Effects of l-lysine and d-lysine on ɛ-Poly-l-lysine biosynthesis and their metabolites by Streptomyces ahygroscopicus GIM8

?-Poly-l-lysine (?-PL), produced by Streptomyces or Kitasatospora strains, is a homo-poly-amino acid of l-lysine, which is used as a safe food preservative. In this study, the effects of l-lysine and its isomer, d-lysine, on ?-PL biosynthesis and their metabolites by the ?-PL-producing strain Streptomyces ahygroscopicus GIM8 were determined. The results indicated that l-lysine added into the fermentation medium in the production phase mainly served as a precursor for ?-PL biosynthesis during the flask culture phase, leading to greater ?-PL production. At an optimum level of 3 mM l-lysine, a ?-PL yield of 1.16 g/L was attained, with a 41.4% increment relative to the control of 0.78 g/L. Regarding d-lysine, the production of ?-PL increased by increasing its concentrations up to 6 mM in the initial fermentation medium. Interestingly, ?-PL production (1.20 g/L) with the addition of 3 mM d-lysine into the initial fermentation medium in flasks was higher than that of the initial addition of 3 mM L-lysine (1.06 g/L). The mechanism by which d-lysine improves ?-PL biosynthesis involves its utilization that leads to greater biomass. After S. ahygroscopicus GIM8 was cultivated in the defined medium with L-lysine, several key metabolites, including 5-aminovalerate, pipecolate, and l-2-aminoadipate formed in the cells, whereas only l-2-aminoadipate was observed after d-lysine metabolism. This result indicates that l-lysine and d-lysine undergo different metabolic pathways in the cells. Undoubtedly, the results of this study are expected to aid the understanding of ?-PL biosynthesis and serve as reference for the formulation of an alternative approach to improve ?-PL productivity using l-lysine as an additional substrate in the fermentation medium.     

Improvement of l-lactic acid production by osmotic-tolerant mutant of Lactobacillus casei at high temperature

l-Lactic acid production by Lactobacillus casei was used as a model to study the mechanism of substrate inhibition and the strategy for enhancing l-lactic acid production. It was found that the concentration of cell growth and l-lactate decreased with the increase of glucose concentration and fermentation temperature. To enhance the osmotic stress resistance of the strain at high temperature, a mutant G-03 was screened and selected with 360?g/L glucose at 45°C as the selective criterion. To further increase the cell growth for lactic acid production, 3?g/L of biotin was supplemented to the medium. As a result, l-lactate concentration by the mutant G-03 reached 198.2?g/L (productivity of 5.5?g?L^?1?h^?1) at 41°C in a 7-L fermentor with 210?g/L glucose as carbon source. l-Lactate concentration and productivity of mutant G-03 were 115.2% and 97.8% higher than those of the parent strain, respectively. The strategy for enhancing l-lactic acid production by increasing osmotic stress resistance at high temperature may provide an alternative approach to enhance organic acid production with other strains.     

Homofermentative production of d-lactic acid from sucrose by a metabolically engineered Escherichia coli

Escherichia coli W, a sucrose-positive strain, was engineered for the homofermentative production of d-lactic acid through chromosomal deletion of the competing fermentative pathway genes (adhE, frdABCD, pta, pflB, aldA) and the repressor gene (cscR) of the sucrose operon, and metabolic evolution for improved anaerobic cell growth. The resulting strain, HBUT-D, efficiently fermented 100?g?sucrose?l^?1 into 85?g?d-lactic acid?l^?1 in 72–84?h in mineral salts medium with a volumetric productivity of ~1?g?l^?1?h^?1, a product yield of 85?% and d-lactic acid optical purity of 98.3?%, and with a minor by-product of 4?g?acetate?l^?1. HBUT-D thus has great potential for production of d-lactic acid using an inexpensive substrate, such as sugar cane and/or beet molasses, which are primarily composed of sucrose.     

NAD+-dependent xylitol dehydrogenase (xdhA) and l-arabitol-4-dehydrogenase (ladA) deletion mutants of Aspergillus oryzae for improved xylitol production

Xylitol dehydrogenase (XDHA) and l-arabitol dehydrogenase (LADA) are two key enzymes in xylan metabolism catalyzing the oxidation of xylitol to d-xylulose and arabitol to l-xylulose, respectively. In Aspergillus oryzae, XDHA and LADA are encoded by xdhA and ladA. We deleted xdhA and ladA and xdhA–ladA to generate mutants with decreased dehydrogenase activities and increased xylitol production. The mutants were constructed by homologous transformation into A. oryzae P4 (?pyrG) using pyrG as a selectable marker. The xylitol productivity of the mutants was measured using d-xylose as the sole carbohydrate source. xdhA, ladA, and the double-deletion mutant produced, respectively, 12.4 g xylitol/l with a yield of 0.24 g/g d-xylose, 12.4 g/l with a yield of 0.33 g/g d-xylose, and 8.6 g/l at a yield of 0.26 g/g d-xylose.     

Biosynthesis of ethylene glycol in Escherichia coli

Ethylene glycol (EG) is an important platform chemical with steadily expanding global demand. Its commercial production is currently limited to fossil resources; no biosynthesis route has been delineated. Herein, a biosynthesis route for EG production from d-xylose is reported. This route consists of four steps: d-xylose?→?d-xylonate?→?2-dehydro-3-deoxy-d-pentonate?→?glycoaldehyde?→?EG. Respective enzymes, d-xylose dehydrogenase, d-xylonate dehydratase, 2-dehydro-3-deoxy-d-pentonate aldolase, and glycoaldehyde reductase, were assembled. The route was implemented in a metabolically engineered Escherichia coli, in which the d-xylose?→?d-xylulose reaction was prevented by disrupting the d-xylose isomerase gene. The most efficient construct produced 11.7 g?L^?1 of EG from 40.0 g?L^?1 of d-xylose. Glycolate is a carbon-competing by-product during EG production in E. coli; blockage of glycoaldehyde?→?glycolate reaction was also performed by disrupting the gene encoding aldehyde dehydrogenase, but from this approach, EG productivity was not improved but rather led to d-xylonate accumulation. To channel more carbon flux towards EG than the glycolate pathway, further systematic metabolic engineering and fermentation optimization studies are still required to improve EG productivity.     

d-Amino Acid-Induced Expression of d-Amino Acid Oxidase in the Yeast Schizosaccharomyces pombe

We investigated d-amino acid oxidase (DAO) induction in the popular model yeast Schizosaccharomyces pombe. The product of the putative DAO gene of the yeast expressed in E.?coli displayed oxidase activity to neutral and basic d-amino acids, but not to an l-amino acid or acidic d-amino acids, showing that the putative DAO gene encodes catalytically active DAO. DAO activity was weakly detected in yeast cells grown on a culture medium without d-amino acid, and was approximately doubled by adding d-alanine. The elimination of ammonium chloride from culture medium induced activity by up to eight-fold. l-Alanine also induced the activity, but only by about half of that induced by d-alanine. The induction by d-alanine reached a maximum level at 2?h cultivation; it remained roughly constant until cell growth reached a stationary phase. The best inducer was d-alanine, followed by d-proline and then d-serine. Not effective were N-carbamoyl-d,l-alanine (a better inducer of DAO than d-alanine in the yeast Trigonopsis variabilis), and both basic and acidic d-amino acids. These results showed that S. pombe DAO could be a suitable model for analyzing the regulation of DAO expression in eukaryotic organisms.     

Production of d-arabitol from raw glycerol by Candida quercitrusa

To promote the effective use of raw glycerol (a by-product of biodiesel production), 110 yeast strains that produce d-arabitol from glycerol were isolated from environmental samples. Among them, strain 17-2A was an effective d-arabitol producer in the presence of 250 g/l glycerol and was identified as Candida quercitrusa based on morphological, physicochemical, and phylogenetic analyses. C. quercitrusa type strain NBRC1022 produced the greatest quantity of d-arabitol (41.7 g/l) when the ability to produce d-arabitol from raw glycerol was compared among C. quercitrusa 17-2A and its phylogenetically related strains in flask culture. Under optimized culture conditions, strain NBRC1022 produced d-arabitol at a concentration of 58.2 g/l after a 7-day cultivation in 250 g/l glycerol, 6 g/l yeast extract, and 2 g/l CaCl₂. The culture conditions were further investigated with raw glycerol using a jar fermenter; the concentration of d-arabitol reached 67.1 g/l after 7 days and 85.1 g/l after 10 days, respectively, which corresponded to 0.40 g/g of glycerol. To our knowledge, the present d-arabitol yield from glycerol is higher than reported previously using microbial production.     

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.     

Characterization of a recombinant l-rhamnose isomerase from Bacillus subtilis and its application on production of l-lyxose and l-mannose

The gene of an l-rhamnose isomerase (RhaA) from Bacillus subtilis was cloned to the pET28a(+) and then expressed in the E. coli ER2566. The expressed enzyme was purified with a specific activity of 3.58 U/mg by His-Trap affinity chromatography. The recombinant enzyme existed as a 194 kDa tetramer and the maximal activity was observed at pH 8.0 and 60°C. The RhaA displayed activity for l-rhamnose, l-lyxose, l-mannose, d-allose, d-gulose, d-ribose, and l-talose, among all aldopentoses and aldohexoses and it showed enzyme activity for l-form monosaccharides such as l-rhamnose, l-lyxose, l-mannose, and l-talose. The catalytic efficiency (k _cat/K _m) of the recombinant enzyme for l-rhamnose, l-lyxose, and l-mannose were 7,460, 1,013, and 258 M/sec. When l-xylulose 100 g/L and l-fructose 100 g/L were used as substrates, the optimum concentrations of RpiB were determined with 6 and 15 U/mL, respectively. The l-lyxose 40 g/L was produced from l-xylulose 100 g/L by the enzyme during 60 min, while l-mannose 25 g/L was produced from l-fructose 100 g/L for 80 min. The results suggest that RhaA from B. subtilis is a potential producer of l-form monosaccharides.     

Amperometric microbiosensor as an alternative tool for investigation of d-serine in brain

This paper discusses the application of a reagentless, selective microbiosensor as a useful alternative tool for monitoring d-serine in neural samples. The main components of the 125-μm-diameter disk biosensor were d-amino acid oxidase for d-serine sensitivity (linear region slope, 61?±?7?μA?cm^–2?mM^–1; limit of detection, 20?nM), and poly-phenylenediamine for rejection of electroactive interference. The response time of the biosensor was of the order of 1?s, ideal for ‘real-time’ monitoring, and detection of systemically administered d-serine in brain extracellular fluid is demonstrated. Exploitation of this probe might resolve queries involving regulation of d-serine in excitotoxicity, and modulation of N-methyl-d-aspartate receptor function by d-serine and glycine in the central nervous system.     

Properties of the sugar carrier in Baker's yeast

Incubation ofSaccharomyces cerevisiae cells withd-galactose induced the formation of galactose-utilizing enzymes, among them a monosaccharide carrier, apparently synthesized as a proteinde novo. The synthesis of the carrier preceded that of galactokinase by as much as 2 h. The inducible carrier shows a preference for monosaccharides with an axial hydroxyl group at carbon 4 of theC1 chair conformation or at carbon 2 of the1C chair conformation. Through its mediation, some sugars normally poorly transported (d-galactose,d-fucose,l-xylose,l-arabinose) can enter into the entire cell water, occupying then one more kinetic (and morphological ?) compartment than before induction. Some other monosaccharides, readily transported even by a constitutive carrier system (e.g.l-sorbose,d-xylose,d-arabinose) share the newly synthesized carrier.     

Function of aspartic acid residues in optimum pH control of l-arabinose isomerase from Lactobacillus fermentum

l-Arabinose isomerase (l-AI) catalyzes the isomerization of l-arabinose to l-ribulose and d-galactose to d-tagatose. Most reported l-AIs exhibit neutral or alkaline optimum pH, which is less beneficial than acidophilic ones in industrial d-tagatose production. Lactobacillus fermentum l-AI (LFAI) is a thermostable enzyme that can achieve a high conversion rate for d-galactose isomerization. However, its biocatalytic activity at acidic conditions can still be further improved. In this study, we report the single- and multiple-site mutagenesis on LFAI targeting three aspartic acid residues (D268, D269, and D299). Some of the lysine mutants, especially D268K/D269K/D299K, exhibited significant optimum pH shifts (from 6.5 to 5.0) and enhancement of pH stability (half-life time increased from 30 to 62 h at pH 6.0), which are more favorable for industrial applications. With the addition of borate, d-galactose was isomerized into d-tagatose by D268K/D269K/D299K at pH 5.0, resulting in a high conversion rate of 62 %. Based on the obtained 3.2-Å crystal structure of LFAI, the three aspartic acid residues were found to be distant from the active site and possibly did not participate in substrate catalysis. However, they were proven to possess similar optimum pH control ability in other l-AI, such as that derived from Escherichia coli. This study sheds light on the essential residues of l-AIs that can be modified for desired optimum pH and better pH stability, which are useful in d-tagatose bioproduction.     

Enhanced saccharification of rice straw using hypochlorite-hydrogen peroxide

Rice straw is a lignocellulosic biomass, and has been recognized as a renewable organic substance and alternative energy source. In this study, rice straw was pretreated with hypochlorite-hydrogen peroxide (Ox-B) solution. The optimal pretreatment conditions were determined via response surface methodology, and the pretreated rice straw was hydrolyzed with exo-glucanase, endoglucanase, hemicellulase, and β-glucosidase Accellerase 1000? (endo-glucanase equivalent activity of 1,250 carboxy methyl cellulose (CMC) U/g of rice straw pretreated for 24 h). The optimal conditions were as follows: 60 min pretreatment using Ox-B solution containing 0.6% hypochlorite and 25% hydrogen peroxide for 1 g of rice straw in a total reaction volume of 240 mL. Under these conditions, 406.8 mg of d-glucose and 224.0 mg of d-xylose were obtained from 1 g of rice straw. The fermentation of enzymatic hydrolysates containing 8.14 g/L d-glucose and 4.49 g/L d-xylose with Pichia stipitis generated 3.65 g/L of ethanol with a corresponding yield of 0.37 g/g. The maximum possible ethanol conversion rate is 72.54%.     

Metabolic engineering of Escherichia coli for biosynthesis of d-galactonate

d-galactose is an attractive substrate for bioconversion. Herein, Escherichia coli was metabolically engineered to convert d-galactose into d-galactonate, a valuable compound in the polymer and cosmetic industries. d-galactonate productions by engineered E. coli strains were observed in shake flask cultivations containing 2 g L^?1 d-galactose. Engineered E. coli expressing gld coding for galactose dehydrogenase from Pseudomonas syringae was able to produce 0.17 g L^?1 d-galactonate. Inherent metabolic pathways for assimilating both d-galactose and d-galactonate were blocked to enhance the production of d-galactonate. This approach finally led to a 7.3-fold increase with d-galactonate concentration of 1.24 g L^?1 and yield of 62.0 %. Batch fermentation in 20 g L^?1 d-galactose of E. coli ?galK?dgoK mutant expressing the gld resulted in 17.6 g L^?1 of d-galactonate accumulation and highest yield of 88.1 %. Metabolic engineering strategy developed in this study could be useful for industrial production of d-galactonate.     

Genetically engineered Pichia pastoris yeast for conversion of glucose to xylitol by a single-fermentation process

Xylitol is industrially synthesized by chemical reduction of d-xylose, which is more expensive than glucose. Thus, there is a growing interest in the production of xylitol from a readily available and much cheaper substrate, such as glucose. The commonly used yeast Pichia pastoris strain GS115 was shown to produce d-arabitol from glucose, and the derivative strain GS225 was obtained to produce twice amount of d-arabitol than GS115 by adaptive evolution during repetitive growth in hyperosmotic medium. We cloned the d-xylulose-forming d-arabitol dehydrogenase (DalD) gene from Klebsiella pneumoniae and the xylitol dehydrogenase (XDH) gene from Gluconobacter oxydans. Recombinant P. pastoris GS225 strains with the DalD gene only or with both DalD and XDH genes could produce xylitol from glucose in a single-fermentation process. Three-liter jar fermentation results showed that recombinant P. pastoris cells with both DalD and XDH converted glucose to xylitol with the highest yield of 0.078 g xylitol/g glucose and productivity of 0.29 g xylitol/L h. This was the first report to convert xylitol from glucose by the pathway of glucose–d-arabitol–d-xylulose–xylitol in a single process. The recombinant yeast could be used as a yeast cell factory and has the potential to produce xylitol from glucose.     

New insights on the role of free d-aspartate in the mammalian brain

Free d-aspartate (d-Asp) occurs in substantial amounts in the brain at the embryonic phase and in the first few postnatal days, and strongly decreases in adulthood. Temporal reduction of d-Asp levels depends on the postnatal onset of d-aspartate oxidase (DDO) activity, the only enzyme able to selectively degrade this d-amino acid. Several results indicate that d-Asp binds and activates N-methyl-d-aspartate receptors (NMDARs). Accordingly, recent studies have demonstrated that deregulated, higher levels of d-Asp, in knockout mice for Ddo gene and in d-Asp-treated mice, modulate hippocampal NMDAR-dependent long-term potentiation (LTP) and spatial memory. Moreover, similarly to d-serine, administration of d-Asp to old mice is able to rescue the physiological age-related decay of hippocampal LTP. In agreement with a neuromodulatory action of d-Asp on NMDARs, increased levels of this d-amino acid completely suppress long-term depression at corticostriatal synapses and attenuate the prepulse inhibition deficits produced in mice by the psychotomimetic drugs, amphetamine and MK-801. Based on the evidence which points to the ability of d-Asp to act as an endogenous agonist on NMDARs and considering the abundance of d-Asp during prenatal and early life, future studies will be crucial to address the effect of this molecule in the developmental processes of the brain controlled by the activation of NMDARs.     

d-Tagatose production in the presence of borate by resting Lactococcus lactis cells harboring Bifidobacterium longum l-arabinose isomerase

Bifidobacterium longum NRRL B-41409 l-arabinose isomerase (l-AI) was overexpressed in Lactococcus lactis using a phosphate depletion inducible expression system. The resting L. lactis cells harboring the B. longum l-AI were used for production of d-tagatose from d-galactose in the presence of borate buffer. Multivariable analysis suggested that high pH, temperature and borate concentration favoured the conversion of d-galactose to d-tagatose. Almost quantitative conversion (92 %) was achieved at 20 g L^?1 substrate and at 37.5 °C after 5 days. The d-tagatose production rate of 185 g L^?1 day^?1 was obtained at 300 g L^?1 galactose, at 1.15 M borate, and at 41 °C during 10 days when the production medium was changed every 24 h. There was no significant loss in productivity during ten sequential 24 h batches. The initial d-tagatose production rate was 290 g L^?1 day^?1 under these conditions.     

High Yield Recombinant Expression, Characterization and Homology Modeling of Two Types of Cis-epoxysuccinic Acid Hydrolases

The cis-epoxysuccinate hydrolases (CESHs), members of epoxide hydrolase, catalyze cis-epoxysuccinic acid hydrolysis to form d(?)-tartaric acid or l(+)-tartaric acid which are important chemicals with broad scientific and industrial applications. Two types of CESHs (CESH[d] and CESH[l], producing d(?)- and l(+)-tartaric acids, respectively) have been reported with low yield and complicated purification procedure in previous studies. In this paper, the two CESHs were overexpressed in Escherichia coli using codon-optimized genes. High protein yields by one-step purifications were obtained for both recombinant enzymes. The optimal pH and temperature were measured for both recombinant CESHs, and the properties of recombinant enzymes were similar to native enzymes. Kinetics parameters measured by Lineweaver?CBurk plot indicates both enzymes exhibited similar affinity to cis-epoxysuccinic acid, but CESH[l] showed much higher catalytic efficiency than CESH[d], suggesting that the two CESHs have different catalytic mechanisms. The structures of both CESHs constructed by homology modeling indicated that CESH[l] and CESH[d] have different structural folds and potential active site residues. CESH[l] adopted a typical ??/??-hydrolase fold with a cap domain and a core domain, whereas CESH[d] possessed a unique TIM barrel fold composed of 8 ??-helices and 8 ??-strands, and 2 extra short ??-helices exist on the top and bottom of the barrel, respectively. A divalent metal ion, preferred to be zinc, was found in CESH[d], and the ion was proved to be crucial to the enzymatic activity. These results provide structural insight into the different catalytic mechanisms of the two CESHs.     

D-amino acids in the cell pool of bacteria

About 30 different bacterial species were tested for the possible presence of freed-amino acids in their cell pool. Gram-positive bacteria particularly the species of the genusBacillus have a fairly large pool of freely extractabled-amino acids. Varied quantities of freed-amino acids were detected inBacillus subtilis B₃,Bacillus subtilis Marburg,Bacillus licheniformis, Bacillus brevis, Bacillus stearothermophilus, Lactobacillus fermenti, Lactobacillus delbrueckii, Staphylococcus aureus andClostridium acetobutylicum. The individual components ofd-amino acids were identified in 5Bacillus species referred to above,d-alanine is the major component; the otherd-amino acids identified are aspartic acid, glutamic acid, histidine, leucines, proline, serine and tyrosine. Thed-amino acid pool size inBacillus subtilis B₃ varies with different culture conditions. The pool size is maximum when growth temperature is 30°C and it fluctuates with change in pH of the medium. The maximum quantity ofd-amino acids could be recovered when the culture was at mid log phase. O₂ supply to the medium has little effect ond-amino acid pool size. The starvation of cells leads to depletion of thed-amino acid pool which is exhausted almost completely within 4 hours by incubation in nutrient-free medium.     

Characterization of the mucilage sheaths ofLemonniera aquatica by lectin-gold labelling

A pre-embedding lectin-gold labelling method was used to characterize the carbohydrate components in the mucilage ofLemonniera aquatica. A specific tissue processing protocol was developed, namely: a) primary fixation in 2% paraformaldehyde and 0.2% glutaraldehyde in PIPES buffer (pH 7.2) for 30 min; b) secondary fixation in 2% glutaraldehyde in the same buffer system for 1 h; c) post-fixation in 1% aqueous OsO₄ for 1h; d) embedment in Möllenhaur's resin. The three gold conjugated lectins used were: concanavalin A, wheat germ agglutinin andLimax flavus agglutinin, allowing detection of their complementary saccharides, namely α-d-mannose/α-d-glucose,N-acetyl-d-glucosamine (GluNAc), andN-acetylneuraminic acid (NANA), respectively.N-Acetyl-d-glucosamine and NANA residues were the major components of germ tube mucilage with only a small amount of α-d-manose/α-d-glucose. However, NANA was restricted to the mucilage in the region of germ tube emergence from the conidial arm. The abundance of GluNAc and NANA residues on hyphae and appressoria was less than that on the germ tube. Conversely, α-d-mannose/α-d-glucose was more abundant in the appressorial mucilage. Variability of mucilage composition was found to exist between different structures of the germinated conidium and also between different regions of the same structure. Further, the conidial cell wall ofL. aquatica is not chitinous, and lacks NANA and α-d-mannose/α-d-gluocse.