Biotechnological Process for Production of β-Dipeptides from Cyanophycin on a Technical Scale and Its Optimization

A triphasic process was developed for the production of β dipeptides from cyanophycin (CGP) on a large scale. Phase I comprises an optimized acid extraction method for technical isolation of CGP from biomass. It yielded highly purified CGP consisting of aspartate, arginine, and a little lysine. Phase II comprises the fermentative production of an extracellular CGPase (CphE_al) from Pseudomonas alcaligenes strain DIP1 on a 500-liter scale in mineral salts medium, with citrate as the sole carbon source and CGP as an inductor. During optimization, it was shown that 2 g liter⁻¹ citrate, pH 6.5, and 37°C are ideal parameters for CphE_al production. Maximum enzyme yields were obtained after induction in the presence of 50 mg liter⁻¹ CGP or CGP dipeptides for 5 or 3 h, respectively. Aspartate at a concentration of 4 g liter⁻¹ induced CphE_al production with only about 30% efficiency in comparison to that with CGP. CphE_al was purified utilizing its affinity for the substrate and its specific binding to CGP. CphE_al turned out to be a serine protease with maximum activity at 50°C and at pH 7 to 8.5. Phase III comprises degradation of CGP to β-aspartate-arginine and β-aspartate-lysine dipeptides with a purity of over 99% (by thin-layer chromatography and high-performance liquid chromatography), employing a crude CphE_al preparation. Optimum degradation parameters were 100 g liter⁻¹ CGP, 10 g liter⁻¹ crude CphE_al powder, and 4 h of incubation at 50°C. The overall efficiency of phase III was 91%, while 78% (wt/wt) of the used CphE_al powder with sustained activity toward CGP was recovered. The optimized process was performed with industrial materials and equipment and is applicable to any desired scale.     

Isolation of cyanophycin-degrading bacteria, cloning and characterization of an extracellular cyanophycinase gene (cphE) from Pseudomonas anguilliseptica strain BI. The cphE gene from P. anguilliseptica BI encodes a cyanophycinhydrolyzing enzyme

Eleven bacteria capable of utilizing cyanophycin (cyanophycin granule polypeptide (CGP)) as a carbon source for growth were isolated. One isolate was taxonomically affiliated as Pseudomonas anguilliseptica strain BI, and the extracellular cyanophycinase (CphE) was studied because utilization of cyanophycin as a carbon source and extracellular cyanophycinases were hitherto not described. CphE was detected in supernatants of CGP cultures and purified from a corresponding culture of strain BI employing chromatography on the anion exchange matrix Q-Sepharose and on an arginine-agarose affinity matrix. The mature form of the inducible enzyme consisted of one type of subunit with M(r) = 43,000 and exhibited high specificity for CGP, whereas proteins and synthetic polyaspartic acid were not hydrolyzed or were only marginally hydrolyzed. Degradation products of the enzyme reaction were identified as aspartic acid-arginine dipeptides (beta-Asp-Arg) by high performance liquid chromatography and electrospray ionization mass spectrometry. The corresponding gene (cphE, 1254 base pairs) was identified in subclones of a cosmid gene library of strain BI by heterologous active expression in Escherichia coli, and its nucleotide sequence was determined. The enzyme exhibited only 27-28% amino acid sequence identity to intracellular cyanophycinases occurring in cyanobacteria. Analysis of the amino acid sequence of cphE revealed a putative catalytic triad consisting of the motif GXSXG plus a histidine and most probably a glutamate residue. In addition, the strong inhibition of the enzyme by Pefabloc((R)) and phenylmethylsulfonyl fluoride indicated that the catalytic mechanism of CphE is related to that of serine type proteases. Quantitative analysis on the release of beta-Asp-Arg dipeptides from C-terminal labeled CGP gave evidence for an exo-degradation mechanism.     

Role of the Bacillus methanolicus citrate synthase II gene,citY, in regulating the secretion of glutamate in L-lysine-secreting mutants

The thermotolerant, restrictive methylotroph Bacillus methanolicus MGA3 (ATCC 53907) can secrete 55 g of glutamate per liter (maximum yield, 0.36 g/g) at 50 degrees C with methanol as a carbon source and a source of ammonia in fed-batch bioreactors. A homoserine dehydrogenase mutant, 13A52-8A66, secreting up to 35 g of L-lysine per liter in fed-batch fermentations had minimal 2-oxoglutarate dehydrogenase activity [7.3 nmol min(-1) (mg of protein)(-1)], threefold-increased pyruvate carboxylase activity [535 nmol min(-1) (mg of protein)(-1)], and elevated citrate synthase (CS) activity [292 nmol min(-1) (mg of protein)(-1)] and simultaneously secreted glutamate (20 to 30 g per liter) and L-lysine. The flow of carbon from oxaloacetate is split between transamination to aspartate and formation of citrate. To investigate the regulation of this branch point, the B. methanolicus gene citY encoding a CSII protein with activity at 50 degrees C was cloned from 13A52-8A66 into a CS-deficient Escherichia coli K2-1-4 strain. A citY-deficient B. methanolicus mutant, NCS-L-7, was also isolated from the parent strain of 13A52-8A66 by N-methyl-N'-nitro-N-nitrosoguanidine mutagenesis, followed by selection with monofluoroacetate disks on glutamate plates. Characterization of these strains confirmed that citY in strain 13A52-8A66 was not altered and that B. methanolicus possessed several forms of CS. Analysis of citY cloned from NCS-L-7 showed that the reduced CS activity resulted from a frameshift mutation. The level of glutamate secreted by NCS-L-7 was reduced sevenfold and the ratio of L-lysine to glutamate secreted was increased 4.5-fold compared to the wild type in fed-batch cultures with glutamate feeding. This indicates that glutamate secretion in L-lysine-overproducing mutants can be altered in favor of increased L-lysine secretion by regulating in vivo CS activity.     

Isomaltose production by modification of the fructose-binding site on the basis of the predicted structure of sucrose isomerase from "Protaminobacter rubrum"

"Protaminobacter rubrum" sucrose isomerase (SI) catalyzes the isomerization of sucrose to isomaltulose and trehalulose. SI catalyzes the hydrolysis of the glycosidic bond with retention of the anomeric configuration via a mechanism that involves a covalent glycosyl enzyme intermediate. It possesses a (325)RLDRD(329) motif, which is highly conserved and plays an important role in fructose binding. The predicted three-dimensional active-site structure of SI was superimposed on and compared with those of other alpha-glucosidases in family 13. We identified two Arg residues that may play important roles in SI-substrate binding with weak ionic strength. Mutations at Arg(325) and Arg(328) in the fructose-binding site reduced isomaltulose production and slightly increased trehalulose production. In addition, the perturbed interactions between the mutated residues and fructose at the fructose-binding site seemed to have altered the binding affinity of the site, where glucose could now bind and be utilized as a second substrate for isomaltose production. From eight mutant enzymes designed based on structural analysis, the R(325)Q mutant enzyme exhibiting high relative activity for isomaltose production was selected. We recorded 40.0% relative activity at 15% (wt/vol) additive glucose with no temperature shift; the maximum isomaltose concentration and production yield were 57.9 g liter(-1) and 0.55 g of isomaltose/g of sucrose, respectively. Furthermore, isomaltose production increased with temperature but decreased at a temperature of >35 degrees C. Maximum isomaltose production (75.7 g liter(-1)) was recorded at 35 degrees C, and its yield for the consumed sucrose was 0.61 g g(-1) with the addition of 15% (wt/vol) glucose. The relative activity for isomaltose production increased progressively with temperature and reached 45.9% under the same conditions.     

Increased Lysine Content Is the Main Characteristic of the Soluble Form of the Polyamide Cyanophycin Synthesized by Recombinant Escherichia coli

Cyanophycin, a polyamide of cyanobacterial or noncyanobacterial origin consisting of aspartate, arginine, and lysine, was synthesized in different recombinant strains of Escherichia coli expressing cphA from Synechocystis sp. strain PCC 6308 or PCC 6803, Anabaena sp. strain PCC 7120, or Acinetobacter calcoaceticus ADP1. The molar aspartate/arginine/lysine ratio of the water-soluble form isolated from a recombinant strain expressing CphA₆₃₀₈ was 1:0.5:0.5, with a lysine content higher than any ever described before. The water-insoluble form consisted instead of mainly aspartate and arginine residues and had a lower proportion of lysine, amounting to a maximum of only 5 mol%. It could be confirmed that the synthesis of soluble cyanobacterial granule polypeptide (CGP) is independent of the origin of cphA. Soluble CGP isolated from all recombinant strains contained a least 17 mol% lysine. The total CGP portion of cell dry matter synthesized by CphA₆₃₀₈ from recombinant E. coli was about 30% (wt/wt), including 23% (wt/wt) soluble CGP, by using terrific broth complex medium for cultivation at 30°C for 72 h. Enhanced production of soluble CGP instead of its insoluble form is interesting for further application and makes recombinant E. coli more attractive as a suitable source for the production of polyaspartic acid or dipeptides. In addition, a new low-cost, time-saving, effective, and common isolation procedure for mainly soluble CGP, suitable for large-scale application, was established in this study.     

Stable production of cyanophycinase in Nicotiana benthamiana and its functionality to hydrolyse cyanophycin in the murine intestine

Food supplementation with the conditionally essential amino acid arginine (Arg) has been shown to have nutritional benefits. Degradation of cyanophycin (CGP), a peptide polymer used for nitrogen storage by cyanobacteria, requires cyanophycinase (CGPase) and results in the release of β‐aspartic acid (Asp)‐Arg dipeptides. The simultaneous production of CGP and CGPase in plants could be a convenient source of Arg dipeptides. Different variants of the cphB coding region from Thermosynechococcus elongatus BP‐1 were transiently expressed in Nicotiana benthamiana plants. Translation and enzyme stability were optimized to produce high amounts of active CGPase. Protein stability was increased by the translational fusion of CGPase to the green fluorescent protein (GFP) or to the transit peptide of the small subunit of RuBisCO for peptide production in the chloroplasts. Studies in mice showed that plant‐expressed CGP fed in combination with plant‐made CGPase was hydrolysed in the intestine, and high levels of ß‐Asp‐Arg dipeptides were found in plasma, demonstrating dipeptide absorption. However, the lack of an increase in Asp and Arg or its metabolite ornithine in plasma suggests that Arg from CGP was not bioavailable in this mouse group. Intestinal degradation of CGP by CGPase led to low intestinal CGP content 4 h after consumption, but after ingestion of CGP alone, high CGP concentrations remained in the large intestine; this indicated that intact CGP was transported from the small to the large intestine and that CGP was resistant to colonic microbes.     

High cell density cultivation of Rhodococcus opacus for lipid production at a pilot-plant scale

The triacylglycerol (TAG)-accumulating bacterium Rhodococcus opacus strain PD630 was investigated with respect to the fermentative production of TAGs consisting of an unusually high fraction of fatty acids with an odd-number of carbon atoms and unsaturated monoenic fatty acids from sugar beet molasses and sucrose. Fed-batch fermentations were optimized at the 30-1 scale in a stirred tank bioreactor at 30 degrees C using a mineral salts medium, which contained sugar beet molasses and sucrose as sole carbon sources. Approximately 37.5 g cell dry matter (CDM) per liter was the highest cell density that was obtained at that scale with a TAG content in the cells of 52%. This fermentative process was also applied to a 500-1 pilot-plant scale. Cell densities as high as 18.4 g CDM per liter were obtained, and 42% of the sucrose present in the medium was converted into cell mass which consisted of 38.4% TAGs.     

Ethanol stimulates glycogenolysis in livers from fed rats.

To determine the reason for the lack of a hypoglycemic effect of ethanol in the fed state, the effect of ethanol on glucose turnover, liver glycogenolysis, and glucose metabolites was determined. Chronically catheterized awake and freely moving fed rats received either ethanol (blood ethanol, 37 +/- 10 mmol/liter, n = 11) or saline (n = 13) intravenously for 4 hr. Glucose turnover was determined using a primed continuous infusion of [3-3H]glucose. The liver was freeze clamped at 4 hr for glycogen and metabolite measurements. Plasma glucose (5.8 +/- 0.3 mmol/liter vs 6.3 +/- 0.2 mmol/liter at 4 hr, ethanol versus saline) and the rate of glucose turnover (61 +/- 9 vs 58 +/- 8 moles/kg.min) were similar during the ethanol and saline infusions. Plasma lactate was significantly higher in the ethanol (1.32 +/- 0.05 mmol/liter) than in the saline (0.86 +/- 0.06 mmol/liter, P less than 0.001) study. Concentrations of gluconeogenic intermediates in the liver (glucose 6-phosphate, fructose 6-phosphate, glucose 1-phosphate, and pyruvate) were all significantly and -30% lower in ethanol-infused than in saline-infused rats. The liver citrate content was similar in ethanol-infused than in saline-infused rats. The liver citrate content was similar in ethanol (0.38 +/- 0.03 mmol/liter) and saline (0.37 +/- 0.04 mmol/liter) studies. Liver glycogen was 75% lower in the ethanol-infused (61 +/- 9 mmol/kg dry wt) than the saline (242 +/- 27 mmol/kg dry wt, P less than 0.001)-infused rats. These data demonstrate that in fed rats given ethanol, glucose turnover is maintained constant by accelerated glycogenolysis. Thus, inhibition of gluconeogenesis by ethanol does not lower hepatic glucose production unless compensatory glycogenolysis can be prevented.     

Excessive excretion of cyclic beta-(1,2)-glucan by Rhizobium trifolii TA-1.

At 25 degrees C, the optimal temperature for growth of Rhizobium trifolii TA-1, extracellular and capsular polysaccharide (EPS and CPS) were the main carbohydrate products synthesized in mannitol-rich medium (10 g of mannitol and 1 g of glutamic acid per liter). In the same medium at 33 degrees C, EPS and CPS production was inhibited, and up to 3.9 g of cyclic beta-(1,2)-glucan was produced during an incubation period of 20 days with a total biomass of 0.55 g of protein. In a medium containing 50 g of mannitol and 10 g of glutamic acid per liter, high cell densities (3.95 g of protein) were obtained at 25 degrees C. This biomass excreted 10.9 g of cyclic beta-(1,2)-glucan within 10 days. Concomitantly, 4.8 g of EPS were synthesized, while CPS production was strongly suppressed. The excreted cyclic beta-(1,2)-glucans were neutral and had degrees of polymerization ranging from 17 to 25, with a degree of polymerization of 19 as the major glucan cycle.     

Excessive excretion of cyclic beta-(1,2)-glucan by Rhizobium trifolii TA-1

At 25 degrees C, the optimal temperature for growth of Rhizobium trifolii TA-1, extracellular and capsular polysaccharide (EPS and CPS) were the main carbohydrate products synthesized in mannitol-rich medium (10 g of mannitol and 1 g of glutamic acid per liter). In the same medium at 33 degrees C, EPS and CPS production was inhibited, and up to 3.9 g of cyclic beta-(1,2)-glucan was produced during an incubation period of 20 days with a total biomass of 0.55 g of protein. In a medium containing 50 g of mannitol and 10 g of glutamic acid per liter, high cell densities (3.95 g of protein) were obtained at 25 degrees C. This biomass excreted 10.9 g of cyclic beta-(1,2)-glucan within 10 days. Concomitantly, 4.8 g of EPS were synthesized, while CPS production was strongly suppressed. The excreted cyclic beta-(1,2)-glucans were neutral and had degrees of polymerization ranging from 17 to 25, with a degree of polymerization of 19 as the major glucan cycle.     

Protamylasse, a residual compound of industrial starch production, provides a suitable medium for large-scale cyanophycin production

Protamylasse is a residual compound occurring during the industrial production of starch from potatoes. It contains a variety of nutrients and all necessary minerals and could be used as a carbon, nitrogen, and energy source for the growth of bacteria and also for cyanophycin (CGP) biosynthesis. Media containing protamylasse as the sole compound diluted only in water were therefore examined for their suitability in CGP production. Among various bacterial strains investigated in this study, a recombinant strain of Escherichia coli DH1 harboring plasmid pMa/c5-914::cphA6803, which carries the cyanophycin synthetase structural gene (cphA) from Synechocystis sp. strain PCC6803, was found to be most suitable. Various cultivation conditions for high CGP contents were first optimized in shake flask cultures. The optimized conditions were then successfully applied to 30- and 500-liter fermentation scales in stirred tank reactors. A maximum CGP content of 28% (wt/wt) CGP per cell dry matter was obtained in 6% (vol/vol) protamylasse medium at an initial pH of 7.0 within a cultivation period of only 24 h. The CGP contents obtained with this recombinant strain employing protamylasse medium were higher than those obtained with the same strain cultivated in mineral salts medium or in expensive commercial complex media such as Luria-Bertani or Terrific broth. It was shown that most amino acids present in the protamylasse medium were almost completely utilized by the cells during cultivation. Exceptions were alanine, tryptophan, tyrosine, and most interestingly, arginine. Furthermore, CGP was easily isolated from protamylasse-grown cells by applying the acid extraction method. The CGP exhibited a molecular mass of about 26 to 30 kDa and was composed of 50% (mol/mol) aspartate, 46% (mol/mol) arginine, and 4% (mol/mol) lysine. The use of cheap residual protamylasse could contribute in establishing an economically and also ecologically feasible process for the biotechnological production of CGP.     

Single cell oil (SCO) production by Mortierella isabellina grown on high-sugar content media

Mortierella isabellina cultivated in nitrogen-limited media presented remarkable cell growth (up to 35.9 g/l) and high glucose uptake even with high initial sugar concentrations (e.g. 100 g/l) in media. After nitrogen depletion, significant fat quantities were accumulated inside the fungal mycelia (50-55%, wt/wt oil in dry biomass), resulting in a notable single cell oil production of 18.1 g/l of culture medium. Total dry biomass and lipid yields presented greatly increased values (0.34 and 0.17 g respectively per gram of glucose consumed). The microbial lipid produced contained gamma-linolenic acid (GLA) at a concentration of 3.5+/-1.0%, wt/wt, which corresponded to 16-19 mg GLA per gram of dry microbial mass and a maximum concentration of 0.801 g GLA per liter of culture medium.     

Highly efficient biotransformation of eugenol to ferulic acid and further conversion to vanillin in recombinant strains of Escherichia coli

The vaoA gene from Penicillium simplicissimum CBS 170.90, encoding vanillyl alcohol oxidase, which also catalyzes the conversion of eugenol to coniferyl alcohol, was expressed in Escherichia coli XL1-Blue under the control of the lac promoter, together with the genes calA and calB, encoding coniferyl alcohol dehydrogenase and coniferyl aldehyde dehydrogenase of Pseudomonas sp. strain HR199, respectively. Resting cells of the corresponding recombinant strain E. coli XL1-Blue(pSKvaomPcalAmcalB) converted eugenol to ferulic acid with a molar yield of 91% within 15 h on a 50-ml scale, reaching a ferulic acid concentration of 8.6 g liter(-1). This biotransformation was scaled up to a 30-liter fermentation volume. The maximum production rate for ferulic acid at that scale was 14.4 mmol per h per liter of culture. The maximum concentration of ferulic acid obtained was 14.7 g liter(-1) after a total fermentation time of 30 h, which corresponded to a molar yield of 93.3% with respect to the added amount of eugenol. In a two-step biotransformation, E. coli XL1-Blue(pSKvaomPcalAmcalB) was used to produce ferulic acid from eugenol and, subsequently, E. coli(pSKechE/Hfcs) was used to convert ferulic acid to vanillin (J. Overhage, H. Priefert, and A. Steinbüchel, Appl. Environ. Microbiol. 65:4837-4847, 1999). This process led to 0.3 g of vanillin liter(-1), besides 0.1 g of vanillyl alcohol and 4.6 g of ferulic acid liter(-1). The genes ehyAB, encoding eugenol hydroxylase of Pseudomonas sp. strain HR199, and azu, encoding the potential physiological electron acceptor of this enzyme, were shown to be unsuitable for establishing eugenol bioconversion in E. coli XL1-Blue.     

Protamylasse, a Residual Compound of Industrial Starch Production, Provides a Suitable Medium for Large-Scale Cyanophycin Production

Protamylasse is a residual compound occurring during the industrial production of starch from potatoes. It contains a variety of nutrients and all necessary minerals and could be used as a carbon, nitrogen, and energy source for the growth of bacteria and also for cyanophycin (CGP) biosynthesis. Media containing protamylasse as the sole compound diluted only in water were therefore examined for their suitability in CGP production. Among various bacterial strains investigated in this study, a recombinant strain of Escherichia coli DH1 harboring plasmid pMa/c5-914::cphA₆₈₀₃, which carries the cyanophycin synthetase structural gene (cphA) from Synechocystis sp. strain PCC6803, was found to be most suitable. Various cultivation conditions for high CGP contents were first optimized in shake flask cultures. The optimized conditions were then successfully applied to 30- and 500-liter fermentation scales in stirred tank reactors. A maximum CGP content of 28% (wt/wt) CGP per cell dry matter was obtained in 6% (vol/vol) protamylasse medium at an initial pH of 7.0 within a cultivation period of only 24 h. The CGP contents obtained with this recombinant strain employing protamylasse medium were higher than those obtained with the same strain cultivated in mineral salts medium or in expensive commercial complex media such as Luria-Bertani or Terrific broth. It was shown that most amino acids present in the protamylasse medium were almost completely utilized by the cells during cultivation. Exceptions were alanine, tryptophan, tyrosine, and most interestingly, arginine. Furthermore, CGP was easily isolated from protamylasse-grown cells by applying the acid extraction method. The CGP exhibited a molecular mass of about 26 to 30 kDa and was composed of 50% (mol/mol) aspartate, 46% (mol/mol) arginine, and 4% (mol/mol) lysine. The use of cheap residual protamylasse could contribute in establishing an economically and also ecologically feasible process for the biotechnological production of CGP.     

Efficient production of L-ribose with a recombinant Escherichia coli biocatalyst

A new synthetic platform with potential for the production of several rare sugars, with l-ribose as the model target, is described. The gene encoding the unique NAD-dependent mannitol-1-dehydrogenase (MDH) from Apium graveolens (garden celery) was synthetically constructed for optimal expression in Escherichia coli. This MDH enzyme catalyzes the interconversion of several polyols and their l-sugar counterparts, including the conversion of ribitol to l-ribose. Expression of recombinant MDH in the active form was successfully achieved, and one-step purification was demonstrated. Using the created recombinant E. coli strain as a whole-cell catalyst, the synthetic utility was demonstrated for production of l-ribose, and the system was improved using shaken flask experiments. It was determined that addition of 50 to 500 microM ZnCl(2) and addition of 5 g/liter glycerol both improved production. The final levels of conversion achieved were >70% at a concentration of 40 g/liter and >50% at a concentration of 100 g/liter. The best conditions determined were then scaled up to a 1-liter fermentation that resulted in 55% conversion of 100 g/liter ribitol in 72 h, for a volumetric productivity of 17.4 g liter(-1) day(-1). This system represents a significantly improved method for the large-scale production of l-ribose.     

Physiological conditions conducive to high cyanophycin content in biomass of Acinetobacter calcoaceticus strain ADP1

The effects of the inorganic medium components, the initial pH, the incubation temperature, the oxygen supply, the carbon-to-nitrogen ratio, and chloramphenicol on the synthesis of cyanophycin (CGP) by Acinetobacter calcoaceticus strain ADP1 were studied in a mineral salts medium containing sodium glutamate and ammonium sulfate as carbon and nitrogen sources, respectively. Variation of all these factors resulted in maximum CGP contents of only about 3.5% (wt/wt) of the cell dry matter (CDM), and phosphate depletion triggered CGP accumulation most substantially. However, addition of arginine to the medium as the sole carbon source for growth promoted CGP accumulation most strikingly. This effect was systematically studied, and an optimized phosphate-limited medium containing 75 mM arginine and 10 mM ammonium sulfate yielded a CGP content of 41.4% (wt/wt) of the CDM at 30 degrees C. The CGP content of the cells was further increased to 46.0% (wt/wt) of the CDM by adding 2.5 microg of chloramphenicol per ml of medium in the accumulation phase. These contents are by far the highest CGP contents of bacterial cells ever reported. CGP was easily isolated from the cells by using an acid extraction method, and this CGP contained about equimolar amounts of aspartic acid and arginine and no detectable lysine; the molecular masses ranged from 21 to 29 kDa, and the average molecular mass was about 25 kDa. Transmission electron micrographs of thin sections of cells revealed large CGP granules that frequently had an irregular shape with protuberances at the surface and often severely deformed the cells. A cphI::OmegaKm mutant of strain ADP1 with a disrupted putative cyanophycinase gene accumulated significantly less CGP than the wild type accumulated, although the cells expressed cyanophycin synthetase at about the same high level. It is possible that the intact CphI protein is involved in the release of CGP primer molecules from initially synthesized CGP. The resulting lower concentration of primer molecules could explain the observed low rate of accumulation at similar specific activities.     

Formation of 2,5-Bis-(d-threo-trihydroxypropyl)pyrazine and Its 6-Isomer by the Oxidative Browning Reaction of d-Xylose with Ammonium Acetate in a Methanolic Medium

A pyruvate kinase-lacking mutant of Brevibacterium flavum produced 22.6 g/liter of l-aspartic acid with glutamic acid as a by-product, when cultured for 48 hr in a medium containing 100 g/liter of glucose. The production clearly depended on the amount of biotin added. This strain, 70, was derived by several steps of mutation from wild strain 2247 producing glutamate, successively via a citrate synthase-defective glutamate auxotroph, strain 214, a prototrophic revertant, strain 15-8, producing 10 g/liter of l-aspartic acid, and an S-(2-aminoethyl)-l-cysteine-resistant mutant, strain 1-231, having low pyruvate kinase and homoserine dehydrogenase and producing lysine. Strain 70, a methionine-insensitive revertant from strain 1-231, had a normal level of homoserine dehydrogenase but no pyruvate kinase. Its citrate synthase activity was about half that of the wild strain at saturated concentrations of the substrates with Michaelis constants for oxalacetate and acetyl-CoA of 110 and 6 times as high as those of the wild-type enzyme, respectively. The mutational step for these alterations in citrate synthase was strain 15-8. Phosphoenolpyruvate carboxylase of strain 70 showed 1.5-fold higher activity in the crude extract at saturated concentrations of phosphoenolpyruvate, a lower Michaelis constant (1.5mM).for the substrate, phosphoenolpyruvate, less sensitivity to the feedback inhibition by aspartate, and higher sensitivities to the activators, acetyl-CoA and fructose-1,6-bisphosphate, than those of the wild strain. The concentrations of aspartate giving 50% inhibition were 6.2- and 4.5-fold higher in the absence and presence of acetyl-CoA, respectively.     

The Effective Production of Shikonin by Cultures with an Increased Cell Population

We have studied the efficient production of shikonin derivatives by suspension cultures of Lithospermum erythrorhizon with an increased cell population. The yield of shikonin derivatives was highest (800 mg/liter) when 2.8 g dry wt/liter of the cells was inoculated into the M-2 medium which we had developed for the production, but the excess inoculum lowered the yield.

We investigated suitable conditions for production with the increased cell population. The optimum amount of inoculum rose to 4.9 g dry wt/liter when the concentrations of all the components contained in the M-8 medium, which we developed for increasing the productivity by modification of the M-2 medium, were increased in proportion to the amount of inoculum, and consequently we could increase the yield of the shikonin derivatives from 1400 mg/liter to 1900 mg/liter. Moreover, the increased rate of oxygen supply in addition to the enrichment of the medium made it possible to produce 2300 mg/liter of the shikonin derivatives from a culture for which 5.6 g dry wt/liter of the cells was inoculated.     

Growth and Polysaccharide Production by Methylocystis parvus OBBP on Methanol

Methylocystis parvus OBBP, an obligate methylotroph originally isolated as a methane-utilizing bacterium, was cultivated on methanol as a sole source of carbon. After adaptation to high methanol levels, this organism grew on methanol with a maximum specific growth rate of 0.65 h. The pH optimum for growth was between 7 and 9, and the temperature optimum was between 30 and 37 degrees C. Methanol concentrations higher than 5% (by weight) were toxic. Formaldehyde, at a concentration greater than 1 mM, inhibited growth. Formate was neither a substrate nor an inhibitor. An extracellular viscous heteropolysaccharide was produced during growth. The maximum production of the total biomass was 14.5 g (dry weight) per liter of broth. The dried biomass contained 22% (wt/wt) crude protein and 62% (wt/wt) polysaccharide. The main components of the polysaccharide were d-glucose (82%) and l-rhamnose (14%).     

Synthesis and accumulation of cyanophycin in transgenic strains of Saccharomyces cerevisiae

Cyanophycin [multi-L-arginyl-poly(L-aspartic acid) (CGP)] was, for the first time, produced in yeast. As yeasts are very important production organisms in biotechnology, it was determined if CGP can be produced in two different strains of Saccharomyces cerevisiae. The episomal vector systems pESC (with the galactose-inducible promoter GAL1) and pYEX-BX (with the copper ion-inducible promoter CUP1) were chosen to express the cyanophycin synthetase gene from the cyanobacterium Synechocystis sp. strain PCC 6308 (cphA(6308)) in yeast. Expression experiments with transgenic yeasts revealed that the use of the CUP1 promoter is much more efficient for CGP production than the GAL1 promoter. As observed by electrophoresis of isolated CGP in sodium dodecyl sulfate-polyacrylamide gels, the yeast strains produced two different types of polymer: the water-soluble and the water-insoluble CGP were observed as major and minor forms of the polymer, respectively. A maximum CGP content of 6.9% (wt/wt) was detected in the cells. High-performance liquid chromatography analysis showed that the isolated polymers consisted mainly of the two amino acids aspartic acid and arginine and that, in addition, a minor amount (2 mol%) of lysine was present. Growth of transgenic yeasts in the presence of 15 mM lysine resulted in an incorporation of up to 10 mol% of lysine into CGP. Anti-CGP antibodies generated against CGP isolated from Escherichia coli TOP10 harboring cphA(6308) reacted with insoluble CGP but not with soluble CGP, if applied in Western or dot blots.