Surface Expression of ω-Transaminase in Escherichia coli

Chiral amines are important for the chemical and pharmaceutical industries, and there is rapidly growing interest to use transaminases for their synthesis. Since the cost of the enzyme is an important factor for process economy, the use of whole-cell biocatalysts is attractive, since expensive purification and immobilization steps can be avoided. Display of the protein on the cell surface provides a possible way to reduce the mass transfer limitations of such biocatalysts. However, transaminases need to dimerize in order to become active, and furthermore, they require the cofactor pyridoxal phosphate; consequently, successful transaminase surface expression has not been reported thus far. In this work, we produced an Arthrobacter citreus ω-transaminase in Escherichia coli using a surface display vector based on the autotransporter adhesin involved in diffuse adherence (AIDA-I), which has previously been used for display of dimeric proteins. The correct localization of the transaminase in the E. coli outer membrane and its orientation toward the cell exterior were verified. Furthermore, transaminase activity was detected exclusively in the outer membrane protein fraction, showing that successful dimerization had occurred. The transaminase was found to be present in both full-length and proteolytically degraded forms. The removal of this proteolysis is considered to be the main obstacle to achieving sufficient whole-cell transaminase activity.     

Substrate oscillations boost recombinant protein release from Escherichia coli

Intracellular production of recombinant proteins in prokaryotes necessitates subsequent disruption of cells for protein recovery. Since the cell disruption and subsequent purification steps largely contribute to the total production cost, scalable tools for protein release into the extracellular space is of utmost importance. Although there are several ways for enhancing protein release, changing culture conditions is rather a simple and scalable approach compared to, for example, molecular cell design. This contribution aimed at quantitatively studying process technological means to boost protein release of a periplasmatic recombinant protein (alkaline phosphatase) from E. coli. Quantitative analysis of protein in independent bioreactor runs could demonstrate that a defined oscillatory feeding profile was found to improve protein release, about 60 %, compared to the conventional constant feeding rate. The process technology included an oscillatory post-induction feed profile with the frequency of 4 min. The feed rate was oscillated triangularly between a maximum (1.3-fold of the maximum feed rate achieved at the end of the fed-batch phase) and a minimum (45 % of the maximum). The significant improvement indicates the potential to maximize the production rate, while this oscillatory feed profile can be easily scaled to industrial processes. Moreover, quantitative analysis of the primary metabolism revealed that the carbon dioxide yield can be used to identify the preferred feeding profile. This approach is therefore in line with the initiative of process analytical technology for science-based process understanding in process development and process control strategies.     

Modulation of guanosine 5′-diphosphate-d-mannose metabolism in recombinant Escherichia coli for production of guanosine 5′-diphosphate-l-fucose

Guanosine 5’-diphosphate (GDP)-l-fucose, an activated form of a nucleotide sugar, plays an important role in a wide range of biological functions. In this study, the enhancement of GDP-l-fucose production was attempted by supplementation of mannose, which is a potentially better carbon source to be converted into GDP-l-fucose than glucose, and combinatorial overexpression of the genes involved in the biosynthesis of GDP-d-mannose, a precursor of GDP-l-fucose. Supply of a mannose and glucose led to a 1.3-fold-increase in GDP-l-fucose concentration (52.5 ± 0.8 mg l^?1) in a fed-batch fermentation of recombinant E. coli BL21star(DE3) overexpressing the gmd and wcaG genes, compared with the case using glucose as a sole carbon source. A maximum GDP-l-fucose concentration of 170.3 ± 2.3 mg l^?1, corresponding to a 4.4-fold enhancement compared with the control strain overexpressing gmd and wcaG genes only, was achieved in a glucose-limited fed-batch fermentation of a recombinant E. coli BL21star(DE3) strain overexpressing manB, manC, gmd and wcaG genes. Further improvement of GDP-l-fucose production was not obtained by additional overexpression of the manA gene.     

Expression and characterization of Kluyveromyces lactis β-galactosidase in Escherichia coli

Kluyveromyces lactis -galactosidase gene, LAC4, was expressed in Escherichia coli as a soluble His-tagged recombinant enzyme under the optimized culture conditions. The expressed protein was multimeric with a subunit molecular mass of 118 kDa. The dimeric form of the -galactosidase was the major fraction but had a lower activity than those of the multimeric forms. The purified enzyme required Mn²⁺ for activity and was inactivated irreversibly by imidazole above 50 mM. The activity was optimal at 37 and 40 °C for o-nitrophenyl--d-galactopyranoside (oNPG) and lactose, respectively. The optimum pH value is 7. The K _m and V _max values of the purified enzyme for oNPG were 1.5 mM and 560 mol min^–1 mg^–1, and for lactose 20 mM and 570 mol min^–1 mg^–1, respectively.     

Expression and characterization of Pichia etchellsii β-glucosidase in Escherichia coli

The β-glucosidase enzyme is important as the terminal enzyme involved in hydrolysis of cellobiose and short-chain cellodextrins generated during enzymatic cellulose degradation. Under controlled reaction conditions the enzyme also displays cello-oligosaccharide synthesizing ability (based on either the thermodynamic or kinetic approach). We present here the purification of the enzyme β-glucosidase (BGL) of Pichia etchellsii from recombinant pBG55 Escherichia coli clone. The kinetic parameters, substrate specificity and oligosaccharide synthesizing ability of the purified enzyme are also reported. The purified 200-kDa protein (tetramer of 50 kDa) was identified as a broad-substrate-specificity enzyme exhibiting increased temperature and glucose tolerance compared to the native yeast enzyme. Temperature directed substrate specificity for aryl β,1–4 linkage, and β(1–2), β(1–4), β(1–6) and β(2-1) linkages in various natural disaccharides was observed. Glycosylation of the enzyme was found to be unimportant for enzyme activity. With both cellobiose and glucose, oligosaccharide synthesis was detected. The implications of this information with regard to cellulose hydrolysis and oligosaccharide synthesis are discussed.     

Introduction of a stress-responsive gene, yggG, enhances the yield of l-phenylalanine with decreased acetic acid production in a recombinant Escherichia coli

A stress-responsive gene, yggG, was introduced into an l-phenylalanine producer, Escherichia coli AJ12741. In shake-flask culture, the yggG-containing recombinant strain (named AJ12741/pHYGG) produced 6.4 g l-phenylalanine l⁻¹ at the end of culture and its yield on glucose was 0.16 g l-phenylalanine g glucose⁻¹. These values are much higher than those of the original AJ12741 strain (3.7 g l-phenylalanine l⁻¹ and 0.09 g l-phenylalanine g glucose⁻¹, respectively). On the other hand, AJ12741/pHYGG strain produced only 4.5 g acetic acid l⁻¹ and its yield on glucose was about a half of that of the AJ12741 culture. Analysis of gene expression revealed that in late growth phase, the expression levels of genes involved in acetic acid production (pta, ackA, and poxB) were relatively low in AJ12741/pHYGG cells. In particular, the level of poxB expression in AJ12741/pHYGG strains was one-seventh of that of the original strain. These results suggest that the formation of a bottleneck for acetic acid production brings about a metabolic flow favorable to l-phenylalanine synthesis in the recombinant strain over-expressing the yggG gene. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Molecular mass of poly[(R )-3-hydroxybutyric acid] produced in a recombinant Escherichia coli

 Poly[(R)-3-hydroxybutyric acid] (PHB) was produced at 37 °C by a recombinant Escherichia coli harboring the Alcaligenes eutrophus biosynthesis phbCAB genes in Luria-Bertani media containing glucose at 10–30 g/l at different pH values and the time-dependent changes in the molecular mass of PHB were studied. PHB polymers accumulated within cells while glucose was present in the medium. The number-average molecular mass of PHB decreased with time during the course of PHB accumulation, and the values for PHB were markedly dependent on the cultivation conditions of the E. coli, ranging from 0.5 MDa to 20 MDa. Under specific conditions (pH 6.0), E. coli produced PHB with an extremely high molecular mass (20 MDa). It has been suggested that a chain-transfer agent is generated in E. coli cells during the accumulation of PHB. Received: 18 July 1996 / Received revision: 4 November 1996 / Accepted: 4 November 1996     

Detection of d-amino acids in purified proteins synthesized in Escherichia coli

It has long been believed that amino acids comprising proteins of all living organisms are only of the l-configuration, except for Gly. However, peptidyl d-amino acids were observed in hydrolysates of soluble high molecular weight fractions extracted from cells or tissues of various organisms. This strongly suggests that significant amounts of d-amino acids are naturally present in usual proteins. Thus we analyzed the d-amino acid contents of His-tag-purified β-galactosidase and human urocortin, which were synthesized by Escherichia coli grown in controlled synthetic media. After acidic hydrolysis for various times at 110°C, samples were derivatized with 4-fluoro-7-nitro-2, 1, 3-benzoxadiazole (NBD-F) and separated on a reverse-phase column followed by a chiral column into d- and l-enantiomers. The contents of d-enantiomers of Ala, Leu, Phe, Val, Asp, and Glu were determined by plotting index d/(d + l) against the incubation time for hydrolysis and extrapolating the linear regression line to 0 h to eliminate the effect of racemization of amino acids during the incubation. Significant contents of d-amino acids were reproducibly detected, the d-amino acid profile being specific to an individual protein. This finding indicated the likelihood that d-amino acids are in fact present in the purified proteins. On the other hand, the d-amino acid contents of proteins were hardly influenced by the addition of d- or l-amino acids to the cultivation medium, whereas intracellular free d-amino acids sensitively varied according to the extracellular conditions. The origin of these d-amino acids detected in proteins was discussed.     

Over-production of human interferon-γ by HCDC of recombinant Escherichia coli

A simple fed-batch process was developed using a modified variable specific growth rate feeding strategy for high cell density cultivation of Escherichia coli BL21 (DE3) expressing human interferon-gamma (hIFN-γ). The feeding rate was adjusted to achieve the maximum attainable specific growth rate during fed-batch cultivation. In this method, specific growth rate was changed from a maximum value of 0.55 h⁻¹ at the beginning of feeding and then it was reduced to 0.4 h⁻¹ at induction time.The final concentration of biomass and IFN-γ was reached to ∼115 g l⁻¹ (DCW) and 42.5 g(hIFN-γ) l⁻¹ after 16.5 h, also the final specific yield and overall productivity of recombinant hIFN-γ (rhIFN-γ) were obtained 0.37 g(hIFN-γ) g⁻¹ DCW and 2.57 g(hIFN-γ) l⁻¹ h⁻¹, respectively. According to available data this is the highest specific yield and productivity that has been reported for recombinant proteins production yet.     

Expression and Purification of an Antimicrobial Peptide, Bovine Lactoferricin Derivative LfcinB-W10 in Escherichia coli

Antimicrobial peptides (AMPs) are extremely attractive candidate for therapeutic agents due to their wide spectrum of antimicrobial activity and action mechanism different from antibiotics. In this study, a method using genetic engineering for obtaining an antimicrobial peptide, bovine lactoferricin derivative peptide LfcinB-W10, has been developed. According to the coden usage of Escherichia coli, a gene encoding the peptide was synthesized and a recombinant vector of E. coli expression pGEX-EN-LFW was constructed. The LfcinB-W10 peptide fused with glutathione S-transferase (GST) was successfully expressed and about 20 mg fusion protein with 90% purity was obtained from 1 l culture. The recombinant LfcinB-W10 (rLfcinB-W10) was released from fusion protein by the enterokinase digestion, and about the LfcinB-W10 yield reached 300 μg per 1 l culture. The purified rLfcinB-W10 was found to have growth inhibition activity against Staphylococcus aureus (S. aureus) ATCC25923.     

Increased poly-β-hydroxybutyrate (PHB) chain length by the modulation of PHA synthase activity in recombinant Escherichia coli

A second promoter (P1) was inserted to the PHA (poly--hydroxyalkanoate) operon (pSP2) of Esherichia coli DH5 with an optimal E. coli ribosome binding site and a trc strong promoter (pSJS1) to obtain poly--hydroxybutyrate (PHB) with long chain length. When the inducer, IPTG was added to the culture at 0.4 mM, the average molecular weight was 1.1 × 10⁶ Da. However, an even greater increase of the PHB average molecular weight to 2.5 × 10⁷ Da was observed without IPTG being added.     

Optimization of recombinant β-NGF expression in Escherichia coli using response surface methodology

Human nerve growth factor a member of the neurotrophin family can be used to treat neurodegenerative diseases. As it has disulfide bonds in its structure, periplasmic expression of it using appropriate signal sequence is beneficial. Therefore, in this work β-nerve growth factor (β-NGF) was expressed in Escherichia coli using pET39b expression vector containing DsbA signal sequence. In an initial step, the effect of isopropyl β-D-1-thiogalactopyranoside (IPTG) and lactose concentration as inducer on protein production was investigated using response surface methodology. Then the effect of different postinduction time and temperature on protein production was studied. Our results indicated that the highest β-NGF production was achieved with 1?mM IPTG and low concentrations of lactose (0–2% w/v), low cultivation temperature of 25°C and postinduction time of 2?hr. Also following β-NGF purification, bioassay test using PC12 cell line was done. The biological activity of the purified β-NGF showed a similar cell proliferation activity with the standard recombinant human β-NGF. In conclusion, the results indicated an optimized upstream process to obtain high yields of biologically active β-NGF.     

Expression of a β-galactosidase gene from Lactobacillus sake in Escherichia coli

Summary A -galactosidase gene from Lactobacillus sake coding for lactose hydrolysis was cloned and expressed in Escherichia coli. Chromosomal DNA from L. sake was partially digested with the restriction enzyme Sau3AI, and the 3–6 Kb fragment was ligated to the cloning vector pSP72 digested with BamHI. One E. coli transformant expressing -galactosidase was isolated on X-gal plates. It contained a plasmid with an insertion of approx. 4 Kb. The restriction map of the recombinant plasmid was constructed. The characteristics of the recombinant -galactosidase were compared with those of the wild type. The optima pH and temperature for both enzymes was 6.5 and 50°C, respectively. Stability of the enzymes at different temperatures and activity on lactose were determined.     

Characterization of rapidly labelled ribonucleic acid in Escherichia coli by deoxyribonucleic acid–ribonucleic acid hybridization

1. Rapidly labelled RNA from Escherichia coli K 12 was characterized by hybridization to denatured E. coli DNA on cellulose nitrate membrane filters. The experiments were designed to show that, if sufficient denatured DNA is offered in a single challenge, practically all the rapidly labelled RNA will hybridize. With the technique employed, 75-80% hybridization efficiency could be obtained as a maximum. Even if an excess of DNA sites were offered, this value could not be improved upon in any single challenge of rapidly labelled RNA with denatured E. coli DNA. 2. It was confirmed that the hybridization technique can separate the rapidly labelled RNA into two fractions. One of these (30% of the total) was efficiently hybridized with the low DNA/RNA ratio (10:1, w/w) used in tests. The other fraction (70% of the total) was hybridized to DNA at low efficiencies with the DNA/RNA ratio 10:1, and was hybridized progressively more effectively as the amount of denatured DNA was increased. A practical maximum of 80% hybridization of all the rapidly labelled RNA was first achieved at a DNA/RNA ratio 210:1 (+/-10:1). This fraction was fully representative of the rapidly labelled RNA with regard to kind and relative amount of materials hybridized. 3. In competition experiments, where additions were made of unlabelled RNA prepared from E. coli DNA, DNA-dependent RNA polymerase (EC 2.7.7.6) and nucleoside 5'-triphosphates, the rapidly labelled RNA fraction hybridized at a low (10:1) DNA/RNA ratio was shown to be competitive with a product from genes other than those responsible for ribosomal RNA synthesis and thus was presumably messenger RNA. At higher DNA/rapidly labelled RNA ratios (200:1), competition with added unlabelled E. coli ribosomal RNA (without messenger RNA contaminants) lowered the hybridization of the rapidly labelled RNA from its 80% maximum to 23%. This proportion of rapidly labelled RNA was not competitive with E. coli ribosomal RNA even when the latter was in large excess. The ribosomal RNA would also not compete with the 23% rapidly labelled RNA bound to DNA at low DNA/RNA ratios. It was thus demonstrated that the major part of E. coli rapidly labelled RNA (70%) is ribosomal RNA, presumably a precursor to the RNA in mature ribosomes. 4. These studies have shown that, when earlier workers used low DNA/RNA ratios (about 10:1) in the assay of messenger RNA in bacterial rapidly labelled RNA, a reasonable estimate of this fraction was achieved. Criticisms that individual messenger RNA species may be synthesized from single DNA sites in E. coli at rates that lead to low efficiencies of messenger RNA binding at low DNA/RNA ratios are refuted. In accordance with earlier results, estimations of the messenger RNA content of E. coli in both rapidly labelled and randomly labelled RNA show that this fraction is 1.8-1.9% of the total RNA. This shows that, if any messenger RNA of relatively long life exists in E. coli, it does not contribute a measurable weight to that of rapidly labelled messenger RNA.     

Efficient biosynthesis of α-aminoadipic acid via lysine catabolism in Escherichia coli

α-Aminoadipic acid (AAA) is a nonproteinogenic amino acid with potential applications in pharmaceutical, chemical and animal feed industries. Currently, AAA is produced by chemical synthesis, which suffers from high cost and low production efficiency. In this study, we engineered Escherichia coli for high-level AAA production by coupling lysine biosynthesis and degradation pathways. First, the lysine-α-ketoglutarate reductase and saccharopine dehydrogenase from Saccharomyces cerevisiae and α-aminoadipate-δ-semialdehyde dehydrogenase from Rhodococcus erythropolis were selected by in vitro enzyme assays for pathway assembly. Subsequently, lysine supply was enhanced by blocking its degradation pathway, overexpressing key pathway enzymes and improving nicotinamide adenine dineucleotide phosphate (NADPH) regeneration. Finally, a glutamate transporter from Corynebacterium glutamicum was introduced to elevate AAA efflux. The final strain produced 2.94 and 5.64 g/L AAA in shake flasks and bioreactors, respectively. This work provides an efficient and sustainable way for AAA production.     

Enhanced production of succinic acid from methanol–organosolv pretreated Strophanthus preussii by recombinant Escherichia coli

Bioprocess and Biosystems Engineering - A biorefinery process for high yield production of succinic acid from biomass sugars was investigated using recombinant Escherichia coli. The major problem...     

Production of γ-aminobutyric acid in Escherichia coli by engineering MSG pathway

Abstract

The compound γ-aminobutyric acid (GABA) has many important physiological functions. The effect of glutamate decarboxylases and the glutamate/GABA antiporter on GABA production was investigated in Escherichia coli. Three genes, gadA, gadB, and gadC were cloned and ligated alone or in combination into the plasmid pET32a. The constructed plasmids were transformed into Escherichia coli BL21(DE3). Three strains, E. coli BL21(DE3)/pET32a-gadA, E. coli BL21(DE3)/pET32a-gadAB and E. coli BL21(DE3)/pET32a-gadABC were selected and identified. The respective titers of GABA from the three strains grown in shake flasks were 1.25, 2.31, and 3.98?g/L. The optimal titer of the substrate and the optimal pH for GABA production were 40?g/L and 4.2, respectively. The highest titer of GABA was 23.6?g/L at 36?h in batch fermentation and was 31.3?g/L at 57?h in fed-batch fermentation. This study lays a foundation for the development and use of GABA.     

The regulatory subunit ε in Escherichia coli FOF1-ATP synthase

F-type ATP synthases are extraordinary multisubunit proteins that operate as nanomotors. The Escherichia coli (E. coli) enzyme uses the proton motive force (pmf) across the bacterial plasma membrane to drive rotation of the central rotor subunits within a stator subunit complex. Through this mechanical rotation, the rotor coordinates three nucleotide binding sites that sequentially catalyze the synthesis of ATP. Moreover, the enzyme can hydrolyze ATP to turn the rotor in the opposite direction and generate pmf. The direction of net catalysis, i.e. synthesis or hydrolysis of ATP, depends on the cell's bioenergetic conditions. Different control mechanisms have been found for ATP synthases in mitochondria, chloroplasts and bacteria. This review discusses the auto-inhibitory behavior of subunit ε found in F_OF₁-ATP synthases of many bacteria. We focus on E. coli F_OF₁-ATP synthase, with insights into the regulatory mechanism of subunit ε arising from structural and biochemical studies complemented by single-molecule microscopy experiments.     

Secretory expression and enzymatic characterization of recombinant Agarivorans albus β-agarase in Escherichia coli

Agarase catalyzes the hydrolysis of agar, which is primarily used as a medium for microbiology, various food additives, and new biomass materials. In this study, we described the expression of the synthetic gene encoding β-agarase from Agarivorans albus (Aaβ-agarase) in Escherichia coli. The synthetic β-agarase gene was designed based on the biased codons of E. coli to optimize its expression and extracellular secretion in an active, soluble form. The synthesized agarase gene, including its signal sequence, was cloned into the pET-26 expression vector, and the pET-Aaβ-agarase plasmid was introduced into E. coli BL21-Star (DE3) cells. The E. coli transformants were cultured for high-yield secretion of recombinant Aaβ-agarase in Luria-Bertani broth containing 0.6?mM isopropyl β-D-1-thiogalactopyranoside for 9?h at 37°C. The expressed recombinant Aaβ-agarase was purified by ammonium sulfate precipitation and diethylaminoethyl-sepharose column chromatography, yielding ～10?mg/L Aaβ-agarase. The purified recombinant Aaβ-agarase exhibited optimal activity at pH 7 and 40°C, and its activity was strongly inhibited by Cu²⁺, Mn²⁺, Zn²⁺, and Al³⁺ ions. Furthermore, the K_M and k_cat values for purified Aaβ-agarase were ～0.02?mM and ～45/s, respectively. These kinetic values were up to approximately 15–100-fold lower than the K_M values reported for other agarases and approximately 7–30-fold higher than the k_cat/K_M values reported for other agarases, indicating that recombinant Aaβ-agarase exhibited good substrate-binding ability and high catalytic efficiency. These results demonstrated that the E. coli expression system was capable of producing recombinant Aaβ-agarase in an active form, at a high yield, and with attributes useful in the relevant industries.     

GroEL–GroES assisted folding of multiple recombinant proteins simultaneously over-expressed in Escherichia coli

Folding of aggregation prone recombinant proteins through co-expression of chaperonin GroEL and GroES has been a popular practice in the effort to optimize preparation of functional protein in Escherichia coli. Considering the demand for functional recombinant protein products, it is desirable to apply the chaperone assisted protein folding strategy for enhancing the yield of properly folded protein. Toward the same direction, it is also worth attempting folding of multiple recombinant proteins simultaneously over-expressed in E. coli through the assistance of co-expressed GroEL–ES. The genesis of this thinking was originated from the fact that cellular GroEL and GroES assist in the folding of several endogenous proteins expressed in the bacterial cell. Here we present the experimental findings from our study on co-expressed GroEL–GroES assisted folding of simultaneously over-expressed proteins maltodextrin glucosidase (MalZ) and yeast mitochondrial aconitase (mAco). Both proteins mentioned here are relatively larger and aggregation prone, mostly form inclusion bodies, and undergo GroEL–ES assisted folding in E. coli cells during over-expression. It has been reported that the relative yield of properly folded functional forms of MalZ and mAco with the exogenous GroEL–ES assistance were comparable with the results when these proteins were overexpressed alone. This observation is quite promising and highlights the fact that GroEL and GroES can assist in the folding of multiple substrate proteins simultaneously when over-expressed in E. coli. This method might be a potential tool for enhanced production of multiple functional recombinant proteins simultaneously in E. coli.