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Applied Microbiology and Biotechnology (v.49, #1)

Biotechnological production of flavours and fragrances by U. Krings; R. G. Berger (pp. 1-8).

The biotechnological generation of natural aroma compounds is rapidly expanding. Aroma chemicals, such as vanillin, benzaldehyde (bitter almond, cherry) and 4-(R)-decanolide (fruity–fatty) are marketed on a scale of several thousand tons per year. Their possible production by single-step biotransformations, bioconversions and de novo synthesis using microorganisms, plant cells or isolated enzymes is shown. The perspectives of bioprocesses for the oxifunctionalisation of lower terpenes by genetically modified organisms and economic aspects are discussed.

Enhanced l-lysine production in threonine-limited continuous culture of Corynebacterium glutamicum by using gluconate as a secondary carbon source with glucose by H.-W. Lee; J.-G. Pan; J.-M. Lebeault (pp. 9-15).

In order to improve the production rate of l-lysine, a mutant of Corynebacterium glutamicum ATCC 21513 was cultivated in complex medium with gluconate and glucose as mixed carbon sources. In a batch culture, this strain was found to consume gluconate and glucose simultaneously. In continuous culture at dilution rates ranging from 0.2 h⁻¹ to 0.25 h⁻¹, the specific l-lysine production rate increased to 0.12 g g⁻¹ h⁻¹ from 0.1 g g⁻¹ h⁻¹, the rate obtained with glucose as the sole carbon source [Lee et al. (1995) Appl Microbiol Biotechnol 43:1019–1027]. It is notable that l-lysine production was observed at higher dilution rates than 0.4 h⁻¹, which was not observed when glucose was the sole carbon source. The positive effect of gluconate was confirmed in the shift of the carbon source from glucose to gluconate. The metabolic transition, which has been characterized by decreased l-lysine production at the higher glucose uptake rates, was not observed when gluconate was added. These results demonstrate that the utilization of gluconate as a secondary carbon source improves the maximum l-lysine production rate in the threonine-limited continuous culture, probably by relieving the limiting factors in the lysine synthesis rate such as NADPH supply and/or phosphoenolpyruvate availability.

Comparative extraction procedures for a galactose-specific lectin involved in flocculation of Kluyveromyces lactis strains by M. El-Behhari; J. Ngondi Ekomé; B. Pucci; J. Coulon; R. Bonaly (pp. 16-23).

The extraction of a lectinic factor involved in yeast flocculation, from two Kluyveromyces lactis strains (a flocculent K. lactis 5c and a non-flocculent K. lactis 5a strain) was performed using EDTA and two surfactants, Hecameg and HTAC. The properties of the different extracts were tested by haemagglutination and reflocculation of deflocculated K. lactis 5c cells. Hecameg gave the highest yields of active lectinic extract but the extraction with EDTA seemed more specific. HTAC extracts showed a very low activity. The possibilities of extraction of the agglutinating factor, either by an ion chelator or by surfactants, suggest that this factor may be anchored in the cell envelope, i.e. the cell wall and the membrane, by different mechanisms. All the assays revealed a galactose-specific lectinic activity was present that in the flocculent as well as in the non-flocculent strain. This indicates that the absence of flocculation with K. lactis 5a is mainly due to a defect in the ligands of the lectin rather than to a loss of the lectinic factor itself.

Improved L-lysine yield with Corynebacterium glutamicum: use of dapA resulting in increased flux combined with growth limitation by L. Eggeling; S. Oberle; H. Sahm (pp. 24-30).

The amino acid L-lysine is produced on a large scale using mutants of Corynebacterium glutamicum. However, as yet recombinant DNA techniques have not succeed in improving strains selected for decades by classic mutagenesis for high productivity. We here report that seven biosynthetic enzymes were assayed and oversynthesis of the dihydrodipicolinate synthase resulted in an increase of lysine accumulation from 220 mM to 270 mM. The synthase, encoded by dapA, is located at the branch point of metabolite distribution to either lysine or threonine and competes with homoserine dehydrogenase for the common substrate aspartate semialdehyde. When graded dapA expression was used, as well as quantification of enzyme activities, intracellular metabolite concentrations and flux rates, a global response of the carbon metabolism to the synthase activity became apparent: the increased flux towards lysine was accompanied by a decreased flux towards threonine. This resulted in a decreased growth rate, but increased intracellular levels of pyruvate-derived valine and alanine. Therefore, modulating the flux at the branch point results in an intrinsically introduced growth limitation with increased intracellular precursor supply for lysine synthesis. This does not only achieve an increase in lysine yield but this example of an intracellularly introduced growth limitation is proposed as a new general means of increasing flux for industrial metabolite overproduction.

Purification and characterization of recombinant spider silk expressed in Escherichia coli by S. Arcidiacono; C. Mello; D. Kaplan; S. Cheley; H. Bayley (pp. 31-38).

A partial cDNA clone, from the 3′ end of the dragline silk gene was isolated from Nephila clavipes major ampullate glands. This clone contains a 1.7-kb insert, consisting of a repetitive coding region of 1.4-kb and a 0.3-kb nonrepetitive coding region; 1.5-kb of the 1.7-kb fragment was cloned into Escherichia coli and a␣43-kDa recombinant silk protein was expressed. Characterization of the purified protein by Western blot, amino acid composition analysis, and matrix-assisted laser desorption ionization/time-of-flight mass spectrometry confirms it to be spider dragline silk.

Construction of a low-serine-type-carboxypeptidase-producing mutant of Aspergillus oryzae by the expression of antisense RNA and its use as a host for heterologous protein secretion by X. F. Zheng; Y. Kobayashi; M. Takeuchi (pp. 39-44).

Using an antisense control strategy, we isolated an Aspergillus oryzae mutant that produced low levels of carboxypeptidases (CPases). The mutant TF_C-1 expressed the antisense RNA of the structural gene of CPase O and showed about 30% of the CPase activity in the parent strain. Gel filtration analysis indicated that this mutant decreased the CPase activities not only of CPase O but also of CPase O-1 and O-2. This result indicated that the antisense RNA was able to control the expression of the CPase genes as a group. Using the mutant as a heterologous protein expression host that produced the low levels of CPases, a stable and higher level of lysozyme expression could be obtained compared with the wild-type. In vitro proteolytic degradation assay also demonstrated that human lysozyme was degraded by purified CPase O.

Stable production of human gastric lipase by chromosomal integration in the fission yeast Schizosaccharomyces pombe by G. R. Smerdon; E. F. Walton; S. J. Aves (pp. 45-50).

Strains of the fission yeast Schizosaccharomyces pombe have been constructed containing single or multiple chromosomally integrated copies of an expression cassette for production of human gastric lipase. Integrant strains of S. pombe secrete active lipase and are stable for lipase production over a minimum of 50 generations in non-selective media. Lipase activity levels for integrant strains containing up to three tandem copies of the expression cassette are strongly correlated with copy number of the cassette in both complete and minimal media. Lipase activity is higher in complete medium than in minimal medium. Strains carrying three chromosomally integrated expression cassette copies can be grown without selection in complete medium and are capable of significantly higher lipase activities than strains containing the expression cassette on a multicopy plasmid.

Expression and secretion of functional miniantibodies McPC603scFvDhlx in cell-wall-less L-form strains of Proteus mirabilis and Escherichia coli : A comparison of the synthesis capacities of L-form strains with an E. coli producer strain by M. J. Kujau; C. Hoischen; D. Riesenberg; J. Gumpert (pp. 51-58).

The paper describes the synthesis of the phosphorylcholine-binding miniantibody McPC603scFvDhl x in cell-wall-less L-form strains of Escherichia coli and Proteus mirabilis. Cells of these strains were transformed with the plasmid pACK02scKan, carrying the miniantibody (miniAb) coding sequence under the control of the lac promoter. L-form transformants of both species were able to synthesize the functional miniAb as an extracellular soluble product. The highest quantities were obtained by P. mirabilis L-form strains after induction with 5 mM isopropyl β-d-thiogalactopyranoside (IPTG). Yields of 45–75 mg/l total antibody protein and of 10–18 mg/l functional miniAb were estimated in the growth medium of shaking cultures 40–80 h after induction with IPTG. About 10% of the active miniAb remained cell-bound. The yields of functional miniAb could be optimized by lowering the growth temperature from 37 °C to 26–32 °C and by supplementation of the medium with 80 mM sodium fumarate. A comparison of the specific activities revealed that the P. mirabilis L-form strains have a similar synthesis capacity (2–4 mg functional miniAb/g cell dry weight) to that of the producer strain E. coli RV308. The results show that the processes of correct folding and assembling of the miniAb molecules are possible without the periplasmic compartment.

Construction of a recA mutant of Burkholderia (formerly Pseudomonas), cepacia by L. G. van Waasbergen; S. P. Kidambi; R. V. Miller (pp. 59-65).

A recA mutant was constructed of a soil isolate of Burkholderia cepacia, strain ATCC 17616. Prior to mutagenesis, the recA gene was cloned from this strain by its ability to complement the methyl methanesulfonate sensitivity of an Escherichia coli recA mutant. Sequence analysis of the strain showed high sequence similarity (94% nucleic acid and 99% amino acid identity) with the recA gene previously cloned from a clinical isolate of B. cepacia, strain JN25. The subcloned recA gene from B. cepacia ATCC 17616 restored UV resistance and recombination proficiency to recA mutants of E. coli and Pseudomonas aeruginosa, as well as restoring the ability of D3 prophages to be induced to lytic growth from a RecA⁻ strain of P. aeruginosa. The recA mutant of B. cepacia ATCC 17616 was constructed by λ-mediated Tn5 mutagenesis of the cloned recA gene in E. coli, followed by replacement of the Tn5-interrupted gene for the wild-type allele in the chromosome of B. cepacia by marker exchange. The RecA⁻ phenotype of the mutant was demonstrated by the loss of UV resistance as compared to the parental strain. Southern hybridization analysis of chromosomal DNA from the mutant indicated the presence of Tn5 in the recA gene, and the location of the Tn5 insertion in the recA allele was identified by nucleotide sequence analysis. A test using the recA mutant to see if acquired resistance to d-serine toxicity in B. cepacia might be a result of RecA-mediated activities proved negative; nevertheless, RecA activity potentially contributes to the overall genomic plasticity of B. cepacia and a recA mutant will be useful in bioengineering of this species.

Overexpression of a cytosolic hydroxymethylglutaryl-CoA reductase leads to squalene accumulation in yeast by T. Polakowski; U. Stahl; C. Lang (pp. 66-71).

The enzyme 3-hydroxy-3-methylglutaryl-coenzyme-A (HMG-CoA) reductase is known as the rate-limiting enzyme in early sterol biosynthesis in eukaryotic cells. To eliminate this regulation in the yeast Saccharomyces cerevisiae, a truncated HMG1 gene, producing a form of the enzyme that lacks the membrane-binding region (i.e. amino acids 1–552), was constructed and overexpressed in this yeast. The transformed strains accumulated large amounts of the sterol precursor squalene, while the levels of ergosterol and a number of other sterol compounds were only slightly elevated. These findings suggest that HMG-CoA reductase is not the only rate-limiting step in sterol synthesis and its overexpression cannot significantly influence this pathway beyond the sterol precursor squalene.

Optimization of docosahexaenoic acid production by Schizochytrium limacinum SR21 by T. Yokochi; D. Honda; T. Higashihara; T. Nakahara (pp. 72-76).

Culture conditions of Schizochytrium limacinum SR21 for the purpose of microbial docosahexaenoic acid (DHA) production were investigated. The strain SR21 showed a wide tolerance to salinity; that is, the optimum salinity was between 50% and 200% that of sea water. Monosaccharides (glucose and fructose) and glycerol supported good cell growth and DHA yield. Di- and polysaccharides, oleic acid, and linseed oil gave low DHA yields. A high content of DHA (more than 30% of total fatty acids) was obtained from culture on glucose, fructose, and glycerol, and also the strain had simple polyunsaturated fatty acid profiles. The major polyunsaturated fatty acids other than DHA were n-6 docosapentaenoic acid only, and the contents of icosapentaenoic acid and arachidonic acid were less than 1%. Using corn steep liquor as a nitrogen source, a high total fatty acid content was obtained. The total fatty acid content in the dry cell weight increased as the concentration of the nitrogen source decreased, reached more than 50%. An increase in carbon source concentration led to a high DHA yield. A maximum DHA yield of more than 4 g/l was obtained in both glucose and glycerol media at 9% and 12% respectively. S. limacinum SR21 was thought to be a promising resource for microbial DHA production yielding a good level of productivity as well as a simple polyunsaturated fatty acid profile.

Enhanced biosynthesis of clavulanic acid in Streptomyces clavuligerus due to oxidative challenge by redox-cycling agents by H.-J. Kwon; S.-U. Kim (pp. 77-83).

Streptomyces clavuligerus produces a clinically important β-lactamase inhibitor, clavulanic acid. When several of the selected redox-cycling agents were treated, an increase in clavulanate production was observed. The stimulatory effect was seen when the reaction was fed with menadione, plumbagin and phenazine methosulfate (PMS), whereas feeding with methyl viologen had a negative effect. PMS exerted the strongest effect, enhancing the accumulation of clavulanic acid by 150%. Induction of superoxide dismutase upon the addition of PMS suggested an involvement of superoxide in the enhancing process. The stimulatory effect of PMS was offset by the addition of butylated hydroxyanisole, further supporting the involvement of the active oxygen. The enhanced production of clavulanic acid correlated well with the increased total activity of clavaminic acid synthase, a key enzyme in its biosynthesis, and the transcription of cas2, its coding gene. The results suggested that active oxygen species could enhance the biosynthesis of secondary metabolites through the transcriptional activation of the biosynthetic gene.

Growth-associated production of poly(hydroxybutyric acid) by Azotobacter beijerinckii from organic nitrogen substrates by E. J. Bormann; M. Leißner; B. Beer (pp. 84-88).

Poly(hydroxybutyric acid) (PHB) was produced by a selectant of Azotobacter beijerinckii in media containing only organic nitrogen sources such as N substrates. The chosen compounds were casein peptone, yeast extract, casamino acids and urea, each combined with carbon substrates glucose or sucrose. The PHB was synthesized under growth-associated conditions. The concentrations amounted to more than 50% of cell dry mass on casein peptone/glucose as well as urea/glucose medium within 45 h fermentation time. Corresponding to these yields, productivities of about 0.8 g PHB l⁻¹ h⁻¹ were discovered. The highest values increased to 1.06 g PHB l⁻¹ h⁻¹ on casein peptone/glucose medium and 1.1 g PHB l⁻¹ h⁻¹ on yeast extract/glucose medium after a period of 20 h. It was found that oxygen limitation was essential for successful product formation, as demonstrated earlier. These data from basic research may support further investigations into the use of technical proteins from renewable sources as substrates for PHB production by a strain of A. beijerinckii.

Enantioselective hydration of 2-arylpropionitriles by a nitrile hydratase from Agrobacterium tumefaciens strain d3 by R. Bauer; H.-J. Knackmuss; A. Stolz (pp. 89-95).

The enantioselective nitrile hydratase from the bacterium Agrobacterium tumefaciens d3 was purified and completely separated from the amidase activity that is also present in cell extracts prepared from this strain. The nitrile hydratase had an activity optimum at pH 7.0 and a temperature optimum of 40 °C. The holoenzyme had a molecular mass of 69 kDa, the subunits a molecular mass of 27 kDa. The enzyme hydrated various 2-arylpropionitriles and other aromatic and heterocyclic nitriles. With racemic 2-phenylpropionitrile, 2-phenylbutyronitrile, 2-(4-chlorophenyl)propionitrile, 2-(4-methoxy)propionitrile or ketoprofen nitrile the corresponding (S)-amides were formed enantioselectively. The highest enantiomeric excesses (ee >90% until about 30% of the respective substrates were converted) were found for the amides formed from 2-phenylpropionitrile, 2-phenylbutyronitrile and ketoprofen nitrile. For the reaction of the purified nitrile hydratase, higher ee values were found than when whole cells were used in the presence of an inhibitor of the amidase activity. The enantioselectivity of the whole-cell reaction was enhanced by increasing the reaction temperature.

Bioconversion of limonene to α-terpineol by immobilized Penicillium digitatum by Q. Tan; D. F. Day (pp. 96-101).

Bioconversion of (4R)-(+)-limonene to (4R)-(+)-α-terpineol by immobilized fungal mycelia of Penicillium digitatum was investigated in batch, repeated-batch and continuously fed systems. The fungi were immobilized in calcium alginate beads. These beads remained active for at least 14 days when they were stored at 4 °C. Three different aeration rates were tested. The highest yield was obtained at a dissolved oxygen level of 50.0 μmol/l. α-Terpineol production by this fungus was 12.83 mg (g beads)⁻¹ day⁻¹, producing a 45.81% bioconversion of substrate. Repeated-batch bioconversion showed yield decreases in the second and the third cycles. Regeneration with nutrient media after the third cycle improved the bioconversion yields. With continuous bioconversion, the half-life was dependent on the aeration. The optimum conditions with a continuous reactor were at an aeration rate of 0.3 standard l/min and a dilution rate of 0.0144 h⁻¹.

Actual and potential rates of hydrogen photoproduction by continuous culture of the purple non-sulphur bacterium Rhodobacter capsulatus by A. A. Tsygankov; A. S. Fedorov; T. V. Laurinavichene; I. N. Gogotov; K. K. Rao; D. O. Hall (pp. 102-107).

The influence of (NH₄)₂SO₄ concentration and dilution rate (D) on actual and potential H₂ photoproduction has been studied in ammonium-limited chemostat cultures of Rhodobacter capsulatus B10. The actual H₂ production in a photobioreactor was maximal (approx. 80 ml h⁻¹l⁻¹) at D = 0.06 h⁻¹ and 4 mM (NH₄)₂SO₄. However, it was lower than the potential H₂ evolution (calculated from hydrogen evolution rates in incubation vials), which amounted to 100–120 ml h⁻¹ l⁻¹ at D = 0.03–0.08 h⁻¹. Taking into account the fact that H₂ production in the photobioreactor under these conditions was not limited by light or lactate, another limiting (inhibiting) factor should be sought. One possibility is an inhibition of H₂ production by the H₂ accumulated in the gas phase. This is apparent from the non-linear kinetics of H₂ evolution in the vials or from its inhibition by the addition of H₂; initial rates were restored in both cases after the vials had been refilled with argon. The actual H₂ production in the photobioreactor at D = 0.06 h⁻¹ was shown to increase from approximately 80 ml h⁻¹ l⁻¹ to approximately 100 ml h⁻¹ l⁻¹ under an argon flow at 100 ml min⁻¹. Under maximal H₂ production rates in the photobioreactor, up to 30% of the lactate feedstock was utilised for H₂ production and 50% for biomass synthesis.

Effects of phenolic compounds on the growth and the fatty acid composition of Lactobacillus plantarum by N. Rozès; C. Peres (pp. 108-111).

The effects of different phenolic compound concentrations on the fatty acid composition of Lactobacillus plantarum isolated from traditional home-made olive brines were determined. Increasing amounts of caffeic and ferulic acids induced a gradual increase in the amounts of myristic, palmitoleic, stearic and 9,10-methylenehexadecanoic (C17Δ, where Δ represents the cyclopropane group) acid with a concomitant decrease of lactobacillic acid (C₁₉Δ). On the other hand, the addition of tannins induced an increase in the C₁₉Δ level at the expense of vaccenic acid content. The presence of acidic phenols and tannins also affected bacterial growth, inducing the most obvious effect with tannin at 1 g l⁻¹.

Fate and transformation of thiocyanate and cyanate under methanogenic conditions by C.-H. Hung; S. G. Pavlostathis (pp. 112-116).

The fate of thiocyanate (SCN⁻) and cyanate (OCN⁻) under methanogenic conditions was investigated at 35 °C. Thiocyanate and cyanate were added to mixed methanogenic cultures along with an organic mixture. Thiocyanate was stable under these conditions, and had no adverse effect on methanogenesis at a concentration as high as 2.5 mM. In contrast, cyanate at a concentration as low as 0.3 mM initially inhibited methanogenesis but, after the complete removal of cyanate, methanogenesis gradually recovered. The inhibitory effect of cyanate on methanogenesis became more profound with repeated additions of cyanate. The transformation of cyanate followed the hydrolytic route to ammonia and bicarbonate under anaerobic conditions and its hydrolysis rate was enhanced by microbial activity. Cyanide was not detected as a cyanate transformation product under the methanogenic conditions of this study.

Utilization of sorbed compounds by microorganisms specifically isolated for that purpose by W.-C. Tang; J. C. White; M. Alexander (pp. 117-121).

A bacterium obtained by enrichment on nonsorbed phenanthrene was unable to degrade phenanthrene sorbed to polyacrylic beads and had little activity on phenanthrene sorbed to lake-bottom sediment. A bacterium obtained by enrichment on phenanthrene sorbed to polyacrylic beads readily mineralized the compound sorbed to the beads or the sediment. Degradation by the second bacterium of phenanthrene sorbed to beads 38–63 μm or 63–150 μm in diameter was more rapid than the rate of desorption of the hydrocarbon in the absence of the bacterium. Little degradation of sorbed, nonleachable phenanthrene in soil was effected by another isolate obtained by enrichment with the nonsorbed hydrocarbon, but a mixed culture and the bacterium obtained by enrichment on the sorbed compound extensively degraded phenanthrene. Because microorganisms specifically obtained for their capacity to degrade sorbed phenanthrene are more active than species not specialized for use of the bound compound, we suggest that microorganisms enriched on nonsorbed compounds may not be appropriate for evaluation of biodegradation and bioremediation of sorbed compounds.

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Applied Microbiology and Biotechnology (v.49, #1)