Characterization of <Emphasis Type="SmallCaps">d</Emphasis>-tagatose-3-epimerase from <Emphasis Type="Italic">Rhodobacter sphaeroides</Emphasis> that converts <Emphasis Type="SmallCaps">d</Emphasis>-fructose into <Emphasis Type="SmallCaps">d-</Emphasis>psicose

A non-characterized gene, previously proposed as the d-tagatose-3-epimerase gene from Rhodobacter sphaeroides, was cloned and expressed in Escherichia coli. Its molecular mass was estimated to be 64 kDa with two identical subunits. The enzyme specificity was highest with d-fructose and decreased for other substrates in the order: d-tagatose, d-psicose, d-ribulose, d-xylulose and d-sorbose. Its activity was maximal at pH 9 and 40°C while being enhanced by Mn²⁺. At pH 9 and 40°C, 118 g d-psicose l⁻¹ was produced from 700 g d-fructose l⁻¹ after 3 h. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Syntheses of dopa glycosides using glucosidases

Syntheses of l-dopa 1a glucoside 10a,b and dl-dopa 1b glycosides 10–18 with d-glucose 2, d-galactose 3, d-mannose 4, d-fructose 5, d-arabinose 6, lactose 7, d-sorbitol 8 and d-mannitol 9 were carried out using amyloglucosidase from Rhizopus mold, β-glucosidase isolated from sweet almond and immobilized β-glucosidase. Invariably, l-dopa and dl-dopa gave low to good yields of glycosides 10–18 at 12–49% range and only mono glycosylated products were detected through glycosylation/arylation at the third or fourth OH positions of l-dopa 1a and dl-dopa 1b. Amyloglucosidase showed selectivity with d-mannose 4 to give 4-O-C1β and d-sorbitol 8 to give 4-O-C6-O-arylated product. β-Glucosidase exhibited selectivity with d-mannose 4 to give 4-O-C1β and lactose 7 to give 4-O-C1β product. Immobilized β-glucosidase did not show any selectivity. Antioxidant and angiotensin converting enzyme inhibition (ACE) activities of the glycosides were evaluated glycosides, out of which l-3-hydroxy-4-O-(β-d-galactopyranosyl-(1′→4)β-d-glucopyranosyl) phenylalanine 16 at 0.9 ± 0.05 mM and dl-3-hydroxy-4-O-(β-d-glucopyranosyl) phenylalanine 11b,c at 0.98 ± 0.05 mM showed the best IC₅₀ values for antioxidant activity and dl-3-hydroxy-4-O-(6-d-sorbitol)phenylalanine 17 at 0.56 ± 0.03 mM, l-dopa-d-glucoside 10a,b at 1.1 ± 0.06 mM and dl-3-hydroxy-4-O-(d-glucopyranosyl)phenylalanine 11a-d at 1.2 ± 0.06 mM exhibited the best IC₅₀ values for ACE inhibition. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

A Metal Ion as a Cofactor Attenuates Substrate Inhibition in the Enzymatic Production of a High Concentration of <Emphasis Type="SmallCaps">D</Emphasis>-glutamate Using <Emphasis Type="Italic">N</Emphasis>-acyl-<Emphasis Type="SmallCaps">D</Emphasis>-glutamate Amidohydrolase

N-Acyl-D-glutamate amidohydrolase (D-AGase) was inhibited by 94 % when 1 mol/l N-acetyl-DL- glutamate was used as a substrate. The addition of 1 mM Co²⁺ stabilized D-AGase. Moreover, the substrate inhibition was weakened to 88% with the addition of 0.4 mM Co²⁺ to the reaction mixture. Although D-AGase is a zinc-metalloenzyme, the addition of Zn²⁺ from 0.01 to 10 mM did not increase the D-glutamic acid production in the saturated substrate. Under optimal conditions, 0.38 M D-glutamic acid was obtained from N-acyl-DL-glutamate with 100% of the theoretical yield after 48 h.     

Importance of the l-galactonolactone pool for enhancing the ascorbate content revealed by l -galactonolactone dehydrogenase-overexpressing tobacco plants

l-Galactono-1,4-lactone (GalL) dehydrogenase (GLDH) is an enzyme that catalyzes the last step of l-ascorbate (AsA) biosynthesis in plants. To re-evaluate the importance of the enzyme and the possibility of manipulating the AsA content in plants, a cDNA encoding GLDH from sweet potato was introduced into tobacco plants by Agrobacterium-mediated transformation under the control of a CaMV 35S promoter. Protein blot analysis revealed the elevation of GLDH protein contents in three GLDH-transformed lines. Furthermore, these transgenic lines showed 6- to 10-fold higher GLDH activities in the roots than the non-transformed plants, SR1. Despite the elevated GLDH activity, the AsA content in the leaves did not change in all lines; i.e., the AsA content in GLDH-transformed lines was 3–7 μmol g⁻¹ FW, comparable to that in the non-transformed plants. Incubation of leaf discs in a GalL solution led to a rapid 2- to 3-fold increase in the AsA content in both GLDH-transformed and non-transformed plants in the same manner. These results suggest that the supply of GalL is a crucial factor for determining the AsA pool size and that the upstream genes in the AsA biosynthetic pathway are responsible for enhancing the AsA content in plants.     

Molecular Cloning,Sequencing, and Expression of a <Emphasis Type="SmallCaps">l</Emphasis>-Glutamine <Emphasis Type="SmallCaps">d</Emphasis>-Fructose 6-Phosphate Amidotransferase Gene from <Emphasis Type="Italic">Volvariella volvacea</Emphasis>

Using 3′-RACE and 5′-RACE, we have cloned and sequenced the genomic gene and complete cDNA encoding l-glutamine d-fructose 6-phosphate amidotransferase (GFAT) from the edible straw mushroom, Volvariella volvacea. Gfat contains five introns, and encodes a predicted protein of 697 amino acids that is homologous to other reported GFAT sequences. Southern hybridization indicated that a single gfat gene locus exists in the V. volvacea genome. Recombinant native V. volvacea GFAT enzyme, over-expressed using Escherichia coli and partially purified, had an estimated molecular mass of 306 kDa and consisted of four equal-sized subunits of 77 kD. Reciprocal plots revealed K _m values of 0.55 and 0.75 mM for fructose 6-phosphate and l-glutamine, respectively. V. volvacea GFAT activity was inhibited by the end-product of the hexosamine pathway, UDP-GlcNAc, and by the glutamine analogues N ³-(4-methoxyfumaroyl)-l-2,3-diaminopropanoic acid and 2-amino-2-deoxy-d-glucitol-6-phosphate.     

Biotechnological production of <Emphasis Type="SmallCaps">l</Emphasis>-ribose from <Emphasis Type="SmallCaps">l</Emphasis>-arabinose

l-Ribose is a rare and expensive sugar that can be used as a precursor for the production of l-nucleoside analogues, which are used as antiviral drugs. In this work, we describe a novel way of producing l-ribose from the readily available raw material l-arabinose. This was achieved by introducing l-ribose isomerase activity into l-ribulokinase-deficient Escherichia coli UP1110 and Lactobacillus plantarum BPT197 strains. The process for l-ribose production by resting cells was investigated. The initial l-ribose production rates at 39°C and pH 8 were 0.46 ± 0.01 g g⁻¹ h⁻¹ (1.84 ± 0.03 g l⁻¹ h⁻¹) and 0.27 ± 0.01 g g⁻¹ h⁻¹ (1.91 ± 0.1 g l⁻¹ h⁻¹) for E. coli and for L. plantarum, respectively. Conversions were around 20% at their highest in the experiments. Also partially purified protein precipitates having both l-arabinose isomerase and l-ribose isomerase activity were successfully used for converting l-arabinose to l-ribose.     

Production of <Emphasis Type="SmallCaps">d</Emphasis>-lactic acid by <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis> under oxygen deprivation

In mineral salts medium under oxygen deprivation, Corynebacterium glutamicum exhibits high productivity of l-lactic acid accompanied with succinic and acetic acids. In taking advantage of this elevated productivity, C. glutamicum was genetically modified to produce d-lactic acid. The modification involved expression of fermentative d-lactate dehydrogenase (d-LDH)-encoding genes from Escherichia coli and Lactobacillus delbrueckii in l-lactate dehydrogenase (l-LDH)-encoding ldhA-null C. glutamicum mutants to yield strains C. glutamicum ΔldhA/pCRB201 and C. glutamicum ΔldhA/pCRB204, respectively. The productivity of C. glutamicum ΔldhA/pCRB204 was fivefold higher than that of C. glutamicum ΔldhA/pCRB201. By using C. glutamicum ΔldhA/pCRB204 cells packed to a high density in mineral salts medium, up to 1,336 mM (120 g l⁻¹) of d-lactic acid of greater than 99.9% optical purity was produced within 30 h.     

Purification and characterization of anl-amino-acid oxidase fromChlamydomonas reinhardtii

Anl-amino-acid oxidase (EC 1.4.3.1) that catalyzes the oxidative deamination of twelvel-amino acids has been purified 21-fold and with 14% yield to electrophoretic homogeneity fromChlamydomonas reinhardtii cells by ammonium-sulfate fractionation, gel filtration through Sephacryl and Superose, anion-exchange chromatography and preparative electrophoresis in polyacrylamide gels. The native enzyme is a protein of 470 kDa and consists of eight identical or similarsized subunits of 60 kDa each. Optimum pH and temperature were 8.2 and 55° C, respectively, with a Q₁₀ (45–55° C) of 1.7 and an activation energy of 45 kJ · mol^–1. Its absorption spectrum showed, in the visible region, maxima at 360 and 444 nm, characteristic of a flavoprotein with a calculated flavin content of 7.7 mol FAD per mol of native enzyme. ApparentK _m values of the twelvel-amino acids which can act as substrates ofl-amino-acid oxidase ranged between 31 M for phenylalanine and 176 M for methionine. The effect of several specific group reagents, chelating agents and bivalent cations on enzyme activity has also been studied.This work was supported by Grant 780-CO2-01 from CICYT, Spain. The skillful secretarial assistance of C. Santos and I. Molina is gratefully acknowledged.     

Characterization of ribose-5-phosphate isomerase of <Emphasis Type="Italic">Clostridium thermocellum</Emphasis> producing <Emphasis Type="SmallCaps">d</Emphasis>-allose from <Emphasis Type="SmallCaps">d</Emphasis>-psicose

The rpiB gene, encoding ribose-5-phosphate isomerase (RpiB) from Clostridium thermocellum, was cloned and expressed in Escherichia coli. RpiB converted d-psicose into d-allose but it did not convert d-xylose, l-rhamnose, d-altrose or d-galactose. The production of d-allose by RpiB was maximal at pH 7.5 and 65°C for 30 min. The half-lives of the enzyme at 50°C and 65°C were 96 h and 4.7 h, respectively. Under stable conditions of pH 7.5 and 50°C, 165 g d-allose l⁻¹ was produced without by-products from 500 g d-psicose l⁻¹ after 6 h.     

Clostridium methylpentosum sp. nov.: a ring-shaped intestinal bacterium that ferments only methylpentoses and pentoses

An intestinal bacterium isolated from a human subject utilized only two methylpentoses (L-rhamnose and L-fucose) and two pentoses (L-lyxose and D-arabinose) as fermentable substrates, among many compounds tested. The isolate was obligately anaerobic and had a distinctive morphology, its cells being rods bent in the shape of rings with the ends slightly overlapping. Single ring-shaped cells and left-handed helical chains of cells were present in cultures. The cells were surrounded by large capsules which appeared as thick, fibrous masses when examined by electron microscopy. Capsules were formed by cells growing in media containing any one of the four fermentable substrates. Terminally located, heat-resistant endospores were formed on plates of an enriched agar medium supplemented with L-rhamnose. End products of L-rhamnose or L-fucose fermentation included acetate, propionate, n-propanol, CO₂, and H₂. The isolate represented a new species of Clostridium for which the name Clostridium methylpentosum (type strain R2. ATCC 43829) is proposed. This organism may participate in intestinal digestive processes by metabolizing rhamnose released via the enzymatic depolymerization of dietary pectin.Abbreviations G+C guanine plus cytosine - OD optical density - TEM transmission electron micrograph     

The alternative<Emphasis Type="SmallCaps"> d</Emphasis>-galactose degrading pathway of<Emphasis Type="Italic"> Aspergillus nidulans</Emphasis> proceeds via<Emphasis Type="SmallCaps"> l</Emphasis>-sorbose

The catabolism of d-galactose in yeast depends on the enzymes of the Leloir pathway. In contrast, Aspergillus nidulans mutants in galactokinase (galE) can still grow on d-galactose in the presence of ammonium—but not nitrate—ions as nitrogen source. A. nidulans galE mutants transiently accumulate high (400 mM) intracellular concentrations of galactitol, indicating that the alternative d-galactose degrading pathway may proceed via this intermediate. The enzyme degrading galactitol was identified as l-arabitol dehydrogenase, because an A. nidulans loss-of-function mutant in this enzyme (araA1) did not show NAD⁺-dependent galactitol dehydrogenase activity, still accumulated galactitol but was unable to catabolize it thereafter, and a double galE/araA1 mutant was unable to grow on d-galactose or galactitol. The product of galactitol oxidation was identified as l-sorbose, which is a substrate for hexokinase, as evidenced by a loss of l-sorbose phosphorylating activity in an A. nidulans hexokinase (frA1) mutant. l-Sorbose catabolism involves a hexokinase step, indicated by the inability of the frA1 mutant to grow on galactitol or l-sorbose, and by the fact that a galE/frA1 double mutant of A. nidulans was unable to grow on d-galactose. The results therefore provide evidence for an alternative pathway of d-galactose catabolism in A. nidulans that involves reduction of the d-galactose to galactitol and NAD⁺-dependent oxidation of galactitol by l-arabitol dehydrogenase to l-sorbose.     

Astrocytes as potential modulators of mercuric chloride neurotoxicity

Summary 1. MC has been shown to inhibit the uptake ofl-glutamate and increased-aspartate release from preloaded astrocytes in a dose-dependent fashion.2. Two sulfhydryl (SH-)-protecting agents; reduced glutathione (GSH), a cell membrane-nonpenetrating compound, and the membrane permeable dithiothreitol (DTT), have been shown consistently to reverse the above effects. MC-inducedd-aspartate release is completely inhibited by the addition of 1 mM DTT or GSH during the actual 5-min perfusion period with MC (5µM); when added after MC treatment, DTT fully inhibits the MC-inducedd-aspartate release, while GSH does not.3. Neither DTT nor GSH, in the absence of MC, have any effect on the rate of astrocyticd-aspartate release. Other studies demonstrate that although MC treatment (5µM) does not induce astrocytic swelling, its addition to astrocytes swollen by exposure to hypotonic medium leads to their failure to volume regulate.4. Omission of calcium from the medium greatly potentiates the effect of MC on astrocyticd-aspartate release, an effect which can be reversed by cotreatment of astrocytes with the dihydropyridine Ca²⁺-channel antagonist nimodipine (10µM), indicating that one possible route of MC entry into the cells is through voltage-gated L-type channels.     

Cultivation ofCandida blankii in simulated bagasse hemicellulose hydrolysate

Summary All fourCandida blankii isolates evaluated for growth in simulated bagasse hemicellulose hydrolysate utilized the sugars and acetic acid completely. The utilization ofd-xylose,l-arabinose and acetic acid were delayed by the presence ofd-glucose, but after glucose depletion the other carbon sources were utilized simultaneously. The maximum specific growth rate of 0.36 h^–1 and cell yield of 0.47 g cells/g carbon source assimilate compared with published results obtained withC. utilis. C. blankii appeared superior toC. utilis for biomass production from hemicellulose hydrolysate in that it utilizedl-arabinose and was capable of growth at higher temperatures.     

Continuous 2-keto-<Emphasis Type="SmallCaps">l</Emphasis>-gulonic acid fermentation from <Emphasis Type="SmallCaps">l</Emphasis>-sorbose by <Emphasis Type="Italic">Ketogulonigenium vulgare</Emphasis> DSM 4025

A single-stage continuous fermentation process for the production of 2-keto-l-gulonic acid (2KGA) from l-sorbose using Ketogulonigenium vulgare DSM 4025 was developed. The chemostat culture with the dilution rate that was calculated based on the relationship between the 2KGA production rate and the 2KGA concentration was feasible for production with high concentration of 2KGA. In this system, 112.2 g/L of 2KGA on the average was continuously produced from 114 g/L of l-sorbose. A steady state of the fermentation was maintained for the duration of more than 110 h. The dilution rate was kept in the range of 0.035 and 0.043 h⁻¹, and the 2KGA productivity was 3.90 to 4.80 g/L/h. The average molar conversion yield of 2KGA from l-sorbose was 91.3%. Under the optimal conditions, l-sorbose concentration was kept at 0 g/L. Meanwhile, the dissolved oxygen level was changing in response to the dilution rate and 2KGA concentration. In the dissolved oxygen (DO) range of 16% to 58%, it was revealed that the relationship between DO and D possessed high degree of positive correlation under the l-sorbose limiting condition (complete consumption of l-sorbose). Increasing D closer to the critical value for washing out point of the continuous fermentation, DO value tended to be gradually increased up to 58%. In conclusion, an efficient and reproducible continuous fermentation process for 2KGA production by K. vulgare DSM 4025 could be developed using a medium containing baker’s yeast without using a second helper microorganism.     

Fermentation of <Emphasis Type="SmallCaps">d</Emphasis>-glucose and <Emphasis Type="SmallCaps">d</Emphasis>-xylose mixtures by <Emphasis Type="Italic">Candida tropicalis</Emphasis> NBRC 0618 for xylitol production

The fermentation of d-glucose and d-xylose mixtures by the yeast Candida tropicalis NBRC 0618 has been studied under the most favourable operation conditions for the culture, determining the most adequate initial proportion in these sugars for xylitol production. In all the experiments a synthetic culture medium was used, with an initial total substrate concentration of 25 g L⁻¹, a constant pH of 5.0 and a temperature of 30 °C. From the experimental results, it was deduced that the highest values of specific rates of production and of overall yield in xylitol were achieved for the mixtures with the highest percentage of d-xylose, specifically in the culture with the initial d-glucose and d-xylose concentrations of 1 and 24 g L⁻¹, respectively, with an overall xylitol yield of 0.28 g g⁻¹. In addition, the specific rates of xylitol production declined over the time course of the culture and the formation of this bioproduct was favoured by the presence of small quantities of d-glucose. The sum of the overall yield values in xylitol and ethanol for all the experiments ranged from 0.26 to 0.56 g bioproduct/g total substrate.     

Double mutation of the <Emphasis Type="Italic">PDC1</Emphasis> and <Emphasis Type="Italic">ADH1</Emphasis> genes improves lactate production in the yeast <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing the bovine lactate dehydrogenase gene

Expression of a heterologous l-lactate dehydrogenase (l-ldh) gene enables production of optically pure l-lactate by yeast Saccharomyces cerevisiae. However, the lactate yields with engineered yeasts are lower than those in the case of lactic acid bacteria because there is a strong tendency for ethanol to be competitively produced from pyruvate. To decrease the ethanol production and increase the lactate yield, inactivation of the genes that are involved in ethanol production from pyruvate is necessary. We conducted double disruption of the pyruvate decarboxylase 1 (PDC1) and alcohol dehydrogenase 1 (ADH1) genes in a S. cerevisiae strain by replacing them with the bovine l-ldh gene. The lactate yield was increased in the pdc1/adh1 double mutant compared with that in the single pdc1 mutant. The specific growth rate of the double mutant was decreased on glucose but not affected on ethanol or acetate compared with in the control strain. The aeration rate had a strong influence on the production rate and yield of lactate in this strain. The highest lactate yield of 0.75 g lactate produced per gram of glucose consumed was achieved at a lower aeration rate.     

Simultaneous utilization of D-cellobiose, D-glucose, and D-xylose by recombinant Corynebacterium glutamicum under oxygen-deprived conditions

Corynebacterium glutamicum R was metabolically engineered to broaden its sugar utilization range to d-xylose and d-cellobiose contained in lignocellulose hydrolysates. The resultant recombinants expressed Escherichia coli xylA and xylB genes, encoding d-xylose isomerase and xylulokinase, respectively, for d-xylose utilization and expressed C. glutamicum R bglF ^317A and bglA genes, encoding phosphoenolpyruvate:carbohydrate phosphotransferase system (PTS) β-glucoside-specific enzyme IIBCA component and phospho-β-glucosidase, respectively, for d-cellobiose utilization. The genes were fused to the non-essential genomic regions distributed around the C. glutamicum R chromosome and were under the control of their respective constitutive promoter trc and tac that permitted their expression even in the presence of d-glucose. The enzyme activities of resulting recombinants increased with the increase in the number of respective integrated genes. Maximal sugar utilization was realized with strain X5C1 harboring five xylA–xylB clusters and one bglF ^317A –bglA cluster. In both d-cellobiose and d-xylose utilization, the sugar consumption rates by genomic DNA-integrated strain were faster than those by plasmid-bearing strain, respectively. In mineral medium containing 40 g l⁻¹ d-glucose, 20 g l⁻¹ d-xylose, and 10 g l⁻¹ d-cellobiose, strain X5C1 simultaneously and completely consumed these sugars within 12 h and produced predominantly lactic and succinic acids under growth-arrested conditions.     

The VANA glycopeptide resistance protein is related to d-alanyl-d-alanine ligase cell wall biosynthesis enzymes

Summary Inducible resistance to the glycopeptide antibiotics vancomycin and teicoplanin is mediated by plasmid pIP816 in Enterococcus faecium strain BM4147. Vancomycin induced the synthesis of a ca. 40 kDa membrane-associated protein designated VANA. The resistance protein was partially purified and its N-terminal sequence was determined. A 1761 by DNA restriction fragment of pIP816 was cloned into Escherichia coli and sequenced. When expressed in E. coli, this fragment encoded a ca. 40 kDa protein that comigrated with VANA from enterococcal membrane fractions. The ATG translation initiation codon for VANA specified the methionine present at the N-terminus of the protein indicating the absence of signal peptide processing. The amino acid sequence deduced from the sequence of the vanA gene consisted of 343 amino acids giving a protein with a calculated Mr of 37400. VANA was structurally related to the d-alanyl-d-alanine (d-ala-d-ala) ligases of Salmonella typhimurium (36% amino acid identity) and of E. coli (28%). The vanA gene was able to transcomplement an E. coli mutant with thermosensitive d-ala-d-ala ligase activity. Thus, the inducible resistance protein VANA was structurally and functionally related to cytoplasmic enzymes that synthesize the target of glycopeptide antibiotics. Based on these observations we discuss the possibility that resistance is due to modification of the glycopeptide target.     

Regulation of metabolite production by precursors and elicitors in liquid cultures of <Emphasis Type="Italic">Hypericum perforatum</Emphasis>

Four precursors (l-phenylalanine, l-tryptophan, cinnamic acid and emodin) and one signal elicitor (methyl jasmonate, MeJA) were added to liquid cultures of Hypericum perforatum L. to study their effect on production of hyperforin and hypericins (pseudohypericin and hypericin). The addition of l-phenylalanine (75 to 100 mg l⁻¹) enhanced production of hypericins, but hyperforin levels were decreased. Hypericin, pseudohypericin and hyperforin concentrations were all decreased when l-tryptophan (25 to 100 mg l⁻¹) was added to the medium. However, addition of l-tryptophan (50 mg l⁻¹) with MeJA (100 μM) stimulated hyperforin production significantly (1.81-fold) and resulted in an increased biomass. Cinnamic acid (25, 50 mg l⁻¹) and emodin (1.0 to 10.0 mg l⁻¹) each enhanced hyperforin accumulation in H. perforatum, but did not affect accumulation of hypericins.     

The pathway ofD-cycloserine biosynthesis inStreptomyces garyphalus

Incubation experiments using washed cells and toluene treated cells ofStreptomyces garyphalus showed that O-acetyl-L-serine and hydroxyurea are intermediates in the biosynthesis ofD-cycloserine. The formation of [¹⁴C]O-ureidoserine from O-acetyl-L-serine and hydroxyurea was demonstrated by incubating an enzyme solution with¹⁴C-labelled substrates. Desalted cell-free extract catalyzed the conversion of O-ureido-D-serine toD-cycloserine in a reaction requiring ATP and Mg²⁺. The results suggested the following pathway forD-cycloserine biosynthesis.