Production of L-Malic Acid by Permeabilized Cells of Commercial Saccharomyces Sp. Strains

Of various yeasts tested in the conversion of fumaric to L-malic acid, Saccharomyces bayanus had the highest activity of fumarase. Cells permeabilized with 0.2% (w/v) CTAB for 5 min gave maximum enzyme activity. Under non-growth conditions, fumarase activity in the permeabilized cells was four times higher (271 U/g) than that of the intact cells (67 U/g). The proposed mathematical model for the batch production of L-malic acid was validated at different initial fumaric acid concentrations. The average conversion of fumaric acid was up to 82% and gave 21, 40, 83 and 175 mM L-malic acid from respectively, 25, 50, 100 and 210 mM: fumaric acid.     

Inducible overexpression of the FUM1 gene in Saccharomyces cerevisiae: localization of fumarase and efficient fumaric acid bioconversion to L-malic acid

Cloning of the Saccharomyces cerevisiae FUM1 gene downstream of the strong GAL10 promoter resulted in inducible overexpression of fumarase in the yeast. The overproducing strain exhibited efficient bioconversion of fumaric acid to L-malic acid with an apparent conversion value of 88% and a conversion rate of 80.4 mmol of fumaric acid/h per g of cell wet weight, both of which are much higher than parameters known for industrial bacterial strains. The only product of the conversion reaction was L-malic acid, which was essentially free of the unwanted by-product succinic acid. The GAL10 promoter situated upstream of a promoterless FUM1 gene led to production and correct distribution of the two fumarase isoenzyme activities between cytosolic and mitochondrial subcellular fractions. The amino-terminal sequence of fumarase contains the mitochondrial signal sequence since (i) 92 of 463 amino acid residues from the amino terminus of fumarase are sufficient to localize fumarase-lacZ fusions to mitochondria and (ii) fumarase and fumarase-lacZ fusions lacking the amino-terminal sequence are localized exclusively in the cytosol. The possibility that both mitochondrial and cytosolic fumarases are derived from the same initial translation product is discussed.     

Inducible overexpression of the FUM1 gene in Saccharomyces cerevisiae: localization of fumarase and efficient fumaric acid bioconversion to L-malic acid.

Cloning of the Saccharomyces cerevisiae FUM1 gene downstream of the strong GAL10 promoter resulted in inducible overexpression of fumarase in the yeast. The overproducing strain exhibited efficient bioconversion of fumaric acid to L-malic acid with an apparent conversion value of 88% and a conversion rate of 80.4 mmol of fumaric acid/h per g of cell wet weight, both of which are much higher than parameters known for industrial bacterial strains. The only product of the conversion reaction was L-malic acid, which was essentially free of the unwanted by-product succinic acid. The GAL10 promoter situated upstream of a promoterless FUM1 gene led to production and correct distribution of the two fumarase isoenzyme activities between cytosolic and mitochondrial subcellular fractions. The amino-terminal sequence of fumarase contains the mitochondrial signal sequence since (i) 92 of 463 amino acid residues from the amino terminus of fumarase are sufficient to localize fumarase-lacZ fusions to mitochondria and (ii) fumarase and fumarase-lacZ fusions lacking the amino-terminal sequence are localized exclusively in the cytosol. The possibility that both mitochondrial and cytosolic fumarases are derived from the same initial translation product is discussed.     

温特曲霉转富马酸为L-苹果酸的初步研究*

从大量霉菌中选育到一株具有较高富马酸酶活性的温特曲霉(Aspergillus wentii) A5-61。在摇瓶培养条件下,32℃ 96小时,产L-苹果酸达10.49g/100ml,对富马酸的转化率达90.80%。利用菌体细胞,进行酶转化试验,结果表明：1.6g湿菌体接入25ml含富马酸10.0%（用NaOH中和至pH7.0）的转化液中,35℃16～24小时,连续转化三次,分别产生L—苹果酸9.61g/100ml、9.73g/100ml、6.93g/100ml。对菌体整体细胞酶学性质的研究表明,其最适反应温度35℃,最适反应pH7.0,Cu2＋对该酶有明显的抑制作用,该酶的Km＝0.154mol/L,Vmax＝0.0571mol/L·h。     

Optimization of L-malic acid production by Aspergillus flavus in a stirred fermentor

Effects of various nutritional and environmental factors on the accumulation of organic acids (mainly L-malic acid) by the filamentous fungus Aspergillus flavus were studied in a 16-L stirred fermentor. Improvement of the molar yield (moles acid produced per moles glucose consumed) of L-malic acid was obtained mainly by increasing the agitation rate (to 350 rpm) and the Fe(z+) ion concentration (to 12 mg/L) and by lowering the nitrogen (to 271 mg/L) and phosphate concentrations (to 1.5 mM) in the medium. These changes resulted in molar yields for L-malic acid and total C(4) acids (L-malic, succinic, and fumaric acids) of 128 and 155%, respectively. The high molar yields obtained (above 100%) are additional evidence for the operation of part of the reductive branch of the tricarboxylic acid cycle in L-malic acid accumulation by A. flavus. The fermentation conditions developed using the above mentioned factors and 9% CaCO(3) in the medium resulted in a high concentration (113 g/L L-malic acid from 120 g/L glucose utilized) and a high overall productivity (0.59 g/L h) of L-malic acid. These changes in acid accumulation coincide with increases in the activities of NAD(+)-malate dehydrogenase, fumarase, and citrate synthase.     

产L-苹果酸重组大肠杆菌的构建

基于产琥珀酸重组大肠杆菌E.coli B0013-1050的琥珀酸合成途径,利用Red同源重组技术结合Xer/dif重组系统敲除富马酸酶基因fumB、fumC,苹果酸酶基因maeB,构建L-苹果酸合成途径,最终得到重组大肠杆菌E.coli2030,该菌株在15 L发酵罐中,产L-苹果酸12.5 g/L,葡萄糖-苹果酸转化率为52.1%,同时对发酵产物中主要杂酸丙酮酸和琥珀酸的生产原因进行了初步的探讨与分析。为进一步提高L-苹果酸的转化率,整合表达来源于黄曲霉的苹果酸脱氢酶基因,构建重组菌E.coli 2040,在15 L发酵罐中产L-苹果酸14 g/L,葡萄糖-苹果酸转化率提高到60.3%。     

A simple plate-assay for the screening of l-malic acid producing microorganisms

A simple plate-assay has been developed to screen microorganisms for L-malic acid production. Acid producing organisms were identified, after microbial colony growth on media containing glucose or fumaric acid as sole carbons sources, by formation of a dark halo of formazan. The halo was observed when the plate was covered with a soft agar overlay containing NAD(+)-malate dehydrogenase, NAD+, phenazine methosulfate (PMS) and 3-[4,5-dimethylthiazol-2-yl]-2,5-diphenyltetrazolium bromide (MTT). The assay developed is simple, specific for L-malic acid and therefore can be used to identify L-malic acid producing filamentous fungi using glucose as carbon source (e.g. Aspergillus strains). The assay is also applicable for screening bacteria with high fumarase activity, able to convert fumaric acid to L-malic acid.     

Characterization of Schizosaccharomyces pombe malate permease by expression in Saccharomyces cerevisiae

In Saccharomyces cerevisiae, L-malic acid transport is not carrier mediated and is limited to slow, simple diffusion of the undissociated acid. Expression in S. cerevisiae of the MAE1 gene, encoding Schizosaccharomyces pombe malate permease, markedly increased L-malic acid uptake in this yeast. In this strain, at pH 3.5 (encountered in industrial processes), L-malic acid uptake involves Mae1p-mediated transport of the monoanionic form of the acid (apparent kinetic parameters: Vmax = 8.7 nmol/mg/min; Km = 1.6 mM) and some simple diffusion of the undissociated L-malic acid (Kd = 0.057 min(-1)). As total L-malic acid transport involved only low levels of diffusion, the Mae1p permease was further characterized in the recombinant strain. L-Malic acid transport was reversible and accumulative and depended on both the transmembrane gradient of the monoanionic acid form and the DeltapH component of the proton motive force. Dicarboxylic acids with stearic occupation closely related to L-malic acid, such as maleic, oxaloacetic, malonic, succinic and fumaric acids, inhibited L-malic acid uptake, suggesting that these compounds use the same carrier. We found that increasing external pH directly inhibited malate uptake, resulting in a lower initial rate of uptake and a lower level of substrate accumulation. In S. pombe, proton movements, as shown by internal acidification, accompanied malate uptake, consistent with the proton/dicarboxylate mechanism previously proposed. Surprisingly, no proton fluxes were observed during Mae1p-mediated L-malic acid import in S. cerevisiae, and intracellular pH remained constant. This suggests that, in S. cerevisiae, either there is a proton counterflow or the Mae1p permease functions differently from a proton/dicarboxylate symport.     

Formation of L-malic acid by yeasts of the genus Dipodascus

The yeast strains of the genus Dipodascus were used for the bioconversion of fumaric acid to L-malic acid. Under nongrowth conditions, the fumarase activity in the intact cells or in the cell-free extract of Dipodascus was 10 times higher than that of Saccharomyces cerevisiae cells. Pretreatment of the Dipodascus with malonate was not necessary because succinate was not detected as a by-product. The fumarase activity in Dipodascus magnusii CCM 8235 was increased approximately 100% when Triton X-305 (0.1%) was added to the reaction mixture.     

L-Malic acid production by polyacrylamide gel entrapped Pichia membranaefaciens

Summary The production of L-malic acid from fumaric acid has been achieved byPichia membraneafaciens cells entrapped in a polyacrylamide gel lattice. The reaction rate was found to be 0.15 mmoles/h/g of immobilized cells. The optimum pH for fumarase activity of immobilized cells was stable after repeated uses it increased after storing the gel pellets at 5°C. A good yield of L-malic acid production (up to 3.77 g/l) was also observed in wine added with Na fumarate.     

黄曲霉发酵薯干粉水解液生产L－苹果酸

经选育和诱变得到一株产苹果酸的黄曲霉菌ＴＨ５００７,通过发酵条件的优化,以薯干粉的水解液为主要原料,发酵５ｄＬ－苹果酸可达到６％左右。在总酸中苹果酸含量平均达７２％以上,杂有机酸主要是柠檬酸,延胡索酸的含量在０．０２％以下。补糖发酵比分批发酵产酸性能更佳。     

Enzymatic synthesis of L-malic acid from fumaric acid using immobilized Escherichia coli cells

Optimal conditions were chosen for cultivation of Escherichia coli 85 cells with a rather high fumarate-hydratase activity on a cheap medium containing no edible raw material. An active biocatalyst for the synthesis of L-malic acid from fumaric acid was obtained based on E. coli 85 cells immobilized in carrageenan. The enzymatic synthesis of L-malic acid from potassium fumarate was kinetically studied and optimized. Some thermodynamic parameters of fumaric acid hydration into malic acid were determined. A technique for assaying the reaction mixture was developed that involved high performance liquid chromatography.     

Continuous propionate production from whey permeate using a novel fibrous bed bioreactor

Continuous production of propionate from whey lactose by Propionibacterium acidipropionici immobilized in a novel fibrous bed bioreactor was studied. In conventional batch propionic acid fermentation, whey permeate without nutrient supplementation was unable to support cell growth and failed to give satisfactory fermentation results for over 7 days. However, with the fibrous bed bioreactor, a high fermentation rate and high conversion were obtained with plain whey permeate and de-lactose whey permeate. About 2% (wt/vol) propionic acid was obtained from a 4.2% lactose feed at a retention time of 35 to 45 h. The propionic acid yield was approximately 46% (wt/vol) from lactose. The optimal pH for fementation was 6.5, and lower fermentation rates and yields were obtained at lower pH values. The optimal temperature was 30 degrees C, but the temperature effect was not dramatic in the range of 25 to 35 degrees C. Addition of yeast extract and trypticase to whey permeate hastened reactor startup and increased the fermentation rate and product yields, but the addition was not required for long-term reactor performance. The improved fermentation results with the immobilized cell bioreactor can be attributed to the high cell density, approximately 50 g/L, attained in the bioreactor, Cells were immobilized by loose attachement to fiber surfaces and entrapment in the void spaces within the fibrous matrix, thus allowing constant renewal of cells. Consequently, this bioreactor was able to operate continuously for 6 months without encountering any clogging, degeneration, or contamination problems. Compared to conventional batch fermentors, the new bioreactor offers many advantages for industrial fermentation, including a more than 10-fold increase in productivity, acceptance of low-nutrient feedstocks such as whey permeate, and resistance to contamination. (c) 1994 John Wiley & Sons, Inc.     

Comparative traits of Lactobacillus brevis, Lact. fructivorans and Leuconostoc oenos immobilized cells for the control of malo-lactic fermentation in wine

Decarboxylation of L-malic to L-lactic acid by heterolactic bacteria and formation of secondary products in table wine were studied using immobilized cells of Lactobacillus brevis, Lact. fructivorans and two strains of Leuconostoc oenos in a continuous flow bioreactor. The conversion ratios were 51.2–53.9%, while the decreases in malic and titratable acidity were equivalent to 62.1–74.7% and 16.4–27.3%, respectively. Upon completion of malo-lactic fermentation, pH increased from 3.15 to 3.28–3.35. The conversion ratio and bioreactor efficiency differed according to the strain tested. Gel beads, prepared with cells immobilized in 2% K-carrageenan in the presence of 5% bentonite silica, contained up to 7–8 × 10¹⁰ cfu/g; the concentration of viable cells was relatively stable over 24–48 h bioreactor operation when Lact. brevis was used and decreased in all other cases. The formation of secondary products affecting wine sensory properties, particularly volatile acids and aromatic compounds, was strain-dependent.     

Design of a low-cost culture medium based in whey permeate for biomass production of enological Lactobacillus plantarum strains

The production of malolactic starter cultures requires the obtention of suitably large biomass at low-cost. In this work it was possible to obtain a good amount of biomass, at laboratory scale, of two enological strains of Lb. plantarum, by formulating a culture medium based on whey permeate (WP), a by-product of the cheese industry usually disposed as waste, when this was supplemented with yeast extract (Y), salts (S) and Tween 80 (T) (WPYST). Bacteria grown in WPYST medium exhibited good tolerance to stress conditions of synthetic wine (pH 3.5, ethanol 13% vol/vol). However, when WPYST was added with 8% vol/vol ethanol, cultures inoculated in synthetic wine, showed a lower viability and capacity to consume L-malic acid than when they were cultured in WPYST without ethanol. Subsequently, strains grown in WPYST were inoculated in sterile wine samples (final stage of alcoholic fermentation) of the red varietals Merlot and Pinot noir, and incubated at laboratory scale. Cultures from WPYST, inoculated in Pinot noir wine, showed a better performance than bacteria grown in MRS broth, and exhibited a consumption of L-malic acid higher than 90%. However, cultures from WPYST or from MRS broth, inoculated in sterile Merlot wine, showed a lower survival. This study allowed the formulation of a low-cost culture medium, based on a by-product of the food industry, which showed to be adequate for the growth of two enological strains of Lb. plantarum, suggesting their potentiality for application in the elaboration of malolactic starter cultures.     

Immobilization of fumarase by entrapment of rat liver mitochondria in polyacrylamide gel using gamma rays

A stable immobilized preparation of fumarase (EC 4.2.1.2) was obtained by entrapment of rat liver mitochondria in acrylamide polymerized by using gamma irradiation (100 kR). The enhanced stability and the efficiency of the entrapped enzyme have shown potential for repeated use for the production of L-malic acid from fumaric acid. The possible formation of succinic acid in the system could be controlled by incorporating malonate along with detergents such as sodium deoxycholate or sodium dodecylsulfate in the reactor system.     

The degradation of malic acid by high density cell suspensions of Leuconostoc oenos

Washed cell suspensions of Leuconostoc oenos catalysed the degradation of L-malic acid to L-lactic acid. Cell suspensions of 10₁₀ cfu ml_-1 degraded 90–95% of the malic acid in a buffer assay system and in wine within 30 min. A reaction time of 6 h was needed to obtain the same extent of degradation with suspensions of 10₉ cfu ml_-1. With a reaction period of 6 h and an initial malic acid concentration of 3 g 1_-1, reaction variables of pH 2.5-4.0, temperature 10–30°C, ethanol up to 15%, and L-lactic acid up to 4 g 1_-1 did not decrease the degradation of malic acid to below 90–95%. Total SO₂ at 100 mg 1_-1 decreased the degradation of malic acid to 80%. The degradation (%) of malic acid was decreased when the concentration of malic acid was decreased below 2 g 1_-1. The results indicate the prospect of using high densities of Leuc. oenos cells in membrane bioreactor systems for the rapid, continuous, deacidification of wine.     

Metabolic engineering of Rhizopus oryzae: Effects of overexpressing pyc and pepc genes on fumaric acid biosynthesis from glucose

Fumaric acid, a dicarboxylic acid used as a food acidulant and in manufacturing synthetic resins, can be produced from glucose in fermentation by Rhizopus oryzae. However, the fumaric acid yield is limited by the co-production of ethanol and other byproducts. To increase fumaric acid production, overexpressing endogenous pyruvate carboxylase (PYC) and exogenous phosphoenolpyruvate carboxylase (PEPC) to increase the carbon flux toward oxaloacetate were investigated. Compared to the wild type, the PYC activity in the pyc transformants increased 56%-83%, whereas pepc transformants exhibited significant PEPC activity (3-6mU/mg) that was absent in the wild type. Fumaric acid production by the pepc transformant increased 26% (0.78g/g glucose vs. 0.62g/g for the wild type). However, the pyc transformants grew poorly and had low fumaric acid yields (<0.05g/g glucose) due to the formation of large cell pellets that limited oxygen supply and resulted in the accumulation of ethanol with a high yield of 0.13-0.36g/g glucose. This study is the first attempt to use metabolic engineering to modify the fumaric acid biosynthesis pathway to increase fumaric acid production in R. oryzae.     

A mathematical model of the link between growth and L-malic acid consumption for five strains of Oenococcus oeni

In winemaking, after the alcoholic fermentation of red wines and some white wines, L-malic acid must be converted into L-lactic acid to reduce the acidity. This malolactic fermentation (MLF) is usually carried out by the lactic acid bacteria Oenococcus oeni. Depending on the level of process control, selected O. oeni is inoculated or the natural microbiota of the cellar is used. This study considers the link between growth and MLF for five strains of O. oeni species. The kinetics of growth and L-malic acid consumption were followed in modified MRS medium (20 °C, pH 3.5, and 10 % ethanol) in anaerobic conditions. A large variability was found among the strains for both their growth and their consumption of L-malic acid. There was no direct link between biomass productivities and consumption of L-malic acid among strains but there was a link of proportionality between the specific growth of a strain and its specific consumption of L-malic acid. Experiments with and without malic acid clearly demonstrated that malic acid consumption improved the growth of strains. This link was quantified by a mathematical model comparing the intrinsic malic acid consumption capacity of the strains.     

Influence of various amounts of fumaric acid on performance and parameters of the acid-base balance of growing bulls fed with grass or maize silage

The aim of the present study was to determine the effects of the potential methane reducer fumaric acid on the fattening performance and acid-base balance of growing bulls fed two different silage types as roughage (maize and grass silage). A total of 62 fattening bulls (German Holstein breed, initial body weight: 266 +/- 42 kg), randomly assigned to eight feeding groups, received four levels of fumaric acid (0, 100, 200 or 300 g/d) at each silage type. The daily feed and water intake and the live weight were measured over the whole testing period of 280 days. In blood samples, blood cells and blood gases as a parameter of acid-base status were analysed. Feed and faeces were collected to determine the apparent nutrient digestibility. Five animals from each group fed maize or grass silage, supplemented with 0 g or 300 g fumaric acid, were slaughtered at 580 kg body weight. After slaughter, rumen fluid pH was measured and dressing percentage was calculated. Neither the total feed intake (8.81 +/- 0.07 kg/d) nor the daily weight gain (1277 +/- 24 g/d) was influenced significantly by treatments. Fumaric acid supplementation did not influence the erythrocyte count or the blood gas concentration. The silage type significantly influenced the apparent digestibility of the whole diet. The dressing percentage was slightly higher (p < 0.1) after fumaric acid supplementation. No signs of an incompatibility to fumaric acid on the animals were observed over the whole experimental period. However, it seems to be necessary to conduct more long-term studies with different silage types and addition of organic acids combined with direct measurements of methane.