A method for the separation of peptides and α-amino acids

1. Peptides and alpha-amino acids, occurring in mixtures from various sources, can be separated into one fraction containing the amino acids and several peptide fractions. This is achieved by chelation of the mixture with Cu(2+) ions and subsequent chromatography of these chelates over the acetate form of diethylaminoethylcellulose or triethylaminoethylcellulose. 2. The amino acid fraction is obtained by elution with 0.01m-collidine-acetate buffer, pH8.0. 3. Peptide fractions are eluted with 0.01m-collidine-acetate buffer, pH4.5, 0.17n-acetic acid and 0.1n-hydrochloric acid respectively. 4. With the exception of aspartic acid and glutamic acid, which are partly found in the acidic peptide fraction, the amino acids are completely separated from the peptides. 5. Contamination of the acidic peptide fraction with glutamic acid and aspartic acid can be largely avoided by previous addition of an excess of arginine. 6. Copper is removed from the eluates by extraction with 8-hydroxyquinoline in chloroform.     

The control by respiration of the uptake of α-methyl glucoside in Escherichia coli K12

The uptake of methyl α-d-glucopyranoside (α-MG) by Escherichia coli K12 was decreased by the addition of substrates which stimulated the rate of oxygen consumption by the cells. The inhibition, which occurred only at non-saturating concentrations of α-MG, was not the result of a stimulation of the rate of exit of intracellular α-MG, and was abolished by the presence of carbonyl cyanide m-chlorophenylhydrazone or sodium azide. Since those drugs inhibit energy conservation at the respiratory chain and did not alter significantly the rate of oxygen consumption under the conditions for the assay of α-MG uptake, it appears that the inhibition of the transport system by respirable substrates is mediated by some form of energy derived from respiration.     

Metabolic engineering of Escherichia coli for α-farnesene production

Sesquiterpenes are important materials in pharmaceuticals and industry. Metabolic engineering has been successfully used to produce these valuable compounds in microbial hosts. However, the microbial potential of sesquiterpene production is limited by the poor heterologous expression of plant sesquiterpene synthases and the deficient FPP precursor supply. In this study, we engineered E. coli to produce α-farnesene using a codon-optimized α-farnesene synthase and an exogenous MVA pathway. Codon optimization of α-farnesene synthase improved both the synthase expression and α-farnesene production. Augmentation of the metabolic flux for FPP synthesis conferred a 1.6- to 48.0-fold increase in α-farnesene production. An additional increase in α-farnesene production was achieved by the protein fusion of FPP synthase and α-farnesene synthase. The engineered E. coli strain was able to produce 380.0 mg/L of α-farnesene, which is an approximately 317-fold increase over the initial production of 1.2 mg/L.     

Pathway engineering of Escherichia coli for α-ketoglutaric acid production

α-Ketoglutaric acid (α-KG) is a multifunctional dicarboxylic acid in the tricarboxylic acid (TCA) cycle, but microbial engineering for α-KG production is not economically efficient, due to the intrinsic inefficiency of its biosynthetic pathway. In this study, pathway engineering was used to improve pathway efficiency for α-KG production in Escherichia coli. First, the TCA cycle was rewired for α-KG production starting from pyruvate, and the engineered strain E. coli W3110Δ4-PCAI produced 15.66 g/L α-KG. Then, the rewired TCA cycle was optimized by designing various strengths of pyruvate carboxylase and isocitrate dehydrogenase expression cassettes, resulting in a large increase in α-KG production (24.66 g/L). Furthermore, acetyl coenzyme A (acetyl-CoA) availability was improved by overexpressing acetyl-CoA synthetase, leading to α-KG production up to 28.54 g/L. Finally, the engineered strain E. coli W3110Δ4-P_(H)CAI_(H)A was able to produce 32.20 g/L α-KG in a 5-L fed-batch bioreactor. This strategy described here paves the way to the development of an efficient pathway for microbial production of α-KG.     

Cloning of the thermostable α-amylase gene from Pyrococcus woesei in Escherichia coli

Pyrococcus woesei (DSM 3773) α-amylase gene was cloned into pET21d(+) and pYTB2 plasmids, and the pET21d(+)α-amyl and pYTB2α-amyl vectors obtained were used for expression of thermostable α-amylase or fusion of α-amylase and intein in Escherichia coli BL21(DE3) or BL21(DE3)pLysS cells, respectively. As compared with other expression systems, the synthesis of α-amylase in fusion with intein in E. coli BL21(DE3)pLysS strain led to a lower level of inclusion bodies formation—they exhibit only 35% of total cell activity—and high productivity of the soluble enzyme form (195,000 U/L of the growth medium). The thermostable α-amylase can be purified free of most of the bacterial protein and released from fusion with intein by heat treatment at about 75°C in the presence of thiol compounds. The recombinant enzyme has maximal activity at pH 5.6 and 95°C. The half-life of this preparation in 0.05 M acetate buffer (pH 5.6) at 90°C and 110°C was 11 h and 3.5 h, respectively, and retained 24% of residual activity following incubation for 2 h at 120°C. Maltose was the main end product of starch hydrolysis catalyzed by this α-amylase. However, small amounts of glucose and some residual unconverted oligosaccharides were also detected. Furthermore, this enzyme shows remarkable activity toward glycogen (49.9% of the value determined for starch hydrolysis) but not toward pullulan.     

High-level Expression of an α-l-arabinofuranosidase from Thermotoga maritima in Escherichia coli for the Production of Xylobiose from Xylan

To efficiently produce xylobiose from xylan, high-level expression of an α-l-arabinofuranosidase gene from Thermotoga maritima was carried out in Escherichia coli. A 1.5-kb DNA fragment, coding for an α-l-arabinofuranosidase of T. maritima, was inserted into plasmid pET-20b without the pelB signal sequence leader, and produced pET-20b-araA1 with 8 nt spacing between ATG and Shine–Dalgarno sequence. A maximum activity of 12 U mg⁻¹ was obtained from cellular extract of E. coli BL21-CodonPlus (DE3)-RIL harboring pET-20b-araA1. The over-expressed α-l-arabinofuranosidase was purified 13-fold with a 94% yield from the cellular extract of E. coli by a simple heat treatment. Production of xylooligosaccharides from corncob xylan by endoxylanase and α-l-arabinofuranosidase was examined by TLC and HPLC: xylobiose was the major product from xylan at 90 °C and its proportion in the xylan hydrolyzates increased with the reaction time. Hydrolysis with in the xylanase absence of α-l-arabinofuranosidase gave only half this yield. Revisions requested 27 October 2005; Revisions received 5 September 2005     

Synthesis of α3 phage DNA in replication mutants of Escherichia coli

Host functions for DNA replication of bacteriophage α3, a representative of group A microvirid phages, were studied using dna and rep mutants of Escherichia coli. In dna⁺ cells, conversion of phage α3 single-stranded DNA (SS) into the double-stranded replicative form (RF) was insensitive to 30–150 μg/ml of chloramphenicol, 200 μg/ml of rifampicin, 50 μg/ml of nalidixic acid, or 200 μg/ml of novobiocin. At 43°C, synthesis of the parental RF was inhibited in dnaG and dnaZ mutants, but not in dnaE and rep strains. Replication of phage α3 progeny RF was prevented by 50 μg/ml of mitomycin C (in hcr⁺ bacteria), 50 μg/ml of nalidixic acid or 200 μg/ml of novoviocin, but neither by 30 μg/ml of chloramphenicol nor by 200 μg/ml of rifampicin. Besides dnaG and dnaZ gene products, dnaE and rep functions were essential for the progeny RF synthesis. Host factor dependence of α3 was relatively simple and, in contrast with phages øX174 and G4, α3 did not require dnaB and dnaC(D) activities.     

High-level expression of human αs1-casein in Escherichia coli

Human _s1-casein was expressed efficiently in Escherichia coli. The overproduced recombinant human a _s1-casein was about 25% of the total cell protein. Two different vectors were constructed to express Met-_s1-casein and Met-_s1-casein with a His-affinity tag at the C-terminus. Recombinant Met-_s1-casein with a His-affinity tag was purified to homogeneity using Ni-nitrilotriacetic acid resin. N-terminal sequence of the first 10 amino acid residues of this purified protein was identical to that of mature human _s1-casein with an extra methionine residue at the N-terminus.     

Delayed supplementation of glycine enhances extracellular secretion of the recombinant α-cyclodextrin glycosyltransferase in Escherichia coli

The targeting of recombinant proteins for secretion to the culture medium of Escherichia coli presents significant advantages over cytoplasmic or periplasmic expression. However, a major barrier is inadequate secretion across two cell membranes. In the present study, we attempted to circumvent this secretion problem of the recombinant α-cyclodextrin glycosyltransferase (α-CGTase) from Paenibacillus macerans strain JFB05-01. It was found that glycine could promote extracellular secretion of the recombinant α-CGTase for which one potential mechanism might be the increase in membrane permeability. However, further analysis indicated that glycine supplementation resulted in impaired cell growth, which adversely affected overall recombinant protein production. Significantly, delayed supplementation of glycine could control cell growth impairment exerted by glycine. As a result, if the supplementation of 1% glycine was optimally carried out at the middle of the exponential growth phase, the α-CGTase activity in the culture medium reached 28.5 U/ml at 44 h of culture, which was 11-fold higher than that of the culture in regular terrific broth medium and 1.2-fold higher than that of the culture supplemented with 1% glycine at the beginning of culture.     

On the function of the various quinone species in Escherichia coli

The respiratory chain of Escherichia?coli contains three quinones. Menaquinone and demethylmenaquinone have low midpoint potentials and are involved in anaerobic respiration, while ubiquinone, which has a high midpoint potential, is involved in aerobic and nitrate respiration. Here, we report that demethylmenaquinone plays a role not only in trimethylaminooxide-, dimethylsulfoxide- and fumarate-dependent respiration, but also in aerobic respiration. Furthermore, we demonstrate that demethylmenaquinone serves as an electron acceptor for oxidation of succinate to fumarate, and that all three quinol oxidases of E.?coli accept electrons from this naphtoquinone derivative.     

Role of α-helical domains in functioning of ATP-dependent Lon protease of Escherichia coli

Homooligomeric ATP-dependent LonA proteases are bifunctional enzymes belonging to the superfamily of AAA⁺ proteins. Their subunits are formed by five successively connected domains, i.e., N-terminal (N), α-helical (HI(CC)), nucleotide-binding (NB), the second α-helical (H), and proteolytic (P) domains. The presence of the inserted HI(CC) domain determines the uniqueness of LonA proteases among the AAA⁺ proteins. The role of the α-helical domains in the LonA protease functioning was studied with an example of E. coli Lon protease (Ec-Lon). The properties of the intact Ec-Lon and its mutant forms, i.e., Lon-R164A and Lon-R542A bearing the substituted arginine residues at the similar positions in the HI(CC) and H domains, were compared. The H domain was shown to play a crucial role in ATP hydrolysis and enzyme binding to the target protein. The HI(CC) domain is not decisive for the manifestation of the catalytic properties of the enzyme. However, it affects the functioning of Lon ATPase and peptidase sites and is involved in maintaining enzyme stability. The participation of the HI(CC) domain in the formation of three-dimensional structures of LonA proteases and/or their complexes with DNA is suggested.     

The Bacteriophage λ Attachment Site in Wild Strains of Escherichia coli

The attachment site (attlambda) of bacteriophage lambda was examined in wild strains of Escherichia coli. Although the att region is non-coding, the DNA sequence was invariant in the 13 strains examined. Two other non-coding regions showed nine changes, all associated with a single strain. In four of 33 strains, sequences were inserted in or near the attlambda site and in two of these the insert was related to lambda. Among strains that can be lysogenized by lambda, integration was via the attlambda site in all cases. Some resistant strains can be lysogenized, and these have been termed "lenient." Most of these fail to give normal phage yield after induction. In some cases rare lysogens have been formed in cells that belong to a mutant subpopulation.     

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.     

Engineering Escherichia coli for the synthesis of short- and medium-chain α,β-unsaturated carboxylic acids

Concerns over sustained availability of fossil resources along with environmental impact of their use have stimulated the development of alternative methods for fuel and chemical production from renewable resources. In this work, we present a new approach to produce α,β-unsaturated carboxylic acids (α,β-UCAs) using an engineered reversal of the β-oxidation (r-BOX) cycle. To increase the availability of both acyl-CoAs and enoyl-CoAs for α,β-UCA production, we use an engineered Escherichia coli strain devoid of mixed-acid fermentation pathways and known thioesterases. Core genes for r-BOX such as thiolase, hydroxyacyl-CoA dehydrogenase, enoyl-CoA hydratase, and enoyl-CoA reductase were chromosomally overexpressed under the control of a cumate inducible phage promoter. Native E. coli thioesterase YdiI was used as the cycle-terminating enzyme, as it was found to have not only the ability to convert trans-enoyl-CoAs to the corresponding α,β-UCAs, but also a very low catalytic efficiency on acetyl-CoA, the primer and extender unit for the r-BOX pathway. Coupling of r-BOX with YdiI led to crotonic acid production at titers reaching 1.5 g/L in flask cultures and 3.2 g/L in a controlled bioreactor. The engineered r-BOX pathway was also used to achieve for the first time the production of 2-hexenoic acid, 2-octenoic acid, and 2-decenoic acid at a final titer of 0.2 g/L. The superior nature of the engineered pathway was further validated through the use of in silico metabolic flux analysis, which showed the ability of r-BOX to support growth-coupled production of α,β-UCAs with a higher ATP efficiency than the widely used fatty acid biosynthesis pathway. Taken together, our findings suggest that r-BOX could be an ideal platform to implement the biological production of α,β-UCAs.     

Production of the catalytic core of human peptidylglycine α-hydroxylating monooxygenase (hPHMcc) in Escherichia coli

Most mammalian bioactive peptides possess a C-terminal amino acid amide moiety. The presence of the C-terminal amide is a significant impediment to the recombinant production of α-amidated peptides. α-Amidated peptides are produced in vivo by the enzymatic cleavage of a precursor with a C-terminal glycine residue. Peptidylglycine α-hydroxylating monooxygenase catalyzes the key step in the oxidation of the glycine-extended precursors to the α-amidated peptide. Herein, we detail the production of the catalytic core of human peptidylglycine α-hydroxylating monooxygenase (hPHMcc) in Escherichia coli possessing a N-terminal fusion to thioredoxin (Trx). Trx was fused to hPHMcc to enhance the yield of the resulting 52 kDa protein as a soluble and catalytically active enzyme. The Trx-hPHMcc-His(6) fusion was purified to homogeneity and exhibited steady-state kinetic parameters that were similar to purified rat PHMcc. The bacterial production of recombinant hPHMcc will foster efforts to generate α-amidated peptides by the co-expression of hPHMcc and the α-amidated peptide precursors in E. coli or the in vitro amidation of recombinantly expressed α-amidated peptide precursors.     

The binding of haem and zinc in the 1.9 Å X-ray structure of Escherichia coli bacterioferritin

The crystal structure of Escherichia coli bacterioferritin has been solved to 1.9 Å, and shows the symmetrical binding of a haem molecule on the local twofold axis between subunits and a pair of metal atoms bound to each subunit at the ferroxidase centre. These metals have been identified as zinc by the analysis of the structure and X-ray data and confirmed by microfocused proton-induced X-ray emission experiments. For the first time the haem has been shown to be linked to both the internal and the external environments via a cluster of waters positioned above the haem molecule.