Enhancement of glutathione production by altering adenosine metabolism of Escherichia coli in a coupled ATP regeneration system with Saccharomyces cerevisiae

Aims: Adenosine triphosphate (ATP) during the enzymatic production of glutathione is necessary. In this study, our aims were to investigate the reason for low glutathione production in Escherichia coli coupled with an ATP regeneration system and to develop a new strategy to improve the system. Methods and Results: Glutathione can be synthesized by enzymatic methods in the presence of ATP and three precursor amino acids (l ‐glutamic acid, l ‐cysteine and glycine). In this study, glutathione was produced from E. coli JM109 (pBV03) coupled with an ATP regeneration system, by using glycolytic pathway of Saccharomyces cerevisiae WSH2 as ATP regenerator from adenosine and glucose. In the coupled system, adenosine used for ATP regeneration by S. cerevisiae WSH2 was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03). As a consequence, S. cerevisiae WSH2 could not obtain enough adenosine for ATP regeneration in the glycolytic pathway in spite of consuming 400 mmol l^?1 glucose within 1 h. By adding adenosine deaminase inhibitor to block the metabolism from adenosine to hypoxanthine, glutathione production (8·92 mmol l^?1) enhanced 2·74‐fold in the coupled system. Conclusions: This unusual phenomenon that adenosine was transformed into hypoxanthine irreversibly by E. coli JM109 (pBV03) revealed that less glutathione production in the coupled ATP regeneration system was because of the poor efficiency of ATP generation. Significance and Impact of the Study: The results presented here provide a strategy to improve the efficiency of the coupled ATP regeneration system for enhancing glutathione production. The application potential can be microbial processes where ATP is needed.     

Efficient production of glutathione in Saccharomyces cerevisiae via a synthetic isozyme system

Glutathione, a tripeptide consisting of cysteine, glutamic acid, and glycine, has multiple beneficial effects on human health. Previous studies have focused on producing glutathione in Saccharomyces cerevisiae by overexpressing γ-glutamylcysteine synthetase (GSH1) and glutathione synthetase (GSH2), which are the rate-limiting enzymes involved in the glutathione biosynthetic pathway. However, the production yield and titer of glutathione remain low due to the feedback inhibition on GSH1. To overcome this limitation, a synthetic isozyme system consisting of a novel bifunctional enzyme (GshF) from Gram-positive bacteria possessing both GSH1 and GSH2 activities, in addition to GSH1/GSH2, was introduced into S. cerevisiae, as GshF is insensitive to feedback inhibition. Given the HSP60 chaperonin system mismatch between bacteria and S. cerevisiae, co-expression of Group-I HSP60 chaperonins (GroEL and GroES) from Escherichia coli was required for functional expression of GshF. Among various strains constructed in this study, the SKSC222 strain capable of synthesizing glutathione with the synthetic isozyme system produced 240 mg L^-1 glutathione with glutathione content and yield of 4.3% and 25.6 mg_glutathione/g_glucose, respectively. These values were 6.6-, 4.9-, and 4.3-fold higher than the corresponding values of the wild-type strain. In a glucose-limited fed-batch fermentation, the SKSC222 strain produced 2.0 g L^-1 glutathione in 67 h. Therefore, this study highlights the benefits of the synthetic isozyme system in enhancing the production titer and yield of value-added chemicals by engineered strains of S. cerevisiae.     

Purification and properties of Saccharomyces cerevisiae acetolactate synthase from recombinant Escherichia coli

The yeast ilv2 gene, encoding acetolactate synthase, was subcloned in an Escherichia coli expression vector. Although a major part of the acetolactate synthase synthesized by E. coli cells harbouring this vector was packaged into protein inclusion bodies, we used these recombinant E. coli cells to produce large quantities of the yeast enzyme. The yeast acetolactate synthase was purified to homogeneity using first streptomycin and ammonium sulfate precipitations, followed by T-gel thiophilic interaction, Sephacryl S-300 gel filtration, Mono Q anion exchange, and Superose 12 gel filtration chromatography. SDS/PAGE and gel filtration of the purified enzyme showed that it is a dimer composed of two subunits, each with the molecular mass of 75 kDa. The purified yeast acetolactate synthase was further characterized with respect to pH optimum, dependence of the substrate, pyruvate, and requirements of the cofactors, thiamin diphosphate, Mg2+, and FAD.     

Heat shock-regulated production of Escherichia coli beta-galactosidase in Saccharomyces cerevisiae.

The HSP90 gene of the yeast Saccharomyces cerevisiae encodes a heat shock-inducible protein with an Mr of 90,000 (hsp90) and unknown function. We fused DNA fragments of a known sequence (namely, either end of a 1.4-kilobase EcoRI fragment which contains the S. cerevisiae TRP1 gene) to an EcoRI site within the coding sequence of the HSP90 gene. When these fusions are introduced into S. cerevisiae they direct the synthesis of unique truncated hsp90 proteins. By determining the size and charge of these proteins we were able to deduce the translational reading frame at the (EcoRI) fusion site. This information allowed us to design and construct a well-defined in-frame fusion between the S. cerevisiae HSP90 gene and the Escherichia coli lacZ gene. When this fused gene is introduced into S. cerevisiae on a multicopy plasmid vector, it directs the heat shock-inducible synthesis of a fused protein, which is an enzymatically active beta-galactosidase. Thus, for the first time, it is possible to quantitate the heat shock response in a eucaryotic organism with a simple enzyme assay.     

Production, purification, and luminometric analysis of recombinant Saccharomyces cerevisiae MET3 adenosine triphosphate sulfurylase expressed in Escherichia coli

ATP sulfurylase cDNA from MET3 on chromosome X of Saccharomyces cerevisiae was amplified and cloned, and recombinant ATP sulfurylase was expressed in Escherichia coli. The synthesis of ATP sulfurylase was directed by an expression system that employs the regulatory genes of the luminous bacterium Vibrio fischeri. A soluble, biologically active form was purified to electrophoretic homogeneity from lysates of recombinant E. coli by ammonium sulfate fractionation, ion-exchange chromatography, and gel filtration. The specific activity of the purified enzyme was estimated to 140 U/mg. The apparent molecular mass of the recombinant enzyme was determined by gel filtration to be 470 kDa, which indicates that the active enzyme is an octamer of identical subunits (the molecular mass of a single subunit is 59.3 kDa). The ATP sulfurylase activity was monitored in real time by a very sensitive bioluminometric method.     

Ethanol production by In situ xylose isomerization using recombinant Escherichia coli and fermentation using conventional Saccharomyces cerevisiae

Xylose isomerase from Geobacillus kaustophilus HTA426 was functionally expressed in Escherichia coli BL21 (DE3) and the recombinant E. coli cells were used together with conventional Saccharomyces cerevisiae to produce ethanol from xylose by simultaneous xylose isomerisation and fermentation. When recombinant E. coli cells were used as the source of xylose isomerase, a significant amount of ethanol was produced from xylose, whereas the control without recombinant E. coli cells did not produce any detectable amount of ethanol from xylose. Ethanol production was increased by 38% by feeding more recombinant E. coli at 48 h compared to adding recombinant E. coli only in the beginning, resulting in more ethanol production than P. stipitis CBS6054 under the same conditions. The xylitol accumulation by the in situ process was only 57% of that produced by the P. stipitis CBS6054.     

Enhancement of 5-aminolevulinate production with recombinant Escherichia coli using batch and fed-batch culture system

5-Aminolevulinate (ALA) production with recombinant Escherichia coli Rosetta (DE3)/pET28a(+)-hemA was studied. In batch fermentation, the addition of glucose and glycine was effective to improve ALA production. Then the fed-batch fermentation was conducted with continuous feeding of precursors. When the concentrations of succinic acid and glycine were 7.0 g/l and 4.0 g/l, respectively, in the feeding, the ALA yield reached 4.1g/l. But the molar yield (ALA/glycine) was decreased in the fed-batch fermentation compared to batch fermentation. And it was found that the pH control during fed-batch cultivation was very important for the cell growth and ALA production. A two-stage pH value controlling strategy was suggested, in which, the pH value in the first 6h was regulated at pH 5.9, after then at pH 6.2, and the ALA yield was as high as 6.6g/l via fed-batch fermentation.     

重组大肠杆菌生产谷胱甘肽发酵条件的研究

研究了重组Ｅ．Ｃｏｌｉ产ＧＳＨ的发酵条件,重点考察了添加酵母膏、前体氨基酸和ＡＴＰ的影响。结果发现,前体氨基酸和ＡＴＰ均能促进胞内ＧＳＨ的积累,若在发酵０ｈ和１２ｈ分别加入２０ｇ／ＬＡＴＰ和９ｍｍｏｌ／Ｌ前体氨基酸,则细胞干重和胞内ＧＳＨ含量可分别比对照提高２４％和１４倍。应用正交试验得出的针对细胞干重和ＧＳＨ总量的最佳组合,最大细胞干重和ＧＳＨ总量比原试验中的最好结果分别提高了１０％和２６％。在分析了该菌对葡萄糖利用情况的基础上,对该菌进行了指数流加培养,２５ｈ细胞干重与发酵液内ＧＳＨ总量分别达到８０ｇ／Ｌ和８８０ｍｇ／Ｌ,比摇瓶最好结果分别提高了８３和４６倍。     

Enhancement of recombinant protein production in Escherichia coli by coproduction of aspartase

As commonly recognized, the excretion of acetate by the aerobic growth of Escherichia coli on glucose is a manifestation of imbalanced flux between glycolysis and the tricarboxylic acid (TCA) cycle. Accordingly, this may restrict the production of recombinant proteins in E. coli, due to the limited amounts of precursor metabolites produced in TCA cycle. To approach this issue, an extra supply of intermediate metabolites in TCA cycle was made by conversion of aspartate to fumarate, a reaction mediated by the activity of L-aspartate ammonia-lyase (aspartase). As a result, in the glucose minimal medium containing aspartate, the production of two recombinant proteins, beta-galactosidase and green fluorescent protein, in the aspartase-producing strain was substantially increased by 5-fold in association with 30-40% more biomass production. This preliminary study illustrates the great promise of this approach used to enhance the production of these two recombinant proteins.     

Evolution of a Saccharomyces cerevisiae metabolic pathway in Escherichia coli

The Saccharomyces cerevisiae glycerol pathway (GPD1 and GPP2) was evolved in vivo in Escherichia coli. The central metabolism of E. coli was engineered to link glucose consumption and glycerol production. The engineered strain was evolved in a chemostat culture and a high glycerol producer was rapidly obtained. The evolution of the strain was associated to a deletion between GPD1 and GPP2, resulting in the production of a fusion protein with both glycerol-3-P dehydrogenase and glycerol-3-P phosphatase activities. The higher efficiency of the fusion protein was due to partial glycerol-3-P channeling between the two active sites. The evolved strain produces glycerol from glucose at high yield, concentration and productivity.     

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。     

Medium optimization for glutathione production by Saccharomyces cerevisiae

Glucose, peptone and magnesium sulphate were found to be suitable components for the cell growth and glutathione (GSH) production in the yeast strain. Saccharomyces cerevisiae CCRC 21727. The Box–Behnken design and response surface methodology were employed to derive a statistical model to investigate the effects of glucose, peptone and magnesium sulphate concentrations on GSH production. Neural networks were compared with a second-order-polynomial model in predicting the effects of component concentrations on the production of GSH and dry cell weight (DCW). Neural network models can predict cell growth and GSH production more precisely than second-order-response-surface models.     

Expression of a Saccharomyces cerevisiae photolyase gene in Escherichia coli.

A 3.3-kilobase PvuII fragment carrying the PHR1 gene of Saccharomyces cerevisiae has been cloned into an Escherichia coli expression vector and introduced into E. coli strains deficient in DNA photolyase. Complementation of the E. coli phr-1 mutation was observed, strongly suggesting that the yeast PHR1 gene encodes a DNA photolyase.     

Polyhydroxyalkanoate production in recombinant Escherichia coli

Abstract The bacterial species Escherichia coli has proven to be a powerful tool in the molecular analysis of polyhydroxyalkanoate (PHA) biosynthesis. In addition, E. coli holds promise as a source for economical PHA production. Using this microorganism, clones have been developed in our laboratory which direct the synthesis of poly-β-hydroxybutyrate (PHB) to levels as high as 95% of the cell dry weight. These clones have been further enhanced by the addition of a genetically mediated lysis system that allows the PHB granules to be released gently and efficiently. This paper describes these developments, as well as the use of an E. coli strain to produce the copolymer poly-(3-hydroxybutyrate- co -3-hydroxyvalerate (PHB- co -3-).     

Metabolism of D-aminoacyl-tRNAs in Escherichia coli and Saccharomyces cerevisiae cells

In Escherichia coli, tyrosyl-tRNA synthetase is known to esterify tRNA(Tyr) with tyrosine. Resulting d-Tyr-tRNA(Tyr) can be hydrolyzed by a d-Tyr-tRNA(Tyr) deacylase. By monitoring E. coli growth in liquid medium, we systematically searched for other d-amino acids, the toxicity of which might be exacerbated by the inactivation of the gene encoding d-Tyr-tRNA(Tyr) deacylase. In addition to the already documented case of d-tyrosine, positive responses were obtained with d-tryptophan, d-aspartate, d-serine, and d-glutamine. In agreement with this observation, production of d-Asp-tRNA(Asp) and d-Trp-tRNA(Trp) by aspartyl-tRNA synthetase and tryptophanyl-tRNA synthetase, respectively, was established in vitro. Furthermore, the two d-aminoacylated tRNAs behaved as substrates of purified E. coli d-Tyr-tRNA(Tyr) deacylase. These results indicate that an unexpected high number of d-amino acids can impair the bacterium growth through the accumulation of d-aminoacyl-tRNA molecules and that d-Tyr-tRNA(Tyr) deacylase has a specificity broad enough to recycle any of these molecules. The same strategy of screening was applied using Saccharomyces cerevisiae, the tyrosyl-tRNA synthetase of which also produces d-Tyr-tRNA(Tyr), and which, like E. coli, possesses a d-Tyr-tRNA(Tyr) deacylase activity. In this case, inhibition of growth by the various 19 d-amino acids was followed on solid medium. Two isogenic strains containing or not the deacylase were compared. Toxic effects of d-tyrosine and d-leucine were reinforced upon deprivation of the deacylase. This observation suggests that, in yeast, at least two d-amino acids succeed in being transferred onto tRNAs and that, like in E. coli, the resulting two d-aminoacyl-tRNAs are substrates of a same d-aminoacyl-tRNA deacylase.     

Optimization of the medium for glutathione production in Saccharomyces cerevisiae

As a powerful statistical experimental design, uniform design (UD) method has been successfully applied in various fields such as fermentation industry, pharmaceuticals, and others. In this paper, UD was applied to optimize the medium composition for glutathione production in shake-flask culture of Saccharomyces cerevisiae T65. The experiments of nine factors (glucose, yeast extract, peptone, malt extract, molasses, MgSO₄, ZnSO₄, (NH₄)₂HPO₄ and thiamine) and nine levels were carried out according to the uniform design table U₂₇(9⁹). The experimental data was analyzed to obtain the regression model and the optimal medium composition was achieved by optimization with UD 3.0 software. The optimal medium consisted of 70 g/L glucose, 3 g/L yeast extract, 5 g/L peptone, 70 g/L malt extract, 20 g/L molasses, 5.6 g/L MgSO₄, 16 mg/L ZnSO₄, 7 g/L (NH₄)₂HPO₄ and 0.2 mg/L thiamine. The GSH yield at the optimal point achieved 74.6 mg/L, which was 1.81 times higher than that of the control. The application of UD method resulted in enhancement in GSH production.     

Continuous production of glutathione by immobilized Saccharomyces cerevisiae cells

Summary Glutathione was continuously produced by an immobilized Saccharomyces cerevisiae IFO 2044 cell column. The production of glutathione was strongly influenced by the level of activity of the glycolytic pathway. This activity was maintained constant by the addition of NAD.Abbreviations ADP adenosine-5-diphosphate - ATP adenosine-5-triphosphate - NAD nicothinamide adenine dinucleotide     

Enhancement of extracellular glucose oxidase production in pH-stat feed-back controlled fed-batch culture of recombinant Saccharomyces cerevisiae

Glucose oxidase (GOD) from Aspergillus niger was expressed in Saccharomyces cerevisiae under the regime of GAL-10 promoter and GAL-7 terminator of S. cerevisiae and -amylase signal sequence of Aspergillus oryzae. The enhancement of the expression level was achieved in pH-stat feed-back controlled fed-batch culture. The highest titre of extracellular GOD was 199 U/ml which marked two fold improvement over the batch (95 U/ml) and 28% above that of non-feed back controlled fed-batch (154 U/ml) operation. © Rapid Science Ltd. 1998