Fed-batch production of <Emphasis Type="SmallCaps">d</Emphasis>-ribose from sugar mixtures by transketolase-deficient <Emphasis Type="Italic">Bacillus subtilis</Emphasis> SPK1

d-Ribose, a five-carbon sugar, is used as a key intermediate for the production of various biomaterials, such as riboflavin and inosine monophosphate. A high d-ribose-producing Bacillus subtilis SPK1 strain was constructed by the chemical mutation of the transketolase-deficient strain, B. subtilis JY1. Batch fermentation of B. subtilis SPK1 with 20 g l^–1 xylose and 20 g l^–1 glucose resulted in 4.78 g l^–1 dry cell mass, 23.0 g l^–1d-ribose concentration, and 0.72 g l^–1 h^–1 productivity, corresponding to a 1.5- to 1.7-fold increase when compared with values for the parental strain. A late-exponential phase was chosen as the best point for switching to a fed-batch process. Optimized fed-batch fermentation of B. subtilis SPK1, feeding a mixture of 200 g l^–1 xylose and 50 g l^–1 glucose after the late-exponential phase reduced the residual xylose and glucose concentrations to less than 7.0 g l^–1 and gave the best results of 46.6 g l^–1d-ribose concentration and 0.88 g l^–1 h^–1 productivity which were 2.0- and 1.2-fold higher than the corresponding values in a simple batch fermentation.     

Improvement of nisin production in pH feed-back controlled,fed-batch culture by <Emphasis Type="Italic">Lactococcus lactis</Emphasis>subsp<Emphasis Type="Italic">. lactis</Emphasis>

Nisin production by Lactococcus lactis subsp. lactisin fed-batch culture was doubled by using a pH feed-back controlled method. Sucrose concentration was controlled at 10 g l^–1 giving 5010 IU nisin ml^–1 compared to 2660 IU nisin ml^–1 in batch culture.     

Production of poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-3-hydroxyhexanoate) with flexible 3-hydroxyhexanoate content in<Emphasis Type="Italic"> Aeromonas hydrophila</Emphasis> CGMCC 0911

Aeromonas hydrophila CGMCC 0911 isolated from lake water was found to be able to synthesize a polyhydroxyalkanoate (PHA) copolymer (PHBHHx) consisting of 3-hydroxybutyrate (HB) and 4–6 mol% 3-hydroxyhexanoate (HHx). The wild-type bacterium accumulated 49% PHBHHx containing 6 mol% HHx in terms of cell dry weight (CDW) when grown on lauric acid for 48 h. When A. hydrophila CGMCC 0911 expressed the Acyl-CoA dehydrogenase gene (yafH) of Escherichia coli, the recombinant strain could accumulate 47% PHBHHx, while the HHx content reached 17.4 mol%. The presence of changing glucose concentration in the culture changed the HHx content both in wild type and recombinant A. hydrophila CGMCC 0911. When 5 g l^–1 glucose was added to a culture containing 5 g l^–1 lauric acid as co-substrate, 45% PHBHHx/CDW consisting of 8.8 mol% HHx was produced by wild-type A. hydrophila CGMCC 0911 compared with only 5% in the absence of glucose. When the recombinant A. hydrophila CGMCC 0911 was grown on a mixed substrate containing lauric acid and 8–10 g l^–1 glucose, the HHx content could be further increased to 35.6 mol%. When the glucose concentration exceeded 10 g l^–1, cell growth, PHA content and mole percentages of HHx in PHBHHx were significantly reduced.     

<Emphasis Type="Italic">Agrobacterium tumefaciens</Emphasis>-mediated transformation of blueberry (<Emphasis Type="Italic">Vaccinium corymbosum</Emphasis> L.)

Transient expression studies using blueberry leaf explants and monitored by -glucuronidase (GUS) assays indicated Agrobacterium tumefaciens strain EHA105 was more effective than LBA4404 or GV3101; and the use of acetosyringone (AS) at 100 M for inoculation and 6 days co-cultivation was optimum compared to 2, 4, 8, 10 or 12 days. Subsequently, explants of the cultivars Aurora, Bluecrop, Brigitta, and Legacy were inoculated with strain EHA105 containing the binary vector pBISN1 with the neomycin phosphotransferase gene (nptII) and an intron-interrupted GUS gene directed by the chimeric super promoter (Aocs)₃AmasPmas. Co-cultivation was for 6 days on modified woody plant medium (WPM) plus 100 M AS. Explants were then placed on modified WPM supplemented with 1.0 mg l^–1 thidiazuron, 0.5 mg l^–1 -naphthaleneacetic, 10 mg l^–1 kanamycin (Km), and 250 mg l^–1 cefotaxime. Selection for Km-resistant shoots was carried out in the dark for 2 weeks followed by culture in the light at 30 E m^–2 s^–1 at 25°C. After 12 weeks, selected shoots that were both Km resistant and GUS positive were obtained from 15.3% of the inoculated leaf explants of cultivar Aurora. Sixty-eight independent clones derived from such shoots all tested positive by the polymerase chain reaction using a nptII primer. Eight of eight among these 68 clones tested positive by Southern hybridization using a gusA gene derived probe. The transformation protocol also yielded Km-resistant, GUS-positive shoots that were also PCR positive at frequencies of 5.0% for Bluecrop, 10.0% for Brigitta and 5.6% for Legacy.     

The effect of<Emphasis Type="Italic"> pfl</Emphasis> gene knockout on the metabolism for optically pure <Emphasis Type="SmallCaps">d</Emphasis>-lactate production by<Emphasis Type="Italic"> Escherichia coli</Emphasis>

The effect of gene knockout on metabolism in the pflA^–, pflB^–, pflC^–, and pflD^– mutants of Escherichia coli was investigated. Batch cultivations of the pfl ^– mutants and their parent strain were conducted using glucose as a carbon source. It was found that pflA^– and pflB^– mutants, but not pflC^– and pflD^– mutants, produced large amounts of d-lactate from glucose under the microaerobic condition, and the maximum yield was 73%. In order to investigate the metabolic regulation mechanism, we measured enzyme activities for the following eight enzymes: glucose 6-phosphate dehydrogenase, 6-phosphogluconate dehydrogenase, glyceraldehyde 3-phosphate dehydrogenase (GAPDH), pyruvate kinase, lactate dehydrogenase (LDH), phosphoenolpyruvate carboxylase, acetate kinase, and alcohol dehydrogenase. Intracellular metabolite concentrations of glucose 6-phosphate, fructose 1,6-bisphosphate, phosphoenolpyruvate, pyruvate, acetyl coenzyme A as well as ATP, ADP, AMP, NADH, and NAD⁺ were also measured. It was shown that the GAPDH and LDH activities were considerably higher in pflA^– and pflB^– mutants, which implies coupling between NADH production and consumption between the two corresponding reactions. The urgent energy requirement was shown by the lower ATP/AMP level due to both oxygen limitation and pfl gene knockout, which promoted significant stepping-up of glycolysis when using glucose as a carbon source. It was shown that the demand for energy is more important than intracellular redox balance, thus excess NADH produced through GAPDH resulted in a significantly higher intracellular NADH/NAD⁺ ratio in pfl ^– mutants. Consequently, the homolactate production was achieved to meet the requirements of the redox balance and the energy production through glycolysis. The effect of using different carbon sources such as gluconate, pyruvate, fructose, and glycerol was investigated.     

Optimization of the solvent-tolerant <Emphasis Type="Italic">Pseudomonas putida</Emphasis> S12 as host for the production of <Emphasis Type="Italic">p</Emphasis>-coumarate from glucose

A Pseudomonas putida S12 strain was constructed that is able to convert glucose to p-coumarate via the central metabolite l-tyrosine. Efficient production was hampered by product degradation, limited cellular l-tyrosine availability, and formation of the by-product cinnamate via l-phenylalanine. The production host was optimized by inactivation of fcs, the gene encoding the first enzyme in the p-coumarate degradation pathway in P. putida, followed by construction of a phenylalanine-auxotrophic mutant. These steps resulted in a P. putida S12 strain that showed dramatically enhanced production characteristics with controlled l-phenylalanine feeding. During fed-batch cultivation, 10 mM (1.7 g l⁻¹) of p-coumarate was produced from glucose with a yield of 3.8 Cmol% and a molar ratio of p-coumarate to cinnamate of 85:1.     

Anaerobic and aerobic continuous cultures of<Emphasis Type="Italic"> Saccharomyces cerevisiae</Emphasis>: comparison of plasmid stability and<Emphasis Type="Italic"> EXG1</Emphasis> gene expression

Two bioreactor continuous cultures, at anaerobic and aerobic conditions, were carried out using a recombinant Saccharomyces cerevisiae strain that over-expresses the homologous gene EXG1. This recombinant system was used to study the effect of dissolved oxygen concentration on plasmid stability and gene over-expression. Bioreactor cultures were operated at two dilution rates (0.14 and 0.03 h^–1) to investigate the effect of other process parameters on EXG1 expression. Both cultures suffered severe plasmid instability during the first 16 generations. Segregational plasmid loss rate for the aerobic culture was two-fold that of the anaerobic operation. In spite of this fact, exo--glucanase activity at aerobic conditions was 12-fold that of the anaerobic culture. This maximal activity (30 U ml^–1) was attained at the lowest dilution rate when biomass reached its greatest value and glucose concentration was zero.     

Unique Distribution of <Emphasis Type="Italic">GAL</Emphasis> Genes on Chromosome XI in the Yeast <Emphasis Type="Italic">Saccharomyces naganishii</Emphasis>

A region of DNA extending from GAL7 to GAL1 was cloned in the yeast Saccharomyces naganishii. Sequence analysis revealed that GAL7 and GAL1 are separated by approximately 2 kbp and share a common promoter region. Although GAL7, GAL10, and GAL1 are clustered in this order in previously studied hemiascomycetous yeasts, GAL10 was not found between GAL7 and GAL1 in S. naganishii. Southern blotting of S. naganishii chromosomal DNA showed that both the GAL7–GAL1 region and GAL10 are located on chromosome XI, but that GAL10 is located more than 10 kbp away from GAL7–GAL1. Thus, S. naganishii and S. cerevisiae, while related phylogenetically, do not share the same orientation with respect to GAL genes. These data are highly relevant to studies of chromosomal evolution in yeast.     

<Emphasis Type="Italic">Narcissus</Emphasis> bulblet formation <Emphasis Type="Italic">in vitro</Emphasis>: effects of carbohydrate type and osmolarity of the culture medium

Shoot clump cultures of Narcissus cultivars St. Keverne and Hawera were used to investigate the effects of culture medium carbon supply, type of carbohydrate and osmolarity on in vitro bulblet development. Increasing the medium osmolarity using mannitol or sorbitol, which did not act as substrates for growth, failed to stimulate bulblet formation with either cultivar. An exception to this was a relatively small increase in total bulblet dry weight per culture, in the cultivar Hawera only, caused by adding 30 g l ^–1 sorbitol in combination with 30 g l^–1 sucrose. Simultaneously increasing the medium osmolarity and carbon supply using the metabolisable carbohydrate sources, sucrose, glucose, fructose or an equimolar mixture of glucose and fructose stimulated bulblet production, total dry matter accumulation and partitioning into bulblets. At comparable levels of carbon supply up to 19.0 g l^–1, bulblet development of both cultivars was similar with monosaccharide and sucrose media. This indicates that substrate supply is more important for bulblet development than osmolarity of the culture medium. The cultivar Hawera also showed similar responses to monosaccharide and sucrose media supplying 37.9 g C l^–1, despite the high osmolarity of monosaccharide media (c. 650 m Osm kg^–1, equivalent to –1.6 MPa, compared to 380 m Osm kg^–1 for sucrose medium). However in St. Keverne total dry matter accumulation and dry weight per bulblet were further stimulated only by increasing the sucrose supply from 19.0 to 37.9 g C l^–1, not by increasing the monosaccharide supply. Implications of the findings for Narcissus micropropagation are discussed.     

A repeated batch process for cultivation of <Emphasis Type="Italic">Bifidobacterium longum</Emphasis>

A repeated batch process was performed to culture Bifidobacterium longum CCRC 14634. An on-line device, oxidation-reduction potential (ORP), was used to monitor cell growth and uptake of nutrients in the culture. The ORP of the culture medium decreased substantially during fermentation until nutrients were depleted. Six cycles of batch fermentation using ORP as a control parameter were successfully carried out. As soon as ORP remained constant or increased, three-quarters of the broth was removed, and the same volume of fresh medium was fed to the fermenter for a new cycle of cultivation. Average cell concentrations of 1.9×10⁹ and 3.4×10⁹ cfu ml^–1 for repeated batch fermentation in MRS (Lactobacilli MRS broth) and WY (containing whey hydrolyzates, yeast extract, l-cysteine) medium, respectively, were achieved. Cell mass productivities for batch, fed-batch and repeated batch fermentation using MRS medium were 0.51, 0.41, and 0.64 g l^–1 h^–1, respectively, and those for batch and repeated batch using WY medium were 0.76, 0.99 g l^–1 h^–1, respectively. The results indicate a possible industrial process to culture Bifidobacteria sp.     

Enhanced production of GDP-<Emphasis Type="SmallCaps">l</Emphasis>-fucose by overexpression of NADPH regenerator in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Biosynthesis of guanosine 5′-diphosphate-l-fucose (GDP-l-fucose) requires NADPH as a reducing cofactor. In this study, endogenous NADPH regenerating enzymes such as glucose-6-phosphate dehydrogenase (G6PDH), isocitrate dehydrogenase (Icd), and NADP⁺-dependent malate dehydrogenase (MaeB) were overexpressed to increase GDP-l-fucose production in recombinant Escherichia coli. The effects of overexpression of each NADPH regenerating enzyme on GDP-l-fucose production were investigated in a series of batch and fed-batch fermentations. Batch fermentations showed that overexpression of G6PDH was the most effective for GDP-l-fucose production. However, GDP-l-fucose production was not enhanced by overexpression of G6PDH in the glucose-limited fed-batch fermentation. Hence, a glucose feeding strategy was optimized to enhance GDP-l-fucose production. Fed-batch fermentation with a pH-stat feeding mode for sufficient supply of glucose significantly enhanced GDP-l-fucose production compared with glucose-limited fed-batch fermentation. A maximum GDP-l-fucose concentration of 235.2 ± 3.3 mg l⁻¹, corresponding to a 21% enhancement in the GDP-l-fucose production compared with the control strain overexpressing GDP-l-fucose biosynthetic enzymes only, was achieved in the pH-stat fed-batch fermentation of the recombinant E. coli overexpressing G6PDH. It was concluded that sufficient glucose supply and efficient NADPH regeneration are crucial for NADPH-dependent GDP-l-fucose production in recombinant E. coli.     

Modeling of the pyruvate production with<Emphasis Type="Italic"> Escherichia coli</Emphasis> in a fed-batch bioreactor

A family of 10 competing, unstructured models has been developed to model cell growth, substrate consumption, and product formation of the pyruvate producing strain Escherichia coli YYC202 ldhA::Kan strain used in fed-batch processes. The strain is completely blocked in its ability to convert pyruvate into acetyl-CoA or acetate (using glucose as the carbon source) resulting in an acetate auxotrophy during growth in glucose minimal medium. Parameter estimation was carried out using data from fed-batch fermentation performed at constant glucose feed rates of q_VG=10 mL h^–1. Acetate was fed according to the previously developed feeding strategy. While the model identification was realized by least-square fit, the model discrimination was based on the model selection criterion (MSC). The validation of model parameters was performed applying data from two different fed-batch experiments with glucose feed rate q_VG=20 and 30 mL h^–1, respectively. Consequently, the most suitable model was identified that reflected the pyruvate and biomass curves adequately by considering a pyruvate inhibited growth (Jerusalimsky approach) and pyruvate inhibited product formation (described by modified Luedeking–Piret/Levenspiel term).List of symbols c_A acetate concentration (g L^–1) - c_A,0 acetate concentration in the feed (g L^–1) - c_G glucose concentration (g L^–1) - c_G,0 glucose concentration in the feed (g L^–1) - c_P pyruvate concentration (g L^–1) - c_P,max critical pyruvate concentration above which reaction cannot proceed (g L^–1) - c_X biomass concentration (g L^–1) - K_I inhibition constant for pyruvate production (g L^–1) - K_I^A inhibition constant for biomass growth on acetate (g L^–1) - K_P saturation constant for pyruvate production (g L^–1) - K_P inhibition constant of Jerusalimsky (g L^–1) - K_S^A Monod growth constant for acetate (g L^–1) - K_S^G Monod growth constant for glucose (g L^–1) - m_A maintenance coefficient for growth on acetate (g g^–1 h^–1) - m_G maintenance coefficient for growth on glucose (g g^–1 h^–1) - n constant of extended Monod kinetics (Levenspiel) (–) - q_V volumetric flow rate (L h^–1) - q_VA volumetric flow rate of acetate (L h^–1) - q_VG volumetric flow rate of glucose (L h^–1) - r_A specific rate of acetate consumption (g g^–1 h^–1) - r_G specific rate of glucose consumption (g g^–1 h^–1) - r_P specific rate of pyruvate production (g g^–1 h^–1) - r_P,max maximum specific rate of pyruvate production (g g^–1 h^–1) - t time (h) - V reaction (broth) volume (L) - Y_P/G yield coefficient pyruvate from glucose (g g^–1) - Y_X/A yield coefficient biomass from acetate (g g^–1) - Y_X/A,max maximum yield coefficient biomass from acetate (g g^–1) - Y_X/G yield coefficient biomass from glucose (g g^–1) - Y_X/G,max maximum yield coefficient biomass from glucose (g g^–1) - growth associated product formation coefficient (g g^–1) - non-growth associated product formation coefficient (g g^–1 h^–1) - specific growth rate (h^–1) - _max maximum specific growth rate (h^–1)     

Effect of modified glucose catabolism on xanthan production in <Emphasis Type="Italic">Xanthomonas oryzae</Emphasis> pv. <Emphasis Type="Italic">oryzae</Emphasis>

In this study, the glucose 6-phosphate dehydrogenase gene (XOO2314) was inactivated in order to modulate the intracellular glucose 6-phosphate, and its effects on xanthan production in a wild-type strain of Xanthomonas oryzae were evaluated. The intracellular glucose 6-phosphate was increased from 17.6 to 99.4 μmol g⁻¹ (dry cell weight) in the gene-disrupted mutant strain. The concomitant increase in the glucose 6-phosphate was accompanied by an increase in xanthan production of up to 2.23 g l⁻¹ (culture medium). However, in defined medium supplemented with 0.4% glucose, the growth rate of the mutant strain was reduced to 52.9% of the wild-type level. Subsequently, when a family B ATP-dependent phosphofructokinase from Escherichia coli was overexpressed in the mutant strain, the growth rate was increased to 142.9%, whereas the yields of xanthan per mole of glucose remained approximately the same.     

High cell density fed-batch cultivation of<Emphasis Type="Italic"> Escherichia coli</Emphasis> using exponential feeding combined with pH-stat

A new feeding strategy in fed-batch culture, exponential feeding combined with pH-stat is suggested to avoid the accumulation of substrate in culture broth. Exponential feeding was stopped whenever a predetermined amount of limiting substrate was supplied and then pH change was observed. When pH rose above an upper limit due to the depletion of substrate, feeding was restarted. With this feeding strategy, recombinant Escherichia coli could be grown to 101 g/l by controlling the specific growth rate at 0.1 h^–1.An erratum to this article can be found at     

Large-scale production of tannase using the yeast <Emphasis Type="Italic">Arxula adeninivorans</Emphasis>

Tannase (tannin acyl hydrolase, EC 3.1.1.20) hydrolyses the ester and depside bonds of gallotannins and gallic acid esters and is an important industrial enzyme. In the present study, transgenic Arxula adeninivorans strains were optimised for tannase production. Various plasmids carrying one or two expression modules for constitutive expression of tannase were constructed. Transformant strains that overexpress the ATAN1 gene from the strong A. adeninivorans TEF1 promoter produce levels of up to 1,642 U L⁻¹ when grown in glucose medium in shake flasks. The effect of fed-batch fermentation on tannase productivity was then investigated in detail. Under these conditions, a transgenic strain containing one ATAN1 expression module produced 51,900 U of tannase activity per litre after 142 h of fermentation at a dry cell weight of 162 g L⁻¹. The highest yield obtained from a transgenic strain with two ATAN1 expression modules was 31,300 U after 232 h at a dry cell weight of 104 g L⁻¹. Interestingly, the maximum achieved yield coefficients [Y(P/X)] for the two strains were essentially identical.     

Modeling of <Emphasis Type="Italic">Fusarium redolens</Emphasis> Dzf2 mycelial growth kinetics and optimal fed-batch fermentation for beauvericin production

Beauvericin (BEA) is a cyclic hexadepsipeptide mycotoxin with notable phytotoxic and insecticidal activities. Fusarium redolens Dzf2 is a highly BEA-producing fungus isolated from a medicinal plant. The aim of the current study was to develop a simple and valid kinetic model for F. redolens Dzf2 mycelial growth and the optimal fed-batch operation for efficient BEA production. A modified Monod model with substrate (glucose) and product (BEA) inhibition was constructed based on the culture characteristics of F. redolens Dzf2 mycelia in a liquid medium. Model parameters were derived by simulation of the experimental data from batch culture. The model fitted closely with the experimental data over 20–50 g l⁻¹ glucose concentration range in batch fermentation. The kinetic model together with the stoichiometric relationships for biomass, substrate and product was applied to predict the optimal feeding scheme for fed-batch fermentation, leading to 54% higher BEA yield (299 mg l⁻¹) than in the batch culture (194 mg l⁻¹). The modified Monod model incorporating substrate and product inhibition was proven adequate for describing the growth kinetics of F. redolens Dzf2 mycelial culture at suitable but not excessive initial glucose levels in batch and fed-batch cultures.     

Combinatorial modulation of <Emphasis Type="Italic">galP</Emphasis> and <Emphasis Type="Italic">glk</Emphasis> gene expression for improved alternative glucose utilization

Phosphoenolpyruvate (PEP) is an important precursor for anaerobic production of succinate and malate. Although inactivating PEP/carbohydrate phosphotransferase systems (PTS) could increase PEP supply, the resulting strain had a low glucose utilization rate. In order to improve anaerobic glucose utilization rate for efficient production of succinate and malate, combinatorial modulation of galactose permease (galP) and glucokinase (glk) gene expression was carried out in chromosome of an Escherichia coli strain with inactivated PTS. Libraries of artificial regulatory parts, including promoter and messenger RNA stabilizing region (mRS), were firstly constructed in front of β-galactosidase gene (lacZ) in E. coli chromosome through λ-Red recombination. Most regulatory parts selected from mRS library had constitutive strengths under different cultivation conditions. A convenient one-step recombination method was then used to modulate galP and glk gene expression with different regulatory parts. Glucose utilization rates of strains modulated with either galP or glk all increased, and the rates had a positive relation with expression strength of both genes. Combinatorial modulation had a synergistic effect on glucose utilization rate. The highest rate (1.64 g/L h) was tenfold higher than PTS⁻ strain and 39% higher than the wild-type E. coli. These modulated strains could be used for efficient anaerobic production of succinate and malate.     

High-level production of arachidonic acid by fed-batch culture of <Emphasis Type="Italic"> Mortierella alpina</Emphasis> using NH<Subscript>4</Subscript>OH as a nitrogen source and pH control

Mortierella alpina was grown in a fed-batch culture using a 12-l jar fermenter with an initial 8-l working volume containing 20 g glucose l⁻¹ and 10 g corn-steep powder l⁻¹. Glucose was intermittently fed to give 32 g l⁻¹ at each time. The pH of culture was maintained using 14% (v/v) NH₄OH, which also acted as a nitrogen source. A final cell density of 72.5 g l⁻¹ was reached after 12.5 days with a content of arachidonic acid (ARA) at 18.8 g l⁻¹. These values were 4 and 1.8 times higher than the respective values in batch culture. Our results suggest that the combined feeding of glucose and NH₄⁺ to the growth of M. alpina could be applied for the industrial scale production of ARA.     

Nucleosome transactions on the<Emphasis Type="Italic"> Hypocrea jecorina</Emphasis> (<Emphasis Type="Italic"> Trichoderma reesei</Emphasis>) cellulase promoter<Emphasis Type="Italic"> cbh2</Emphasis> associated with cellulase induction

The 5 regulatory region of the cbh2 gene of Hypocrea jecorina contains the cbh2 activating element (CAE) which is essential for induction of cbh2 gene expression by sophorose and cellulose. The CAE consists of two motifs, a CCAAT box on the template strand and a GTAATA box on the coding strand, which cooperate during induction. Northern analyses of cbh2 gene expression has revealed an absolute dependence on induction, but no direct effect of Cre1-mediated carbon catabolite repression. Investigation of the chromatin structure in the wild-type strain showed that, under repressing conditions, there is a nucleosome free region (nfr) around the CAE, which is flanked by strictly positioned nucleosomes. Induction results in a loss of positioning of nucleosomes –1 and –2 downstream of the CAE, thus making the TATA box accessible. Simultaneous mutation of both motifs of the CAE, or of the CCAAT-box alone, also leads to shifting of nucleosome –1, which normally covers the TATA-box under repressing conditions, whereas mutation of the GTAATA element results in a narrowing of the nfr, indicating that the proteins that bind to both motifs in the CAE interact with chromatin, although in different ways. A cellulase-negative mutant strain, which has previously been shown to be altered in protein binding to the CAE, still displayed the induction-specific changes in nucleosome structure, indicating that none of the proteins that directly interact with CAE are affected, and that nucleosome rearrangement and induction of cbh2 expression are uncoupled. Interestingly, the carbon catabolite repressor Cre1 is essential for strict nucleosome positioning in the 5 regulatory sequences of cbh2 under all of the conditions tested, and induction can occur in a promoter that lacks positioned nucleosomes. These data suggest that Cre1, the Hap2/3/5 complex and the GTAATA-binding protein are all involved in nucleosome assembly on the cbh2 promoter, and that the latter two respond to inducing conditions by repositioning nucleosome –1.Communicated by C. A. M. J. J. van den Hondel     

Overexpression of the <Emphasis Type="Italic">plg</Emphasis>1 gene encoding pectin lyase in <Emphasis Type="Italic">Penicillium griseoroseum</Emphasis>

The pectin lyase (PL) is an industrially important enzyme since it is used for maceration and clarification in the process of fruit juice production in food industries. In order to increase the yields of pectin lyase we cloned the plg1 (pectin lyase 1) from Penicillium griseoroseum gene under the control of the strong constitutive promoter of the glyceraldehyde-3-phosphate dehydrogenase gene (gpdA) and the terminator region of the tryptophan synthetase (trpC) gene from Aspergillus nidulans (plasmid pAN52-Plg1) and transformed this construct into the P. griseoroseum strain PG63. One of the pAN52-Plg1 multi-copy transformants (strain 105) grown in culture medium containing glucose or sugar cane juice showed PL activities of 4,804 or 5,202 U ml⁻¹ respectively, which represented 57- and 132-fold increases. In addition, the apparent specific activity of PL produced by this strain was much higher than the one observed for a commercial pectinase preparation. Evaluation of the extracellular proteins in the culture supernatant of strain 105 by SDS-PAGE showed the presence of a clear and strong band of approximately 40 kDa that probably corresponds to PL. The enzyme yields reported here demonstrate that the system we developed is able to express pectin lyase at levels comparable to, or exceeding, previously reported data.