Effect of calcium on synthesis of dipicolinic acid inPenicillium citreoviride and its feedback resistant mutant

Dipicolinic acid synthesis inPenicillium citreoviride strain 3114 was inhibited by Ca²⁺ ions, but not by Ba²⁺, Cu²⁺or Fe²⁺. Among the metals tested, only Zn²⁺ inhibited the synthesis of dipicolinic acid and promoted sporulation. None of these metals reversed the inhibition by Ca²⁺ or Zn²⁺. A mutant 27133-dpa-ca selected for resistance to feedback inhibition by dipicolinic acid: Ca²⁺ complex showed cross-resistance to inhibition by dipicolinic acid: Zn²⁺. Both 3114 and271 33-dpa-ca excreted a number of aliphatic and amino acids during secondary metabolism of dipicolinic acid. In the presence of 1000 ppm of Ca²⁺, accumulation of citric acid and α-aminoadipic acid was completely inhibited under conditions of inhibition of dipicolinic acid in parent strain 3114 but not in the mutant. Citric acid with or without Ca²⁺ did not inhibit thede novo synthesis of dipicolinic acid in the strain 3114. In fact, citric acid in the presence of Ca²⁺ improved significantly rate of dipicolinic acid synthesis. Apart from resistance to feed back inhibition by dipicolinic acid: Ca²⁺ complex, mutant differed from the parent in three other aspectsviz. (i) dipicolinic acid synthesis was not subject to catabolite repression by glucose, (ii) sporulation as well as dipicolinic acid synthesis was dependent on the presence of Ca²⁺ ions in the medium and (iii) Mg²⁺ requirement for the mutant increased three fold. Higher requirement of the Mg²⁺ could be partially relieved by Ca²⁺ during secondary metabolism. The results support the inference thatde novo synthesis of dipicolinic acid is regulated through feedback inhibition by dipicolinic acid: Ca²⁺complex.     

A constitutive catabolite repression mutant of a recombinantSaccharomyces cerevisiae strain improves xylose consumption during fermentation

Efficient xylose utilisation by microorganisms is of importance to the lignocellulose fermentation industry. The aim of this work was to develop constitutive catabolite repression mutants in a xylose-utilising recombinantSaccharomyces cerevisiae strain and evaluate the differences in xylose consumption under fermentation conditions.S. cerevisiae YUSM was constitutively catabolite repressed through specific disruptions within theMIG1 gene. The strains were grown aerobically in synthetic complete medium with xylose as the sole carbon source. Constitutive catabolite repressed strain YCR17 grew four-fold better on xylose in aerobic conditions than the control strain YUSM. Anaerobic batch fermentation in minimal medium with glucose-xylose mixtures and N-limited chemostats with varying sugar concentrations were performed. Sugar utilisation and metabolite production during fermentation were monitored. YCR17 exhibited a faster xylose consumption rate than YUSM under high glucose conditions in nitrogen-limited chemostat cultivations. This study shows that a constitutive catabolite repressed mutant could be used to enhance the xylose consumption rate even in the presence of high glucose in the fermentation medium. This could help in reducing fermentation time and cost in mixed sugar fermentation.     

A novel <Emphasis Type="Italic">Candida glycerinogenes</Emphasis> mutant with high glycerol productivity in high phosphate concentration medium

A novel Candida glycerinogenes mutant, which possesses high glycerol productivity in a high phosphate concentration medium, was obtained by mutagenesis of an industrial glycerol producer. The mutant accumulated a total biomass of 11.5 g l⁻¹, which is less than the 15 g l⁻¹of the wild-type strain, but it consumed glucose faster than the wild-type strain did. The mutant reached its maximal glycerol concentration of 129 g l⁻¹ in 84 h compared to 96 h for the wild-type strain. High cytoplasmic glycerol-3-phosphate dehydrogenase activity of the mutant in the early glycerol formation phase, leading to a rapid glycerol synthesis and accumulation, may be the main reason for the short fermentation process.     

Citric acid production from sugar cane molasses by 2-deoxyglucose-resistant mutant strain ofAspergillus niger

Citric acid production from sugar cane molasses byAspergillus niger NIAB 280 was studied in a batch cultivation process. A maximum of 90 g/L total sugar was utilized in citric acid production medium. From the parental strainA. niger, mutant strains showing resistance to 2-deoxyglucose in Vogal's medium containing molasses as a carbon source were induced by γ-irradiation. Among the new series of mutant strains, strain RP7 produced 120 g/L while the parental strain produced 80 g/L citric acid (1.5-fold improvement) from 150 g/L of molasses sugars. The period of citric acid production was shortened from 10 d for the wild-type strain to 6–7 d for the mutant strain. The efficiency of substrate uptake rate with respect to total volume substrate consumption rate,Q _s (g per L per h) and specific substrate consumption rate,q _s (g substrate per g cells per h) revealed that the mutant grew faster than its parent. This indicated that the selected mutant is insensitive to catabolite repression by higher concentrations of sugars for citric acid production. With respect to the product yield coefficient (Y _p/x), volume productivity (Q _p) and specific product yields (q _p), the mutant strain is significantly (p≤0.05) improved over the parental strain.     

Catabolite repression of β-galactosidase synthesis in Escherichia coli

1. Repression by glucose of β-galactosidase synthesis is spontaneously reversible in all strains of Escherichia coli examined long before the glucose has all been consumed. The extent of recovery and the time necessary for reversal differ among various strains. Other inducible enzymes show similar effects. 2. This transient effect of glucose repression is observed in constitutive (i⁻) and permease-less (y⁻) cells as well as in the corresponding i⁺ and y⁺ strains. 3. Repression is exerted by several rapidly metabolizable substrates (galactose, ribose and ribonucleosides) but not by non-metabolized or poorly metabolized compounds (2-deoxyglucose, 2-deoxyribose, phenyl thio-β-galactoside and 2-deoxyribonucleosides). 4. The transient repression with glucose is observed in inducible cells supplied with a powerful inducer of β-galactosidase synthesis (e.g. isopropyl thio-β-galactoside) but not with a weak inducer (lactose); in the latter instance glucose repression is permanent. Diauxic growth on glucose plus lactose can be abolished by including isopropyl thio-β-galactoside in the medium. 5. In some strains phosphate starvation increases catabolite repression; in others it relieves it. Adenine starvation in an adenine-requiring mutant also relieves catabolite repression by glycerol but not that by glucose. Restoration of phosphate or adenine to cells starved of these nutrients causes a pronounced temporary repression. Alkaline-phosphatase synthesis is not affected by the availability of adenine. 6. During periods of transient repression of induced enzyme synthesis the differential rate of RNA synthesis, measured by labelled uracil incorporation in 2min. pulses, shows a temporary rise. 7. The differential rate of uracil incorporation into RNA falls during exponential growth of batch cultures of E. coli. This is equally true for uracil-requiring and non-requiring strains. The fall in the rate of incorporation has been shown to be due to a real fall in the rate of RNA synthesis. The significance of the changes in the rate of RNA synthesis is discussed. 8. A partial model of catabolite repression is presented with suggestions for determining the chemical identification of the catabolite co-repressor itself.     

Effects of pulse feeding of beet molasses on recombinant benzaldehyde lyase production by Escherichia coli BL21(DE3)

The effect of fed-batch operation (FBO) strategy was investigated using pretreated-beet molasses, containing galactose that induces the lac promoter, on benzaldehyde lyase (BAL) production by recombinant Escherichia coli BL21(DE3)pLySs. After batch cultivation with 30 g l^?1 pretreated-beet molasses consisting of 7.5 g l^?1 glucose and 7.5 g l^?1 fructose, three FBO strategies were applied at dissolved oxygen (=40%) cascade to air-flow rate. In FBO1 when air-flow rate decreased considerably, feed was given to the system in pulses in such a way that pretreated-beet molasses concentration increased by 10 kg m^?3 (containing 2.5 g l^?1 glucose+2.5 g l^?1 fructose); however, decrease in air-flow rate demonstrated only the absence of glucose but not fructose. Thus, in FBO2 when fructose and glucose were completely utilized, pretreated-beet molasses was pulse-fed and its concentration increased by 10 g l^?1. In FBO3 with the decreased amount of pretreated-beet molasses (6 g l^?1), shift response time from glucose to fructose consumption was avoided, and glucose and fructose consumptions were well correlated with air-flow rate, and the highest C _X (8.04 g l^?1) and BAL (2,315 U ml^?1) production were obtained (t?=?24 h) with the highest substrate yield on cell and product formation.     

Engineering a repression-free catabolite-enhanced expression system for a thermophilic alpha-amylase from Bacillus licheniformis MSG

Most expression systems used for the over production of many enzymes employ carbon catabolite repressible promoters and hence must use sugar free, rich complex media. Use of expression systems to overcome carbon repression opens an avenue for exploiting cheap carbon sources for the production of recombinant enzymes. A self-inducible, catabolite repression free and above all a glucose-activated expression system has been developed using an industrially suitable thermophilic alpha-amylase as a model. The alpha-amylase gene of Bacillus licheniformis MSG without the 5' cre operator produced unimpeded glucose-enhanced expression when fused to the phosphate starvation-inducible strong pst promoter with optimum translation signals in a protease deficient Bacillus subtilis. A combination of high glucose with limited phosphate permitted sufficient biomass and fast transition to quiescent phase by phosphate starvation permitting 1250-fold induction for 70 h. A ~300-fold high productivity (9070 U mL^-1) and 131-fold increase in specific expression in 2% glucose and a 100-fold high yield in 4% molasses were obtained compared to the production by the parent strain. The yield was 18.5-fold higher than that from the native promoter in an isogenic clone. This strategy of catabolite enhanced enzyme expression uncoupled from biomass formation can be applied for cost effective high production of proteins using starch or molasses.     

Influence of calcium on alginate production and composition in continuous cultures of Azotobacter vinelandii

Summary Azotobacter vinelandii strain E was cultivated in PO ₄ ^-- limited continuous cultures. The influence of growth medium Ca⁺⁺ levels on dry cell weight and alginate production and composition was examined. Low Ca⁺⁺ concentrations (<0.34 mM) were observed to inhibit growth, particularly in cultures maintained at a high dilution rate (D=0.32 hr^-1). In cultures with high levels of polysaccharide (>1.0 g l^-1), the production of alginate with a predominantly heteropolymeric structure was favoured by increasing Ca⁺⁺ levels. In cultures containing less polysaccharide (<1.0 g l^-1) increasing Ca⁺⁺ levels (0.068–0.34 mM Ca⁺⁺) resulted in the production of alginates high in polyguluronate. With further increases in Ca⁺⁺ levels (0.34–2.72 mM Ca⁺⁺) synthesis of alginates with a more heteropolymeric structure occurred. It is proposed that extracellular epimerisation of alginate is influenced by intermolecular associations, the formation of which is mediated by both Ca⁺⁺ concentration and the concentration of the polymer itself.     

Construction of lactose-consuming Saccharomyces cerevisiae for lactose fermentation into ethanol fuel

Two lactose-consuming diploid Saccharomyces cerevisiae strains, AY-51024A and AY-51024M, were constructed by expressing the LAC4 and LAC12 genes of Kluyveromyces marxianus in the host strain AY-5. In AY-51024A, both genes were targeted to the ATH1 and NTH1 gene-encoding regions to abolish the activity of acid/neutral trehalase. In AY-51024M, both genes were respectively integrated into the MIG1 and NTH1 gene-encoding regions to relieve glucose repression. Physiologic studies of the two transformants under anaerobic cultivations in glucose and galactose media indicated that the expression of both LAC genes did not physiologically burden the cells, except for AY-51024A in glucose medium. Galactose consumption was initiated at higher glucose concentrations in the MIG1 deletion strain AY-51024M than in the corresponding wild-type strain and AY-51024A, wherein galactose was consumed until glucose was completely depleted in the mixture. In lactose medium, the Sp. growth rates of AY-51024A and AY-51024M under anaerobic shake-flasks were 0.025 and 0.067 h^?1, respectively. The specific lactose uptake rate and ethanol production of AY-51024M were 2.50 g lactose g CDW^?1 h^?1 and 23.4 g l^?1, respectively, whereas those of AY-51024A were 0.98 g lactose g CDW^?1 h^?1 and 24.3 g lactose g CDW^?1 h^?1, respectively. In concentrated cheese whey powder solutions, AY-51024M produced 63.3 g l^?1 ethanol from approximately 150 g l^?1 initial lactose in 120 h, conversely, AY-51024A consumed 63.7 % of the initial lactose and produced 35.9 g l^?1 ethanol. Therefore, relieving glucose repression is an effective strategy for constructing lactose-consuming S. cerevisiae.     

Improvement of l-lactic acid production by osmotic-tolerant mutant of Lactobacillus casei at high temperature

l-Lactic acid production by Lactobacillus casei was used as a model to study the mechanism of substrate inhibition and the strategy for enhancing l-lactic acid production. It was found that the concentration of cell growth and l-lactate decreased with the increase of glucose concentration and fermentation temperature. To enhance the osmotic stress resistance of the strain at high temperature, a mutant G-03 was screened and selected with 360?g/L glucose at 45°C as the selective criterion. To further increase the cell growth for lactic acid production, 3?g/L of biotin was supplemented to the medium. As a result, l-lactate concentration by the mutant G-03 reached 198.2?g/L (productivity of 5.5?g?L^?1?h^?1) at 41°C in a 7-L fermentor with 210?g/L glucose as carbon source. l-Lactate concentration and productivity of mutant G-03 were 115.2% and 97.8% higher than those of the parent strain, respectively. The strategy for enhancing l-lactic acid production by increasing osmotic stress resistance at high temperature may provide an alternative approach to enhance organic acid production with other strains.     

Isolation and characterisation of lactic acid bacterium for effective fermentation of cellobiose into optically pure homo <Emphasis Type="SmallCaps">l</Emphasis>-(+)-lactic acid

Effective utilisation of cellulosic biomasses for economical lactic acid production requires a microorganism with potential ability to utilise efficiently its major components, glucose and cellobiose. Amongst 631 strains isolated from different environmental samples, strain QU 25 produced high yields of l-(+)-lactic acid of high optical purity from cellobiose. The QU 25 strain was identified as Enterococcus mundtii based on its sugar fermentation pattern and 16S rDNA sequence. The production of lactate by fermentation was optimised for the E. mundtii QU25 strain. The optimal pH and temperature for batch culturing were found to be 7.0°C and 43°C, respectively. E. mundtii QU 25 was able to metabolise a mixture of glucose and cellobiose simultaneously without apparent carbon catabolite repression. Moreover, under the optimised culture conditions, production of optically pure l-lactic acid (99.9%) increased with increasing cellobiose concentrations. This indicates that E. mundtii QU 25 is a potential candidate for effective lactic acid production from cellulosic hydrolysate materials.     

Kissiris: A mineral support for the promotion of ethanol fermentation by Saccharomyces cerevisiae

Ethanol production using Saccharomyces cerevisiae, promoted by the mineral kissiris, is reported on. A three-fold increase of ethanol productivity in the fermentation of molasses was achieved. An ethanol yield factor 0.43 g/g and conversion of 93.3% at an initial sugar concentration (ISC) 208.5 g/l were obtained in the presence of this mineral in molasses fermentation, compared to 0.21 g/g and 44.2% in its absence. It is also shown that the fermentation of molasses takes place even at relatively higher ethanol levels, with kissiris contributing to a 35% reduction of the energy demand in grade-fuel and potable ethanol production. The proposed mineral was shown to have a smaller effect in fermentations carried out in synthetic media containing glucose or saccharose.     

Efficient production of l-lactic acid by newly isolated thermophilic Bacillus coagulans WCP10-4 with high glucose tolerance

A thermophilic Bacillus coagulans WCP10-4 with tolerance to high concentration of glucose was isolated from soil and used to produce optically pure l-lactic acid from glucose and starch. In batch fermentation at pH?6.0, 240 g/L of glucose was completely consumed giving 210 g/L of l-lactic acid with a yield of 95 % and a productivity of 3.5 g/L/h. In simultaneous saccharification and fermentation at 50 °C without sterilizing the medium, 200 g/L of corn starch was completely consumed producing 202.0 g/L of l-lactic acid. To the best of our knowledge, this strain shows the highest osmotic tolerance to glucose among the strains ever reported for lactic acid production. This is the first report of simultaneous saccharification and fermentation of starch for lactic acid production under a non-sterilized condition.     

Fermentation of sugar mixtures using Escherichia coli catabolite repression mutants engineered for production of L-lactic acid

Conversion of lignocellulose to lactic acid requires strains capable of fermenting sugar mixtures of glucose and xylose. Recombinant Escherichia coli strains were engineered to selectively produce L-lactic acid and then used to ferment sugar mixtures. Three of these strains were catabolite repression mutants (ptsG ⁻) that have the ability to simultaneously ferment glucose and xylose. The best results were obtained for ptsG ⁻ strain FBR19. FBR19 cultures had a yield of 0.77 (g lactic acid/g added sugar) when used to ferment a 100 g/l total equal mixture of glucose and xylose. The strain also consumed 75% of the xylose. In comparison, the ptsG ⁺ strains had yields of 0.47–0.48 g/g and consumed 18–22% of the xylose. FBR19 was subsequently used to ferment a variety of glucose (0–40 g/l) and xylose (40 g/l) mixtures. The lactic acid yields ranged from 0.74 to 1.00 g/g. Further experiments were conducted to discover the mechanism leading to the poor yields for ptsG ⁺ strains. Xylose isomerase (XI) activity, a marker for induction of xylose metabolism, was monitored for FBR19 and a ptsG ⁺ control during fermentations of a sugar mixture. Crude protein extracts prepared from FBR19 had 10–12 times the specific XI activity of comparable samples from ptsG ⁺ strains. Therefore, higher expression of xylose metabolic genes in the ptsG ⁻ strain may be responsible for superior conversion of xylose to product compared to the ptsG ⁺ fermentations. Received 14 December 2000/ Accepted in revised form 28 June 2002     

The effect of hexose ratios on metabolite production in Saccharomyces cerevisiae strains obtained from the spontaneous fermentation of mezcal

Mezcal from Tamaulipas (México) is produced by spontaneous alcoholic fermentation using Agave spp. musts, which are rich in fructose. In this study eight Saccharomyces cerevisiae isolates obtained at the final stage of fermentation from a traditional mezcal winery were analysed in three semi-synthetic media. Medium M1 had a sugar content of 100 g l^?1 and a glucose/fructose (G/F) of 9:1. Medium M2 had a sugar content of 100 g l^?1 and a G/F of 1:9. Medium M3 had a sugar content of 200 g l^?1 and a G/F of 1:1. In the three types of media tested, the highest ethanol yield was obtained from the glucophilic strain LCBG-3Y5, while strain LCBG-3Y8 was highly resistant to ethanol and the most fructophilic of the mezcal strains. Strain LCBG-3Y5 produced more glycerol (4.4 g l^?1) and acetic acid (1 g l^?1) in M2 than in M1 (1.7 and 0.5 g l^?1, respectively), and the ethanol yields were higher for all strains in M1 except for LCBG-3Y5, -3Y8 and the Fermichamp strain. In medium M3, only the Fermichamp strain was able to fully consume the 100 g of fructose l^?1 but left a residual 32 g of glucose l^?1. Regarding the hexose transporters, a high number of amino acid polymorphisms were found in the Hxt1p sequences. Strain LCBG-3Y8 exhibited eight unique amino acid changes, followed by the Fermichamp strain with three changes. In Hxt3p, we observed nine amino acid polymorphisms unique for the Fermichamp strain and five unique changes for the mezcal strains.     

Construction of industrial baker's yeast strains able to assimilate maltose under catabolite repression conditions

Spore progeny from an industrial baker's yeast strain were mutagenized with UV and mutants resistant to 2-deoxyglucose isolated. One of these mutants (10a12–13) showed high levels of maltase (-glucosidase) and external invertase, and assimilated maltose when growing under catabolite repression conditions. This mutant was not allelic to any of the catabolite repression mutants tested cat4, cat80, cid1, cyc8, hex2, hxk2 and tup1. Mutant 10a12–13 was crossed with appropriate strains to construct hybrids that were also able to assimilate maltose in the presence of glucose. These hybrids may be useful in fermentation processes where both glucose and maltose are present.     

Production of acetone-butanol by extractive fermentation using dibutylphthalate as extractant

Extractive fermentation of glucose, glucose-xylose mixtures and hydrolysates of lignocellulosics to acetone-butanol solvents were studied and compared with similar fermentations in the absence of extractant. The extractant selected for this research was dibutylphthalate which, in addition to having satisfactory physical properties for this purpose, is non-toxic and mildly stimulating to the growth of the organism used, Clostridium acetobutylicum P262. Sugar concentrations mainly in the range of 80 to 100 g/l resulted in solvent concentrations of 28 to 30 g/l in 24 h extractive fermentations, compared to 18 to 20 g/l for non-extractive control fermentations. Conversion factors of 0.33 to 0.37 g solvents/g sugar consumed were obtained. Rapid fermentation was achieved by high cell concentrations and cell recycle from each 24 h fermentation to the succeeding similar 24 h fermentation. Somewhat higher nutrients were also helpful. By this means, 255 l of acetone-butanol solvents were obtained per tonne of aspen wood, 298 l per tonne of pine and 283 l per tonne of corn stover. Such high product yields from inexpensive substrates offer the prospect of economic viability for the process.     

beta-Carotene production in sugarcane molasses by a Rhodotorula glutinis mutant

Several wild strains and mutants of Rhodotorula spp. were screened for growth, carotenoid production and the proportion of -carotene produced in sugarcane molasses. A better producer, Rhodotorula glutinis mutant 32, was optimized for carotenoid production with respect to total reducing sugar (TRS) concentration and pH. In shake flasks, when molasses was used as the sole nutrient medium with 40 g l⁻¹ TRS, at pH 6, the carotenoid yield was 14 mg l⁻¹ and -carotene accounted for 70% of the total carotenoids. In a 14-l stirred tank fermenter, a 20% increase in torulene content was observed in plain molasses medium. However, by addition of yeast extract, this effect was reversed and a 31% increase in -carotene content was observed. Dissolved oxygen (DO) stat fed-batch cultivation of mutant 32 in plain molasses medium yielded 71 and 185 mg l⁻¹ total carotenoids in double- and triple-strength medium, respectively. When supplemented with yeast extract, the yields were 97 and 183 mg l⁻¹ total carotenoid with a 30% increase in -carotene and a simultaneous 40% decrease in torulene proportion. Higher cell mass was also achieved by double- and triple-strength fed-batch fermentation. Journal of Industrial Microbiology & Biotechnology (2001) 26, 327–332. Received 18 September 2000/ Accepted in revised form 02 March 2001     

The production of 2,3-butanediol by fermentation of high test molasses

Summary Klebsiella oxytoca fermented 199 g·l^–1 high test or invert molasses using batch fermentation with substrate shift to produce 95.2–98.6 g 2,3-butanediol·l^–1 and 2,4–4.3 g acetoin·l^–1 with a diol yield of 96–100% of the theoretical value and a diol productivity of 1.0–1.1 g·l^–1·h^–1. Fermentation was performed numerous times with molasses in repeated batch culture with cell recovery. Such repeated batch fermentation, in addition to a high product yield, also showed a very high product concentration. For example, 118 g 2,3-butanediol·l^–1 and 2.3 g acetoin·l^–1 were produced from 280 g·l^–1 of high test molasses. The diol productivity in this fermentation amounted to 2.4 g·l^–1·h^–1 and can undoubtedly be further increased by increasing the cell concentration. Because the Klebsiella cultures ferment 2,3-butanediol at an extremely high rate once the sugar has been consumed, the culture was inhibited completely by the addition of 15 g ethanol·l^–1 and switching off aeration. Offprint requests to: A. S. Afschar     

Production of erythritol from glucose by an osmophilic mutant of Candida magnoliae

Candida magnoliae and its mutants were analyzed to produce erythritol from glucose with high yield and productivity. One mutant, M2, showed higher erythritol conversion yield and productivity than the wild strain. The osmophilic mutant produced 25 g erythritol l^–1 after 83 h of a flask culture in a medium containing 10% (w/v) glucose, corresponding to a 25% increase in erythritol and a 30% increase in erythritol productivity compared with the wild type. The fermentation properties were further improved by cultivating the osmophilic mutant in a fermenter containing 20% (w/v) glucose medium with 0.54 g l^–1 h^–1 of erythritol productivity and 43% of erythritol conversion yield based on glucose.