l-Malic acid production from fumaric acid by a laboratory Saccharomyces cerevisiae strain SHY2

Summary l-Malic acid was produced efficiently from fumaric acid by Saccharomyces cerevisiae SHY2. The amount of l-malic acid produced increased with the increase in initial fumaric acid concentration (from 20 to 120 g/L). The average specific and volumetric production rates reached up to 0.708 g/g·h and 2.787 g/L·h, respectively, in 24 hours. Final l-malic acid concentration of up to 109 g/L was obtained in 96 hours.     

The cytosolic pathway of l-malic acid synthesis in Saccharomyces cerevisiae: the role of fumarase

Saccharomyces cerevisiae accumulates l-malic acid but only minute amounts of fumaric acid. A ¹³C-nuclear magnetic resonance study following the label from glucose to l-malic acid indicates that the l-malic acid is synthesized from pyruvic acid via oxaloacetic acid. From this, and from previously published studies, we conclude that a cytosolic reductive pathway leading from pyruvic acid via oxaloacetic acid to l-malic acid is responsible for the l-malic acid production in yeast. The non-production of fumaric acid can be explained by the conclusion that, in the cell, cytosolic fumarase catalyzes the conversion of fumaric acid to l-malic acid but not the reverse. This conclusion is based on the following findings. (a) The cytosolic enzyme exhibits a 17-fold higher affinity towards fumaric acid than towards l-malic acid; the K _m for l-malic acid is very high indicating that l-malic acid is not an in vivo substrate of the enzyme. (b) Overexpression of cytosolic fumarase does not cause accumulation of fumaric acid (but rather more l-malic acid). (c) According to ¹³C NMR studies there is no interconversion of cytosolic l-malic and fumaric acids.     

Histidine decarboxylase production by Lactobacillus hilgardii: Effect of organic acids

Histidine decarboxylase production from Lactobacillus hilgardii 5w, isolated from wine, was inhibited by the presence of l-malic acid in the basal culture medium. The inhibition was related to l-malic acid concentration. The maximal production of the enzyme at 12 h of culture incubated at 30°C was inhibited 71% by 2 g/L l-malic acid and 47% by 0.5 g/L. In these conditions l-malic acid consumption was 16% and 20% respectively. The addition of 300 mg/L citric acid to the basal medium stimulated the enzyme production from 9 to 45 nmoles/min/mg dry weight, and the increase was correlated with citric acid concentration. When different concentrations of l-malic acid were added to the basal medium plus 200 mg/L citric acid, reversion of stimulation was observed, achieving the maximum at a concentration of 2 g/L. In this case, citric acid comsumption was not modified, whereas L-malic acid utilization was higher.     

Overexpression of cytosolic malate dehydrogenase (MDH2) causes overproduction of specific organic acids in Saccharomyces cerevisiae

Saccharomyces cerevisiae accumulates l-malic acid through a cytosolic pathway starting from pyruvic acid and involving the enzymes pyruvate carboxylase and malate dehydrogenase. In the present study, the role of malate dehydrogenase in the cytosolic pathway was studied. Overexpression of cytosolic malate dehydrogenase (MDH2) under either the strong inducible GAL10 or the constitutive PGK promoter causes a 6- to 16-fold increase in cytosolic MDH activity in growth and production media and up to 3.7-fold increase in l-malic acid accumulation in the production medium. The high apparent K _m of MDH2 for l-malic acid (11.8 mM) indicates a low affinity of the enzyme for this acid, which is consistent with the cytosolic function of the enzyme and differs from the previously published K _m of the mitochondrial enzyme (MDH1, 0.28 mM). Under conditions of MDH2 overexpression, pyruvate carboxylase appears to be a limiting factor, thus providing a system for further metabolic engineering of l-malic acid production. The overexpression of MDH2 activity also causes an elevation in the accumulation of fumaric acid and citric acid. Accumulation of fumaric acid is presumably caused by high intracellular l-malic acid concentrations and the activity of the cytosolic fumarase. The accumulation of citric acid may suggest the intriguing possibility that cytosolic l-malic acid is a direct precursor of citric acid in yeast. Received: 22 January 1997 / Received revision: 14 April 1997 / Accepted: 19 April 1997     

Malic acid accumulation by Aspergillus flavus

Summary ¹³C Nuclear magnetic resonance and fumarase and NAD-malate dehydrogenase isoenzyme studies were carried out in a strain of A. flavus which produces relatively high levels of l-malic acid from glucose. The results of the ¹³C NMR showed that the ¹³C label from [1-¹³C] glucose was incorporated only to C-3 (-CH₂-) of l-malic acid and indicated that this acid must be synthesized from pyruvate mainly via oxaloacetate. Electrophoretic analysis has established the presence of unique mitochondrial and cytosolic isoenzymes for fumarase and malate dehydrogenase. Changes in the isoenzyme pattern were observed for malate dehydrogenase but not for fumarase during acid production. Cycloheximide inhibited profoundly both l-malic acid production and the increase in the major isoenzyme of malate dehydrogenase, without affecting either the total activity of fumarase or its isoenzyme pattern. The results suggested that de novo protein synthesis is involved in the increase in the activity of the major isoenzyme of malate dehydrogenase and that this isoenzyme is essential for l-malic acid production and accumulation.     

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.     

Metabolic pathways and biotechnological production of l-cysteine

l-Cysteine is an important amino acid both biologically and commercially. Although most amino acids are commercially produced by fermentation, cysteine is mainly produced by protein hydrolysis. However, synthetic or biotechnological products have been preferred in the market. Biotechnological processes for cysteine production, both enzymatic and fermentative processes, are discussed. Enzymatic process, the asymmetric hydrolysis of dl-2-amino-Δ²-thiazoline-4-carboxylic acid to l-cysteine, has been developed and industrialized. The l-cysteine biosynthetic pathways of Escherichia coli and Corynebacterium glutamicum, which are used in many amino acid production processes, are also described. These two bacteria have basically same l-cysteine biosynthetic pathways. l-Cysteine-degrading enzymes and l-cysteine-exporting proteins both in E. coli and C. glutamicum are also described. In conclusion, for the effective fermentative production of l-cysteine directly from glucose, the combination of enhancing biosynthetic activity, weakening the degradation pathway, and exploiting the export system seems to be effective.     

Genomic variations of <Emphasis Type="Italic">Oenococcus oeni</Emphasis> strains and the potential to impact on malolactic fermentation and aroma compounds in wine

Malolactic fermentation (MLF) is the bacterially driven decarboxylation of l-malic acid to l-lactic acid and carbon dioxide, and brings about deacidification, flavour modification and microbial stability of wine. The main objective of MLF is to decrease wine sourness by a small increase in wine pH via the metabolism of l-malic acid. Oenococcus oeni is the main lactic acid bacterium to conduct MLF in virtually all red wine and an increasing number of white and sparkling wine bases. Over the last decade, it is becoming increasingly recognized that O. oeni exhibits a diverse array of secondary metabolic activities during MLF which can modify the sensory properties of wine. These secondary activities include the metabolism of organic acids, carbohydrates, polysaccharides and amino acids, and numerous enzymes such as glycosidases, esterases and proteases, which generate volatile compounds well above their odour detection threshold. Phenotypic variation between O. oeni strains is central for producing different wine styles. Recent studies using array-based comparative genome hybridization and genome sequencing of three O. oeni strains have revealed the large genomic diversity within this species. This review will explore the links between O. oeni metabolism, genomic diversity and wine sensory attributes.     

Eco-Efficiency Analysis of biotechnological processes

For almost 50 years now, biotechnological production processes have been used for industrial production of amino acids. Market development has been particularly dynamic for the flavor-enhancer glutamate and the animal feed amino acids l-lysine, l-threonine, and l-tryptophan, which are produced by fermentation processes using high-performance strains of Corynebacterium glutamicum and Escherichia coli from sugar sources such as molasses, sucrose, or glucose. But the market for amino acids in synthesis is also becoming increasingly important, with annual growth rates of 5–7%. The use of enzymes and whole cell biocatalysts has proven particularly valuable in production of both proteinogenic and nonproteinogenic l-amino acids, d-amino acids, and enantiomerically pure amino acid derivatives, which are of great interest as building blocks for active ingredients that are applied as pharmaceuticals, cosmetics, and agricultural products. Nutrition and health will continue to be the driving forces for exploiting the potential of microorganisms, and possibly also of suitable plants, to arrive at even more efficient processes for amino acid production.     

l-Malic Acid Fermentation by Mixed Culture of Rhizopus arrhizus and Proteus vulgaris

When Rhizopus arrhizus NRRL 1526 was mix-cultured with Proteus vulgaris AHU 1144, a strain having a high fumarase activity, in a medium containing glucose as a substrate, fumaric acid fermentation was successively converted to l-malic acid fermentation and large amounts of l-malic acid were accumulated as an end product.

As an inoculum of P. vulgaris for this fermentation, cells in the stationary growth phase (48 to 72 hr culture) were much more favorable than those in the exponential growth phase (18 hr culture) and malic acid yields in the former case were as high as about 70 to 75 % based on initial glucose after 3 to 4 days of the mixed culture.     

High-level production of poly (β-<Emphasis Type="SmallCaps">l</Emphasis>-malic acid) with a new isolated <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis> strain

Poly (β-l-malic acid) (PMLA) is a water-soluble polyester with many attractive properties in chemical industry and medicine development. However, the low titer of PMLA in the available producer strains limits further industrialization efforts and restricts its many potential applications. In order to solve this problem, a new strain with the distinguished high productivity of PMLA was isolated from fresh plants samples. It was characterized as the candidate of Aureobasidium pullulans based on the morphology and phylogenetic analyses of the internal transcribed spacer sequences. After the optimization of culture conditions, the highest PMLA concentration (62.27 g l⁻¹) could be achieved in the shake flask scale. In addition, the contribution of the carbon flux to exopolysaccharide (EPS) and PMLA could be regulated by the addition of CaCO₃ in the medium. This high-level fermentation process was further scaled up in the 10 l benchtop fermentor with a high PMLA concentration (57.2 g l⁻¹) and productivity (0.35 g l⁻¹ h⁻¹), which are the highest level in all the literature. Finally, the suitable acid hydrolysis conditions of PMLA were also investigated with regard to the production of l-malic acid, and the kinetics of PMLA acid hydrolysis was modeled to simulate the whole degradation process. The present work paved the road to produce this multifunctional biomaterial (PMLA) at industrial scale and promised one alternative method to produce l-malic acid in the future.     

Improvement of production of l-aspartic acid using immobilized microbial cells

Summary In our laboratory, EAPc-7 a strain having higher aspartase activity was derived from Escherichia coli ATCC 11303. For the improvement of l-aspartic acid productivity using EAPc-7 cells immobilized in -carrageenan, it was necessary to eliminate the fumarase activity which converts fumaric acid to l-malic acid. Several treatments for specifically eliminating fumarase activity from EAPc-7 cells were tested and it was found that when EAPc-7 cells were treated in a culture broth (pH 4.9) containing 50 mM l-aspartic acid at 45° C for 1 h, fumarase activity was almost completely eliminated without inactivation of the aspartase.The treated cells, immobilized in -carrageenan, were used for continuous production of l-aspartic acid from ammonium fumarate. The formation of l-malic acid was negligible and the half-life of the immobilized preparation was 126 days.Productivity of immobilized preparation of treated EAPc-7 cells in l-aspartic acid production was six times of that of the parent cell preparation.     

Production of l (+) lactic acid by Lactobacillus delbrueckii immobilized in functionalized alginate matrices

The role of functionalized alginate gels as immobilized matrices in production of l (+) lactic acid by Lactobacillus delbrueckii was studied. L. delbrueckii cells immobilized in functionalized alginate beads showed enhanced bead stability and selectivity towards production of optically pure l (+) lactic acid in higher yields (1.74Yp/s) compared to natural alginate. Palmitoylated alginate beads revealed 99% enantiomeric selectivity (ee) in production of l (+) lactic acid. Metabolite analysis during fermentation indicated low by-product (acetic acid, propionic acid and ethanol) formation on repeated batch fermentation with functionalized immobilized microbial cells. The scanning electron microscopic studies showed dense entrapped microbial cell biomass in modified immobilized beads compared to native alginate. Thus the methodology has great importance in large-scale production of optically pure lactic acid.     

Schizosaccharomyces malidevorans sp.n., a yeast decomposing L-malic acid

A new yeastSchizosaccharomyces malidevorans sp.n. is described. It resemblesSchizosaccharomyces pombe but differs from it in appearance of the spores and inability to ferment maltose. It decomposesl-malic acid completely in all grape juice and synthetic media tested, but not thed-isomer. During fermentation a copious evolution of hydrogen sulphide occurs.     

Zum Abbau derl-Äpfelsäure durch Milchsäurebakterien

Zusammenfassung Es wird die Aktivität von intaktenL. plantarum-Zellen verschiedener Arten gegenüberl-Äpfelsäure, Oxalessigsäure und Brenztraubensäure getestet. Bei der Dissimilation vonl-Äpfelsäure lassen sich zwei pH-Optima unterscheiden, 2,6–3,0 für eine MDH-Aktivität und 3,6–4,0 für eine Malic-Enzym-Aktivität. Stoffwechselprodukte der Brenztraubensäure-Decarboxylierung sind außer Kohlendioxid Äthylalkohol und Acetoin bzw. Diacetyl.L. plantarum ist außerdem zur Oxydation der Brenztraubensäure befähigt. Ausl-Äpfelsäure entsteht kein Acetoin (Stamm L).

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The dissimilation ofl-malic acid by lactic acid bacteriaIV. The activity of intact cells ofLactobacillus plantarum particularly considering the decarboxylation of pyruvic acid

Summary The decomposition ofl-malic, oxaloacetic and pyruvic acids by intact cells of three strains ofL. plantarum is investigated. The dissimilation ofl-malic acid shows two pH-optima, at pH2.6–3.0 for a malatedehy drogenase activity and at pH 3.6–4.0 for a malic enzyme activity. The decarboxylation of pyruvic acid yields CO₂, ethyl alcohol, acetoin and diacetyl.L. plantarum is also able to oxidize pyruvic acid. The acetoin produced byL. plantarum Strain L does not originate froml-malic acid.

     

Obtaining functional membrane vesicles from Leuconostoc oenos to study l-malate transport mechanisms

Membrane vesicles from the malolactic bacterium Leuconostoc oenos were obtained by a modified version of the procedure of Kaback [Methods Enzymol 22:99–120 (1971)]. Protoplasts were produced at frequencies greater than 95% by a method entailing mutanolysis digestion and osmotic shock. Glycerol or polyethyleneglycol 600 was required as an osmotic stabilizer while the use of sucrose prevented closed vesicle formation during osmotic shock. The membrane vesicles retained their functional properties and accumulated l-malic acid in response to an ATPase-induced proton gradient across the membrane of ATP-loaded vesicles. l-Malate uptake was strongly inhibited by dicyclohexylcarbodiimide, a specific inhibitor of membrane-bound ATPase. These data support the possibility of a pH-dependent transport of l-malate. Vesicles not loaded with ATP were slightly permeable to malic acid with an initial uptake rate (0.5 nmol·l^–1·s^–1) similar to the diffusion rate obtained previously in a L. oenos malate-transport-deficient strain. These results confirm two simultaneous uptake mechanisms in L. oenos, a permease-mediated transport and a passive diffusion for the anionic and the undissociated forms of l-malic acid respectively.     

Biological acidification during grape must fermentation using mixed cultures of <Emphasis Type="Italic">Kluyveromyces thermotolerans</Emphasis> and <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Four mixed culture fermentations of grape must were carried out with Kluyveromyces thermotolerans strain TH941 and Saccharomyces cerevisiae strain SCM952. In the first culture, both yeasts were added together, whereas in the remaining three cultures S. cerevisiae was added 1, 2, and 3 days after the inoculation of K. thermotolerans. The growth and survival of the K. thermotolerans strain and the amount of the produced l-lactic acid depend on the time of inoculation of the S. cerevisiae strain and provided an effective acidification during alcoholic fermentation. The four cultures contained, respectively, at the end of fermentation 0.18, 1.80, 4.28, and 5.13 g l-lactic acid l⁻¹. The grape must with an initial pH of 3.50 was effectively acidified (70% increase in titratable acidity, 0.30 pH unit decrease) by the production of 5.13 g l-lactic acid l⁻¹.     

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.     

Predominance of malolactic fermentation overd-glucose utilization inLactobacillus plantarum andLactobacillus curvatus wine strains

Summary Two selected wine strains of the genusLactobacillus (L. plantarum 197 andL. curvatus 783) were tested for their ability to complete malolactic fermentation (MLF) in a synthetic medium (PBM-broth) supplemented withL-malic acid (7.5–74.6 mM) andD-glucose (5.5–55 mM). The 24 directed fermentation assays, 12 for each bacterial strain, were carried out at 20°C and pH 3.5. MLF was completed (residualL-malic acid 0.2 mM) in eight days in 19 of the 24 fermentation assays, even in the presence of 74.6 mML-malic acid or 55.5 mMD-Glucose utilization was generally simultaneous to MLF but was completed (residual concentrations 0.2 mM) only in 6 of the 24 fermentation assays. These results support the use of these strains in directed MLF assays at the very differentL-malic acid andD-glucose concentrations tested.     

Diffusion in immobilized-cell agar layers: influence of microbial burden and cell morphology on the diffusion coefficients ofl-malic acid and glucose

Summary The diffusivities ofl-malic acid and glucose in an agar membrane entrapping small amounts ofEscherichia coli orRhodospirillum rubrum whole cells were measured using time lag (TL) and steady state (SS) methods. Diffusivities were overestimated by the SS method. For concentrations of immobilizedR. rubrum cells ranging between 10⁴ and 10⁹ organisms cm^–3 agar (20 ng-2 mg dry weight cm^–3 agar), the diffusion coefficient ofl-malic acid, determined by both methods, was related to the logarithm of the membrane cell content by a decreasing linear relationship. The diffusion coefficient of glucose obtained by TL analysis was not significantly affected by the presence in the membrane of 3 ng-0.3 mg dry wt.E. coli cm^–3 agar. However, values arising from the SS method decreased linearly as a function of the amount of immobilized organisms. Membranes containingR. rubrum cells offered higher diffusional resistance tol-malic acid and glucose than those loaded with the same amount ofE. coli cells.