Engineering of an <Emphasis Type="SmallCaps">l</Emphasis>-arabinose metabolic pathway in <Emphasis Type="Italic">Corynebacterium glutamicum</Emphasis>

Corynebacterium glutamicum was metabolically engineered to broaden its substrate utilization range to include the pentose sugar l-arabinose, a product of the degradation of lignocellulosic biomass. The resultant CRA1 recombinant strain expressed the Escherichia coli genes araA, araB, and araD encoding l-arabinose isomerase, l-ribulokinase, and l-ribulose-5-phosphate 4-epimerase, respectively, under the control of a constitutive promoter. Unlike the wild-type strain, CRA1 was able to grow on mineral salts medium containing l-arabinose as the sole carbon and energy source. The three cloned genes were expressed to the same levels whether cells were cultured in the presence of d-glucose or l-arabinose. Under oxygen deprivation and with l-arabinose as the sole carbon and energy source, strain CRA1 carbon flow was redirected to produce up to 40, 37, and 11%, respectively, of the theoretical yields of succinic, lactic, and acetic acids. Using a sugar mixture containing 5% d-glucose and 1% l-arabinose under oxygen deprivation, CRA1 cells metabolized l-arabinose at a constant rate, resulting in combined organic acids yield based on the amount of sugar mixture consumed after d-glucose depletion (83%) that was comparable to that before d-glucose depletion (89%). Strain CRA1 is, therefore, able to utilize l-arabinose as a substrate for organic acid production even in the presence of d-glucose.     

Cloning,Purification and Characterization of an NAD-Dependent <Emphasis Type="SmallCaps">d</Emphasis>-Arabitol Dehydrogenase from Acetic Acid Bacterium, <Emphasis Type="Italic">Acetobacter suboxydans</Emphasis>

d-Xylulose-forming d-arabitol dehydrogenase (aArDH) is a key enzyme in the bio-conversion of d-arabitol to xylitol. In this study, we cloned the NAD-dependent d-xylulose-forming d-arabitol dehydrogenase gene from an acetic acid bacterium, Acetobacter suboxydans sp. The enzyme was purified from A. suboxydans sp. and was heterogeneously expressed in Escherichia coli. The native or recombinant enzyme was preferred NAD(H) to NADP(H) as coenzyme. The active recombinant aArDH expressed in E. coli is a homodimer, whereas the native aArDH in A. suboxydans is a homotetramer. On SDS–PAGE, the recombinant and native aArDH give one protein band at the position corresponding to 28 kDa. The optimum pH of polyol oxidation and ketone reduction is found to be pH 8.5 and 5.5 respectively. The highest reaction rate is observed when d-arabitol is used as the substrate (K _m = 4.5 mM) and the product is determined to be d-xylulose by HPLC analysis.     

d-Glucose does not catabolite repress a transketolase-deficientd-ribose-producingBacillus subtilis mutant strain

WhenBacillus subtilis strain ATCC 21951, a transketolase-deficientd-ribose-producing mutant, was grown ond-glucose plus a second substrate which is metabolized via the oxidative pentose phosphate cycle (d-gluconic acid,d-xylose,l-arabinose ord-xylitol),d-glucose did not catabolite repress metabolism of the second carbon source. Thed-ribose yield obtained with the simultaneously converted carbon substrates, significantly exceeded that when onlyd-glucose was used. In addition, the concentration of glycolytic by-products and the fermentation time significantly decreased. Based on these findings, a fermentation process was developed withB. subtilis strain ATCC 21951 in whichd-glucose (100 g L^–1) andd-gluconic acid (50 g L^–1) were converted into 45 g L^–1 ofd-ribose and 7.5 g L^–1 of acetoin. A second process, based ond-glucose andd-xylose (100 g L^–1 each), yielded 60 g L^–1 ofd-ribose and 4 g L^–1 of acetoin plus 2,3-butanediol. Both mixed carbon source fermentations provide excellent alternatives to the less efficientd-glucose-based processes used so far.     

Control of erythritol dehydrogenase in Schizophyllum commune

Summary An NAD-dependent erythritol dehydrogenase was detected in cell-extracts of basidiospore germinants of Schizophyllum commune following culture on either meso-erythritol or glycerol as sole carbon sources. Induction of erythritol dehydrogenase was also observed in purely vegetative mycelium (str. 845 or str. 699). Erythritol dehydrogenase was not observed in ungerminated basidiospores or germinants which arose on d-glucose, d-mannitol, sorbitol, ribitol, xylitol, d-arabitol or l-arabitol. NAD-coupled polyol dehydrogenases for all the latter sugar alcohols were observed in ungerminated basidiospores, germinants, and vegetative mycelium of S. commune cultured on d-glucose. Basidiospore germination on d-glucose plus meso-erythritol led to a 90% decrease in erythritol dehydrogenase and the specific activity of ribitol dehydrogenase was directly comparable to that seen in d-glucose germinants. Storage experiments of crude extracts of meso-erythritol germinants indicated differential enzyme decay of dehydrogenases for d-mannitol, sorbitol and erythritol while the respective enzymes could be further distinguished by heat-stability as well as preferential utilization of analogues of NAD. DEAE-cellulose column chromatography led to separation of sorbitol dehydrogenase which was also active with xylitol, erythritol dehydrogenase, and mannitol dehydrogenase which was also active with d-arabitol.     

Fermentation of seaweed sugars by Lactobacillus species and the potential of seaweed as a biomass feedstock

It is known that seaweeds differ greatly from land plants in their sugar composition. The current research on the L-lactic acid fermentation process focuses on land plant sugars as a carbon source, with the potential of seaweed sugars being largely ignored. This study examined the feasibility of seaweed biomass as a possible carbon source for the production of l-lactic acid, by comparing the fermentation of seaweed sugars (d-galactose, d-mannitol, l-rhamnose, d-glucuronic acid, and l-fucose) and land plant sugars (d-glucose, d-xylose, d-mannose, and l-arabinose). The experiments were repeated with 2 sugar acids (d-gluconic acid, d-glucaric acid) in order to investigate the effect of the degree of reduction of carbon source on the fermentation yield. This research also examined the effect of bacterial strain on the characteristics of fermentation reactions, by conducting l-lactic acid fermentation with 7 different Lactobacillus species. Taking into account the sugar composition of seaweed and the levels of lactic acid production from each pure sugar, it was possible to predict the lactic acid production yield of various seaweeds and land plants. From comparative analysis of the predicted lactic acid production yield, it was found that seaweeds are already comparable to lignocellulosics at the current stage of technology. If new technologies for the utilization of non-fermentable seaweed sugars are developed, seaweeds show promise as an even more useful biomass feedstock than lignocellulosics.     

New quinoproteins in oxidative fermentation

Several quinoproteins have been newly indicated in acetic acid bacteria, all of which can be applied to fermentative or enzymatic production of useful materials by means of oxidative fermentation. (1) D-Arabitol dehydrogenase from Gluconobacter suboxydans IFO 3257 was purified from the bacterial membrane and found to be a versatile enzyme for oxidation of various substrates to the corresponding oxidation products. It is worthy of notice that the enzyme catalyzes D-gluconate oxidation to 5-keto-D-gluconate, whereas 2-keto-D-gluconate is produced by a flavoprotein D-gluconate dehydrogenase. (2) Membrane-bound cyclic alcohol dehydrogenase was solubilized and purified for the first time from Gluconobacter frateurii CHM 9. When compared with the cytosolic NAD-dependent cyclic alcohol dehydrogenase crystallized from the same strain, the reaction rate in cyclic alcohol oxidation by the membrane enzyme was 100 times stronger than the cytosolic NAD-dependent enzyme. The NAD-dependent enzyme makes no contribution to cyclic alcohol oxidation but contributes to the reduction of cyclic ketones to cyclic alcohols. (3) Meso-erythritol dehydrogenase has been purified from the membrane fraction of G. frateurii CHM 43. The typical properties of quinoproteins were indicated in many respects with the enzyme. It was found that the enzyme, growing cells and also the resting cells of the organism are very effective in producing L-erythrulose. Dihydroxyacetone can be replaced by L-erythrulose for cosmetics for those who are sensitive to dihydroxyacetone. (4) Two different membrane-bound D-sorbitol dehydrogenases were indicated in acetic acid bacteria. One enzyme contributing to L-sorbose production has been identified to be a quinoprotein, while another FAD-containing D-sorbitol dehydrogenase catalyzes D-sorbitol oxidation to D-fructose. D-Fructose production by the oxidative fermentation would be possible by the latter enzyme and it is superior to the well-established D-glucose isomerase, because the oxidative fermentation catalyzes irreversible one-way oxidation of D-sorbitol to D-fructose without any reaction equilibrium, unlike D-glucose isomerase. (5) Quinate dehydrogenase was found in several Gluconobacter strains and other aerobic bacteria like Pseudomonas and Acinetobacter strains. It has become possible to produce dehydroquinate, dehydroshikimate, and shikimate by oxidative fermentation. Quinate dehydrogenase was readily solubilized from the membrane fraction by alkylglucoside in the presence of 0.1 M KCl. A simple purification by hydrophobic chromatography gave a highly purified quinate dehydrogenase that was monodispersed and showed sufficient purity. When quinate dehydrogenase purification was done with Acinetobacter calcoaceticus AC3, which is unable to synthesize PQQ, purified inactive apo-quinate dehydrogenase appeared to be a dimer and it was converted to the monomeric active holo-quinate dehydrogenase by the addition of PQQ.     

Production, purification and structural characterization of an exopolysaccharide produced by a probiotic Lactobacillus plantarum MTCC 9510

Exopolysaccharides (EPS) from lactic acid bacteria contribute to specific rheology and texture of fermented milk products and finds applications even in non-dairy foods and in therapeutics. Box-Behnken model of response surface methodology (RSM) was employed to formulate the production medium for exopolysaccharide (EPS). FT-IR spectral analysis of the purified EPS from Lactobacillus plantarum MTCC 9510 revealed prominent characteristic groups corresponding to polyhydric alcohols. The degradation temperature (Td) of the polysaccharide was found to be 260°C with the help of thermo gravimetric analysis (TGA). Structure elucidation of the EPS showed that it consists of a trisaccharide repeating unit of α-d-glucose, β-d-glucose and α-d-mannose.     

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.     

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.     

Identification in Agrobacterium tumefaciens of the d-galacturonic acid dehydrogenase gene

There are at least three different pathways for the catabolism of d-galacturonate in microorganisms. In the oxidative pathway, which was described in some prokaryotic species, d-galacturonate is first oxidised to meso-galactarate (mucate) by a nicotinamide adenine dinucleotide (NAD)-dependent dehydrogenase (EC 1.1.1.203). In the following steps of the pathway mucate is converted to 2-keto-glutarate. The enzyme activities of this catabolic pathway have been described while the corresponding gene sequences are still unidentified. The d-galacturonate dehydrogenase was purified from Agrobacterium tumefaciens, and the mass of its tryptic peptides was determined using MALDI-TOF mass spectrometry. This enabled the identification of the corresponding gene udh. It codes for a protein with 267 amino acids having homology to the protein family of NAD(P)-binding Rossmann-fold proteins. The open reading frame was functionally expressed in Saccharomyces cerevisiae. The N-terminally tagged protein was not compromised in its activity and was used after purification for a kinetic characterization. The enzyme was specific for NAD and accepted d-galacturonic acid and d-glucuronic acid as substrates with similar affinities. NMR analysis showed that in water solution the substrate d-galacturonic acid is predominantly in pyranosic form which is converted by the enzyme to 1,4 lactone of galactaric acid. This lactone seems stable under intracellular conditions and does not spontaneously open to the linear meso-galactaric acid.     

Durable continuous fermentation of a model mixture of d(+)-glucose and l(−)-sodium monoglutamate under non-axenic conditions

The possible durability of non-axenic fermentation profiles is of major importance in controlled environmental biotechnology. The durability of the non-axenic anaerobic fermentation profile of a model mixture of d(+)-glucose and l(–)-sodium monoglutamate was documented in a fabricated bioreactor for a period of more than 6 months. A cyclic scheme of reactor loading induced a cyclic, reproducible and durable fermentation profile. Equimolar amounts of n-butyric acid as well as acetic acid, and of H₂ and CO₂ were observed as steady metabolites. Correspondence to: E.-J. Nyns     

Improved xylanase production by<Emphasis Type="Italic"> Trichoderma reesei</Emphasis> grown on <Emphasis Type="SmallCaps">l</Emphasis>-arabinose and lactose or <Emphasis Type="SmallCaps">d</Emphasis>-glucose mixtures

Trichoderma reesei Rut C-30 was grown on eight different natural or rare aldopentoses as the main carbon source and on mixtures of an aldopentose with d-glucose or lactose. The fungal cells consumed all aldopentoses tested, except l-xylose and l-ribose. The highest total xylanase and cellulase activities were achieved when cells were grown on l-arabinose as the main carbon source. The total xylanase activity produced by cells grown on l-arabinose was even higher than that produced by cells grown on an equal amount of lactose. In co-metabolism of d-glucose (15 g l^–1) and l-arabinose (5 g l^–1), the total volumetric and specific xylanase productivities were improved (derepressed) approximately 23- and 18-fold, respectively, compared to a cultivation on only d-glucose (20 g l^–1). In a similar experiment, in which cells were grown on a mixture of lactose and l-arabinose, the xylanase productivity was approximately doubled, compared to a cultivation on only lactose. The cellulase productivities, however, were not improved by the addition of l-arabinose. Compared with a typical industrial fungal enzyme production process with lactose as the main carbon source, better volumetric and specific xylanase productivities were achieved both on a lactose/arabinose mixture and on a glucose/arabinose mixture.     

Studies on the inactivation of the flavoproteind-amino acid oxidase fromTrigonopsis variabilis

Inactivation ofd-amino acid oxidase occured by different mechanisms. The enzyme showed a rapid loss of activity in the presence of micromolar amounts of Cu²⁺ and Hg²⁺. It was also sensitive to oxidative inactivation by Fe²⁺ and H₂O₂ when both reagents were added in millimolar amounts. When oxidatively inactivatedd-amino acid oxidase and a corresponding non-treated control were modified with the sulfhydryl-modifying, fluorescent reagent monobromobimane and subsequently digested with endoproteinase Glu-C, Cys-298 was identified to be a target for oxidative modification according to differences in the known peptide profile of fluorescence intensity. Another reason for the observed loss of enzyme activity in crude extracts was the specific proteolytic digestion ofd-amino acid oxidase, which was dependent on the growth phase of the cells used. This cleavage was catalyzed by a serine-type proteinase and was the introductory step for the further complete degradation of the enzyme. In addition, a coenriched 50-kDa protein, identified as NADPH-specific glutamate dehydrogenase, significantly decreased the stability of thed-amino acid oxidase activity. Treatment of apo-d-amino acid oxidase fromT. variabilis with monobromobimane resulted in a significantly increased fluorescence of two peptides, neither of which contained any cysteine residue. Thus, an involvement of cysteine residues in binding the FAD coenzyme should be excluded.     

d-lactic acid production from cellooligosaccharides and β-glucan using l-LDH gene-deficient and endoglucanase-secreting Lactobacillus plantarum

In order to achieve direct fermentation of an optically pure d-lactic acid from cellulosic materials, an endoglucanase from a Clostridium thermocellum (CelA)-secreting plasmid was introduced into an l-lactate dehydrogenase gene (ldhL1)-deficient Lactobacillus plantarum (∆ldhL1) bacterial strain. CelA expression and its degradation of β-glucan was confirmed by western blot analysis and enzyme assay, respectively. Although the CelA-secreting ∆ldhL1 assimilated cellooligosaccharides up to cellohexaose (although not cellotetraose), the main end product was acetic acid, not lactic acid, due to the conversion of lactic acid to acetic acid. Cultivation under anaerobic conditions partially suppressed this conversion resulting in the production of 1.27 g/l of D-lactic acid with a high optical purity of 99.5% from a medium containing 2 g/l of cellohexaose. Subsequently, D-lactic acid fermentation from barley β-glucan was carried out with the addition of Aspergillus aculeatus β-glucosidase produced by recombinant Aspergillus oryzae and 1.47 g/l of D-lactic was produced with a high optical purity of 99.7%. This is the first report of direct lactic acid fermentation from β-glucan and a cellooligosaccharide that is a more highly polymerized sugar than cellotriose.     

Properties of recombinant <Emphasis Type="Italic">Strep</Emphasis>-tagged and untagged hyperthermophilic D-arabitol dehydrogenase from <Emphasis Type="Italic">Thermotoga maritima</Emphasis>

The first hyperthermophilic d-arabitol dehydrogenase from Thermotoga maritima was heterologously purified from Escherichia coli. The protein was purified with and without a Strep-tag. The enzyme exclusively catalyzed the NAD(H)-dependent oxidoreduction of d-arabitol, d-xylitol, d-ribulose, or d-xylulose. A twofold increase of catalytic rates was observed upon addition of Mg²⁺ or K⁺. Interestingly, only the tag-less protein was thermostable, retaining 90% of its activity after 90 min at 85 °C. However, the tag-less form of d-arabitol dehydrogenase had similar kinetic parameters compared to the tagged enzyme, demonstrating that the Strep-tag was not deleterious to protein function but decreased protein stability. A single band at 27.6 kDa was observed on SDS-PAGE and native PAGE revealed that the protein formed a homohexamer and a homododecamer. The enzyme catalyzed oxidation of d-arabitol to d-ribulose and therefore belongs to the class of d-arabitol 2-dehydrogenases, which are typically observed in yeast and not bacteria. The product d-ribulose is a rare ketopentose sugar that has numerous industrially applications. Given its thermostability and specificity, d-arabitol 2-dehydrogenase is a desirable biocatalyst for the production of rare sugar precursors.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-alanine by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Escherichia coli W was genetically engineered to produce l-alanine as the primary fermentation product from sugars by replacing the native d-lactate dehydrogenase of E. coli SZ194 with alanine dehydrogenase from Geobacillus stearothermophilus. As a result, the heterologous alanine dehydrogenase gene was integrated under the regulation of the native d-lactate dehydrogenase (ldhA) promoter. This homologous promoter is growth-regulated and provides high levels of expression during anaerobic fermentation. Strain XZ111 accumulated alanine as the primary product during glucose fermentation. The methylglyoxal synthase gene (mgsA) was deleted to eliminate low levels of lactate and improve growth, and the catabolic alanine racemase gene (dadX) was deleted to minimize conversion of l-alanine to d-alanine. In these strains, reduced nicotinamide adenine dinucleotide oxidation during alanine biosynthesis is obligately linked to adenosine triphosphate production and cell growth. This linkage provided a basis for metabolic evolution where selection for improvements in growth coselected for increased glycolytic flux and alanine production. The resulting strain, XZ132, produced 1,279 mmol alanine from 120 g l⁻¹ glucose within 48 h during batch fermentation in the mineral salts medium. The alanine yield was 95% on a weight basis (g g⁻¹ glucose) with a chiral purity greater than 99.5% l-alanine. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

A single membrane-bound enzyme catalyzes the conversion of 2,5-diketo-d-gluconate to 4-keto-d-arabonate in d-glucose oxidative fermentation by Gluconobacter oxydans NBRC 3292

4-Keto-d-arabonate synthase (4KAS), which converts 2,5-diketo-d-gluconate (DKGA) to 4-keto-d-arabonate (4KA) in d-glucose oxidative fermentation by some acetic acid bacteria, was solubilized from the Gluconobacter oxydans NBRC 3292 cytoplasmic membrane, and purified in an electrophoretically homogenous state. A single membrane-bound enzyme was found to catalyze the conversion from DKGA to 4KA. The 92-kDa 4KAS was a homodimeric protein not requiring O₂ or a cofactor for the conversion, but was stimulated by Mn²⁺. N-terminal amino acid sequencing of 4KAS, followed by gene homology search indicated a 1,197-bp open reading frame (ORF), corresponding to the GLS_c04240 locus, GenBank accession No. CP004373, encoding a 398-amino acid protein with a calculated molecular weight of 42,818 Da. An Escherichia coli transformant with the 4kas plasmid exhibited 4KAS activity. Furthermore, overexpressed recombinant 4KAS was purified in an electrophoretically homogenous state and had the same molecular size as the natural enzyme.     

Pathways of d-fructose and d-glucose catabolism in marine species of Alcaligenes,Pseudomonas marina,and Alteromonas communis

Cell-free extracts of d-fructose grown cells of marine species of Alcaligenes as well as Pseudomonas marina contained an activity which catalyzed a P-enolpyruvate-dependent phosphorylation of d-fructose in the 1-position as well as activities of the following enzymes: 1-P-fructokinase, fructose-1,6-P₂ aldolase, PPi-dependent 6-P-fructokinase, fructokinase, glucokinase, P-hexose isomerase, glucose-6-P dehydrogenase, 6-P-gluconate dehydrase, and 2-keto-3-deoxy-6-P-gluconate aldolase. The presence of these enzyme activities would allow d-fructose to be degraded by the Embden-Meyerhof pathway and/or the Entner-Doudoroff pathway. In cell-free extracts of d-glucose grown cells, the activity catalyzing a P-enolpyruvate-dependent phosphorylation of d-fructose as well as 1-P-fructokinase activity were reduced or absent while the remaining enzymes were present at levels similar to those found in d-fructose grown cells. Radiolabeling experiments suggested that both d-fructose and d-glucose were utilized primarily via the Entner-Doudoroff pathway. Alteromonas communis, a marine species lacking 1-P-fructokinase and the PPi-dependent 6-P-fructokinase, contained all the enzyme activities necessary for the catabolism of d-fructose and d-glucose by the Entner-Doudoroff pathway; the involvement of this pathway was also consistent with the results of the radiolabeling experiments.Non-Standard Abbreviations EDP Entner-Doudoroff pathway - EMP Embden-Meyerhof pathway - FDP fructose-1,6-P₂ - FDPase FDP phosphatase - F-1-P fructose-1-P - F-6-P fructose-6-P - FPTS PEP: d-fructose phosphotransferase system - PPi-6-PFK PPi dependent 6-PFK - G-6-P glucose-6-P - KDPG 2-keto-3-deoxy-6-P-gluconate - PEP P-enolpyruvate - 1-PFK 1-P-fructokinase - 6-PFK 6-P-fructokinase - 6-PGA 6-P-gluconate     

Catabolite Repression of induction of aldose reductase activity and utilization of mixed hemicellulosic surgars in Candida guilliermondii

NADPH-dependent aldose reductase activity induced by d-xylose or l-arabinose was detected in cell-free extracts of Candida guilliermondii, but only negligible activities were observed if d-glucose served as carbon source. The induction of aldose reductase activity on mixed sugars was investigated under resting cell conditions. d-Glucose repressed enzyme induction by d-xylose or l-arabinose to varying degrees, and l-arabinose inhibited enzyme induction by d-xylose. During incubation in a mixture of d-xylose-d-glucose, glucose consumption by cells was fast and simultaneous with d-xylose utilization. l-arabinose consumption was poor when it was present as the only sugar and in a mixture with d-glucose; this pentose depletion occurred only when all hexose was consumed. When d-xylose and l-arabinose were present in a mixture, the consumption of both pentoses was reduced by the presence of the second sugar, although both sugars were consumed simultaneously by cells. The results show that induction of aldose reductase activity and d-xylose utilization by cells of Candida guilliermondii are under control of glucose repression.     

Biotechnological production of <Emphasis Type="SmallCaps">d</Emphasis>-glyceric acid and its application

Glycerol is currently produced in large amounts as a by-product during fat splitting and biodiesel fuel production. Over the past decade, both chemical and biotechnological processes to convert glycerol to value-added chemicals have been increasingly explored. This mini-review provides recent information about the biotechnological production of a glycerol derivative, d-glyceric acid (d-GA), and its possible applications. Little is known about GA as a bioproduct, but it is naturally found in different kinds of plants as a phytochemical constituent and is reported to have some biological activity. A racemic mixture of dl-GA can be obtained from glycerol via chemical oxidation; however, d-GA is mainly biotechnologically produced with the aid of bacteria. Under aerobic conditions, some acetic acid bacteria transform glycerol into d-GA, and optimization of initial glycerol concentration and aeration rate provided a yield of more than 80 g/l d-GA, using a strain of Gluconobacter frateurii.