Enhanced production of D-(-)-3-hydroxybutyric acid by recombinant Escherichia coli

Wild-type bacteria including Escherichia coli normally do not produce extracellular D-(-)-3-hydroxybutyric acid (3HB). To produce extracellular chiral 3HB, a new pathway for synthesis of 3HB was constructed by simultaneous expression of genes of beta-ketothiolase (phbA), acetoacetyl-CoA reductase (phbB), phosphor-transbutyrylase (ptb) and butyrate kinase (buk) in E. coli strain DH5alpha. E. coli DH5alpha containing any one of the four plasmids pBHR69, pUCAB, p68CM or pKKAB that harbor the phbA and phbB genes produced small amounts of 3HB, ranging from 75 to 400 mg l(-1), while E. coli DH5alpha harboring p68CMPTK containing genes of phbA, phbB, ptb and buk increased the 3HB concentration to 1.4 g l(-1) in shake flasks supplemented with LB broth and 20 g l(-1) glucose. 3HB production was further improved to over 2 g l(-1) in shake flasks when E. coli DH5alpha hosted two plasmids simultaneously that separately contained phbA and phbB in one plasmid while ptb and buk in the other. A batch fermentation run in a 5-l fermenter produced approximately 5 g l(-1) 3HB after 24 h. A fed-batch process increased 3HB production to 12 g l(-1) after 48 h of fermentation.     

Efficient production of polylactic acid and its copolymers by metabolically engineered Escherichia coli

Polylactic acid (PLA) is one of the promising biodegradable polymers, which has been produced in a rather complicated two-step process by first producing lactic acid by fermentation followed by ring opening polymerization of lactide, a cyclic dimer of lactic acid. Recently, we reported the production of PLA and its copolymers by direct fermentation of metabolically engineered Escherichia coli equipped with the evolved propionate CoA-transferase and polyhydroxyalkanoate (PHA) synthase using glucose as a carbon source. When employing these initially constructed E. coli strains, however, it was necessary to use an inducer for the expression of the engineered genes and to feed succinate for proper cell growth. Here we report further metabolic engineering of E. coli strain to overcome these problems for more efficient production of PLA and its copolymers. This allowed efficient production of PLA and its copolymers without adding inducer and succinate. The finally constructed recombinant E. coli JLXF5 strain was able to produce P(3HB-co-39.6 mol% LA) having the molecular weight of 141,000 Da to 20 g l⁻¹ with a polymer content of 43 wt% in a chemically defined medium by the pH-stat fed-batch culture.     

Production of succinic acid from sucrose and sugarcane molasses by metabolically engineered Escherichia coli

Sucrose-utilizing genes (cscKB and cscA) from Escherichia coli KO11 were cloned and expressed in a metabolically engineered E. coli KJ122 to enhance succinate production from sucrose. KJ122 harboring a recombinant plasmid, pKJSUC, was screened for the efficient sucrose utilization by growth-based selection and adaptation. KJ122-pKJSUC-24T efficiently utilized sucrose in a low-cost medium to produce high succinate concentration with less accumulation of by-products. Succinate concentrations of 51 g/L (productivity equal to 1.05 g/L/h) were produced from sucrose in anaerobic bottles, and concentrations of 47 g/L were produced in 10 L bioreactor within 48 h. Antibiotics had no effect on the succinate production by KJ122-pKJSUC-24T. In addition, succinate concentrations of 62 g/L were produced from sugarcane molasses in anaerobic bottles, and concentrations of 56 g/L in 10 L bioreactor within 72 h. These results demonstrated that KJ122-pKJSUC-24T would be a potential strain for bio-based succinate production from sucrose and sugarcane molasses.     

以葡萄糖为唯一碳源合成聚-4-羟基丁酸的重组大肠杆菌的构建

为实现重组大肠杆菌以葡萄糖为唯一碳源合成均聚的P( 4HB) ,PCR扩增大肠杆菌编码谷氨酸:琥珀酰半缩醛转氨基酶基因(gabT) ,谷氨酸脱羧酶基因(gadA)以及富养罗尔斯通氏菌(Ralstoniaeutropha)H16的4_羟基丁酸脱氢酶基因(gadB) ,并组装到携带富养罗尔斯通氏菌(Ralstoniaeutropha)H16的PHA聚合酶基因(phaC)和克氏梭菌(Clostridiumkluyveri)中编码4_羟基丁酸:CoA转移酶基因(orfZ)的重组质粒pKESS5 3上,形成一个大的操纵元。携带重组质粒的大肠杆菌获得从三羧酸循环的中间物———α_酮戊二酸到P( 4HB)的代谢途径。结果表明,重组大肠杆菌可以以葡萄糖为唯一碳源合成均聚的P( 4HB) ,当向以葡萄糖为唯一碳源的无机培养基添加蛋白胨、酵母提取物、酪蛋白水解物时,P( 4HB)的含量可以高达菌体干重的30 %。     

Production of succinate and polyhydroxyalkanoate from substrate mixture by metabolically engineered Escherichia coli

The strategic design of this study aimed at producing succinate and polyhydroxyalkanoate (PHA) from substrate mixture of glycerol/glucose and fatty acid in Escherichia coli. To accomplish this, an E. coli KNSP1 strain derived from E. coli LR1110 was constructed by deletions of ptsG, sdhA and pta genes and overexpression of phaC1 from Pseudomonas aeruginosa. Cultivation of E. coli KNSP1 showed that this strain was able to produce 21.07 g/L succinate and 0.54 g/L PHA (5.62 wt.% of cell dry weight) from glycerol and fatty acid mixture. The generated PHA composed of 58.7 mol% 3-hydroxyoctanoate (3HO) and 41.3 mol% 3-hydroxydecanoate (3HD). This strain would be useful for complete utilization of byproducts glycerol and fatty acid of biodiesel production process.     

Comparison of recombinant Escherichia coli strains for synthesis and accumulation of poly-(3-hydroxybutyric acid) and morphological changes

A stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid (PHA) biosynthesis genes was constructed. This plasmid was transferred to seven Escherichia coli strains (K12, B, W, XL1-Blue, JM109, DH5alpha, and HB101), which were subsequently compared for their ability to synthesize and accumulate ploy- (3-hydroxybutyric acid) (PHB). Growth of recombinant cells and PHB synthesis were investigated in detail in Luria-Bertani (LB) medium containing 20 g/L glucose. Cell growth, the rate of PHB synthesis, the extent of PHB accumulation, the amount of glucose utilized, and the amount of acetate formed varied from one strain to another. XL1-Blue (pSYL105) and B (pSYL105) synthesized PHB at the fastest rate, which was ca. 0.2 g PHB/g true cell mass-h, and produced PHB up to 6-7 g/L. The yields of cell mass, true cell mass, and PHB varied considerably among the strains. The PHB yield of XL1-Blue (pSYL105) in LB plus 20 g/L glucose was as high as 0.369 g PHB/g glucose. Strains W (pSYL105) and K12 (pSYL105) accumulated the least amount of PHB with the lowest PHB yield at the lowest synthesis rate. JM109 (pSYL105) accumulated PHB to the highest extent (85.6%) with relatively low true cell mass (0.77 g/L). Considerable filamentation of cells accumulating PHB was observed for all strains except for K12 and W, which seemed to be due either to the overexpression of the foreign PHA biosynthesis enzymes or to the accumulation of PHB. (c) 1994 John Wiley & Sons, Inc.     

Production of D-(--)-3-hydroxyalkanoic acid by recombinant Escherichia coli

Pathways for extracellular production of chiral D-(-)-3-hydroxybutyric acid (3HB) and D-(-)-3-hydroxyalkanoic acid (mcl-3HA) were constructed by co-expression of genes of beta-ketothiolase (phbA), acetoacetyl-CoA reductase (phbB) and 3-hydroxyacyl-ACP CoA transacylase (phaG), respectively, in Escherichia coli strain DH5alpha. The effect of acrylic acid and glucose on production of both 3HB and mcl-3HA was investigated. It was found that the addition of acrylic acid significantly increased production of 3HB and mcl-3HA consisting of 3-hydroxyoctanoic acid and 3-hydroxydecanoic acid in a ratio of 1:3 from 199 mg x l(-1) to 661 mg x l(-1) and from 27 mg x l(-1) to 135 mg x l(-1), respectively, in shake flask studies when glucose was present in the medium at the very beginning of fermentation. The timing of glucose addition had no effect on 3HB production. In contrast, mcl-3HA production was affected by glucose addition, an mcl-3HA concentration of 193 mg x l(-1) was obtained when glucose was added to the culture at 12 h. A more than seven-fold increase was obtained when compared with that in medium containing glucose at the beginning of fermentation. However, a decrease in production of 3HB and mcl-3HA was found when glucose was added at 12 h to the culture containing acrylic acid. The repressive effect of acrylic acid on acetic acid production was also evaluated and discussed.     

Production of (R)-3-hydroxybutyric acid by fermentation and bioconversion processes with Azohydromonas lata

Feasibility of producing (R)-3-hydroxybutyric acid ((R)-3-HB) using wild type Azohydromonas lata and its mutants (derived by UV mutation) was investigated. A. lata mutant (M5) produced 780 mg/l in the culture broth when sucrose was used as the carbon source. M5 was further studied in terms of its specificity with various bioconversion substrates for production of (R)-3-HB. (R)-3-HB concentration produced in the culture broth by M5 mutant was 2.7-fold higher than that of the wild type strain when sucrose (3% w/v) and (R,S)-1,3-butanediol (3% v/v) were used as carbon source and bioconversion substrate, respectively. Bioconversion of resting cells (M5) with glucose (1% v/w), ethylacetoacetate (2% v/v), and (R,S)-1,3-butanediol (3% v/v), resulted in (R)-3-HB concentrations of 6.5 g/l, 7.3 g/l and 8.7 g/l, respectively.     

基于多酶级联协调表达策略高效催化合成(S)-2-羟基丁酸

2-羟基丁酸(2-hydroxybutyric acid,2-HBA)是合成生物可降解材料和各种药物的重要中间体,化学法合成的外消旋2-HBA需要去消旋才能获得光学纯对映异构体,应用于工业.文中通过在大肠杆菌Escherichia coli BL21(DE3)中共表达苏氨酸脱氨酶(Threonine deaminase...     

Production of p-Aminobenzoic acid by metabolically engineered Escherichia coli

The production of chemical compounds from renewable resources is an important issue in building a sustainable society. In this study, Escherichia coli was metabolically engineered by introducing T7lac promoter-controlled aroF^fbr, pabA, pabB, and pabC genes into the chromosome to overproduce para-aminobenzoic acid (PABA) from glucose. Elevating the copy number of chromosomal P_T7lac-pabA-pabB distinctly increased the PABA titer, indicating that elevation of 4-amino-4-deoxychorismic acid synthesis is a significant factor in PABA production. The introduction of a counterpart derived from Corynebacterium efficiens, pabAB (ce), encoding a fused PabA and PabB protein, resulted in a considerable increase in the PABA titer. The introduction of more than two copies of P_T7lac-pabAB (ce-mod), a codon-optimized pabAB (ce), into the chromosome of a strain that simultaneously overexpressed aroF^fbr and pabC resulted in 5.1?mM PABA from 55.6?mM glucose (yield 9.2%). The generated strain produced 35?mM (4.8?g?L^?1) PABA from 167?mM glucose (yield 21.0%) in fed-batch culture.     

Engineering Escherichia coli for efficient production of 5-aminolevulinic acid from glucose

5-Aminolevulinic acid (ALA) recently received much attention due to its potential applications in many fields. In this study, we developed a metabolic strategy to produce ALA directly from glucose in recombinant Escherichia coli via the C5 pathway. The expression of a mutated hemA gene, encoding a glutamyl-tRNA reductase from Salmonella arizona, significantly improved ALA production from 31.1 to 176 mg/L. Glutamate-1-semialdehyde aminotransferase from E. coli was found to have a synergistic effect with HemA^M from S. arizona on ALA production (2052 mg/L). In addition, we identified a threonine/homoserine exporter in E. coli, encoded by rhtA gene, which exported ALA due to its broad substrate specificity. The constructed E. coli DALA produced 4.13 g/L ALA in modified minimal medium from glucose without adding any other co-substrate or inhibitor. This strategy offered an attractive potential to metabolic production of ALA in E. coli.     

利用代谢工程改善大肠杆菌的3-脱氢莽草酸生产

3-脱氢莽草酸是芳香族氨基酸合成代谢途径中的一种重要中间产物。除可作为一种高效的抗氧化剂,还可用于合成己二酸、香草醛等一些重要的化工产品,具有重要的应用价值。相关研究证明具有去酪氨酸反馈抑制的3-脱氧-D-阿拉伯庚酮糖-7-磷酸合成酶基因aroFFBR以及转酮醇酶基因tktA可以有效影响3-脱氢莽草酸的过量合成。通过增加aroFFBR和tktA串联过量表达的拷贝数,可使工程菌株在摇瓶发酵条件下3-脱氢莽草酸产量提高2.93倍。通过同源重组无痕基因敲除技术依次敲除出发菌大肠杆菌Escherichia coli AB2834的乳酸、乙酸、乙醇等副产物合成途径中的重要基因ldhA、ackA-pta和adhE,可使工程菌株的3-脱氢莽草酸产量进一步提高,达到了1.83 g/L,是初始出发菌株大肠杆菌E.coli AB2834产量的6.7倍。利用5 L发酵罐进行分批补料发酵,62 h后工程菌株3-脱氢莽草酸产量达到了25.48 g/L。本研究可为构建有应用前景的3-脱氢莽草酸生产菌株提供重要参考。     

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.     

代谢工程改造大肠杆菌合成丙二酸

丙二酸是一种重要的有机二元羧酸,其应用价值遍及化工、医药、食品等领域。本文以大肠杆菌为底盘细胞,过表达了ppc、aspC、panD、pa0132、yneI和pyc基因,成功构建了丙二酸合成重组菌株大肠杆菌BL21(TPP)。该菌株在摇瓶发酵条件下,丙二酸产量达到0.61 g/L。在5 L发酵罐水平,采用间歇补料的方式丙二酸的积累量达3.32 g/L。本研究应用了融合蛋白技术,将ppc和aspC、pa0132和yneI分别进行融合表达,构建了工程菌BL21(SCR)。在摇瓶发酵水平,该菌株丙二酸的积累量达到了0.83 g/L,较出发菌株BL21(TPP)提高了36%。在5 L发酵罐中,工程菌BL21(SCR)的丙二酸产量最高达5.61 g/L,较出发菌株BL21(TPP)提高了69%。本研究实现了丙二酸在大肠杆菌中的生物合成,为构建丙二酸合成的细胞工厂提供了理论依据和技术基础,同时也对其他二元羧酸的生物合成具有启发和指导意义。     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant <Emphasis Type="Italic">Escherichia coli arcA</Emphasis> mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the 'one-factor-at-a-time' technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett-Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box-Wilson design. Under such optimized conditions (22.02 g l(-1) glycerol, 1.78 g l(-1) CAS, and 1.83 g l(-1) inoculum) microaerobic batch cultures gave rise to 8.37 g l(-1) CDW and 3.52 g l(-1) PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l(-1). After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l(-1), respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures.     

Production of isopropanol by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

A genetically engineered strain of Escherichia coli JM109 harboring the isopropanol-producing pathway consisting of five genes encoding four enzymes, thiolase, coenzyme A (CoA) transferase, acetoacetate decarboxylase from Clostridium acetobutylicum ATCC 824, and primary–secondary alcohol dehydrogenase from C. beijerinckii NRRL B593, produced up to 227 mM of isopropanol from glucose under aerobic fed-batch culture conditions. Acetate production by the engineered strain was approximately one sixth that produced by a control E. coli strain bearing an expression vector without the clostridial genes. These results demonstrate a functional isopropanol-producing pathway in E. coli and consequently carbon flux from acetyl-CoA directed to isopropanol instead of acetate. This is the first report on isopropanol production by genetically engineered microorganism under aerobic culture conditions.     

Genetic engineering of Escherichia coli for production of tetrahydrobiopterin

Tetrahydrobiopterin (BH4) is an essential cofactor for various enzymes in mammals. In vivo, it is synthesized from GTP via the three-step pathway of GTP cyclohydrolase I (GCHI), 6-pyruvoyl-tetrahydropterin synthase (PTPS) and sepiapterin reductase (SPR). BH4 is a medicine used to treat atypical hyperphenylalaninemia. It is currently synthesized by chemical means, which consists of many steps, and requires costly materials and complicated procedures. To explore an alternative microbial method for BH4 production, we utilized recombinant DNA technology to construct recombinant Escherichia coli (E. coli) strains carrying genes expressing GCHI, PTPS and SPR enzymes. These strains successfully produced BH4, which was detected as dihydrobiopterin and biopterin, oxidation products of BH4. In order to increase BH4 productivity we made further improvements. First, to increase the de novo GTP supply, an 8-azaguanine resistant mutant was isolated and an additional guaBA operon was introduced. Second, to augment the activity of GCHI, the folE gene from E. coli was replaced by the mtrA gene from Bacillus subtilis. These modifications provided us with a strain showing significantly higher productivity, up to 4.0 g of biopterin/L of culture broth. The results suggest the possibility of commercial BH4 production by our method.     

Enantioselective synthesis of ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE) from ethyl-3-oxo-3-phenylpropanoate using recombinant fatty acid synthase (FAS2) from Kluyveromyces lactis KCTC 7133 in Pichia pastoris GS115

Various yeast strains were examined for the microbial reduction of ethyl-3-oxo-3-phenylpropanoate (OPPE) to ethyl-(S)-3-hydroxy-3-phenylpropanoate (S-HPPE), which is the chiral intermediate for the synthesis of a serotonin uptake inhibitor, Fluoxetine. Kluyveromyces lactis KCTC 7133 was found as the most efficient strain in terms of high yield (83% at 50 mM) and high optical purity ee > 99% of S-HPPE. Based on the protein purification, activity analysis and the genomic analysis, a fatty acid synthase (FAS) was identified as the responsible β-ketoreductase. To increase the productivity, a recombinant Pichia pastoris GS115 over-expressing FAS2 (α-subunit of FAS) of K. lactis KCTC7133 was constructed. In the optimized media condition, the recombinant P. pastoris functionally over-expressed the FAS2. Recombinant P. pastoris showed 2.3-fold higher reductase activity compared with wild type P. pastoris. With the recombinant P. pastoris, the 91% yield of S-HPPE was achieved at 50 mM OPPE maintaining the high optical purity of the product (ee > 99%).     

Effect of amino acid supplementation on the synthesis of poly(3-hydroxybutyrate) by recombinant pha Sa + Escherichia coli

The effect of different amino acid supplements to the basal medium on poly(3-hydroxybutyrate) (PHB) accumulation by recombinant pha _Sa ⁺ Escherichia coli (ATCC: PTA-1579) harbouring the poly(3-hydroxybutyrate)-synthesizing genes from Streptomyces aureofaciens NRRL 2209 was studied. With the exception of glycine and valine, all other amino acid supplements brought about enhancement of PHB accumulation. In particular, cysteine, isoleucine or methionine supplementation increased PHB accumulation by 60, 45 and 61% respectively by the recombinant E. coli as compared with PHB accumulation by this organism in the basal medium. The effect of co-ordinated addition of assorted combinations of these three amino acids on PHB accumulation was studied using a 2³ factorial design. The three-factor interaction analyses revealed that the effect of the three amino acids on PHB accumulation by the recombinant E. coli was in the order of cysteine > methionine > isoleucine. The defined medium supplemented with cysteine, methionine and isoleucine at the concentration of 150 mgl^–1 each and glycerol as the carbon source was the optimum medium that resulted in the accumulation of about 52% PHB of cell dry weight.     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant Escherichia coli arcA mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the ‘one-factor-at-a-time’ technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett–Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box–Wilson design. Under such optimized conditions (22.02 g l⁻¹ glycerol, 1.78 g l⁻¹ CAS, and 1.83 g l⁻¹ inoculum) microaerobic batch cultures gave rise to 8.37 g l⁻¹ CDW and 3.52 g l⁻¹ PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l⁻¹. After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l⁻¹, respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at