HPLC separation of enterobactin and linear 2,3-dihydroxybenzoylserine derivatives: a study on mutants ofEscherichia coli defective in regulation (fur), esterase (fes) and transport (fepA)

Reversed-phase HPLC separation of enterobactin and its 2,3-dihydroxybenzoylserine derivatives was used for a comparative analysis of mutants of Escherichia coli, defective in the regulation of enterobactin biosynthesis (fur), enterobactin transport (fepA) and enterobactin esterase (fes). A complete separation of all 2,3-dihydroxybenzoylserine compounds was achieved: the monomer (DHBS), the linear dimer (DHBS)₂ and trimer (DHBS)₃, the cyclic trimer, enterobactin, as well as 2,3-dihydroxybenzoic acid. The production of all these compounds was followed after ethylacetate extraction from acidified culture fluids. Enterobactin was found to be the predominant product in all mutant strains. The mutant strains behaved differently with regard to the breakdown products. All degradation products, such as DHBS, (DHBS)₂ and (DHBS)₃, were detected in the overproducing fur mutant where both transport and esterase are still functioning, while only the monomer, DHBS, was detected in the fepA mutant and no degradation was found in the esterase-deficient fes mutant. From the pattern of breakdown products it may be inferred that the esterase acts in two different ways, depending on whether transport is functioning or not. Thus, esterolytic cleavage of ferric enterobactin after entering the cells results in a mixture of all three hydrolysis products, i.e. DHBS, (DHBS)₂ and (DHBS)₃, while cleavage of iron-free enterobactin subsequent to its biosynthesis yields only the monomer. Thus, the results of quantitative HPLC analysis of enterobactin and its breakdown products show that different enterobactin esterase products arise, depending on whether iron is bound to enterobactin or not.     

Export of the siderophore enterobactin in Escherichia coli: involvement of a 43 kDa membrane exporter

The enterobactin system for iron transport in Escherichia coli is well characterized with the exception of the mechanism of enterobactin secretion to the extracellular environment. Escherichia coli membrane protein P43, encoded by ybdA in the chromosomal region of genes involved in enterobactin synthesis, shows strong homology to the 12-transmembrane segment major facilitator superfamily of export pumps. A P43-null mutation was created and siderophore nutrition assays, performed with a panel of E. coli strains expressing one or more outer membrane receptors for enterobactin-related compounds, demonstrated that the P43 mutant was unable to secrete enterobactin efficiently. Products released from the mutant strain were identified with thin-layer chromatography (TLC) and high-performance liquid chromatography (HPLC), revealing that the P43 mutant secretes little, if any, enterobactin, but elevated levels of enterobactin breakdown products 2,3- dihydroxybenzoylserine (DHBS) monomer, dimer, and trimer. These data establish that P43 is a critical component of the E. coli enterobactin secretion machinery and provides a rationale for the designation of the previous genetic locus ybdA as entS to reflect its relevant biological function.     

The effect of carbon dioxide on the production of an extracellular nuclease of Staphylococcus aureus

The production of the extracellular nuclease secreted by Staphylococcus aureus (Foggi strain) was studied in a fermentor in an attempt to improve yield and allow large-scale production of the enzyme. In shake flask cultures, 600 units/mL of the enzyme were produced routinely. However, only 450 units/mL of the enzyme at best were obtained in a small-scale fermentor (3 L). The supplementation of the air supply to the fermentor with carbon dioxide [20% (v/v)] increased levels of enzyme in the culture medium to 770 units/mL. Subsequently, this result was reproduced in larger fermentors (10 and 150 L). The possible mechanisms of the effect of carbon dioxide upon the growth of Staphylococcus aureus (Foggi) and the production of the enzyme are discussed.     

Phenylalanine- and tyrosine-dependent production of enterobactin in Escherichia coli

Abstract Under low-iron conditions, Escherichia coli synthesizes the siderophore enterobactin. When compared to wild-type cells grown in iron sufficient medium, cells grown under iron limitation, in the absence of tyrosine and phenylalanine or the presence of both, increased catechol production (a measure of enterobactin and its degradation product 2,3-dihydroxybenzoic acid) 5- to 9-fold while cells supplemented with tyrosine alone produced a 10- to 20-fold increase. Mutations in fur , tyrA , pheA , or pheU generally resulted in increased enterobactin production, while a tyrR mutant was unaffected by combinations of tyrosine and phenylalanine.     

Two-phase airlift fermentor operation with elicitation for the enhanced production of enzophenanthridine alkaloids in cell suspensions of Escherichia californica

Approaches to increasing the productivity of benzophenanthridine alkaloids in suspension cultures in Escherichia californica were made in an airlift fermentor under different culture conditions. Elicitation with yeast extract elicitor reduced the time required to obtain a certain amount of alkaloid production. In a two-phase airlift fermentor with compounded silicone fluid, total alkaloid concentration in silicone fluid was 153.1 mg/L and that in the aqueous cellular phase was 8.2 mg/L at day 21 from inoculation. The large accumulation capacity of silicone fluid made it possible to store correspondingly large amounts of total alkaloid and increased the alkaloid production. Act day 21 from inoculation, the volumetric alkaloid productivity and the netproduction in a two-phase airlift fermentor were 1.4 and 1.5 times higher than those of normal airlift fermentor operation. This performance was furthermore enhanced by elicitation. Elicitation in two-phase airlift fermentor operation increased the volumetric productivity and the new production 3.3- and 3.5-fold compared to those of normal airlift fermentor operation. (c) 1994 John Wiley & Sons, Inc.     

Increase of xylitol production rate by controlling redox potential in Candida parapsilosis

The effect of redox potential on xylitol production by Candida parapsilosis was investigated. The redox potential was found to be useful for monitoring the dissolved oxygen (DO) level in culture media, especially when the DO level was low. An increase in the agitation speed in a 5 L fermentor resulted in an increased culture redox potential as well as enhanced cell growth. Production of xylitol was maximized at a redox potential of 100 mV. As the initial cell concentration increased from 8 g/L to 30 g/L, the volumetric productivity of xylitol increased from 1.38 g/L. h to 4.62 g/L. h. A two-stage xylitol production strategy was devised, with stage 1 involving rapid production of cells under well-aerated conditions, and stage 2 involving cultivation with reduced aeration such that the culture redox potential was 100 mV. Using this technique, a final xylitol concentration of 180 g/L was obtained from a culture medium totally containing 254.5 g/L xylose in a 3,000 L pilot scale fermentor after 77 h fermentation. The volumetric productivity of xylitol during the fermentation was 2.34 g/L. h.     

代谢工程改造大肠杆菌合成丁二酸及发酵罐放大工艺

【背景】Escherichia coli AFP111发酵生产丁二酸时大量副产乙酸,丁二酸得率低。【目的】代谢工程改造EscherichiacoliAFP111,提高丁二酸得率,降低副产物乙酸的生成,建立100 L规模的丁二酸发酵工艺。【方法】一步同源重组敲除乙酸合成途径关键酶基因,改造丁二酸合成途径关键酶启动子实现过表达;单因素优化5L发酵罐培养条件。【结果】敲除乙酸产生途径编码乙酸激酶和磷酸转乙酰酶的基因ackA-pta、苏氨酸脱羧酶和2-酮丁酸甲酸裂解酶的基因tdcDE获得SX02菌株,摇瓶发酵条件下其乙酸产量下降了53.42%,丁二酸得率提高9.85%。在SX02菌株基础上,经启动子改造过表达编码葡萄糖激酶的基因glk后获得菌株SX03,其Glk酶活性提高3.66倍,乙酸产量下降了31.62%,丁二酸得率提高8.28%。SX03菌株发酵生产丁二酸在5 L发酵罐进行放大,其乙酸产量为3.97 g/L,丁二酸得率为1.62 mol/mol葡萄糖,相比出发菌株的乙酸产量下降了75.76%,丁二酸得率提高19.12%。在5L发酵罐上对比研究了中和剂Na2CO3和NaOH混合液替换碱式MgCO3的发酵效果,并优化了发酵pH、搅拌转速和葡萄糖浓度,获得如下最适发酵条件:pH6.8,搅拌转速250r/min,葡萄糖100g/L,发酵结束时乙酸产量为2.24 g/L,丁二酸得率为1.66 mol/mol葡萄糖。中和剂替换优化后乙酸产量下降了20.65%,丁二酸得率提高2.47%。菌株SX03发酵工艺进一步在100 L发酵罐上实现放大,其乙酸产量为1.91 g/L,丁二酸得率为1.30 mol/mol葡萄糖。【结论】通过代谢工程改造的大肠杆菌,其副产物乙酸含量显著下降,丁二酸得率提高,并在5 L和100 L发酵罐上实现了工艺放大,展现出较大的工业化利用潜力。     

营养及环境因素对黄色短杆菌发酵生产L-亮氨酸的影响

目的:研究葡萄糖、玉米浆、蛋氨酸等主要营养物质以及环境因素对发酵生产L-亮氨酸的影响。方法:应用单因素实验确定发酵条件,采用高效液相色谱法测定产量。结果:在最优发酵条件下,以种龄36h、接种量为10%,摇瓶产L-亮氨酸的量可达19.4g/L,采用10L罐分批补料发酵64h可积累29.47g/L的亮氨酸。结论:营养及环境因素对发酵生产L-亮氨酸具有重要影响。     

Formation of carotenoids by rhodotorula glutinis in whey ultrafiltrate

The growth and carotenoid biosynthesis of the yeast Rhodotorula glutinis was studied by cocultivation with Lactobacillus helveticus in cheese ultrafiltrate containing 3.9% and 7.1% lactose. By growing this mixed culture in a 15-L fermentor MBR AG (Switzerland) at an air flow rate of 0.5 L/L min and agitation at 220 rpm for 6 days, a total yield of carotenoids of 268 mug/g dry cells wasobtained. Carotenoids were formed almost parallel with the cell growth, anda maximum production was reached at an early stationary phase. A high-performance liquid chromatographic system (HPLC) permitting simultaneous determination of major carotenoid pigments was used. The three main pigments (torularhodin, beta-carotene, and torulene) were formed in Rhodotorula glutinis, and reached a maximum concentration as follows: 182.0, 43.9, 23.0 mug,g dry cells. (c) 1994 John Wiley & Sons, Inc.     

Inhibitory effect of carbon dioxide on the fed-batch culture of Ralstonia eutropha: evaluation by CO2 pulse injection and autogenous CO2 methods

In order to see the effect of CO(2) inhibition resulting from the use of pure oxygen, we carried out a comparative fed-batch culture study of polyhydroxybutyric acid (PHB) production by Ralstonia eutropha using air and pure oxygen in 5-L, 30-L, and 300-L fermentors. The final PHB concentrations obtained with pure O(2) were 138.7 g/L in the 5-L fermentor and 131.3 g/L in the 30-L fermentor, which increased 2.9 and 6.2 times, respectively, as compared to those obtained with air. In the 300-L fermentor, the fed-batch culture with air yielded only 8.4 g/L PHB. However, the maximal CO(2) concentrations in the 5-L fermentor increased significantly from 4.1% (air) to 15.0% (pure O(2)), while it was only 1.6% in the 30-L fermentor with air, but reached 14.2% in the case of pure O(2). We used two different experimental methods for evaluating CO(2) inhibition: CO(2) pulse injection and autogenous CO(2) methods. A 10 or 22% (v/v) CO(2) pulse with a duration of 3 or 6 h was introduced in a pure-oxygen culture of R. eutropha to investigate how CO(2) affects the synthesis of biomass and PHB. CO(2) inhibited the cell growth and PHB synthesis significantly. The inhibitory effect became stronger with the increase of the CO(2) concentration and pulse duration. The new proposed autogenous CO(2) method makes it possible to place microbial cells under different CO(2) level environments by varying the gas flow rate. Introduction of O(2) gas at a low flow rate of 0.42 vvm resulted in an increase of CO(2) concentration to 30.2% in the exit gas. The final PHB of 97.2 g/L was obtained, which corresponded to 70% of the PHB production at 1.0 vvm O(2) flow rate. This new method measures the inhibitory effect of CO(2) produced autogenously by cells through the entire fermentation process and can avoid the overestimation of CO(2) inhibition without introducing artificial CO(2) into the fermentor.     

Role of the entC gene in enterobactin and menaquinone biosynthesis in Escherichia coli

Tn10 mutants of Escherichia coli MC4100 were screened for their inability to grow under iron deficiency and for their inability to grow under anaerobiosis in the presence of fumarate as an electron acceptor. A strain so obtained (E. coli PBB1) lacked the ability to convert chorismic acid to isochorismic acid. This shows that the gene (entC) encoding isochorismate synthase was mutated. E. coli PBB1 did not produce any detectable amounts of menaquinones (vitamin K2) or enterobactin. When supplemented with isochorismic acid this strain produced menaquinones, indicating that isochorismic acid is involved not only in enterobactin but also in menaquinone biosynthesis. The entC gene was isolated and was shown to be part of the enterobactin gene cluster: It was located on a DNA fragment (9 kb in length) which also carried the entA gene. The DNA fragment was identified by restriction site mapping and was compared to a previously published map of the enterobactin gene cluster. The entC gene on this fragment responds not only to conditions (iron deficiency) that stimulate enterobactin biosynthesis but also to anaerobiosis which results in increased isochorismic acid formation and increased menaquinone biosynthesis. We conclude that isochorismic acid, isochorismic synthase, and the gene (entC) encoding this enzyme are involved in catalytic events at a metabolic branch point from which both enterobactin and menaquinones originate.     

Design,solid-phase synthesis and evaluation of enterobactin analogs for iron delivery into the human pathogen Campylobacter jejuni

The human enteropathogen Campylobacter jejuni, like many bacteria, employs siderophores such as enterobactin for cellular uptake of ferric iron. This transport process has been shown to be essential for virulence and presents an attractive opportunity for further study of the permissiveness of this pathway to small-molecule intervention and as inspiration for the development of synthetic carriers that may effectively transport cargo into Gram-negative bacteria. In this work, we have developed a facile and robust microscale assay to measure growth recovery of C. jejuni NCTC 11168 in liquid culture as a result of ferric iron uptake. In parallel, we have established the solid-phase synthesis of catecholamide compounds modeled on enterobactin fragments. Applying these methodological developments, we show that small synthetic iron chelators of minimal dimensions provide ferric iron to C. jejuni with equal or greater efficiency than enterobactin.     

A numerical evaluation of a hollow fiber extractive fermentor process for the production of ethanol

The economics of a process for the production of ethanol employing a hollow fiber extractive fermentor have been investigated. A computer simulation of the process incorporating a mathematical model of the fermentor was used to calculate the mass and energy balances. The results of the process simulation were read into a computer spreadsheet programmed with the economic calculations from which a final ethanol product cost was obtained. The process was found to be as competitive as conventional fermentation processes even at the currently high cost--$4/sq ft--of hollow fibers. It was determined that the 1986 price of 46.2 cents/L of ethanol produced by the process would be reduced by 1.8 cents/L for every $1/sq foot drop in the price of hollow fibers. A comparison of this process with conventional fermentation processes indicates that its potential savings lie in its ability to use a concentrated sugar feed, and the fermentor's increased productivity and ability to produce a concentrated ethanol stream which is removed by the extracting solvent.     

Iron transport in Salmonella typhimurium: mutants blocked in the biosynthesis of enterobactin

A number of mutants of Salmonella typhimurium were isolated which are blocked in the biosynthesis of enterobactin, an iron chelator that is secreted by the wild-type bacteria when they are grown on low iron media. One class of these enb mutants accumulates the enterobactin precursor 2,3-dihydroxybenzoic acid, and another class does not accumulate any detectable catechol precursor. The enb mutants grow very well on a glucose-mineral salts medium. Addition of citrate, itself an iron chelator, to the medium drastically inhibits growth unless the medium is supplemented with enterobactin or iron salts. Citrate inhibits iron uptake from the medium by enb mutants; enterobactin counteracts this inhibition and also, by itself, increases iron uptake. Thus, the apparent function of enterobactin is to promote the absorption of iron from the medium by the bacteria. Transduction experiments showed that the genes for enterobactin biosynthesis are closely linked on the S. typhimurium chromosome. It is suggested that they form an operon which is repressed by the presence of iron. S. typhimurium can utilize the iron chelate ferrichrome. (Deferriferrichrome is a cyclic hexapeptide that is produced by some fungi but not by S. typhimurium.) The enb mutants use ferrichrome as an effective growth factor.     

Large scale production and semi-purification of kedarcidin in a 1000-L fermentor

Summary Actinomycete strain ATCC 53650 was grown in a 1000-L fermentor containing 680 L of medium and the production of kedarcidin was monitored by HPLC. The titers of kedarcidin in the fermentor cultures were 0.49–0.53 mg ml^–1. A quick and efficient purification method involving the use of anion exchange resin DE23 (batch adsorption-desorption) and an ultrafiltration system yielded high recovery (65% yield) of kedarcidin from the fermentor culture. Over 200 grams of lyophilized kedarcidin of 70% purity was recovered from each of two 1000-L fermentor cultures using this process.     

Statistical optimization of culture conditions for bacterial cellulose production using Box-Behnken design

Culture conditions in a jar fermentor for bacterial cellulose (BC) production from A. xylinum BPR2001 were optimized by statistical analysis using Box-Behnken design. Response surface methodology was used to predict the levels of the factors, fructose (X1), corn steep liquor (CSL) (X2), dissolved oxygen (DO) (X3), and agar concentration (X4). Total 27 experimental runs by combination of each factor were carried out in a 10-L jar fermentor, and a three-dimensional response surface was generated to determine the effect of the factors and to find out the optimum concentration of each factor for maximum BC production and BC yield. The fructose and agar concentration highly influenced the BC production and BC yield. However, the optimum conditions according to changes in CSL and DO concentrations were predicted at almost central values of tested ranges. The predicted results showed that BC production was 14.3 g/L under the condition of 4.99% fructose, 2.85% CSL, 28.33% DO, and 0.38% agar concentration. On the other hand, BC yield was predicted in 0.34 g/g under the condition of 3.63% fructose, 2.90% CSL, 31.14% DO, and 0.42% agar concentration. Under optimized culture conditions, improvement of BC production and BC yield were experimentally confirmed, which increased 76% and 57%, respectively, compared to BC production and BC yield before optimizing the culture conditions.