Microbial biosynthesis and secretion of l-malic acid and its applications

l-Malic acid has many uses in food, beverage, pharmaceutical, chemical and medical industries. It can be produced by one-step fermentation, enzymatic transformation of fumaric acid to l-malate and acid hydrolysis of polymalic acid. However, the process for one-step fermentation is preferred as it has many advantages over any other process. The pathways of l-malic acid biosynthesis in microorganisms are partially clear and three metabolic pathways including non-oxidative pathway, oxidative pathway and glyoxylate cycle for the production of l-malic acid from glucose have been identified. Usually, high levels of l-malate are produced under the nitrogen starvation conditions, l-malate, as a calcium salt, is secreted from microbial cells and CaCO₃ can play an important role in calcium malate biosynthesis and regulation. However, it is still unclear how it is secreted into the medium. To enhance l-malate biosynthesis and secretion by microbial cells, it is very important to study the mechanisms of l-malic acid biosynthesis and secretion at enzymatic and molecular levels.     

Comprehensive assessment of the l-lysine production process from fermentation of sugarcane molasses

l-Lysine is an essential amino acid that can be produced by chemical processes from fossil raw materials, as well as by microbial fermentation, the latter being a more efficient and environmentally friendly procedure. In this work, the production process of l-lysine-HCl is studied using a systematic approach based on modeling and simulation, which supports decision making in the early stage of process design. The study considers two analysis stages: first, the dynamic analysis of the fermentation reactor, where the conversion of sugars from sugarcane molasses to l-lysine with a strain of Corynebacterium glutamicum is carried out. In this stage, the operation mode (either batch or fed batch) and operating conditions of the fermentation reactor are defined to reach the maximum technical criteria. Afterwards, the second analysis stage relates to the industrial production process of l-lysine-HCl, where the fermentation reactor, upstream processing, and downstream processing are included. In this stage, the influence of key parameters on the overall process performance is scrutinized through the evaluation of several technical, economic, and environmental criteria, to determine a profitable and sustainable design of the l-lysine production process. The main results show how the operating conditions, process design, and selection of evaluation criteria can influence in the conceptual design. The best plant design shows maximum product yield (0.31 g l-lysine/g glucose) and productivity (1.99 g/L/h), achieving 26.5% return on investment (ROI) with a payback period (PBP) of 3.8 years, decreasing water and energy consumption, and with a low potential environmental impact (PEI) index.

     

Fermentative Production of l-Leucine with Auxotrophic Mutants of Corynebaeterium glutamicum

An auxotrophic mutant of Corynebaeterium glutamicum was found to accumulate a large amount of l-leucine in the culture medium. The nutritional requirement of the mutant is rather complex but it’s growth was most remarkably stimulated by l-phenylalanine. Acetate (1.5~3.0%) or pyruvate (3%) stimulated the l-leucine production. By a further mutagenic treatment, 329 mutants earring some defect in addition to phenylalanine auxotrophy were derived from the mutant No. 190. Among them, a histidine auxotrophic derivative produced twice as much l-leucine as the parent strain, i.e., the level of l-leucine production by this derivative reached 16 mg/ml in a medium containing 12% glucose, 1 % (NH₄)₂SO₄ and 2.5% CH₃COONH₄ as carbon and nitrogen sources. Some other auxotrophic markers such as isoleucine- (or threonine-), threonine-, purine(s)-, homoserine-, or methionine- auxotrophy also improved the L-leucine production by No, 190.     

l-3-n-Butylphthalide Activates Akt/mTOR Signaling,Inhibits Neuronal Apoptosis and Autophagy and Improves Cognitive Impairment in Mice with Repeated Cerebral Ischemia–Reperfusion Injury

l-3-n-Butylphthalide (l-NBP) exerts neuroprotective effects in animal models of cerebral ischemia, but its potential benefits in repeated cerebral ischemia–reperfusion (RCIR) injury remain unknown. We investigated the effect of l-NBP on cognitive impairment induced by RCIR in mice. Male C57Bl/6 mice received sham surgery or bilateral common carotid artery occlusion (3 times, 20 min each) and were orally administered preoperative l-NBP (30 mg/kg/day, 7 days), postoperative l-NBP (30 or 60 mg/kg/day, 28 days) or postoperative vehicle (28 days). Learning and memory were assessed by the Morris water maze task and step-down passive avoidance test. Nissl staining was used to identify pathologic changes in the hippocampal CA1 region. The expressions of proteins associated with signaling, apoptosis and autophagy were assessed by quantitative PCR and western blot. RCIR induced deficits in learning and memory that were alleviated by preoperative or postoperative l-NBP administration. Pathologic lesions in the hippocampal CA1 region induced by RCIR were less severe in mice treated with l-NBP. Preoperative or postoperative l-NBP administration in mice receiving RCIR promoted hippocampal expression of phospho-Akt and phospho-mTOR (suggesting activation of Akt/mTOR signaling), increased the Bcl-2/Bax ratio (indicating suppression of apoptosis) and reduced the LC3-II/LC3-I ratio (implying inhibition of autophagy). Preoperative or postoperative l-NBP administration also depressed hippocampal levels of beclin-1 mRNA (indicating suppression of autophagy). These findings suggest that the effect of l-NBP to alleviate learning and memory deficits in mice following RCIR may involve activation of Akt/mTOR signaling and regulation of the expressions of proteins related to apoptosis and autophagy.

     

Engineered Bacillus subtilis 168 produces l-malate by heterologous biosynthesis pathway construction and lactate dehydrogenase deletion

In the present work, Bacillus subtilis was engineered to produce l-malate. Initially, the study revealed that the slight fumarase activity under anaerobic conditions is extremely favourable for l-malate one-step fermentation accumulation. Subsequently, an efficient heterologous biosynthesis pathway formed by Escherichia coli phosphoenolpyruvate carboxylase and Saccharomyces cerevisiae malate dehydrogenase was introduced into B. subtilis, which led to 6.04?±?0.19?mM l-malate production. Finally, the l-malate production was increased 1.5-fold to 9.18?±?0.22?mM by the deletion of lactate dehydrogenase. Under two-stage fermentation conditions, the engineered B. subtilis produced up to 15.65?±?0.13?mM l-malate, which was 86.3?% higher than that under anaerobic fermentation conditions. Though the l-malate production by the recombinant was low, this is the first attempt to produce l-malate in engineered B. subtilis and paves the way for further improving l-malate production in B. subtilis.     

Purification,characterization, gene cloning and nucleotide sequencing of D-stereospecific amino acid amidase from soil bacterium: Delftia acidovorans

The D-amino acid amidase-producing bacterium was isolated from soil samples using an enrichment culture technique in medium broth containing D-phenylalanine amide as a sole source of nitrogen. The strain exhibiting the strongest activity was identified as Delftia acidovorans strain 16. This strain produced intracellular D-amino acid amidase constitutively. The enzyme was purified about 380-fold to homogeneity and its molecular mass was estimated to be about 50 kDa, on sodium dodecyl sulfate polyacrylamide gel electrophoresis. The enzyme was active preferentially toward D-amino acid amides rather than their L-counterparts. It exhibited strong amino acid amidase activity toward aromatic amino acid amides including D-phenylalanine amide, D-tryptophan amide and D-tyrosine amide, yet it was not specifically active toward low-molecular-weight D-amino acid amides such as D-alanine amide, L-alanine amide and L-serine amide. Moreover, it was not specifically active toward oligopeptides. The enzyme showed maximum activity at 40°C and pH 8.5 and appeared to be very stable, with 92.5% remaining activity after the reaction was performed at 45°C for 30 min. However, it was mostly inactivated in the presence of phenylmethanesulfonyl fluoride or Cd²⁺, Ag⁺, Zn²⁺, Hg²⁺ and As³⁺ . The NH₂ terminal and internal amino acid sequences of the enzyme were determined; and the gene was cloned and sequenced. The enzyme gene damA encodes a 466-amino-acid protein (molecular mass 49,860.46 Da); and the deduced amino acid sequence exhibits homology to the D-amino acid amidase from Variovorax paradoxus (67.9% identity), the amidotransferase A subunit from Burkholderia fungorum (50% identity) and other enantioselective amidases.

     

Optimal Conditions for the Enzymatic Production of l-Aromatic Amino Acids from the Corresponding 5-Substituted Hydantoins

The reaction conditions for the production of l-tryptophan from dl-5-indolyl- methylhydantoin by Flavobacterium sp. AJ-3940, and the cultural conditions for the formation of the enzyme involved by this bacterium were investigated. The optimal pH of this reaction was around 8.5 and the optimal temperature was between 45 to 55°C. The amount of l-tryptophan produced was remarkably increased by the addition of inosine, which formed a water insoluble adduct with l-tryptophan, to the reaction mixture because of the release of end-product inhibition by l-tryptophan. This enzyme was inducibly and intracellularly produced by Flavobacterium sp. AJ-3940 in proportion to the increase in cell growth. Cells showing high activity were obtained using a medium containing 5 g glucose, 5 g (NH₄)₂SO₄, 1 g KH₂PO₄, 3 g K₂HPO₄, 0.1 g MgSO₄ · 7H₂O, 0.01 g CaCl₂ · 2H₂O, 50 ml corn steep liquor and 3.5 g dl-5-indolylmethylhydantoin in a total volume of 1 liter (pH 7.0). Under the best conditions, 43 mg/ml of l-tryptophan was produced from 50 mg/ml of dl-5-indolylmethylhydantoin with a molar yield of 97% in the presence of cells of Flavobacterium sp. AJ-3940. In addition, other l-aromatic amino acids such as l-phenylalanine, l-tyrosine, l-DOPA and related l-amino acids were also produced from the corresponding 5-substituted hydantoins by this bacterium containing the l-tryptophan-producing enzyme induced by dl-5-indolylmethylhydantoin.     

Production of d-lactic acid by Lactobacillus delbrueckii ssp. delbrueckii from orange peel waste: techno-economical assessment of nitrogen sources

In this study, the effect of several organic nitrogen sources (namely peptone, meat extract—ME, yeast extract—YE, and corn steep liquor—CSL) on d-lactic acid production by Lactobacillus delbrueckii ssp. delbrueckii has been studied. While lactic acid bacteria (LAB) are well-known for their complex nutritional requirements, organic nitrogen source-related cost can be as high as 38% of total operational costs (OPEX), being its nature and concentration critical factors in the growth and productivity of the selected strain. Corn steep liquor (CSL) has been chosen for its adequacy, on the grounds of the d-lactic acid yield, productivity, and its cost per kilogram of product. Finally, orange peel waste hydrolysate supplemented with 37 g/l CSL has been employed for d-lactic acid production, reaching a final yield of 88% and a productivity of 2.35 g/l h. CSL cost has been estimated at 90.78$/ton of d-lactate.

     

Fermentative Production of l-Proline with Auxotrophs of Corynebacterium glutamicum

Two auxotrophic mutants of Corynebacterium glutamicum were found to produce a large amount of l-proline in the culture medium. High concentration of MgSO₄ or MnSO₄ in the medium stimulated the l-proline production by an isoleucine auxotroph. Optimum concentration of l-isoleucine was 200 μg/ml, and the higher concentration of l-isoleucine reduced the l-proline production. The auxotroph produced 14.8 mg/ml of l-proline when cultured in a medium containing 12% glucose, 1.7% NH₄C1,0.6% MgSO₄·7H₂O, 0.06% MnSO₄·4H₂O and 200 μg/ml of l-isoleucine. The other mutant, whose growth responds to the bases of nucleic acids, produced 7 to 13 mg/ml of l-proline in a cane molasses (15%, as glucose concentration)-medium containing 2% of the acid-hydrolyzate of soybean meal. The l-proline production by this mutant increased to a level of 27 to 31 mg/ml when the growth was suppressed by the addition of 4% NH₄C1 to the medium, or by the addition of 2 mg/ml of polyoxyethylenestearylamine, a surfactant, to a culture at an appropriate stage of the fermentation.     

Glutamate Metabolism in a Glutamate-producing Bacterium,Brevibacterium flavum

Brevibacterium flavum No. 2247 was found to grow with l-glutamate as the sole carbon and nitrogen source on an agar-plate medium when high concentrations of l-glutamate, FeSO₄ and biotin were added to the medium. It grew on l-glutamate in liquid medium only when yeast extract or high concentrations of FeSO₄ and glucose or organic acids of the tricarboxylic acid cycle were added to the medium. The growth on l-glutamate in liquid medium was also stimulated by high concentrations of l-glutamate, biotin and MgSO₄, and inhibited by a high concentration of (NH₄)₂SO₄.

Aspartate aminotransferase (TA)- and α-ketoglutarate dehydrogenase (KD)-defective mutants did not grow on l-glutamate, and glutamate-utilizing revertants derived from these mutants recovered TA and KD activity, respectively, whereas glutamate dehydrogenase (GD)-defective mutants grew on l-glutamate. Washed cells of strain No. 2247 grown on glutamate decomposed the amino acid, whereas those grown on glucose did not. The degradation was observed only under aerobic conditions. The former cells showed higher KD, succinate dehydrogenase and fumarase activities than the latter cells. Of 75 mutants which did not grow on glutamate but grew on succinate, three strains lacked KD but showed the same glutamate productivity as the parent strain. Four other strains with normal KD levels showed higher glutamate productivity than the parent.     

Biological production of <Emphasis Type="SmallCaps">l</Emphasis>-malate: recent advances and future prospects

As intermediates in the TCA cycle, l-malate and its derivatives have been widely applied in the food, pharmaceutical, agriculture, and bio-based material industries. In recent years, biological routes have been regarded as very promising approaches as cost-effective ways to l-malate production from low-priced raw materials. In this mini-review, we provide a comprehensive overview of current developments of l-malate production using both biocatalysis and microbial fermentation. Biocatalysis is enzymatic transformation of fumarate to l-malate, here, the source of enzymes, catalytic conditions, and enzymatic molecular modification may be concluded. For microbial fermentation, the types of microorganisms, genetic characteristics, biosynthetic pathways, metabolic engineering strategies, fermentation substrates, and optimization of cultivation conditions have been discussed and compared. Furthermore, the combination of enzyme and metabolic engineering has also been summarized. In future, we also expect that novel biological approaches using industrially relevant strains and renewable raw materials can overcome the technical challenges involved in cost-efficient l-malate production.     

An Update on Design and Pharmacology of Dendritic Poly(l-lysine)

Dendritic nanomaterials are unique due to their flexible architectures. So far, many structural analogues of dendritic poly(l-lysine) have been developed. Since its monomer unit is a biodegradable amino acid, poly(l-lysine) derived nanocarriers are biocompatible and safe. In this overview, structural diversity of dendritic poly(l-lysine) scaffold and patents filed on them so far are described. Furthermore, biopharmaceutical properties and therapeutic activity modulations observed from their drug delivery applications are highlighted. Poly(l-lysine) based dendriplexes, dendrosomes and dendrisomes remain novel and nearly unexplored. Since structural modifications can control the biopharmaceutical properties of aforementioned scaffold, achieving programmed drug delivery is possible. Many such structures have demonstrated not only excellent carrier characteristics but few intrinsic therapeutic activities also. A poly(l-lysine) dendrimer product VivaGel is currently under consideration in a new drug application category of various regulatory bodies. As dendritic poly(l-lysine) scaffold is biocompatible unlike many other nanocarriers, its clinical utilization would prove considerably beneficial.

     

CO(2) Metabolism in Corn Roots. III. Inhibition of P-enolpyruvate Carboxylase by l-malate

Phosphoenolpyruvate carboxylase was purified from corn root tips about 80-fold by centrifugation, ammonium sulfate fractionation, and anion exchange and gel filtration chromatography. The resulting preparation was essentially free from malate dehydrogenase, isocitrate dehydrogenase, malate enzyme, NADH oxidase, and pyruvate kinase activity. Kinetic analysis indicated that l-malate was a noncompetitive inhibitor of P-enolpyruvate carboxylase with respect to P-enolpyruvate (K_I = 0.8 mm). d-Malate, aspartate, and glutamate inhibited to a lesser extent; succinate, fumarate, and pyruvate did not inhibit. Oxaloacetate was also a noncompetitive inhibitor of P-enolpyruvate carboxylase with an apparent K_I of 0.4 mm. A comparison of oxaloacetate and l-malate inhibition suggested that the mechanisms of inhibition were different. These data indicated that l-malate may regulate CO₂ fixation in corn root tips by a feedback or end product type of inhibition.     

Thermostable and highly specific l-aspartate oxidase from Thermococcus litoralis DSM 5473: cloning,overexpression, and enzymological properties

We successfully expressed the l-aspartate oxidase homolog gene (accession no: OCC_06611) of Thermococcus litoralis DSM 5473 in the soluble fraction of Escherichia coli BL21 (DE3) using a pET21b vector with 6X His tag at its C-terminus. The gene product (Tl-LASPO) showed l-aspartate oxidase activity in the presence of FAD in vitro, and this report is the first that details an l-aspartate oxidase derived from a Thermococcus species. The homologs of Tl-LASPO existed mainly in archaea, especially in the genus of Thermococcus, Pyrococcus, Sulfolobus, and Halobacteria. The quaternary structure of Tl-LASPO was homotrimeric with a subunit molecular mass of 52 kDa. The enzyme activity of Tl-LASPO increased with temperature up to 70 °C. Tl-LASPO was active from pH 6.0 to 9.0, and its highest activity was at pH 8.0. Tl-LASPO was stable at 80 °C for 1 h. The highest k _cat/K _m value was observed in assays at 70 °C. Tl-LASPO was highly specific for l-aspartic acid. Tl-LASPO utilized fumaric acid, 2,6-dichlorophenolindophenol, and ferricyanide in addition to FAD as a cofactor under anaerobic conditions. The absorption spectrum of holo-Tl-LASPO exhibited maxima at 380 and 450 nm. The FAD dissociation constant, K _d, of the FAD-Tl-LASPO complex was determined to be 5.9 × 10⁻⁹ M.

     

Efficient production of indigoidine in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Indigoidine is a bacterial natural product with antioxidant and antimicrobial activities. Its bright blue color resembles the industrial dye indigo, thus representing a new natural blue dye that may find uses in industry. In our previous study, an indigoidine synthetase Sc-IndC and an associated helper protein Sc-IndB were identified from Streptomyces chromofuscus ATCC 49982 and successfully expressed in Escherichia coli BAP1 to produce the blue pigment at 3.93 g/l. To further improve the production of indigoidine, in this work, the direct biosynthetic precursor l-glutamine was fed into the fermentation broth of the engineered E. coli strain harboring Sc-IndC and Sc-IndB. The highest titer of indigoidine reached 8.81 ± 0.21 g/l at 1.46 g/l l-glutamine. Given the relatively high price of l-glutamine, a metabolic engineering technique was used to directly enhance the in situ supply of this precursor. A glutamine synthetase gene (glnA) was amplified from E. coli and co-expressed with Sc-indC and Sc-indB in E. coli BAP1, leading to the production of indigoidine at 5.75 ± 0.09 g/l. Because a nitrogen source is required for amino acid biosynthesis, we then tested the effect of different nitrogen-containing salts on the supply of l-glutamine and subsequent indigoidine production. Among the four tested salts including (NH₄)₂SO₄, NH₄Cl, (NH₄)₂HPO₄ and KNO₃, (NH₄)₂HPO₄ showed the best effect on improving the titer of indigoidine. Different concentrations of (NH₄)₂HPO₄ were added to the fermentation broths of E. coli BAP1/Sc-IndC+Sc-IndB+GlnA, and the titer reached the highest (7.08 ± 0.11 g/l) at 2.5 mM (NH₄)₂HPO₄. This work provides two efficient methods for the production of this promising blue pigment in E. coli.     

Extracellular Production of l-Lysine α-Oxidase in Wheat Bran Culture of a Strain of Trichoderma viride

A mold strain Y244-2 capable of producing l-lysine α-oxidase, a new enzyme catalyzing the α-oxidative deamination of l-lysine, was identified as Trichoderma viride. Among strains belonging to the genus Trichoderma tested, only Trichoderma viride Y244-2 produced the enzyme in wheat bran culture. The maximum enzyme production by the mold grown on wheat bran was observed after 10 and 14 days incubation with and without NaN0₃, respectively. Addition of NaN0₃, NH₄N0₃, adenine, purine nucleosides, l-histidine, glycine or l-glutamine to wheat bran stimulated the production of the enzyme. In the liquid culture, the enzyme was produced extracellulary under the aerobic conditions, although the production was much lower than that in the wheat bran culture.     

Sodium ions activated phosphofructokinase leading to enhanced d-lactic acid production by Sporolactobacillus inulinus using sodium hydroxide as a neutralizing agent

Sporolactobacillus inulinus is a superior d-lactic acid-producing bacterium and proposed species for industrial production. The major pathway for d-lactic acid biosynthesis, glycolysis, is mainly regulated via the two irreversible steps catalyzed by the allosteric enzymes, phosphofructokinase (PFK) and pyruvate kinase. The activity level of PFK was significantly consistent with the cell growth and d-lactic acid production, indicating its vital role in control and regulation of glycolysis. In this study, the ATP-dependent PFK from S. inulinus was expressed in Escherichia coli and purified to homogeneity. The PFK was allosterically activated by both GDP and ADP and inhibited by phosphoenolpyruvate; the addition of activators could partly relieve the inhibition by phosphoenolpyruvate. Furthermore, monovalent cations could enhance the activity, and Na⁺ was the most efficient one. Considering this kind activation, NaOH was investigated as the neutralizer instead of the traditional neutralizer CaCO₃. In the early growth stage, the significant accelerated glucose consumption was achieved in the NaOH case probably for the enhanced activity of Na⁺-activated PFK. Using NaOH as the neutralizer at pH 6.5, the fermentation time was greatly shortened about 22 h; simultaneously, the glucose consumption rate and the d-lactic acid productivity were increased by 34 and 17%, respectively. This probably contributed to the increased pH and Na⁺-promoted activity of PFK. Thus, fermentations by S. inulinus using the NaOH neutralizer provide a green and highly efficient d-lactic acid production with easy subsequent purification.

     

The use of a potential-sensitive cyanine dye for studying ion-dependent electrogenic renal transport of organic solutes. Uptake of l-malate and d-malate by luminal-membrane vesicles

The mechanisms of uptake of dicarboxylic acids by rabbit renal luminal-membrane vesicles were studied by the use of filtration and spectrophotometric techniques as described in an accompanying paper [Kragh-Hansen, Jørgensen & Sheikh (1982) Biochem. J. 208, 359–368]. Addition of l- or d-malate to dye-membrane-vesicle suspensions in the presence of Na⁺ gradients (extravesicular>intravesicular) resulted in spectral curves indicative of depolarization events. The renal uptake of dicarboxylic acids was dependent on the type of Na⁺-salt anion present and could be correlated with the ability of the anions to penetrate biological membranes (i.e. Cl⁻>SO₄²⁻>gluconate). Identical results were obtained by a filtration technique with Sartorius membrane filters. The results indicate that the dicarboxylic acids are taken up by the membrane vesicles in an electrically positive form (i.e. Na⁺/substrate coupling ratio 3:1) by an Na⁺-dependent transport system. This proposal was further supported by spectrophotometric experiments with various ionophores such as valinomycin, gramicidin and nigericin. The absorbance changes associated with simultaneous addition of l- and d-malate and spectrophotometric competition studies revealed that the two isomers are taken up by a common transport system. Spectral changes of the dye induced by addition of increasing concentrations of l- or d-malate indicated that the transport system favours the unphysiological d-form rather than the l-form of malate. Furthermore, it was observed that the affinity of both isomers for the transport system was dependent on the concentration of Na⁺ in the medium.     

Characterization of the Dicarboxylate Transporter DctA in Corynebacterium glutamicum

Transporters of the dicarboxylate amino acid-cation symporter family often mediate uptake of C₄-dicarboxylates, such as succinate or l-malate, in bacteria. A member of this family, dicarboxylate transporter A (DctA) from Corynebacterium glutamicum, was characterized to catalyze uptake of the C₄-dicarboxylates succinate, fumarate, and l-malate, which was inhibited by oxaloacetate, 2-oxoglutarate, and glyoxylate. DctA activity was not affected by sodium availability but was dependent on the electrochemical proton potential. Efficient growth of C. glutamicum in minimal medium with succinate, fumarate, or l-malate as the sole carbon source required high dctA expression levels due either to a promoter-up mutation identified in a spontaneous mutant or to ectopic overexpression. Mutant analysis indicated that DctA and DccT, a C₄-dicarboxylate divalent anion/sodium symporter-type transporter, are the only transporters for succinate, fumarate, and l-malate in C. glutamicum.In bacteria, the uptake of dicarboxylates, such as the tricarboxylic acid (TCA) cycle intermediates succinate, fumarate, and l-malate, is mediated by transporters of different protein families. Whereas Dcu-type transporters facilitate dicarboxylate uptake under anaerobic conditions, the most common aerobic dicarboxylate transporters are members of the dicarboxylate amino acid-cation symporter (DAACS), divalent anion sodium symporter (DASS), tripartite ATP-independent periplasmic (TRAP), and CitMHS transporter families. DAACS transporters are responsible for C₄-dicarboxylate uptake under aerobic conditions in various bacteria, e.g., DctA from Escherichia coli, Bacillus subtilis, or Rhizobium leguminosarum, and are involved in different physiological functions (2, 4, 27, 41). The first described member of the TRAP family is the C₄-dicarboxylate transporter DctPQM from Rhodobacter capsulatus, which facilitates substrate uptake by the use of an extracytoplasmic solute receptor (8). An example of the DASS family, members of which occur in bacteria, as well in eukaryotes, is the well-characterized transporter SdcS from Staphylococcus aureus (13). Members of the CitHMS family import citrate in symport with the cation Mg²⁺ or Ca²⁺. Whereas E. coli possesses one DctA and four different Dcu carriers, no Dcu transporter-encoding genes were found in Corynebacterium glutamicum (16, 19), which is used for the industrial production of amino acids, such as glutamate (33) or l-lysine (39), and is capable of succinate and l-lactate production under oxygen deprivation conditions. A dctA gene was annotated (19); however, C. glutamicum is not able to utilize succinate, malate, or fumarate as a sole carbon source. The uptake systems CitH and TctCBA have been characterized recently as citrate uptake systems (3, 26). Interestingly, we and others have shown that C. glutamicum possesses a DASS family transporter (DccT) for uptake of the C₄-dicarboxylates succinate, fumarate, and l-malate (36, 40). Spontaneous mutants showing fast growth in succinate or fumarate minimal medium were isolated and shown to possess promoter-up mutations in the dccT gene (40). In l-malate minimal medium, these spontaneous mutants showed relatively slow growth, and the affinity of DccT for succinate and fumarate was found to be 5- and 12-fold higher than for l-malate, respectively (40). These findings prompted us to search for other uptake systems for l-malate in C. glutamicum. Here, we describe the identification and characterization of the DAACS family protein DctA from C. glutamicum as a proton motive force-driven uptake system for C₄-dicarboxylate intermediates of the TCA cycle. Additionally, we compare both uptake systems, DccT and DctA, from C. glutamicum.