Enhancement of glutathione production in a coupled system of adenosine deaminase-deficient recombinant Escherichia coli and Saccharomyces cerevisiae

Adenosine triphosphate (ATP) is necessary in the enzymatic production of glutathione (GSH). Our aim was to improve GSH production by increasing the efficiency of ATP regeneration in a coupled system. Previous results suggested that low GSH production in the coupled system is due to the irreversible transformation of adenosine (Ado) to hypoxanthine (Hx) via inosine (Ino) pathway in Escherichia coli JM109 (pBV03). In this study, to block the transformation of Ado into Hx and enhance GSH production, a coupled ATP regeneration system was constructed with adenosine deaminase-deficient recombinant E. coli JW1615 (pBV03) and Saccharomyces cerevisiae WSH2. GSH production was improved (2.94-fold of the control), and ATP regeneration reaction was established in the coupled system. The results are applicable to ATP regeneration in other microbial processes.     

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。     

Glycolytic pathway as an ATP generation system and its application to the production of glutathione and NADP

Efficient ATP generation is required to produce glutathione and NADP. Hence, the generation of ATP was investigated using the glycolytic pathway of yeast. Saccharomyces cerevisiae cells immobilized using polyacrylamide gel generated ATP from adenosine, consuming glucose and converting it to ethanol and carbon dioxide. Under optimal conditions, the ATP-generating activity of immobilized yeast cells was 7.0 μmol h^?1 ml^?1 gel. A column packed with these immobilized yeast cells was used for continuous ATP generation. The half-life of the column was 19 days at a space velocity of (SV) 0.3 h^?1 at 30°C. The properties of glutathione- and NADP-producing reactions coupled with the ATP-generating reaction were investigated. Escherichia coli cells with glutathione synthesizing activity and Brevibacterium ammoniagenes cells with NAD kinase activity were immobilized in a polyacrylamide gel lattice. Under optimal conditions, the immobilized E. coli cells and immobilized B. ammoniagenes cells produced glutathione and NADP at the rates of 2.1 and 0.65 μmol h^?1 ml^?1 gel, respectively, adding ATP to the reaction mixture. In order to produce glutathione and NADP economically and efficiently, the glutathione- and NADP-producing reactions were finally coupled with the ATP-generating reaction catalysed by immobilized S. cerevisiae cells. To compare the productivities of glutathione and NADP, and to compare the efficiency of ATP utilization for the production of these two compounds, the two reactor systems, co-immobilized cell system and mixed immobilized cell system, were designed. As a result, these two compounds were also found to be produced by these two kinds of reactor systems. Using the data obtained, the feasibility and properties of ATP generation by immobilized yeast cells are discussed in terms of the production of glutathione and NADP.     

Production of glutathione using a bifunctional enzyme encoded by gshF from Streptococcus thermophilus expressed in Escherichia coli

Glutathione (GSH) is one of the most ubiquitous non-protein thiols that is involved in numerous cellular activities. The gene coding for a novel bifunctional enzyme catalyzing the reaction for glutathione synthesis, gshF, was cloned from Streptococcus thermophilus SIIM B218 and expressed in Escherichia coli JM109. In the presence of the precursor amino acids and ATP, the induced cells of E. coli JM109 (pTrc99A-gshF) could accumulate 10.3 mM GSH in 5 h. The S. thermophilus GshF was insensitive to feedback inhibition caused by GSH even at 20 mM. At elevated concentrations of the precursor amino acids and ATP, E. coli JM109 (pTrc99A-gshF) produced 36 mM GSH with a molar yield of 0.9 mol/mol based on added cysteine and of 0.45 mol/mol based on added ATP. When ATP was replaced with glucose, E. coli JM109 (pTrc99A-gshF) produced 7 mM in 3 h. Saccharomyces cerevisiae was used to generate ATP for GSH production. In the presence of glucose and the pmr1 mutant of S. cerevisiae BY4742, JM109 (pTrc99A-gshF) produced 33.9 mM GSH in 12 h with a yield of 0.85 mol/mol based on added l-cysteine. It is shown that the S. thermophilus GshF can be successfully used for GSH production.     

Glutathione production by immobilized Saccharomyces cerevisiae cells containing an ATP regeneration system

Summary Whole cells of Saccharomyces cerevisiae were immobilized in polyacrylamide gel. Consuming glucose, the immobilized cells produced glutathione from its constituent amino acids, and glutathione produced was excreted out of the gels. The conditions for immobilization of the yeast cells and for glutathione production were studied. Based on these data, the properties and the feasibility of the glycolytic pathway as an ATP regeneration system were discussed in reference to glutathione production.     

Production of l-phenylalanine from trans-cinnamic acids by high-level expression of phenylalanine ammonia lyase gene from Rhodosporidium toruloides in Escherichia coli

A combined promoter expression vector pBV–PAL for high-level expression of phenylalanine ammonia lyase gene of Rhodosporidium toruloides was constructed. Pal gene was cloned and inserted into the region between SalI and PstI restriction sites of expression vector pBV220 (containing P_LP_R promoter) to obtain recombinant expression vector pBV220–PAL. The tac promoter obtained from the plasmid pKtac was inserted into the expression vector pBV220–PAL to construct expression vector pBV–PAL. The recombinant plasmid pBV220–PAL and pBV–PAL were introduced into Escherichia coli JM109 by transformation. The result showed that the transformant E. coli JM109 (pBV–PAL) gave a much higher PAL activity than that transformant E. coli JM109 (pBV220–PAL). Recombinant PAL expression level of the transformant JM109 (pBV–PAL) was about 9.6% of total cellular protein, specific enzyme activity was 2.3-fold higher than that of the transformant JM109 (pBV220–PAL), reached 35 U/g (dry cells weight, DCW). PAL specific activity of 123 U/g (DCW) could be achieved in a 5-l fermentor. 80.5% conversion rate of trans-cinnamic acid to l-phenylalanine and 5.12 g/l l-phenylalanine were obtained after 3 h bioconversion using the transformant JM109 (pBV–PAL). The recombinant strain JM109 containing the combined promoter expression vector pBV–PAL was shown to be effective and practical to product l-phenylalanine.     

Elevated glutathione production by adding precursor amino acids coupled with ATP in high cell density cultivation of Candida utilis

Aims: Three precursor amino acids and adenosine triphosphate ( ATP) are necessary for fermentative production of glutathione. In this study, our aims were to develop a strategy to enhance glutathione production by adding three precursor amino acids coupled with ATP in high cell density (HCD) cultivation of Candida utilis. Methods and Results: A high-glutathione yeast strain, C. utilis WSH 02-08, was used in this study. Whole fermentative process for glutathione production was divided into two phases of cell growth and glutathione synthesis. Cells concentration was increased by HCD cultivation. Meanwhile, intracellular glutathione content was enhanced by the addition of three precursor amino acids. Concentrations of three precursor amino acids added at stationary phase were optimized by response surface methodology. Moreover, the addition of ATP 15 h after the addition of the three amino acids can further enhance glutathione production. Based on aforementioned phenomenon, a strategy of adding three precursor amino acids coupled with ATP was developed to enhance glutathione production. Conclusion: Without the addition of three precursor amino acids and the ATP, a total glutathione of 1123 mg l⁻¹ was achieved after 60-h cultivation. In comparison, addition of three precursor amino acid counterparts resulted in a total glutathione of 1841 mg l⁻¹. Moreover, by adding amino acids combined with ATP, a total glutathione of 2043 mg l⁻¹ was achieved after 72-h cultivation, increased by 81·9% and 11%, respectively, as compared with the control and the one without ATP addition. Significance and Impact of the Study: This is the first report on investigating changes of the intracellular three precursor amino acids and ATP, and γ-glutamylcysteine synthase activity in HCD cultivation of C. utilis for glutathione production. A strategy of combining addition of three precursor amino acids with ATP was developed to enhance glutathione production in C. utilis.     

Bioaugmentation of the decolorization rate of acid red GR by genetically engineered microorganism <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109 (pGEX-AZR)

The study showed that the genetically engineered microorganism (GEM) bioaugment successfully the dye wastewater biotreatment systems to enhance acid red GR (ARGR) removal. Escherichia coli JM109 (pGEX-AZR) was the GEM with higher azoreductase activity. The kinetics of the ARGR decolorization by the E. coli JM109 (pGEX-AZR) agreed with Andrews model. The kinetic parameters, r _dye,max, K _s and K _i , were found to be 42.45 mg g⁻¹ h⁻¹, 584.93 mg L⁻¹ and 556.89 mg L⁻¹, respectively. The E. coli JM109 (pGEX-AZR) was tested in anaerobic sequencing batch reactors (AnSBR) in order to enhance the ARGR decolorization. The decolorization rate of ARGR was affected by the amount of E. coli JM109 (pGEX-AZR) inoculation and the best amount of inoculation was 10%. The continuous operations of the four bioreactors with different E. coli JM109 (pGEX-AZR) immobilization supports showed that the E. coli JM109 (pGEX-AZR) could bioaugment decolorization in AnSBRs with suspended and immobilized on macroporous foam carriers. For 42 days continuous operation in the AnSBRs, both the tolerance to ARGR concentration shock and the decolorization rate in these two bioaugmented AnSBRs are higher than those of the other two systems, control system and bioaugmented AnSBRs system with the sodium-alginate immobilized cells, the decolorization rate reached 90%. Changes in microbial community were detected by ribosomal intergenic spacer analysis (RISA) and amplified ribosomal DNA restriction analysis (ARDRA), which revealed that the introduced E. coli JM109 (pGEX-AZR) was persistent in the augmented systems and maintained higher metabolic activity.     

Degradation of 5′ adenosine monophosphate in a cell-free system ofEscherichia coli

Sonicated cells ofEscherichia coli contain an enzyme system degrading 5′ adenosine monophosphate (5′ AMP) to hypoxanthine. This enzyme system is located in the fraction sedimenting at 20,000 xg. It has a pH optimum at 8.0. In the fraction sedimenting at 20,000 xg the enzyme activity was inhibited by adenosine triphosphate (ATP). Adenosine and adenine are deaminated by this enzyme preparation to inosine and to hypoxanthine, these activities not being inhibited by ATP.     

Degradation of trichloroethylene by recombinant E. coli in continuous culture

Trichloroethylene (TCE) degradation by the recombinant E. coli JM109 harboring a TCE-degradative plasmid (pIO720 or pIO72K) in continuous culture was studied. The ampicillin-resistant plasmid, pIO720, contained the cumene dioxygenase genes and the dimethyl sulfide monooxygenase genes. pIO72K was constructed according to replacement of an ampicillin resistance gene on pIO720 by a kanamycin resistance gene. In the case of E. coli JM109 (pIO720) in continuous culture, TCE degradation activity decreased rapidly after continuous culture started, and the remaining number of host cells harboring pIO720 also decreased rapidly. In the case of E. coli JM109 (pIO72K) in continuous culture, TCE degradation activity was stable during continuous culture for at least 300 h and the number of the host cells harboring pIO72K did not decrease. TCE degradation activity of E. coli JM109 (pIO72K) was the highest at a dilution rate of 0.2 h^–1.     

Glutathione production by efficient ATP-regenerating Escherichia coli mutants

There is an ongoing demand to improve the ATP-regenerating system for industrial ATP-driven bioprocesses because of the low efficiency of ATP regeneration. To address this issue, we investigated the efficiency of ATP regeneration in Escherichia coli using the Permeable Cell Assay. This assay identified 40 single-gene deletion strains that had over 150% higher total cellular ATP synthetic activity relative to the parental strain. Most of them also showed higher ATP-driven glutathione synthesis. The deleted genes of the identified strains that showed increased efficiency of ATP regeneration for glutathione production could be divided into the following four groups: (1) glycolytic pathway-related genes, (2) genes related to degradation of ATP or adenosine, (3) global regulatory genes, and (4) genes whose contribution to the ATP regeneration is unknown. Furthermore, the high glutathione productivity of Δ nlpD , the highest glutathione-producing mutant strain, was due to its reduced sensitivity to the externally added ATP for ATP regeneration. This study showed that the Permeable Cell Assay was useful for improving the ATP-regenerating activity of E. coli for practical applications in various ATP-driven bioprocesses, much as that of glutathione production.     

Enzymatic glutathione production using metabolically engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> as a whole-cell biocatalyst

We developed a novel enzymatic glutathione (GSH) production system using Saccharomyces cerevisiae as a whole-cell biocatalyst, and improved its GSH productivity by metabolic engineering. We demonstrated that the metabolic engineering of GSH pathway and ATP regeneration can significantly improve GSH productivity by up to 1.7-fold higher compared with the parental strain, respectively. Furthermore, the combination of both improvements in GSH pathway and ATP regeneration is more effective (2.6-fold) than either improvement individually for GSH enzymatic production using yeast. The improved whole-cell biocatalyst indicates its great potential for applications to other kinds of ATP-dependent bioproduction.     

Extension of Chronological Lifespan by ScEcl1 Depends on Mitochondria in Saccharomyces cerevisiae

We constructed two plasmids that have a strong tac promoter and a structural gene for tryptophanase of Enterohacter aerogenes SM-18 (pKT901EA) or Escherichia coli K-12 (pKT951EC). The tryptophanase activity of E. coli JM109 transformed with pKT90lEA (JM109/pKT901EA) was inducible with isopropyl-β-D-thiogalactopyranoside, and 3.6 times higher than that of E. aerogenes SM-18. Cells of JM109/pKT901EA induced for tryptophanase synthesized L-tryptophan from indole, ammonia, and pyruvate more efficiently than E. aerogenes SM-18. Although JM109/pKT951EC expressed a similar level of tryptophanase activity to that of JM109/pKT901EA, the synthesis of L-tryptophan by the cells of JM109/pKT951EC did not proceed well compared with JM109/pKT901EA. Tryptophanases from E. aerogenes and E. coli K-12 were purified, and their properties were investigated. The purified E. aerogenes tryptophanase showed higher stability against heat inactivation than E. coli tryptophanase.     

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.     

Comparison of optimal conditions for mass production of carboxymethylcellulase by <Emphasis Type="Italic">Escherichia coli</Emphasis> JM109/A-68 with other recombinants in pilot-scale bioreactor

The optimal conditions for mass production of carboxymethylcellulase (CMCase) by E. coli JM109/A-68 were investigated and compared with other E. coli JM109 recombinants producing CMCase. The optimal agitation speed and aeration rate for cell growth of E. coli JM109/A- 68 were 500 rpm and 0.50 vvm in a 7 L bioreactor, whereas those for production of CMCase were 416 rpm and 0.95 vvm. The optimal vessel pressures for cell growth as well as production of CMCase in a 100 L bioreactor were 0.04 MPa. The maximal production of CMCase by E. coli JM109/A-68 under the optimized conditions in a 100 L bioreactor was 11.0 times higher than its wild type, B. velezensis A-68. Optimal conditions for mass production of CMCase by recombinants were different from those for wild strains. The higher production of CMCase by E. coli JM109/A-68 and other recombinant of E. coli seemed to result from its higher cell growth under the optimal conditions for dissolved oxygen and its mixed-growth associated production pattern compared to the growthassociated production of B. velezensis A-68.     

多聚磷酸盐激酶双底物通道腔的理性设计及其在无细胞催化生产谷胱甘肽中的应用

三磷酸腺苷(adenosine triphosphate,ATP)是一种重要的辅助因子,参与许多需能的生物催化反应。多聚磷酸盐激酶(polyphosphate kinases,PPK)由于其底物聚磷酸盐廉价易得,可以为消耗ATP的反应提供能量。本研究选择哈氏噬纤维菌(Cytophaga hutchinsonii)来源的ChPPK,进行了底物谱和耐受性分析,通过分子对接和定点突变,理性改造多聚磷酸盐激酶的双底物通道腔来提高PPK酶的催化活性。与野生型相比,筛选得到突变体ChPPK_K81H-K103V的相对酶活提高了326.7%,同时,双突变扩大了ChPPK的底物利用范围与耐受性,提高了该酶的耐热性与耐碱性。基于该ATP再生系统,本研究偶联谷胱甘肽双功能酶GshAB和ChPPK_K81H-K103V,破细胞后采用无细胞催化生产谷胱甘肽,加入5 mmol/L ATP后,该体系6 h可以生产(25.4±1.9) mmol/L的谷胱甘肽,比突变前的催化体系提高了41.9%。优化无细胞催化体系的缓冲液、裂解液菌体量、补料时间后,无细胞体系可产生(45.2±1.8) mmol/L谷胱甘肽,底物l-半胱氨酸的转化率达到90.4%。提高ChPPK生产ATP的能力,可有效增强底物的转化率,降低催化成本,实现了无细胞催化生产谷胱甘肽的高产量、高转化率与高经济价值的统一。本研究提供了一种绿色高效的ATP再生系统,可为消耗ATP的生物催化反应平台提供可持续动力。     

Significantly enhanced production of recombinant nitrilase by optimization of culture conditions and glycerol feeding

The production of a recombinant nitrilase expressed in Escherichia coli JM109/pNLE was optimized in the present work. Various culture conditions and process parameters, including medium composition, inducer, induction condition, pH and temperature, were systematically examined. The results showed that nitrilase production in E. coli JM109/pNLE was greatly affected by the pH condition and the temperature in batch culture, and the highest nitrilase production was obtained when the fermentation was carried out at 37°C, initial pH 7.0 without control and E. coli was induced with 0.2 mM isopropyl-β-d-thiogalactoside at 4.0 h. Furthermore, enzyme production could be significantly enhanced by adopting the glycerol feeding strategy with lower flow rate. The enzyme expression was also authenticated by sodium dodecyl phosphate polyacrylamide gel electrophoresis analysis. Finally, under the optimized conditions for fed-batch culture, cell growth, specific activity and nitrilase production of the recombinant E. coli were increased by 9.0-, 5.5-, and 50-fold, respectively.     

Glutathione: a review on biotechnological production

This Mini-Review summarizes the historic developments and technological achievements in the biotechnological production of glutathione in the past 30 years. Glutathione is the most abundant non-protein thiol compound present in living organisms. It is used as a pharmaceutical compound and can be used in food additives and the cosmetic industries. Glutathione can be produced using enzymatic methods in the presence of ATP and its three precursor amino acids (l-glutamic acid, l-cysteine, glycine). Alternatively, glutathione can be produced by direct fermentative methods using sugar as a starting material. In the latter method, Saccharomyces cerevisiae and Candida utilis are currently used to produce glutathione on an industrial scale. At the molecular level, the genes gshA and gshB, which encode the enzymes -glutamylcysteine synthetase and glutathione synthetase, respectively, have been cloned from Escherichia coli and over-expressed in E. coli, S. cerevisiae, and Lactococcus lactis. It is anticipated that, with the design and/or discovery of novel producers, the biotechnological production of glutathione will be further improved to expand the application range of this physiologically and medically important tripeptide.     

Fermentative glycolysis with purified Escherichia coli enzymes for in vitro ATP production and evaluating an engineered enzyme

Each of the twelve enzymes for glycolytic fermentation, eleven from Escherichia coli and one from Saccharomyces cerevisiae, have been over-expressed in E. coli and purified with His-tags. Simple assays have been developed for each enzyme and they have been assembled for fermentation of glucose to ethanol. Phosphorus-31 NMR revealed that this in vitro reaction accumulates fructose 1,6-bisphosphate while recycling the cofactors NAD⁺ and ATP. This reaction represents a defined ATP-regeneration system that can be tailored to suit in vitro biochemical reactions such as cell-free protein synthesis. The enzyme from S. cerevisiae, pyruvate decarboxylase 1 (Pdc1; EC 4.1.1.1), was identified as one of the major ‘flux controlling’ enzymes for the reaction and was replaced with an evolved version of Pdc1 that has over 20-fold greater activity under glycolysis reaction conditions. This substitution was only beneficial when the ratio of glycolytic enzymes was adjusted to suit greater Pdc1 activity.     

Production of glucose-6-phosphate by glucokinase coupled with an ATP regeneration system

A process of glucose-6-phosphate (G-6-P) production coupled with an adenosine triphosphate (ATP) regeneration system was constructed that utilized acetyl phosphate (ACP) via acetate kinase (ACKase). The genes glk and ack from Escherichia coli K12 were amplified and cloned into pET-28a(+), then transformed into E. coli BL21 (DE3) and the recombinant strains were named pGLK and pACK respectively. Glucokinase (glkase) in pGLK and ACKase in pACK were both overexpressed in soluble form. G-6-P was efficiently produced from glucose and ACP using a very small amount of ATP. The conversion yield was greater than 97 % when the reaction solution containing 10 mM glucose, 20 mM ACP-Na₂, 0.5 mM ATP, 5 mM Mg²⁺, 50 mM potassium phosphate buffer (pH 7.0), 4.856 U glkase and 3.632 U ACKase were put into 37 °C water bath for 1 h.