Production of mannitol by a novel strain of Candida magnoliae

A novel microorganism was isolated which is able to produce mannitol when grown in the presence of fructose and glucose as carbon sources. In flask culture in a medium containing 150 g fructose l^–1, it yielded 67 g mannitol l^–1 after 168 h. In fed-batch culture with 3–12% (w/v) fructose, production reached a maximum of 209 g mannitol l^–1 after 200 h, corresponding to an 83% yield and a 1.03 g l^–1 h^–1 productivity. The isolated strain was identified as Candida magnoliae based on identical sequences in the D1/D2 domain of its 26S rDNA and a similar carbon source utilization pattern with C. magnoliae reference strains.     

High-level production of D-mannitol with membrane cell-recycle bioreactor

Ten heterofermentative lactic acid bacteria were compared in their ability to produce D-mannitol from D-fructose in a resting state. The best strain, Leuconostoc mesenteroides ATCC-9135, was examined in high cell density membrane cell-recycle cultures. High volumetric mannitol productivity (26.2 g l⁻¹ h⁻¹) and mannitol yield (97 mol%) were achieved. Using the same initial biomass, a stable high-level production of mannitol was maintained for 14 successive bioconversion batches. Applying response surface methodology, the temperature and pH were studied with respect to specific mannitol productivity and yield. Moreover, increasing the initial fructose concentration from 100 to 120 and 140 g l⁻¹ resulted in decreased productivities due to both substrate and end-product inhibition of the key enzyme, mannitol dehydrogenase (MDH). Nitrogen gas flushing of the bioconversion media was unnecessary, since it did not change the essential process parameters. Journal of Industrial Microbiology & Biotechnology (2002) 29, 44–49 doi:10.1038/sj.jim.7000262 Received 12 November 2001/ Accepted in revised form 30 March 2002     

Ca<Superscript>2+ </Superscript>and Cu<Superscript>2+ </Superscript>supplementation increases mannitol production by <Emphasis Type="Italic">Candida magnoliae</Emphasis>

Supplementation with CaCl₂·2H₂O (50 mg l⁻¹) or CuSO₄·5H₂O (10 mg l⁻¹) improved mannitol production by Candida magnoliae by 14.5 and 18.6% (25 and 32 g/L), respectively. When used in combination, they acted synergistically: Ca²⁺ decreased the intracellular concentration of mannitol 30%, whereas Cu²⁺ increased the intracellular activity of mannitol dehydrogenase 1.6-times more than control. Ca²⁺ probably works by altering the permeability of cells to mannitol, whereas, Cu²⁺ increases the activity of an enzyme responsible for mannitol biosynthesis.     

Effects of culture conditions on isolated microspore response of barley cultivar Igri

Pretreatment of anthers in mannitol prior to isolation of microspores by glass rod homogenization was effective for in vitro induction of embryogenesis in barley cv. Igri. A procedure for separation of viable microspores using centrifugation on 20% maltose was developed. The concentration of microspores was important and greatly increased the number of developing structures. Initial culture of microspores on FHG medium containing 62 g l^-1 maltose, 4.4 M (1 mg l^-1) BA and 200 g l^-1 Ficoll-400 resulted in high frequencies of plant regeneration. Albino plant frequency was correlated to length of time in culture. Stock plant condition appeared to be a major factor influencing induction frequency. From 868 to 1738 green plants per 100 anthers were produced. The number of calli and embryos obtained and the number of green plantlets regenerated were improved by increasing the Ficoll concentration from 100 g l^-1 to 400 g l^-1 during the culture period compared to continuous culture on FHG Ficoll 200 g l^-1.Abbreviations BA benzyladenine     

In vitro corm production of Gladiolus dalenii and G. tristis

The ability of the summer flowering Gladiolus dalenii Van Geel and the winter flowering G. tristis L. to form corms in vitro was investigated. G. dalenii spontaneously formed corms on a shoot induction medium consisting of the basal medium of Murashige & Skoog (1962) with up to 2.0 mg l^-1 benzyladenine (BA), 3% sucrose and solidified with 2 g l^-1 Gelrite^®. The effect of different BA and sucrose concentrations as well as different temperatures on in vitro corm production of G. tristis was further investigated. The best production of shoots per explant was achieved on a medium containing 0.5 to 1.0 mg l^-1 BA, sucrose concentrations of 6 to 9% and cultured at 15°C. The best corm production was achieved at the same temperature and with the same medium with the exception that BA was omitted from the medium. To test the effect of the osmotic potential on the formation of shoots and corms, sucrose was substituted by mannitol at various concentrations. Sucrose proved to be essential for both shoot and corm production and the use of mannitol had no beneficial effect.     

<Emphasis Type="Italic">Gluconobacter oxydans</Emphasis> NAD-dependent, <Emphasis Type="SmallCaps">D</Emphasis>-fructose reducing,polyol dehydrogenases activity: screening,medium optimisation and application for enzymatic polyol production

Gluconobacter oxydans LMG 1489 was selected as the best strain for NAD(P)-dependent polyol dehydrogenase production. The highest enzyme activities were obtained when this strain was cultivated on a medium consisting of 30 g glycerol l^–1, 7.2 g peptone l–1 and 1.8 g yeast extract l^–1. Two D-fructose reducing, NAD-dependent intracellular enzymes were present in the G. oxydans cell-free extract: sorbitol dehydrogenase, and mannitol dehydrogenase. Substrate reduction occurred optimally at a low pH (pH 6), while the optimum for substrate oxidation was situated at alkaline pHs (pH 9.5–10.5). The mannitol dehydrogenase was more thermostable than the sorbitol dehydrogenase. The cell-free extract could be used to produce D-mannitol and D-sorbitol enzymatically from D-fructose. Efficient coenzyme regeneration was accomplished by formate dehydrogenase-mediated oxidation of formate into CO₂.     

Ethanol production from seaweed extract

Extracts from Laminaria hyperborea could possibly be fermented to ethanol commercially. In particular, seaweed harvested in the autumn contains high levels of easily extractable laminaran and mannitol. Four microorganisms were tested to carry out this fermentation, one bacterium and three yeasts. Only Pichia angophorae was able to utilise both laminaran and mannitol for ethanol production, and its substrate preferences were investigated in batch and continuous cultures. Laminaran and mannitol were consumed simultaneously, but with different relative rates. In batch fermentations, mannitol was the preferred substrate. Its share of the total laminaran and mannitol consumption rate increased with oxygen transfer rate (OTR) and pH. In continuous fermentations, laminaran was the preferred substrate at low OTR, whereas at higher OTR, laminaran and mannitol were consumed at similar rates. Optimisation of ethanol yield required a low OTR, and the best yield of 0.43 g ethanol (g substrate)⁻¹ was achieved in batch culture at pH 4.5 and 5.8 mmol O₂ l⁻¹ h⁻¹. However, industrial production of ethanol from seaweed would require an optimisation of the extraction process to yield a higher ethanol concentration. Journal of Industrial Microbiology & Biotechnology (2000) 25, 249–254. Received 25 February 2000/ Accepted in revised form 05 August 2000     

Age and Physiological Condition of Donor Plants Affect in vitro Morphogenesis in Leaf Explants of Passiflora edulis f. flavicarpa

The regeneration potential of D.alata L. germplasm preserved in vitro was compared with the micropropagation of fresh material. Nodal cuttings were conserved for 9 months in different treatments based on D-571 culture medium modified, using several variable components (mannitol, benzylaminopurine and activated charcoal). Regeneration at 8 weeks, assessed by means of percentage of explant regenerating and the multiplication at 5 weeks through the shoot length and de novo bud count formation per explant were determined. The results showed high rates (100 and 98%) of explant regeneration and micropropagation from in vitro material maintained in D-571 medium with 1.5% of mannitol + 0.1 or 1 mg l^–1 of benzylaminopurine + 2 g l^–1 of activated charcoal, respectively.     

Effects of pH and corn steep liquor variability on mannitol production by Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius NRRL B-3693 produced mannitol, lactic acid, and acetic acid when grown on fructose at 37°C. The optimal pH for mannitol production from fructose by the heterofermentative lactic acid bacterium (LAB) in pH-controlled fermentation was at pH 5.0. It produced 160.7 ± 1.1 g mannitol in 40 h with a volumetric productivity of 4.0 g l⁻¹ h⁻¹ in a simplified medium containing 250 g fructose, 50 g corn steep liquor (CSL), and 33 mg MnSO₄ per liter. However, the mannitol production by the LAB was severely affected by the variability of CSL. The supplementation of CSL with soy peptone (5 g/l), tryptophan (50 mg/l), tryptophan (50 mg/l) plus tyrosine (50 mg/l), or commercial protease preparation (2 ml/100 g of CSL) enhanced the performance of the inferior CSL and thus helped to overcome the nutrient limitations.     

Plant regeneration from protoplasts of Gentiana by embedding protoplasts in gellan gum

A protoplast-to-plant system was developed in Gentiana using a gellan gum-embedding culture. Viable protoplasts could be routinely isolated from in vitro-grown plantlets, and they were embedded in 0.2% gellan gum-solidified B5 medium containing 2 mg l^-1 NAA, 0.1 mg l^-1 TDZ, 0.1 M sucrose and 0.4 M mannitol. Weekly addition of fresh liquid medium was essential for preventing cell browning. Colony growth was promoted by lowering mannitol concentration of the culture media after one month, and visible colonies were produced after 2 months of culture. Shoot regeneration from protoplast-derived calluses was stimulated by 1 to 10 mg l^-1 TDZ in combination with 0.1 mg l^-1 NAA. Protoplast-derived plants were recovered following rooting of the shoots in plant growth regulator-free medium and they were successfully transferred to soil.Abbreviations BA benzylaminopurine - FDA fluorescein diacetate - FW fresh weight - MES 2-N-morpholinoethane sulfonic acid - NAA -naphthaleneacetic acid - TDZ N-1,2,3-thiadiazol-5-yl-N-phenylurea (also called thidiazuron)     

Expression of glf Z.m. increases D-mannitol formation in whole cell biotransformation with resting cells of Corynebacterium glutamicum

A recombinant oxidation/reduction cycle for the conversion of D-fructose to D-mannitol was established in resting cells of Corynebacterium glutamicum. Whole cells were used as biocatalysts, supplied with 250 mM sodium formate and 500 mM D-fructose at pH 6.5. The mannitol dehydrogenase gene (mdh) from Leuconostoc pseudomesenteroides was overexpressed in strain C. glutamicum ATCC 13032. To ensure sufficient cofactor [nicotinamide adenine dinucleotide (reduced form, NADH)] supply, the fdh gene encoding formate dehydrogenase from Mycobacterium vaccae N10 was coexpressed. The recombinant C. glutamicum cells produced D-mannitol at a constant production rate of 0.22 g (g cdw)⁻¹ h⁻¹. Expression of the glucose/fructose facilitator gene glf from Zymomonas mobilis in C. glutamicum led to a 5.5-fold increased productivity of 1.25 g (g cdw)⁻¹ h⁻¹, yielding 87 g l⁻¹ D-mannitol from 93.7 g l⁻¹ D-fructose. Determination of intracellular NAD(H) concentration during biotransformation showed a constant NAD(H) pool size and a NADH/NAD⁺ ratio of approximately 1. In repetitive fed-batch biotransformation, 285 g l⁻¹ D-mannitol over a time period of 96 h with an average productivity of 1.0 g (g cdw)⁻¹ h⁻¹ was formed. These results show that C. glutamicum is a favorable biocatalyst for long-term biotransformation with resting cells. Dedicated to Prof. Hermann Sahm on the occasion of his 65th birthday.     

Molecular breeding of a Brevibacterium lactofermentum l-phenylalanine producer using a cloned prephenate dehydratase gene

Summary The prephenate dehydratase gene was cloned from a mutant of Brevibacterium lactofermentum, AJ11957 that produced enzyme free from feedback inhibition. The recombinant plasmids pPH11 and pPH14 complemented a phenylalanine auxotroph of B. lactofermentum, A-15, provided the transformant with the desensitized enzyme and caused an increased level of the enzyme compared to that of a wild strain. Plasmid pPH14 was introduced into l-phenylalanine producers genetically induced from B. lactofermentum; MF358 and FP-1 excreting l-tyrosine and anthranilate, respectively, as by-products. Both transformants predominantly accumulated l-phenylalanine at the expense of by-product formation. Co-existence of pPH14 and pTAR16, a recombinant plasmid expressing desensitized 3-deoxy-d-arabino-hepturosonate-7-phosphate synthase had a marked effect on further improvement in l-phenylalanine productivity, accompanied by an increase in the corresponding enzyme activity. The parent, MF358, accumulating 5.5 g/l l-phenylalanine, 6.8 g/l l-tyrosine and 0.3 g/l anthranilate turned into a potent l-phenylalanine producer producing 18.2 g/l l-phenylalanine and 1.0 g/l l-tyrosine by-product. Offprint requests to: Hisao Ito     

Arabitol accumulation in Geotrichum candidum

Culture conditions which lead to the intracellular accumulation of arabitol and mannitol in Geotrichum candidum were investigated. The accumulation of arabitol was dependent on the concentrations of metabolizable hexoses, the non-metabolizable disaccharide sucrose, NaCl and KCl in the growth medium. In media containing 2% (w/v) glucose, fructose or l-sorbose cultures contained only mannitol after 48 h or 72 h growth. In media containing 10% (w/v) to 30% (w/v) glucose, or 25% (w/v) fructose or l-sorbose there was an increase in the total concentration of intracellular polyol due to the accumulation of arabitol. This pentitol was also found to accumulate intracellularly when the organism was grown in medium containing 34% (w/v) sucrose, 0.7 M NaCl or 0.7 M KCl in addition to 2% (w/v) glucose. Under the conditions tested no change in the accumulation of mannitol or ethanol-soluble carbohydrate, believed to be primarily composed of trehalose, was evident.Intracellular polyol was released during incubation of arthrospores obtained from media containing 25% or 10% glucose, in distilled water at 25° C, but no polyol was released under these conditions from arthrospores obtained from growth in 2% glucose medium.     

Production of ethanol from mannitol by Zymobacter palmae

Extracts from brown seaweeds could possibly be fermented to ethanol, particularly seaweeds harvested in the autumn, which contain high levels of easily extractable laminaran and mannitol. Few microorganisms are able to utilise mannitol as a substrate for ethanol production and Zymobacter palmae was tested for this purpose. Bacterial growth as well as ethanol yield depended on the amount of oxygen present. Strictly anaerobic growth on mannitol was not observed. At excessive aeration, a change in the fermentation pattern was observed with high production of acetate and propionate. Under oxygen-limiting conditions, the bacteria grew and produced ethanol in a synthetic mannitol medium with a yield of 0.38 g ethanol (g mannitol)⁻¹. Z. palmae was also successfully applied for fermentation of mannitol from Laminaria hyperborea extracts. Journal of Industrial Microbiology & Biotechnology (2000) 24, 51–57. Received 27 June 1999/ Accepted in revised form 23 September 1999     

l-Carnitine enhances resistance to oxidative stress by reducing DNA damage in Ataxia telangiectasia cells

In this study, the modulating effect of l-carnitine on tert-butyl-hydroperoxide-induced DNA damage was compared with that of mannitol, a well known scavenger of hydroxyl radicals, both in normal and Ataxia telangiectasia mutated (ATM)-deficient lymphoblastoid cell lines established from A. telangiectasia (A-T) patients. The alkaline version of the comet assay was employed to measure the frequency of single-strand breaks (SSBs) and alkali-labile sites induced by t-butyl-OOH immediately after treatment and at different recovery times in normal and A-T cell lines, with and without pre-treatment with l-carnitine. In addition, both the yield of induced chromosomal damage and the effect on cell proliferation were evaluated. Our results show that pre-treatment of cells with l-carnitine produced an enhancement of the rate and extent of DNA repair in A-T cell lines at early recovery time; furthermore, in samples pre-treated with l-carnitine a reduction of all types of chromosomal aberration was observed, both in A-T and in wild-type cell lines. The reducing effect of l-carnitine pre-treatment on oxidative DNA damage was more prominent than that of pre-treatment with mannitol. In conclusion, we demonstrated a protective effect of l-carnitine on oxidative stress-induced DNA damage in A-T cells, suggesting its possible role in future pharmacological applications in A-T therapy.     

Transformation of Nε-CBZ-l-lysine to CBZ-l-oxylysine using l-amino acid oxidase from Providencia alcalifaciens and l-2-hydroxy-isocaproate dehydrogenase from Lactobacillus confusus

Summary Biotransformations were developed to oxidize N-carbobenzoxy(CBZ)-l-lysine and to reduce the product keto acid to l-CBZ-oxylysine. Lysyl oxidase (l-lysine: O₂ oxidoreductase, EC 1.4.3.14) from Trichoderma viride was relatively specific for l-lysine and had very low activity with N-substituted derivatives. l-Amino acid oxidase (l-amino acid: O₂ oxidoreductase [deaminating], EC 1.4.3.2) from Crotalus adamanteus venom had low activity with l-lysine but high activity with N-formyl-, t-butyoxycarbonyl(BOC)-, acetyl-, trifluoroacetyl-, or CBZ-l-lysine. l-2-Hydroxyisocaproate dehydrogenase (EC 1.1.1.-) from Lactobacillus confusus catalyzed the reduction by NADH of the keto acids from N-acetyl-, trifluoroacetyl-, formyl- and CBZ-l-lysine but was inactive with the products from oxidation of l-lysine, l-lysine methyl ester, l-lysine ethyl ester or N-t-BOC-l-lysine. Providencia alcalifaciens (SC9036, ATCC 13159) was a good microbial substitute for the snake venom oxidase and also provided catalase (H₂O₂:H₂O₂ oxidoreductase EC 1.11.1.6). N-CBZ-l-Lysine was converted to CBZ-l-oxylysine in 95% yield with 98.5% optical purity by oxidation using P. alcalifaciens cells followed by reduction of the keto acid using l-2-hydroxyisocaproate dehydrogenase. NADH was regenerated using formate dehydrogenase (formate: NAD oxidoreductase, EC 1.2.1.2) from Candida boidinii. The Providencia oxidase was localized in the particulate fraction and catalase activity was predominantly in the soluble fraction of sonicated cells. The pH optima and kinetic constants were determined for the reactions. Correspondence to: R. L. Hanson     

Characterization of an inducible mannitol-binding protein fromPseudomonas aeruginosa

Pseudomonas aeruginosa strain PAO formed a mannitol-binding protein that was coinducible with mannitol uptake activity. One species of mannitol-binding protein was isolated from disrupted cell suspensions and the protein also was released from mannitol-grown cells by osmotic shock treatment. The mannitol-binding protein )molecular weight 37,000) was purified 49-fold and resolved from the enzyme mannitol dehydrogenase (molecular weight 85,000), which did not exhibit mannitol-binding activity. Mannitol-binding protein had an isoelectric point (pI) of 8.3 and an apparent dissociation constant (K _D ) of 2.3 M for mannitol. Mannitol binding was unaffected by glucose and glycerol in competitive inhibition studies, although mannose, fructose, and sorbitol caused 5 to 20% inhibition of binding at concentrations equimolar with mannitol.     

Hyper-production of l-trytophan via fermentation with crystallization

A stable and fast l-tryptophan producer, AGX1757, was isolated from Escherichia coli W3110 trpAE1 trpR tnaA, which carried pSC101-trpI15·14. Cells of AGX1757 did not lose the composite plasmid during fermentation. Whenever a fed-batch culture of AGX1757 attained an l-tryptophan concentration of about 30 g/l, indole began to appear in the broth. The emergence of indole was caused by inhibition of tryptophan synthase due to accumulated l-tryptophan. Hence, the production rate of l-tryptophan sharply decreased. A higher solubility of l-tryptophan in the supernatant of culture broth (about 32 g/l) than that in the initial medium (about 22 g/l) was attributed to some unknown interaction between l-tryptophan and certain macromolecular material(s) coming from the bacterial cells. An addition of non-ionic detergents into the supernatant was effective for decreasing the solubility of l-tryptophan, hence causing crystallization of l-tryptophan. Pluronic L-61 was supplied from outside to an extent of 0.5% in terms of wt% concentration at around 45 h of fermentation when the l-tryptophan accumulated reached about 25 g/l. This addition actually caused crystallization of l-tryptophan and, as a result, the inhibitory effect of tryptophan synthase by l-tryptophan accumulated in the broth could be alleviated. Thus far, further fermentation became possible. l-Tryptophan of more than 50 g/l was finally produced by feeding solutions of both glucose and anthranilic acid. Correspondence to: H. Tsunekawa     

Growth yields and the efficiency of oxidative phosphorylation of Paracoccus denitrificans during two- (carbon) substrate-limited growth

Paracoccus denitrificans was grown aerobically during two-(carbon)substrate-limitation on mannitol and methanol in chemostat cultures. Theoretical growth parameters were calculated based on the presence of 2 or 3 sites in the electron-transport chain of Paracoccus denitrificans. Experimental growth parameters determined during two-(carbon)substrate growth were conform to the presence of 3 sites of oxidative phosphorylation, while cells grown only on mannitol possessed 2 sites. The maximum growth yield on adenosine triphosphate (ATP), corrected for maintenance requirements, determined in chemostat experiments in which the methanol concentration is less than 2.11 times the mannitol concentration was 8.6 g of biomass. When the methanol concentration was more than 2.11 times the mannitol concentration the maximum growth yield on adenosine triphosphate decreased due to the more energy consuming process of CO₂-assimilation. Cells use methanol only as energy source to increase the amount of mannitol used for assimilation purposes. When the methanol concentration in chemostat experiments was more than 2.11 times the mannitol concentration, all mannitol was used for assimilation and excess energy derived from methanol was used for CO₂-assimilation via the ribulose-bisphosphate cycle. The synthesis of ribulosebisphosphate carboxylase was repressed when the methanol concentration in chemostat experiments was less than 2.11 times the mannitol concentration or when Paracoccus denitrificans was grown in batch culture on both methanol and mannitol. When in chemostat experiments the methanol concentration was more than 2.11 times the mannitol concentration ribulose-bisphosphate carboxylase activity could be demonstrated and CO₂-assimilation will occur. It is proposed that energy produced in excess activates or derepresses the synthesis of the necessary enzymes of the ribulose-bisphosphate cycle in Paracoccus denitrificans. Consequently growth on any substrate will be carbonas well as energy-limited. When methanol is present in the nutrient cells of Paracoccus denitrificans synthesize a CO-binding type of cytochrome c, which is essential for methanol oxidase activity.The reason for the increase in efficiency of oxidative phosphorylation from 2 to 3 sites is most probably the occurrence of this CO-binding type of cytochrome c in which presence electrons preferentially pass through the a-type cytochrome region of the electron-transport chain.Non Standard Abbreviations X prosthetic group of methanol dehydrogenase - q _substrate specific rate of consumption of substrate (mol/g biomass. h.) - Y _substrate, Y _substrate ^MAX are respectively the growth yield and the maximum growth yield corrected for maintenance requirements (g biomass/mol) - m _substrate maintenance requirement (mol substrate/g biomass) - specific growth rate (h^-1) - M [methanol]/[mannitol] ratio in the nutrient - N part of mannitol that is assimilated when M=o - R _m amount of methanol-equivalents that has the same energy content as 1 mannitol-equivalent - P/O _N , P/O _F , P/O _X is the amount of ATP produced during electron-transport of two electrons from respectively NADH+H⁺, FADH₂ and XH₂ to oxygen