest concentrations of xylitol in shake-flask cultures (approximately 275 mM in LB cultures, approximately 180 mM using minimal medium). Expression of CbXR in strain PC09 (crp*, DeltaxylB) in a 10-L controlled fermentation containing minimal medium resulted in production of approximately 250 mM xylitol (38 g/L), with concomitant utilization of approximately 150 mM glucose. The ratio of moles xylitol produced (from xylose) per mole glucose consumed was improved to > 3.7:1 using metabolically active "resting" cells.     

Aerobic fermentation of D-glucose by an evolved cytochrome oxidase-deficient Escherichia coli strain

Fermentation of glucose to D-lactic acid under aerobic growth conditions by an evolved Escherichia coli mutant deficient in three terminal oxidases is reported in this work. Cytochrome oxidases (cydAB, cyoABCD, and cbdAB) were removed from the E. coli K12 MG1655 genome, resulting in the ECOM3 (E. coli cytochrome oxidase mutant) strain. Removal of cytochrome oxidases reduced the oxygen uptake rate of the knockout strain by nearly 85%. Moreover, the knockout strain was initially incapable of growing on M9 minimal medium. After the ECOM3 strain was subjected to adaptive evolution on glucose M9 medium for 60 days, a growth rate equivalent to that of anaerobic wild-type E. coli was achieved. Our findings demonstrate that three independently adaptively evolved ECOM3 populations acquired different phenotypes: one produced lactate as a sole fermentation product, while the other two strains exhibited a mixed-acid fermentation under oxic growth conditions with lactate remaining as the major product. The homofermenting strain showed a D-lactate yield of 0.8 g/g from glucose. Gene expression and in silico model-based analyses were employed to identify perturbed pathways and explain phenotypic behavior. Significant upregulation of ygiN and sodAB explains the remaining oxygen uptake that was observed in evolved ECOM3 strains. E. coli strains produced in this study showed the ability to produce lactate as a fermentation product from glucose and to undergo mixed-acid fermentation during aerobic growth.     

Use of n-hexadecane as an oxygen vector to improve Phaffia rhodozyma growth and carotenoid production in shake-flask cultures

AIMS: To identify beneficial oxygen vectors for Phaffia rhodozyma in liquid cultures, and to evaluate their use to improve the oxygen transfer and carotenoid production in the yeast cultures. METHODS AND RESULTS: Several liquid hydrocarbons were tested as oxygen vectors for improving the yeast growth and carotenoid production in shake-flask cultures of P. rhodozyma. While all nontoxic organic liquids (Log P: > or =5.6) showed a positive effect, n-hexadecane was proved to be the most beneficial for the yeast growth and carotenoid production. The addition of 9% (v/v) n-hexadecane to the liquid medium at the time of inoculation was found to be optimal, increasing the carotenoid yield by 58% (14.5 mg l(-1) vs 9.2 g l(-1) in the control) and the oxygen transfer rate (OTR) by 90%. CONCLUSIONS: The addition of n-hexadecane to shake-flask cultures of P. rhodozyma significantly improved the oxygen transfer in culture, thus increasing the carotenoid production. SIGNIFICANCE AND IMPACT OF THE STUDY: Use of organic oxygen vectors such as n-hexadecane may be a simple and useful means for enhancing oxygen transfer and carotenoid production in liquid fermentation of P. rhodozyma.     

Oxygen requirements of yeasts

Type species of 75 yeast genera were examined for their ability to grow anaerobically in complex and mineral media. To define anaerobic conditions, we added a redox indicator, resazurin, to the media to determine low redox potentials. All strains tested were capable of fermenting glucose to ethanol in oxygen-limited shake-flask cultures, even those of species generally regarded as nonfermentative. However, only 23% of the yeast species tested grew under anaerobic conditions. A comparative study with a number of selected strains revealed that Saccharomyces cerevisiae stands out as a yeast capable of rapid growth at low redox potentials. Other yeasts, such as Torulaspora delbrueckii and Candida tropicalis, grew poorly mu max, 0.03 and 0.05 h-1, respectively) under anaerobic conditions in mineral medium supplemented with Tween 80 and ergosterol. The latter organisms grew rapidly under oxygen limitation and then displayed a high rate of alcoholic fermentation. It can be concluded that these yeasts have hitherto-unidentified oxygen requirements for growth.     

Oxygen requirements of yeasts.

Type species of 75 yeast genera were examined for their ability to grow anaerobically in complex and mineral media. To define anaerobic conditions, we added a redox indicator, resazurin, to the media to determine low redox potentials. All strains tested were capable of fermenting glucose to ethanol in oxygen-limited shake-flask cultures, even those of species generally regarded as nonfermentative. However, only 23% of the yeast species tested grew under anaerobic conditions. A comparative study with a number of selected strains revealed that Saccharomyces cerevisiae stands out as a yeast capable of rapid growth at low redox potentials. Other yeasts, such as Torulaspora delbrueckii and Candida tropicalis, grew poorly mu max, 0.03 and 0.05 h-1, respectively) under anaerobic conditions in mineral medium supplemented with Tween 80 and ergosterol. The latter organisms grew rapidly under oxygen limitation and then displayed a high rate of alcoholic fermentation. It can be concluded that these yeasts have hitherto-unidentified oxygen requirements for growth.     

An interlaboratory comparison of physiological and genetic properties of four Saccharomyces cerevisiae strains

To select a Saccharomyces cerevisiae reference strain amenable to experimental techniques used in (molecular) genetic, physiological and biochemical engineering research, a variety of properties were studied in four diploid, prototrophic laboratory strains. The following parameters were investigated: 1) maximum specific growth rate in shake-flask cultures; 2) biomass yields on glucose during growth on defined media in batch cultures and steady-state chemostat cultures under controlled conditions with respect to pH and dissolved oxygen concentration; 3) the critical specific growth rate above which aerobic fermentation becomes apparent in glucose-limited accelerostat cultures; 4) sporulation and mating efficiency; and 5) transformation efficiency via the lithium-acetate, bicine, and electroporation methods. On the basis of physiological as well as genetic properties, strains from the CEN.PK family were selected as a platform for cell-factory research on the stoichiometry and kinetics of growth and product formation.     

Extracellular 5-aminolevulinic acid production by Escherichia coli containing the Rhodopseudomonas palustris KUGB306 hemA gene

The Rhodopseudomonas palustris KUGB306 hemA gene codes for 5-aminolevulinic acid (ALA) synthase. This enzyme catalyzes the condensation of glycine and succinyl-CoA to yield ALA in the presence of the cofactor pyridoxal 5'- phosphate. The R. palustris KUGB306 hemA gene in the pGEX-KG vector system was transformed into Escherichia coli BL21. The effects of physiological factors on the extracellular production of ALA by the recombinant E. coli were studied. Terrific Broth (TB) medium resulted in significantly higher cell growth and ALA production than did Luria-Bertani (LB) medium. ALA production was significantly enhanced by the addition of succinate together with glycine in the medium. Maximal ALA production (2.5 g/l) was observed upon the addition of D-glucose as an ALA dehydratase inhibitor in the late-log culture phase. Based on the results obtained from the shake-flask cultures, fermentation was carried out using the recombinant E. coli in TB medium, with the initial addition of 90 mM glycine and 120 mM succinate, and the addition of 45 mM D-glucose in the late-log phase. The extracellular production of ALA was also influenced by the pH of the culture broth. We maintained a pH of 6.5 in the fermenter throughout the culture process, achieving the maximal levels of extracellular ALA production (5.15 g/l, 39.3 mM).     

Quasi-continuous combined scattered light and fluorescence measurements: a novel measurement technique for shaken microtiter plates

A novel quasi-continuous on-line measuring technique for shaken microtiter plates is presented. Light scattering as well as intracellular and/or protein fluorescence (e.g. NADH, YFP) is measured during the shaking procedure, thus allowing a process monitoring of 96 different simultaneous cultures in a microtiter plate. In contrast to existing measurement techniques, the shaking process does not have to be stopped to take the measurements, thus avoiding the corresponding interruption of the cultures' oxygen supply and any unpredictable effects on the cultures. Experiments were conducted with E. coli in LB, TB, and MOPS minimal medium and V. natriegens in modified LB and TB media. Intensity curves of scattered light and NADH fluorescence were used to distinguish different lag phases, growth velocities, or inoculation densities. Data from this new method corresponded well to the off-line measured optical densities and to the oxygen transfer rates of cultures run in simultaneously conducted shake flask experiments at equivalent oxygen transfer capacities. With the aid of yellow fluorescence protein fused to interleukin-6 the optimal induction time of an expressing E. coli strain could be determined by on-line monitoring of product formation. Thus, this measuring technique enables the researcher to evaluate and to discriminate different cultures on a screening level and to improve screening conditions, process development and scale-up.     

Spent media from cultures of environmental isolates of Escherichia coli can suppress the deficiency of biofilm formation under anoxic conditions of laboratory E. coli strains

The prevailing lifestyle of bacteria is sessile and they attach to surfaces in structures known as biofilms. In Escherichia coli, as in many other bacteria, biofilms are formed at the air-liquid interface, suggesting that oxygen has a critical role in the biofilm formation process. It has been reported that anaerobically growing E. coli laboratory strains are unable to form biofilms even after 96 h of incubation on Luria Bertani (LB) medium. After analyzing 22,000 transposon-induced and 26,000 chemically-induced mutants we failed to isolate an E. coli laboratory strain with the ability to form biofilm under anaerobic growth conditions. Notably, seven strains from a collection of E. coli isolated from different hosts and the environment had the ability to form biofilm in the absence of oxygen. Interestingly, spent medium from cultures of one strain, Souza298, can promote biofilm formation of E. coli laboratory strains growing under anaerobic conditions. Our results led us to propose that laboratory E. coli strains do not release (or synthesize) a molecule needed for biofilm formation under anoxic conditions but that they bear all the required machinery needed for this process.     

产顺,顺-粘康酸细胞工厂的构建与优化

顺,顺-粘康酸是重要的平台化学品。目前,生物合成顺,顺-粘康酸还缺乏高性能菌株,已报道的主要工程菌株不仅需要诱导表达,遗传不稳定,而且发酵培养基组分复杂,不利于大规模工业化生产。构建能利用简单无机盐培养基、遗传稳定且不需要诱导表达的新型工程菌受到人们的关注。本研究在实验室前期构建的产三脱氢莽草酸工程菌株WJ060中,整合合成顺,顺-粘康酸的3个外源基因(aro Z、aro Y、cat A),并且利用3个不同强度的组成型启动子进行组合调控,成功构建了27株顺,顺-粘康酸工程菌,得到的最优工程菌MA30的产量达到1.7 g/L。为了进一步提高顺,顺-粘康酸工程菌的生产能力,利用基因组复制工程构建突变体库,结合高通量筛选方法,经过两轮筛选,成功筛选到了顺,顺-粘康酸产量提高超过8%的大肠杆菌MA30-G2。利用5 L发酵罐进行分批补料发酵,MA30-G2的顺,顺-粘康酸产量达到了11.5 g/L。本研究采用组合调控和高通量筛选相结合的策略不仅促进了顺,顺-粘康酸的生物合成,同时也为其他生物基化学品的生物制造提供了重要参考。     

通过参数相关性分析对发酵控制策略在植酸酶高密度发酵中的作用探讨

为了优化植酸酶高密度发酵条件,有必要获取在发酵过程中由于控制策略引起有关参数的实时变化及其关联性.本研究利用传感器对植酸酶工程菌高密度发酵过程进行数据在线采集,通过改变转速、接种量与补料甘油,探讨三方面控制因素对高密度发酵产酶过程参数具体影响及各参数变化之间的相关性,建立起与转速-细胞密度-溶氧-乳酸相关的发酵罐内外环...     

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.     

Nisin高产菌株的高通量筛选

【目的】乳酸链球菌素(nisin)是一种天然生物活性抗菌肽,对包括食品腐败菌和致病菌在内的许多革兰氏阳性菌具有强烈的抑制作用,而用作食品的防腐剂。本研究通过建立高通量筛选方法,实现高效快速省力的高产菌株筛选,为工业上筛选高产菌株提供研究方案。【方法】通过对Lactococcus lactis ATCC11454菌株进行紫外诱变,获得2511株突变株。利用Biomek FXP自动工作站建立96微孔板的高通量筛选方法,突变株经高通量挑选、菌种培养及菌液稀释后,加入到生长至对数中期的藤黄微球菌中,采用改进后的比浊法快速检测nisin生物活性。用此方法对突变株进行初筛、复筛后可得到nisin高产菌株,并通过摇瓶发酵评估高通量筛选方法。【结果】确定比浊法检测的条件为:nisin活性稀释在10–25 IU/m L范围内,与藤黄微球菌反应2 h后检测藤黄微球菌的菌体量(OD600)。2511株突变株经过2轮高通量筛选,最终获得约50株产量提升的菌株,对其中8株进行摇瓶精确测量,显示产量均有提高,并且其中一株产量提升了30%,成功建立了高通量筛选nisin高产菌株的方法。【结论】利用比浊检测法,在其基础上成功建立高通量筛选高产nisin菌的方法,经过初筛复筛,整个周期由1人耗时5 d即可完成2511株突变株的筛选工作。相较于传统的选育方法,高通量筛选具有快速、稳定、高效的特点,提高了筛选效率,缩短了选育周期,是工业上筛选高产nisin菌的有效手段。     

Expression of beta-lactamase by recombinant Escherichia coli strains containing plasmids of different sizes--effects of pH, phosphate, and dissolved oxygen

The characteristics of growth and synthesis of plasmid-encoded protein were studied for strains of recombinant E. coli JM103 which carried the beta-lactamase gene on plasmids of different sizes. The plasmids used included the vector pUC8 and its recombinant derivatives containing varying-sized inserts of Drosophila DNA (not expressed in E. coli). Luria broth (LB) and a minimal medium (M9) supplemented in some cases with additional inorganic phosphate were used as growth media. There was no evidence of segregational instability in these experiments, where no antibiotic selection pressure was employed. Responses of the recombinant strains to variations in environmental parameters including pH, phosphate concentration in the medium, and aeration rate were examined. While the cell growth rate in LB decreased with pH in the range 7.0-8.0, the bulk beta-lactamase activity was maximized at an intermediate pH. The recombinant cell growth rate decreases with increasing plasmid size in the minimal medium, while such decrease is not significant when a rich medium such as LB is used. There is an intermediate plasmid size in the range studied (2.7-8.7 kb), at which beta-lactamase activity is maximum. While reduction in aeration rate (which determines the dissolved oxygen level) is detrimental for cell growth, it is beneficial for beta-lactamase synthesis. The bulk beta-lactamase activity therefore exhibits a maximum with respect to aeration rate. Cell growth and beta-lactamase production are affected in a similar manner by phosphate concentration in the minimal medium and therefore both are maximized at the same phosphate concentration. This investigation demonstrates clearly how the production of a recombinant plasmid-encoded protein can be maximized by proper manipulation of culture conditions and how it is affected by plasmid size.     

Engineering Escherichia coli to improve culture performance and reduce formation of by-products during recombinant protein production under transient intermittent anaerobic conditions

Three E. coli strains, named VAL22, VAL23, and VAL24, were engineered at the level of mixed-acid fermentation pathways to improve culture performance under transient anaerobic conditions. VAL22 is a single mutant with an inactivated poxB gene that codes for pyruvate oxidase which converts pyruvate to acetate. VAL23 is a double mutant unable to produce lactate and formate due to deletions of the ldhA and pflB genes that code for lactate dehydrogenase and pyruvate-formate lyase, respectively. VAL24 is a triple mutant with ldhA and pflB deleted and poxB inactivated. Engineered strains were cultured under oscillating dissolved oxygen tension (DOT) in a scale-down system, to simulate gradients occurring in large-scale bioreactors. Kinetic and stoichiometric parameters of constant (10%) and oscillating DOT cultures of the engineered strains were compared with those of the parental strain, W3110. All strains expressed recombinant green fluorescent protein (GFP) as a protein model. Mutant strains showed improved specific growth rate, reduced by-product formation, and reduced specific glucose uptake rate compared to the parental strain, when cultured under oscillating DOT. In particular, lactate and formate production was abolished and acetate accumulation was reduced by 9-12%s. VAL24 showed the best performance, as specific growth and GFP production rates, and maximum GFP concentration were not affected by DOT gradients and were at least twofold higher than those of W3110 under constant DOT. Under oscillating DOT, VAL24 wasted about 40% less carbon into fermentation by-products than W3110. It was demonstrated that, although E. coli responds rapidly to DOT fluctuations by deviating to fermentative metabolism, such pathways can be eliminated as they are not necessary for bacterial survival during the short circulation times typical of large-scale cultures. The approach shown here opens new possibilities for designing metabolically engineered strains, with reduced sensitivity to DOT gradients and improved performance under typical conditions of large-scale cultures.     

Elevated Fis expression enhances recombinant protein production in Escherichia coli

A genetic strategy to enhance recombinant protein production is discussed. A small DNA bending protein, Fis, which has been shown to activate rRNA synthesis upon a nutrient upshift, was overexpressed in E. coli strain W3110 carrying vector pUCR1. Overexpression of Fis during exponential growth was shown to activate rrn promoters to different extents. A 5-fold improvement in chloramphenicol acetyltransferase (CAT) production in cultures with elevated Fis level was observed in shake-flask cultivations. A similar improvement in the culture performance was also observed during fed-batch fermentation; the specific CAT activity increased by more than 50% during the fed-batch phase for cultures with elevated Fis expression. In contrast, no increase in specific CAT activity was detected for cultures carrying pUCR2, expressing a frame-shift Fis mutant. Expression of Fis from a complementary vector, pKFIS, restored CAT production from W3110:pUCR2 to approximately the same level as cultures carrying pUCR1, indicating that the enhancement in CAT production was indeed Fis-dependent. The framework presented here suggests that differential activation in recombinant protein production may be achieved with differential Fis overexpression. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 138-144, 1997.     

Improving 1,3-propanediol production from glycerol in a metabolically engineered Escherichia coli by reducing accumulation of sn-glycerol-3-phosphate

High levels of glycerol significantly inhibit cell growth and 1,3-propanediol (1,3-PD) production in anaerobic glycerol fermentation by genetically engineered Escherichia coli (E. coli) strains expressing genes from the Klebsiella pneumoniae dha (K.pneumoniae) regulon. We have previously demonstrated that 1,3-PD production by the engineered E. coli can be improved by reducing the accumulation of methylglyoxal. This study focuses on investigation of another lesser-known metabolite in the pathways related to 1,3-PD production-glycerol-3-phosphate (G3P). When grown anaerobically on glycerol in the absence of an exogenous acceptor, the engineered E. coli strains have intracellular G3P levels that are significantly higher than those in K. pneumoniae, a natural 1,3-PD producer. Furthermore, in the engineered E. coli strains, the G3P levels increase with increasing glycerol concentrations, whereas, in K. pneumoniae, the concentrations of G3P remain relatively constant. Addition of fumarate, which can stimulate activity of anaerobic G3P dehydrogenase, into the fermentation medium led to a greater than 30-fold increase in the specific activity of anaerobic G3P dehydrogenase and a significant decrease in concentrations of intracellular G3P and resulted in better cell growth and an improved production of 1,3-PD. This indicates that the low activity of G3P dehydrogenase in the absence of an exogenous electron acceptor is one of the reasons for G3P accumulation. In addition, spent media from E.coli Lin61, a glycerol kinase (responsible for conversion of glycerol to G3P) mutant, contains greatly decreased concentrations of G3P and shows improved production of 1,3-PD (by 2.5-fold), when compared to media from its parent strain E. coli K10. This further suggests that G3P accumulation is one of the reasons for the inhibition of 1,3-PD production during anaerobic fermentation.     

Proposed mechanism of acetate accumulation in two recombinant Escherichia coli strains during high density fermentation

The productivity of Escherichia coli as a producer of recombinant proteins is affected by its metabolic properties, especially by acetate production. Two commercially used E. coli strains, BL21 (lambdaDE3) and JM109, differ significantly in their acetate production during batch fermentation at high initial glucose concentrations. E. coli BL21 grows to an optical density (OD, 600 nm) of 100 and produces no more than 2 g/L acetate, while E. coli JM109 grows to an OD (600 nm) of 80 and produces up to 14 g/L acetate. Even in fed-batch fermentation, when glucose concentration is maintained between 0.5 and 1.0 g/L, JM109 accumulates 4 times more acetate than BL21. To investigate the difference between the two strains, metabolites and enzymes involved in carbon utilization and acetate production were analyzed (isocitrate, ATP, phosphoenolpyruvate, pyruvate, isocitrate lyase, and isocitrate dehydrogenase). The results showed that during batch fermentation isocitrate lyase activity and isocitrate concentration were higher in BL21 than in JM109, while pyruvate concentration was higher in JM109. The activation of the glyoxylate shunt pathway at high glucose concentrations is suggested as a possible explanation for the lower acetate accumulation in E. coli BL21. Metabolic flux analysis of the batch cultures supports the activity of the glyoxylate shunt in E. coli BL21.