Industrial biotransformations for the production of d-amino acids

Optically pure d-amino acids are industrially manufactured by biotransformations of cheap starting materials produced by chemical synthesis or fermentation in combination with the development of enzyme catalysts suitable for the starting materials. dl-Alaninamide, an intermediate of the chemical synthesis of dl-alanine, was efficiently converted to d-alanine by stereoselective hydrolysis with a d-isomer specific amidohydrolase produced by Arthrobacter sp. NJ-26. The total utilization system of dl-alaninamide for the production of optically pure d- and l-alanine was constructed by stereospecific amidohydrolases. On the other hand, d-amino acids were also produced from corresponding l-isomers, which are efficiently manufactured by fermentation. d-Glutamic acid was produced from l-glutamic acid. l-Glutamate was converted to the dl-form by the recombinant glutamate racemase of Lactobacillus brevis ATCC8287. Then l-glutamate in a racemic mixture was selectively decarboxylated to γ-aminobutyrate by the l-glutamate decarboxylase of E. coli ATCC11246. As a result of successive enzymatic reactions, d-glutamate was efficiently produced from l-glutamate by a one-pot reaction. d-Proline was produced by the same strategy from l-proline using the recombinant proline racemase of Clostridium sticklandii ATCC12262. In this case, l-proline was degraded by Candida sp. PRD-234. The strategy from l-amino acids to d-amino acids could be applicable to the manufacture of many d-amino acids.     

Starch-hydrolyzing Enzymes in Germinating Kidney Bean

Enzymatic production of D-Glu was investigated by the succesive reactions of a glutamate racemase (EC 5.1.1.3) and a glutamate decarboxylase (EC 4.1.1.15) on L-Glu.Lactobacillus brevis ATCC8287 was chosen as a source of glutamate racemase. This strain produced a glutamate decarboxylase simultaneously. The glutamate racemase activity in the cell free extracts was 0.035 units/mg protein. The enzyme kept its activity even at 500 Mm of L-Glu (74g/liter). The optimum pHs of the racemase and the decarboxylase were at around 8.5 and below 4.0, respectively. Both enzymes had no activity at the optimum pH for the other enzyme. L-Glu was racemized first by the glutamate racemase at pH 8.5, then the pH was shifted to 4.0 at which L-Glu was decarboxylated by the glutamate decarboxylase. Starting from 100 g/liter of L-Glu, 50 g/liter of D-Glu was produced and no L-Glu remained in the reaction mixture.     

Application of l-glutamate to l-proline fermentation by Corynebacterium acetoacidophilum

l-Proline-producing mutants were screened from Corynebacterium acetoacidophilum ATCC 13870. Proline accumulation in test tube cultivation by TA-20 strain was most effectively stimulated by addition of l-glutamate, rising from 11.8 g/l to 30.8 g/l in the presence of 2% of l-glutamate. Use of radioactively labeled glutamate demonstrated that the increased amount of proline derived from the quantitative conversion of glutamate to proline. Unlike other strains reported previously, this strain showed no dependence on biotin concentration or high (more than 4%) salt concentration. In 2-l jar fermentors, proline productivity was also stimulated by the addition of glutamate. The amount of proline accumulated increased with the concentration of glutamate in the range of 2% to 6%. With 6% of glutamate and 2.5% of ammonium sulfate, 108.3 g/l of l-proline was accumulated in 42 h of cultivation.     

Improvement of gamma-amino butyric acid production by an overexpression of glutamate decarboxylase from Pyrococcus horikoshii in Escherichia coli

In this study, the effect of glutamate decarboxylase from Pyrococcus horikoshii on gamma-aminobutyric acid (GABA) production was investigated in Escherichia coli for the first time. E. coli with overexpressed P. horikoshii glutamate decarboxylase was cultured at various pH levels and temperatures to determine the optimum conditions for GABA production. The highest final GABA concentration, 5.07 g/L, was obtained from 10 g/L of monosodium glutamate (MSG) with a GABA yield of 83% at 30°C and pH 3.5. When P. horikoshii glutamate decarboxylase was introduced into a GABA aminotransferase knock-out E. coli XBT strains, 5.69 g/L of GABA was produced with a GABA yield of 93%.     

Pyruvic acid production by a lipoic acid auxotroph of Escherichia coliW1485

A lipoic acid auxotroph of Escherichia coli K-12, strain W1485lip2 (ATCC25645), produced pyruvic acid aerobically from glucose under the lipoic acid-deficient conditions, while the prototrophic parent strain, W1485 (ATCC12435), produced 2-oxoglutaric acid as the main product. The mechanism of the pyruvic acid production by strain W1485lip2 was found to be the impaired oxidative decarboxylation of pyruvic acid caused by the decrease in the activity of pyruvate dehydrogenase complex under the conditions of lipoic acid deficiency. Under the optimum culture conditions using the pH-controlled jar fermentor, 25.5?g/l pyruvic acid was obtained from 50?g/l glucose after the culture for 32–40?h at pH?6.0. The relationship between the pyruvic acid productivity and the pyruvate dehydrogenase complex activity in jar-fermentor culture was discussed.     

Overexpression of Neurospora crassa OR74A glutamate decarboxylase in Escherichia coli for efficient GABA production

This study investigated the effect of glutamate decarboxylase from Neurospora crassa OR74A on GABA production in Escherichia coli. GABA is one of the inhibitory neurotransmitters in the mammalian central nervous system, and can be used as a precursor of promising biopolymer Nylon 4. E. coli that overexpressed N. crassa glutamate decarboxylase was cultured at various pH levels and temperatures to determine optimum conditions for GABA production. When the recombinant E. coli strain was cultured at 30°C and pH 3, a final GABA concentration of 5.26 g/L was obtained from 10 g/L of monosodium glutamate (MSG), corresponding to a GABA yield of 86.23%.     

Pyruvic acid production by a lipoic acid auxotroph of Escherichia coliW1485

A lipoic acid auxotroph of Escherichia coli K-12, strain W1485lip2 (ATCC25645), produced pyruvic acid aerobically from glucose under the lipoic acid-deficient conditions, while the prototrophic parent strain, W1485 (ATCC12435), produced 2-oxoglutaric acid aas the main product. The mechanism of the pyruvic acid production by strain W1485lip2 was found to be the impaired oxidative decarboxylation of pyruvic acid caused by the decrease in the activity of pyruvate dehydrogenase complex under the conditions of lipoic acid deficiency. Under the optimum culture conditions using the pH-controlled jar fermentor, 25.5 g/l pyruvic acid was obtained from 50 g/l glucose after the culture for 32–40 h at pH6.0. The relationship between the pyruvic acid productivity and the pyruvate dehydrogenase complex activity in jar-fermentor culture was discussed.     

Screening of Indonesian peat soil bacteria producing antimicrobial compounds

The development and world-wide spread of multidrug-resistant (MDR) bacteria have a high concern in the medicine, especially the extended-spectrum of beta-lactamase (ESBL) producing Escherichia coli and methicillin-resistant Staphylococcus aureus (MRSA). There are currently very limited effective antibiotics to treat infections caused by MDR bacteria. Peat-soil is a unique environment in which bacteria have to compete each other to survive, for instance, by producing antimicrobial substances. This study aimed to isolate bacteria from peat soils from South Kalimantan Indonesia, which capable of inhibiting the growth of Gram-positive and Gram-negative bacteria. Isolates from peat soil were grown and identified phenotypically. The cell-free supernatant was obtained from broth culture by centrifugation and was tested by agar well-diffusion technique against non ESBL-producing E. coli ATCC 25922, ESBL-producing E. coli ATCC 35218, methicillin susceptible Staphylococcus aureus (MSSA) ATCC 29,213 and MRSA ATCC 43300. Putative antimicrobial compounds were separated using SDS-PAGE electrophoresis and purified using electroelution method. Antimicrobial properties of the purified compounds were confirmed by measuring the minimum inhibitory concentration (MIC) and minimum bactericidal concentration (MBC). In total 28 isolated colonies were recovered; three (25PS, 26PS, and 27PS) isolates produced proteins with strong antimicrobial activities against both reference strains. The substance of proteins from three isolates exerted strong antimicrobial activity against ESBL-producing E. coli ATCC 35,218 (MIC = 2,80 µg/mL (25PS), 3,76 µg/mL (26PS), and 2,41 µg/mL (27PS), and MRSA ATCC 43,300 (MIC = 4,20 µg/mL (25PS), 5,65 µg/mL (26PS), and 3,62 µg/mL (27PS), and also had the ability bactericidal properties against the reference strains. There were isolates from Indonesian peat which were potentials sources of new antimicrobials.     

Microbial Production of Lysine and Threonine from Whey Permeate

Extracellular accumulation of lysine and threonine was investigated in modified whey permeate by using Brevibacterium lactofermentum ATCC 21086 and Escherichia coli ATCC 21151. Whey permeate was prepared from whey by membrane ultrafiltration, and lactose was hydrolyzed by treating permeate with HCl or β-galactosidase. The highest amount of lysine (3.3 g/liter) was produced from a mixture of acid-hydrolyzed whey permeate and yeast extract (0.2%). The highest amount of threonine (3.6 g/liter) was produced from a mixture of whey permeate, (NH₄)₂SO₄ (1.4%), yeast extract (0.1%), and Na₂CO₃ (0.3%).     

Required characteristics of Paenibacillus polymyxa JB-0501 as potential probiotic

The ability of Paenibacillus polymyxa to inhibit the growth of Escherichia coli generic ATCC 25922 (Escherichia coli ATCC 25922) and to adhere to monolayers of the enterocyte-like human cell line Caco-2 was evaluated. P. polymyxa JB-0501 (P. polymyxa JB-0501), found in a livestock feed probiotic supplement, was compared to P. polymyxa reference strain ATCC 43685 and ATCC 7070 (P. polymyxa ATCC) in terms of carbohydrate utilization and resistance to lysozyme, acid, bile salts, and hydrogen peroxide. JB-0501 grew at pH 4.5 and at H₂O₂ concentrations less than 7.3 μg/ml and presented a higher affinity to hexadecane and decane. Bile salts at 0.2 % inhibited the growth of all three strains. P. polymyxa JB-0501 and P. polymyxa ATCC 43865 adhered to Caco-2 cell monolayers. The percentage of cells that adhered ranged from about 0.35 to 6.5 % and was partially proportional to the number applied. Contact time (from 15 min to 1 h) had little impact on adhesion. P. polymyxa JB-0501 inhibited the growth of E. coli ATCC 25922, as proven by the diffusion tests in agar. Taken together, these results suggested that P. polymyxa JB-0501 has the potential probiotic properties to justify its consideration as a livestock feed supplement.     

Molecular cloning, expression, and characterization of a thermostable glutamate racemase from a hyperthermophilic bacterium, Aquifex pyrophilus

A gene encoding glutamate racemase has been cloned from Aquifex pyrophilus, a hyperthermophilic bacterium, and expressed in Escherichia coli. The A. pyrophilus glutamate racemase is composed of 254 amino acids and shows high homology with glutamate racemase from Escherichia coli, Bacillus subtilis, or Lactobacillus brevis. This racemase converts l- or d-glutamate to d- or l-glutamate, respectively, but not other amino acids such as alanine, aspartate, and glutamine. The cloned gene was expressed and the protein was purified to homogeneity. The A. pyrophilus racemase is present as a dimer but it oligomerizes as the concentration of salt is increased. The K _m and k_cat values of the overexpressed A. pyrophilus glutamate racemase for the racemization of l-glutamate to the d-form and the conversion of d-glutamate to the l-form were measured as 1.8 ± 0.4 mM and 0.79 ± 0.06 s⁻¹ or 0.50 ± 0.07 mM and 0.25 ± 0.01 s⁻¹, respectively. Complete inactivation of the racemase activity by treatment with cysteine-modifying reagents suggests that cysteine residues may be important for activity. The protein shows strong thermostability in the presence of phosphate ion, and it retains more than 50% of its activity after incubation at 85°C for 90 min. Received: September 11, 1998 / Accepted: January 12, 1999     

Synthesis of nylon 4 from gamma-aminobutyrate (GABA) produced by recombinant Escherichia coli

In this study, we developed recombinant Escherichia coli strains expressing Lactococcus lactis subsp. lactis Il1403 glutamate decarboxylase (GadB) for the production of GABA from glutamate monosodium salt (MSG). Syntheses of GABA from MSG were examined by employing recombinant E. coli XL1-Blue as a whole cell biocatalyst in buffer solution. By increasing the concentration of E. coli XL1-Blue expressing GadB from the OD₆₀₀ of 2–10, the concentration and conversion yield of GABA produced from 10 g/L of MSG could be increased from 4.3 to 4.8 g/L and from 70 to 78 %, respectively. Furthermore, E. coli XL1-Blue expressing GadB highly concentrated to the OD₆₀₀ of 100 produced 76.2 g/L of GABA from 200 g/L of MSG with 62.4 % of GABA yield. Finally, nylon 4 could be synthesized by the bulk polymerization using 2-pyrrolidone that was prepared from microbially synthesized GABA by the reaction with Al₂O₃ as catalyst in toluene with the yield of 96 %.     

Bacterial cell-surface displaying of thermo-tolerant glutamate dehydrogenase and its application in l-glutamate assay

In this paper, glutamate dehydrogenase (Gldh) is reported to efficiently display on Escherichia coli cell surface by using N-terminal region of ice the nucleation protein as an anchoring motif. The presence of Gldh was confirmed by SDS-PAGE and enzyme activity assay. Gldh was detected mainly in the outer membrane fraction, suggesting that the Gldh was displayed on the bacterial cell surface. The optimal temperature and pH for the bacteria cell-surface displayed Gldh (bacteria-Gldh) were 70 °C and 9.0, respectively. Additionally, the fusion protein retained almost 100% of its initial enzymatic activity after 1 month incubation at 4 °C. Transition metal ions could inhibit the enzyme activity to different extents, while common anions had little adverse effect on enzyme activity. Importantly, the displayed Gldh is most specific to l-glutamate reported so far. The bacterial Gldh was enabled to catalyze oxidization of l-glutamate with NADP⁺ as cofactor, and the resultant NADPH can be detected spectrometrically at 340 nm. The bacterial-Gldh based l-glutamate assay was established, where the absorbance at 340 nm increased linearly with the increasing l-glutamate concentration within the range of 10 − 400 μM. Further, the proposed approach was successfully applied to measure l-glutamate in real samples.     

Application of a thermostable glutamate racemase from Bacillus sp. SK-1 for the production of -phenylalanine in a multi-enzyme system

A gene encoding glutamate racemase (GluRA) was found in a thermophilic Bacillus strain named SK-1. The gene was cloned and expressed in Escherichia coli WM335, a -glutamate auxotroph. It consists of 792 bp with a start codon, TTG. The amino acid sequence deduced from the gene indicates that the GluRA has two cysteines and their surrounding regions are well conserved. The GluRA produced in the recombinant E. coli was purified to homogeneity by heat-treatment and Resource Q and Phenyl sepharose column chromatographies. The enzyme, which was determined to be a monomeric protein with a molecular weight of 29,000, did not require a cofactor such as pyridoxal 5′-phosphate, nicotinamide, or flavin for its activity. The enzyme was stable after incubation at 55 °C and retained 60% of its original activity after incubation at 60 °C. It was found to be stable in the region of pH 6.0–11.5. The thermostable GluRA was used as a catalyst in a multi-enzyme system composed of four enzyme reactions for the production of -phenylalanine. By running the multi-enzyme system for 35 h, 58 g l⁻¹ of -phenylalanine was produced with 100% of optical purity from equimolar amount of phenylpyruvate.     

Improvement of productivity of active form of glutamate racemase in Escherichia coli by coexpression of folding accessory proteins

Since two classes of folding accessory proteins, molecular chaperones and foldases, prevent the misfolding of newly synthesized polypeptides in the cell, their coexpression could be expected to improve the productivity of soluble and active recombinant proteins. Escherichia coli cytoplasmic glutamate racemase (GluR), which has five cysteine thiol groups and no disulfide bond, was selected as a model enzyme and overexpressed in E. coli. The effects of coexpressing a series of folding accessory proteins (DnaK, DnaJ, GrpE, GroEL/ES, trigger factor (TF), DsbA, DsbB, DsbC, DsbD, and thioredoxin (Trx)) on the productivity of active GluR in E. coli were examined. A relatively large amount of active GluR produced by mild induction with 10 μM isopropyl-β-d-thiogalactopyranoside (IPTG). Active GluR productivity was further increased 2.2–2.3-fold by coexpression of GroEL/ES, Trx, or DsbB–DsbD (DsbBD), while it was decreased by coexpression of DnaK–DnaJ–GrpE and TF. These results demonstrate that coexpression of appropriate folding accessory proteins could significantly improve the productivity of active form of proteins in E. coli.     

Adsorption of charged substrates and products on an enzyme reactor prepared by glutaraldehyde coupling on alkylamine derivatives of Ti(IV)-coated porous silica beads

Ti(IV) coating of porous silica beads, followed by derivatization with 1,6-diaminohexane and activation with glutaraldehyde was tested for the immobilization of glutamate decarboxylase (l-glutamate 1-carboxylyase, EC 4.1.1.15). The enzyme column prepared with the immobilized glutamate decarboxylase was designed for the preparation of 1 μmol γ-[¹³N]aminobutyric acid, a new tracer for positron emission tomography. Preliminary results, indicating high immobilization yields of active enzyme with good long term stabilities, led to a more detailed investigation of the Ti(IV) coating. When a column, containing about 1 g of enzyme-loaded beads was used for the synthesis of γ-[¹³N]aminobutyric acid (GABA) from l-[¹³N]glutamate, most of the¹³N activity remained adsorbed onto the column. The elution patterns of l-glutamate and GABA from columns of glutamate decarboxylase, immobilized on Ti(IV) coated silica beads, were investigated by using an h.p.l.c. u.v. detector. Different treatments of the Ti(IV) coated supports were tested to improve the desorption kinetics of GABA and l-glutamate. None of these methods gave a satisfactory improvement of the elution patterns of GABA and l-glutamate. The results indicate that the Ti(IV) coated silica beads have a large adsorption capacity, even though the enzyme is covalently linked. The described immobilization method is not recommended for enzymes having charged substrates or products and in which a small amount of substrate has to be applied onto a reactor containing a large amount of Ti(IV) coated support. The method can be applied when the enzyme reactor is operated in steady state conditions with continuous supply of substrate.     

Production of mesaconate in Escherichia coli by engineered glutamate mutase pathway

Mesaconate is an intermediate in the glutamate degradation pathway of microorganisms such as Clostridium tetanomorphum. However, metabolic engineering to produce mesaconate has not been reported previously. In this work, two enzymes involved in mesaconate production, glutamate mutase and 3-methylaspartate ammonia lyase from C. tetanomorphum, were recombinantly expressed in Escherichia coli. To improve mesaconate production, reactivatase of glutamate mutase was discovered and adenosylcobalamin availability was increased. In addition, glutamate mutase was engineered to improve the in vivo activity. These efforts led to efficient mesaconate production at a titer of 7.81 g/L in shake flask with glutamate feeding. Then a full biosynthetic pathway was constructed to produce mesaconate at a titer of 6.96 g/L directly from glucose. In summary, we have engineered an efficient system in E. coli for the biosynthesis of mesaconate.     

Reversal Effect of Potassium Ion on Microbial Growth Inhibition by Combinations of NaCl,Ethanol and Perillaldehyde

The glutamate racemase (EC 5.1.1.3) gene of a lactic acid bacterium, Pediococcus pentosaceus, was cloned into Escherichia coli C600 with a vector plasmid, pBR322. The requirement of l-glutamate for the growth of E. coli in the minimum medium containing d-glutamate and the formation of a red pigment in a coupled enzyme reaction mixture were used to select clones expressing glutamate racemase activity. Glutamate racemase overproduced as 0.3— 2.0% of the total soluble proteins in a clone carrying the plasmid pICR221, 10.3 kb of DNA, was purified from cell extracts about 130-fold to homogeneity. The purified enzyme has a molecular weight of about 40,000 and is a single polypeptide chain. Glutamate is the sole substrate for the enzyme. Unlike many other amino acid racemases, glutamate racemase is devoid of cofactors: there is no evidence for pyridoxal 5’-phosphate or FAD in the ultraviolet spectrum of the purified enzyme, and the enzyme is not inactivated by carbonyl reagents such as hydroxylamine and sodium borohydride.     

Optimization of single-cell-protein production from cassava starch using Schwanniomyces castellii

Schwanniomyces castellii B5285 grew faster and produced greater biomass and higher protein yield than either S. alluvius ATCC 26074 or S. alluvius 81Y when these amylolytic yeasts were grown with 2% (w/v) cassava starch as sole C source. With 0.5% (w/v) glutamate as N source, S. castellii reached 7.12 g cell dry mass/l, with a protein yield of 6.4 g/100 g starch. The optimal agitation speed, aeration rate and pH for growth of this yeast in a fermenter were 400 rev/min, 1.67 vol./vol.min. and 5.0, respectively. Tween 80 at 0.1% increased cell dry mass to 8.90 g/l, cell yield to 44 g/100 g starch and protein yield to 7.4 g/100 g starch.The authors are with the Department of industrial Biotechnology, Faculty of Agro-Industry, Prince of Songkla University, Hat Yai 90110, Thailand