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.     

Production of l-Valine by 2-Thiazolealanine Resistant Mutants Derived from Glutamic Acid Producing Bacteria

Potent l-valine producers were screened among 2-thiazolealanine resistant mutants derived from three typical l-glutamic acid producing bacteria: Brevibacterium lactofermentum, Corynebacterium acetoacidophilum, Arthrobacter citreus. By strain No. 487, the best producer derived from Brevibacterium, 31 mg/ml of l-valine was produced after 72 hr when 10% glucose was supplied as a carbon source, thus giving the yield of 31% from glucose. Accumulation of the other amino acids was negligible. The addition of l-isoleucine and l-leucine in the culture medium did not reduce the l-valine production, indicating that the l-valine biosynthesis is insensitive to these end products in the l-valine producer.     

Biosynthesis of polymalic acid in fermentation: advances and prospects for industrial application

Some microorganisms naturally produce β-poly(l-malic acid) (PMA), which has excellent water solubility, biodegradability, and biocompatibility properties. PMA has broad prospective applications as novel biopolymeric materials and carriers in the drug, food, and biomedical fields. Malic acid, a four-carbon dicarboxylic acid, is widely used in foods and pharmaceuticals, as a platform chemical. Currently, malic acid produced through chemical synthesis and is available as a racemic mixture of l- and d-forms. The d-form malic acid exhibits safety concerns for human consumption. There is extensive interest to develop economical bioprocesses for l-malic acid and PMA production from renewable biomass feedstocks. In this review, we focus on PMA biosynthesis by Aureobasidium pullulans, a black yeast with a large genome containing genes encoding many hydrolases capable of degrading various plant materials. The metabolic and regulatory pathways for PMA biosynthesis, metabolic engineering strategies for strain development, process factors affecting fermentation kinetics and PMA production, and downstream processing for PMA recovery and purification are discussed. Prospects of microbial PMA and malic acid production are also considered.     

Studies on Metabolism of Pyrrolidone Carboxylic Acid in Bacteria

The present investigation is concerned with l-glutamic acid production in the presence of pyrrolidone carboxylic acid and glucose in Bacillus megaterium st. 6126. This strain does not grow on dl-pyrrolidone carboxylic acid (dl-PCA)¹⁾ as the sole source of carbon and nitrogen. The optimal concentration of yeast extract required for the maximal production of l-glutamic acid was 0.005% under the conditions used. As the yeast extract concentration was increased, growth increased proportionally; but the l-glutamic acid production did not exceed the control’s to which glucose and ammonium chloride had been added. l-Glutamic acid produced by both growing cultures and resting cells was derived from glucose and ammonium salt of dl-PCA. Isotope experiments suggested that the l-glutamic acid produced was partially derived from ammonium salt of dl-PCA in the growing culture which had been supplemented with d-glucose-U-¹⁴C or dl-PCA-1-¹⁴C and that ammonium salt of dl-PCA was consumed as the source of nitrogen and carbon for l-glutamic acid.     

Studies on the Mechanism of Strengthening Fish Gel by Basic Amino Acids

An electro-energizing fermentation (E-E F) method has been developed. In this method, a direct electrical current is applied to a microbial culture to accelerate the reductive metabolism of microorganisms or to impart profitable effects to microbial cells. This E-E F method was applied to l-glutamic acid fermentation by Brevibacterium flavum No. 2247. When glucose was used as a substrate, the addition of 0.01 mm neutral red (NR), redox dye (electron carrier), to the fermentation broth at the beginning of cultivation was effective for l-glutamate (l-Glu) production. A direct current of 200~300 μA/cm² at 1.5 V was applied through out the cultivation of this bacterium. This resulted in about a 10% increase in yield of l-Glu.     

Conversion of the Extracellular Dextransucrase Isoenzymes from Leuconostoc mesenteroides NRRL B-1299

Effect of oxygen tension on l-lysine, l-threonine and l-isoleucine accumulation was investigated. Sufficient supply of oxygen to satisfy the cell’s oxygen demand was essential for the maximum production in each fermentation. The dissolved oxygen level must be controlled at greater than 0.01 atm in every fermentation, and the optimum redox potentials of culture media were above ?170 mV in l-lysine and l-threonine and above ?180 mV in l-isoleucine fermentations. The maximum concentrations of the products were 45.5 mg/ml for l-lysine, 10.3 mg/ml for l-threonine and 15.1 mg/ml for l-isoleucine. The degree of the inhibition due to oxygen limitation was slight in the fermentative production of l-lysine, l-threonine and l-isoleucine, whose biosynthesis is initiated with l-aspartic acid, in contrast to the accumulation of l-proline, l-glutamine and l-arginine, which is biosynthesized by way of l-glutamic acid.     

Production of l-Leucine by a Mutant of Brevibacterium lactofermentum 2256

A potent l-leucine producer was screened among mutants of glutamic acid producing bacteria. This strain, No. 218, is one of 2-thiazolealanine resistant mutants derived from a methionine isoleucine double auxotroph of Brevibacterium lactofermentum 2256 by nitroso-guanidine.

Strain No. 218 produced 19 mg/ml of l-leucine after 72 hr cultivation when 8 % glucose and 4 % ammonium sulfate were supplied as a carbon and a nitrogen source, respectively, thus giving the yield of 23.1 % from glucose.

The addition of Fe²⁺ and Mn²⁺ in combination gave much more productivity than that of Fe²⁺ or Mn²⁺ alone.

Effects of amino acids, nucleic acids, vitamins, and the other nutrients on l-leucine production were investigated.

The fermentation product was isolated and purified from the culture, and identified as l-leucine.     

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.     

Cultural Conditions for l-Leucine Production by Strain No. 218, a Mutant of Brevibacterium lactofermentum 2256

The excellent l-leucine producing mutant No. 218, derived from a biotin requiring glutamic acid producing strain, is methionine and isoleucine auxotrophic. A suboptimum growth condition made by adding a limiting amount of isoleucine was necessary for the maximum production of l-leucine. On the other hand, methionine was indifferent to the productivity if sufficiently supplied for growth.

Biotin of more than 50 μg/liter caused the accumulation of l-leucine; less than 50 μg/liter, however, gave a drastic change in accumulation pattern from l-leucine to l-glutamic acid. Strain No. 218 produced 28 mg/ml of l-leucine after 72 hr cultivation when 13 % glucose was supplied as a carbon source, thus giving the yield of 21.6%.

Effects on l-leucine production of concentrations of inorganic salts, pH, temperature and aeration were also investigated.     

Absolute Configuration of (+)-1-Acetoxy-p-menth-3-one Isolated from Essential Oil of Mentha gentilis (L.)

The most effective electro-energizing fermentation (E-E F) conditions for l-glutamate (l-Glu) production by Brevibacterium flavum No. 2247 were determined. The adding of 0.01 mm neutral red at the beginning of cultivation was found most effective. A 1.5 V direct current was applied to the culture broth at 6~8 hr after inoculation in the cathode compartment, l-Glu was produced at 51.0 mg per ml, and this is about a 15 % increase in yield compared to the yield of the not electro-energizing (E-E) control (44.3 mg/ml).     

Production of l-Threonine by Analog-resistant Mutants

Mutants resistant to α-amino-β-hydroxyvaleri0c acid (AHV) were derived from various bacteria which belong to Corynebacterium, Brevibacterium, Arthrobacter, Microbacterium, or Bacillus by mutational treatment with N-methyl-N′-nitro-N-nitrosoguanidine(NTG), and screened for their ability to produce l-threonine. A number of l-threonine producers were obtained from each group of bacteria. Among them, the mutants derived from C. glutamicum KY9159(Met^?) were further mutagenized with NTG to derive thialysine(S-Lys)-resistant mutants. An AHV-resistant mutant, KY10484 was proved to be much more sensitive to the growth inhibition by thialysine than the parent strain, KY9159. From KY10484, a number of AHV- and thialysine-resistant mutants were derived. Approximately a half of these mutants were found to produce more l-threonine than KY10484. Among these mutants, KY10440 (Met^?, AHV^R, s-Lys^R) was used to investigate the cultural conditions for l-threonine production. The growth of KY10440 decreased largely with addition of l-homoserine, a threonine precursor. l-Asparagine, l-cystine, l-glutamine or l-arginine partially reversed the inhibitory effect of l-homoserine. Addition of these amino acids at low level led to increase l-threonine production. The amount of l-threonine accumulation reached to a level of 14mg/ml with a medium containing 10% glucose and to a level of 10 mg/ml with a medium containing 5% molasses (as glucose).

Another AHV- and thialysine-resistant mutant, KY10251 which was also derived from KY9159 was found to produce both 9 mg/ml of l-threonine and 5.5 mg/ml of l-lysine in a culture broth.     

Enzymatic Studies on the Oxidation of Sugar and Sugar Alcohol

During the course of studies on the oxidative metabolism of d-sorbitol by acetic acid bacteria, it was found that d-sorbitol was almost quantitatively converted to 5-keto-d-fructose via l-sorbose by a certain strain of Gluconobacter suboxydans. In addition to 5-keto-d-fructose, three γ-pyrone compounds, kojic acid, 5-oxymaltol, and 3-oxykojic acid, 2-keto-l-gulonate, and several organic acids such as succinic, glycolic, and glyceric acids were confirmed in the culture filtrate of this bacterium.

• The most suitable carbon source for 5-ketofructose fermentation by Gluconobacter suboxydans Strain 1 was confirmed to be d-sorbitol or l-sorbose using growing and resting cells. d-Fructose had little effect on the formation of this dicarbonylhexose.

• The optimal pH for the formation from l-sorbose by intact cells was found to be at 4.2.

• The activity of the pentose phosphate cycle in the resting cells was calculated as 13~17 μatoms/hr/mg of dry cells by the use of the manometric techniques.

• There was no strain tested so far which could accumulate a large amount of 5- keto-d-fructose from d-sorbitol except this bacterium.

• The experimental results shown in this paper makes the prediction that a certain dehydrogenating system of l-sorbose is functional in the organism, and the metabolic pathways of d-sorbitol via l-sorbose and 5-keto-d-fructose is proposed.

     

Essential Role of Aspartokinase in L-Threonine Production by Escherichia coli W Mutants

We previously constructed an l-threonine-producing strain of E. coli W, KY8280, which is an Ile⁺ revertant of KY8279 which requires l-methionine, a,£-diaminopimelic acid and l-isoleucine [H. Kase et al., Agric. Biol. Chem., 35, 2089 (1971)]. From KY8280, another l-threonine-hyperproducing strain, KY8366, was obtained as an α-amino-β-hydroxy valeric acid (AHV, a threonine analog)-resistant mutant. Enzymatic analysis revealed that KY8280 constitutively expressed 8-fold higher l-threonine-sensitive aspartokinase I activity than KY8279. In addition, KY8366 constitutively expressed 13-fold higher l-lysine-sensitive aspartokinase III activity than KY8280. Such elevated levels of aspartokinases may contribute to the hyperproduction of l-threonine by these mutant strains. KY8366 produced 28 mg/ml of l-threonine in a culture medium fed with 12% glucose.     

2-Keto-l-gulonic Acid Fermentation

l-Sorbose metabolism in Pseudomonas aeruginosa IFO 3898 was studied. When the strain was cultivated in l-sorbose medium, l-idonic and 2-keto-l-gulonic acids were detected in the culture broth.

From the results on the metabolism of various sugars and sugar acids with the cell suspension and the metabolites accumulated, the following pathway was proposed for the l-sorbose metabolism in Ps. aeruginosa IFO 3898.

l-Sorbose → l-idose → l-idonic acid → 2-keto-l-gulonic acid.     

Occurrence of 3-Hydroxy-3-methyl-glutaryl Coenzyme A Reductase in Sweet Potato

Illumination of the dark-grown Euglena gracilis, both the wild-green type and a permanently bleached mutant, for 4 hr at 2,000 lux caused about 6-fold increase of the cellular content of total l-ascorbic acid. The increase was mainly due to an increase of reduced-form l-ascorbic acid. From the action spectrum only blue light was found to be effective for the increase. Darkening stopped the increase and reillumination started a renewed increase. The activity of l-gulono-γ-lactone dehydrogenase, catalyzing the last step of l-ascorbic acid biosynthesis, was also increased two fold by illumination for 2 hr, and was changed in parallel to that of the cellular content of l-ascorbic acid depending on the presence or absence of illumination. The augmentation of l-ascorbic acid formation was markedly inhibited by various inhibitors and uncouplers, but not by dichlorophenyldimethylurea. The results in sum suggest that the light-dependent increase of l-ascorbic acid formation in E. gracilis is not primarily associated with photosynthesis, but is apparently related to the adaptation of the dark-grown cells to the illuminated state.     

Studies on the Polymorphism of l-Glutamic Acid

The effects on the polymorphic crystallization of l-glutamic acid were examined of many substances including amino acids, inorganic salts, surface active agents, and sodium salt or hydrochloride of l-glutamic acid, when contained in the mother liquor.

The co-existence of amino acids, especially of l-aspartic acid, l-phenylalanine, l-tyrosine, l-lcucine and l-cystine contributed to the crystallization of l-glutamic acid in α-form, and these amino acid showed an inhibitory action on the transition of α-crystals as the solid phase in the aqueous solution, to β-crystals.

In the presence of a large amount of l-glutamate or the hydrochloride at the time of nucleation of l-glutamic acid, mostly β-crystals appeared even in the presence of the amino acids named above.     

l-Isoleucine Production by Analog-resistant Mutants Derived from Threonine-producing Strain of Corynebacterium glutamicum

A thiaisoleucine-resistant mutant, ASAT–372, derived from a threonine producer of Corynebacterium glutamicum, KY 10501, produced 5 mg/ml each of l-isoleucine and l-threonine. l-Isoleucine productivity of ASAT–372 was improved stepwise, with concurrent decrease in threonine production, by successively endowing it with resistivity to such substances as ethionine, 4-azaleucine and α-aminobutyric acid. The mutant strain finally selected, RAM–83, produced 9.7 mg/ml of l-isoleucine with a medium containing 10% (as sugar) molasses.

l-Isoleucine production was significantly affected by the concentration of ammonium sulfate in the fermentation medium. At 4% ammonium sulfate l-isoleucine production was enhanced whereas l-threonine production was suppressed. At 2% ammonium sulfate l-threonine production was stimulated while l-isoleucine production decreased.     

Microbial Production of l-Phenylalanine from n-Alkanes

A tyrosine auxotroph derived from a hydrocarbon utilizing bacterium, Corynebacterium sp. KY 4309, was found to accumulate a large amount of l-phenylalanine in the broth. The cultural conditions for l-phenylalanine production were studied. The pH value during cultivations exhibited a remakable effect on l-phenylalanine production. The addition of l-tryptophan enhanced the l-phenylalanine accumulation. Shikimic acid and phenylpyruvic acid are possible precursors of phenylalanine biosynthesis in this bacterium. Production of l-phenylalanine attained to a level of 10 mg per ml for 68 hr under optimal conditions.     

2-Keto-l-gulonic Acid Fermentation

A number of bacterial strains from type culture collections and natural sources were examined in their metabolic characteristics toward sorbitol and l-sorbose.

Paper chromatographic analyses of sorbitol and l-sorbose metabolites obtained from the cultures of various bacteria revealed that the organisms producing 2-keto-l-gulonic acid from sorbitol were merely found in the genera Acetobacter, Gluconobacter and Pseudomonas, whereas those producing the acid from l-sorbose were distributed in the twelve genera of bacteria: Acetobacter, Alcaligenes, Aerobacter, Azotobacter, Bacillus, Escherichia, Gluconobacter, Klebsiella, Micrococcus, Pseudomonas, Serratia and Xanthomonas.

G. melanogenus, which was characterized by excellent production of 2-keto-l-gulonic acid from sorbitol, also formed several other sugars and sugar acids as the sorbitol metabolites. These compounds were identified to be d-fructose, l-sorbose, d-mannonic acid, L-idonic acid, 2-keto-d-gluconic acid and 5-keto-d-mannonic acid, respectively, by means of two-dimensional paper chromatography.

Bacteria producing 2-keto-l-gulonic acid from sorbitol were usually isolated from fruits but not from soil.     

A Growth Factor for Malo-lactic Fermentation Bacteria

A growth factor (TJF) for a malo-lactic fermentation bacterium has been isolated from tomato juice, and found to be a β-glucoside. The NMR spectra of TJF and its acetate revealed that the glucosyl residue linked to the hydroxyl group at C-2′ or C-4′ of d- or l-pantothenic acid moiety. Then, 2′-O-(β-d-glucopyranosyl)-dl-pantothenic acid (I), 4′-O-(β-d-glucopyranosyl)-dl-pantothenic acid (II) and 4′-O-(β-d-glucopyranosyl)-d(R)-pantothenic acid (II-a) were synthesized, and Il-a and 4′-O-(β-d-glucopyranosyl)-l-pantothenic acid (II-b) were obtained by the optical resolution of the acetate of II. Among the above compounds, II-a was identical with natural TJF regarding to the biological activity, NMR and ORD spectra, and thin-layer chromatography.