Acetopyruvate hydrolase production by Pseudomonas putida O1--optimization of batch and fed-batch fermentations

The main objective of this work was the optimization of the production of the beta-ketolase, acetopyruvate hydrolase, from Pseudomonas putida O1. Orcinol was used as an inducer for enzyme production. The growth medium was optimized in two steps. In the first step, screening for optimal glucose concentration was performed. In the second step, a central composite design was used to optimize carbon and nitrogen sources in the medium. After this optimization procedure, a medium was obtained which produced seven times more biomass than the initial medium. Acetopyruvate hydrolase enzyme production was optimized by determining the optimal time of feed and amount of orcinol, using statistical methods. In a subsequent step, the maximal orcinol-degradation rate was determined. The results obtained were used to find an optimal feeding profile for enzyme production. By using the optimized fed-batch process, acetopyruvate hydrolase activity was enhanced from 10 units l(-1)to 400 units l(-1), in comparison with previously reported fermentation experiments. Productivity could even be increased by a factor of 75, to a value of 20 units l(-1 )h(-1).     

Integrated approach for production of recombinant acetylacetone dioxygenase from Acinetobacter johnsonii

The C–C bond-cleaving acetylacetone dioxygenase Dke1 (EC 1.13.11.50) is a Fe^2?+?-dependent enzyme from Acinetobacter johnsonii that activates oxygen to convert a range of β-dicarbonyl substrates into α-oxo-aldehyde and acid products. Previous methods of downstream processing yielded Dke1 with substoichiometric Fe^2?+? content. This paper reports the integration of enzyme production in E. coli and affinity chromatography to prepare recombinant Dke1 that is completely loaded with its metal cofactor. The specific activity of Dke1 in E. coli cell extracts could be increased up to 20-fold, compared to optimized enzyme production with the natural host. Introduction of an affinity-tag allowed the isolation of fully active Dke1 in a single purification step with high yield (70%). Mass spectrometric analysis revealed at the level of >80% sequence coverage that the isolated enzyme corresponded exactly to the predicted gene product. Tagged Dke1 is shown to have retained the functional properties of native Dke1.     

Fast determination of operational stability of the soluble acetylacetone-cleaving enzyme Dke1 in an enzyme membrane reactor

The main aim of this study was the determination of the operational stability of soluble Dke1 (EC 1.13.11.50) in an enzyme membrane reactor. In order to calculate the half-life of soluble Dke1, the K _M of oxygen must be known. The determination of this constant was done using progress curve analysis (K _M=260 μmol l⁻¹). In a next step, the reactor system was studied by building a mathematical model for calculation of the reactor system, using Berkeley Madonna ver. 8.0.1 software. After that, the determination of the half-life of Dke1 under operational conditions at different temperatures (5, 10, 15, 25, 30, 35°C) was performed. The quantitative criterion for stability was the value of the first-order rate constant of monomolecular inactivation. The experiments showed that soluble Dke1 is poorly stable. The half-life ranged from 308 min at 5°C to 9 min at 35°C. This method for determining the half-life is quite applicable for enzymes which are poorly stable. In addition, both the storage stability and the operational stability can be determined.     

Novel optimal temperature profile for acidification process of <Emphasis Type="Italic">Lactobacillus bulgaricus</Emphasis> and <Emphasis Type="Italic">Streptococcus thermophilus</Emphasis> in yoghurt fermentation using artificial neural network and genetic algorithm

The acidification behavior of Lactobacillus bulgaricus and Streptococcus thermophilus for yoghurt production was investigated along temperature profiles within the optimal window of 38–44 °C. For the optimal acidification temperature profile search, an optimization engine module built on a modular artificial neural network (ANN) and genetic algorithm (GA) was used. Fourteen batches of yoghurt fermentations were evaluated using different temperature profiles in order to train and validate the ANN sub-module. The ANN captured the nonlinear relationship between temperature profiles and acidification patterns on training data after 150 epochs. This served as an evaluation function for the GA. The acidification slope of the temperature profile was the performance index. The GA sub-module iteratively evolved better temperature profiles across generations using GA operations. The stopping criterion was met after 11 generations. The optimal profile showed an acidification slope of 0.06117 compared to an initial value of 0.0127 and at a set point sequence of 43, 38, 44, 43, and 39 °C. Laboratory evaluation of three replicates of the GA suggested optimum profile of 43, 38, 44, 43, and 39 °C gave an average slope of 0.04132. The optimization engine used (to be published elsewhere) could effectively search for optimal profiles of different physico-chemical parameters of fermentation processes.     

Improved production of laccase by Daedalea flavida: consideration of evolutionary process optimization and batch-fed culture

The genetic algorithm was used effectively to find the optimal values of eight process variables for the maximum laccase production by Daedalea flavida in a stationary culture. The algorithm was modified suitably to improve laccase production with 18 parallel experiments in 4 generations. A high enzyme titer of 65 % was achieved after the optimization and compared to the titer obtained before optimization. To study the effect of the surface immobilized growth on the enzyme production, the fungus was grown on three solid carriers. When cultured on polymer composite fibers, polyurethane foam, or steel wool, at least 2.5 times more biomass was produced, compared to the biomass produced in support-free growth. On the contrary, the mycelia grown on solid support produced much less laccase than non-adhering mycelia. Four parallel runs of batch-fed cultures were done, using the cell mass of D. flavida to evaluate the influence of four different volumes of medium exchanged on laccase production. For sustainable production of the enzyme, complete exchange of medium was favorable, where the laccase activity increased continuously in six consecutive cycles, though, 50 % exchange of medium produced the maximum laccase in terms of mean enzyme activity obtained in six cycles.     

Some aspects of the regulation of the production of extracellular proteolytic enzymes by a marine bacterium

A highly proteolytic Gram-negative, rod-shaped bacterium was isolated from the gills of fresh plaice and the effect of culture conditions on the production of proteolytic enzymes was investigated. When the organism, strain SA 1, was grown in the presence of complex mixtures of proteins and amino acids, both endopeptidase and aminopeptidase activity was demonstrated in the cell-free culture medium. However, synthesis of these enzymes was not observed when the organism was grown in a mineral medium with lactate or succinate as the only carbon and energy source. Synthesis of both endopeptidase and aminopeptidase was induced by the presence of amino acids in the medium. Of the amino acids tested, l-phenylalanine was found to be the best single inducer for the production of endopeptidase. When in addition one or more different amino acids were added, endopeptidase production was found to increase with increasing complexity of the mixture, up to a maximum which was obtained with five different amino acids. Production of the aminopeptidase was optimal when l-glutamic acid was used as a single inducer. For this enzyme the amount of enzyme activity released in the medium decreased with increasing complexity of the amino acid mixture. Endopeptidase as well as aminopeptidase activity was found to accumulate in the medium at the end of the logarithmic growth phase, when the culture was no longer growing exponentially. When the stationary phase was reached, enzyme production stopped. Production of both enzymes was immediately halted upon addition of chloramphenicol and was found to be repressed by glucose and lactate. These results suggest that synthesis of proteolytic extracellular enzymes by the organism studied is controlled by an efficient regulatory mechanism, in which growth rate is an important parameter.     

Effective production of a thermostable alpha-glucosidase from Sulfolobus solfataricus in Escherichia coli exploiting a microfiltration bioreactor

A microfiltration (MF) membrane bioreactor was developed for an efficient production of a recombinant thermostable alpha-glucosidase (rSsGA) from Sulfolobus solfataricus MT-4. The aim of the membrane bioreactor was to improve the control of the concentration of key components in the growth of genetic engineered microorganisms, such as Escherichia coli. The influence of medium composition was studied in relation to cell growth and alpha-glucosidase production. The addition of components such as yeast extract and tryptone resulted in a higher enzyme production. High cell density cultivation of E. coli BL21(DE3) on semidefined medium, exploiting a microfiltration bioreactor, was studied in order to optimize rSsGA production. In addition to medium composition, the inducer employed (either isopropyl beta-D-thiogalactopyranoside or lactose), the induction duration, and the cultivation mode influenced both the final biomass and the enzyme yield. The MF bioreactor allowed a cell concentration of 50 g/L dry weight and a corresponding alpha-glucosidase production of 11,500 U/L. The improvement obtained in the enzyme production combining genetic engineering and the microfiltration strategy was estimated to be 2,000-fold the wild-type strain.     

Modelling and optimization of environmental conditions for kefiran production by Lactobacillus kefiranofaciens

A mathematical model for kefiran production by Lactobacillus kefiranofaciens was established, in which the effects of pH, substrate and product on cell growth, exopolysaccharide formation and substrate assimilation were considered. The model gave a good representation both of the formation of exopolysaccharides (which are not only attached to cells but also released into the medium) and of the time courses of the production of galactose and glucose in the medium (which are produced and consumed by the cells). Since pH and both lactose and lactic acid concentrations differently affected production and growth activity, the model included the effects of pH and the concentrations of lactose and lactic acid. Based on the mathematical model, an optimal pH profile for the maximum production of kefiran in batch culture was obtained. In this study, a simplified optimization method was developed, in which the optimal pH profile was determined at a particular final fermentation time. This was based on the principle that, at a certain time, switching from the maximum specific growth rate to the critical one (which yields the maximum specific production rate) results in maximum production. Maximum kefiran production was obtained, which was 20% higher than that obtained in the constant-pH control fermentation. A genetic algorithm (GA) was also applied to obtain the optimal pH profile; and it was found that practically the same solution was obtained using the GA.     

Induction of cellulase and hemicellulase activities of Thermoascus aurantiacus by xylan hydrolyzed products

Thermoascus aurantiacus is able to secrete most of the hemicellulolytic and cellulolytic enzymes. To establish the xylanase inducers of T. aurantiacus, the mycelia were first grown on glucose up until the end of the exponential growth phase, followed by washing and re-suspension in a basal medium without a carbon source. Pre-weighed amounts of xylose (final concentration of 3.5 mg/ml), xylobiose (7 mg/ml) and hydrolyzed xylan from sugarcane bagasse (HXSB) which contained xylose, xylobiose and xylotriose (6.8 mg/ml) were evaluated as inducers of xylanase. It was observed that xylose did not suppress enzyme induction of T. aurantiacus when used in low concentrations, regardless of whether it was inoculated with xylobiose. Xylobiose promoted fast enzyme production stopping after 10 h, even at a low consumption rate of the carbon source; therefore xylobiose appears to be the natural inducer of xylanase. In HXSB only a negligible xylanase activity was determined. Xylose present in HXSB was consumed within the first 10 h while xylobiose was partially hydrolyzed at a slow rate. The profile of α-arabinofuranosidase induction was very similar in media induced with xylobiose or HXSB, but induction with xylose showed some positive effects as well. The production profile for the xylanase was accompanied by low levels of cellulolytic activity. In comparison, growth in HXSB resulted in different profiles of both xylanase and cellulase production, excluding the possibility of xylanase acting as endoglucanases.     

Citrus peel influences the production of an extracellular naringinase by Staphylococcus xylosus MAK2 in a stirred tank reactor

Staphylococcus xylosus MAK2, Gram-positive coccus, a nonpathogenic member of the coagulase-negative Staphylococcus family was isolated from soil and used to produce naringinase in a stirred tank reactor. An initial medium at pH 5.5 and a cultivation temperature of 30°C was found to be optimal for enzyme production. The addition of Ca⁺² caused stimulation of enzyme activity. The effect of various physico-chemical parameters, such as pH, temperature, agitation, and inducer concentration was studied. The enzyme production was enhanced by the addition of citrus peel powder (CPP) in the optimized medium. A twofold increase in naringinase production was achieved using different technological combinations. The process optimization using technological combinations allowed rapid optimization of large number of variables, which significantly improved enzyme production in a 5-l reactor in 34 h. An increase in sugar concentration (15 g l⁻¹) in the fermentation medium further increased naringinase production (8.9 IU ml⁻¹) in the bioreactor. Thus, availability of naringinase renders it attractive for potential biotechnological applications in citrus processing industry.     

Physiological studies of the regulation of beta-lactamase expression in Pseudomonas maltophilia.

The kinetics of beta-lactamase induction in Pseudomonas maltophilia IID1275/873 were investigated. Upon induction with beta-lactam antibiotics, a correlation was seen between the increase in specific beta-lactamase activity and the generation time, as well as the concentration of inducer in the medium. The specific beta-lactamase activity increased slowly within the first 0.5 generation and then more rapidly; it decreased regularly after about 2 generations of growth in the presence of inducer. This decrease could presumably be attributed to the continuous breakdown of inducer by beta-lactamases in the culture medium. In a chemostat culture with continuous supply of fresh inducer-containing medium, the specific beta-lactamase activity could be stabilized at a high level over several generations. Removal of the beta-lactam after a certain induction time showed that a short exposure of the bacteria to inducer caused induction kinetics comparable to those resulting from continuous exposure of the cells to inducer. The two beta-lactamases of P. maltophilia, L1 and L2, were induced simultaneously under various experimental conditions.     

产胞外邻苯二酚1.2—双加氧酶的菌种筛选和发酵条件的研究

Two strains of Pseudomonus sp. having the extracellular catechol 1, 2-dioxygenase activity were selected from 112 bacterial strains. The conditions for enzyme production of the strains were examined. The optimal temperature and pH for enzyme formation were 30 degrees C and pH 6.8-7.0 respectively. Enzyme formation was enhanced by sodium benzoate, and was markedly inhibited by glucose, maltose and glycerol. Ammoniacal nitrogen sources were essential for cell growth and enzyme production. Sodium succinate was an effective inducer for enzyme formation. When the organism was grown in 0.15% sodium benzoate medium (pH 6.8-7.0) at 30 degrees C for 72 hours, about 10 units of catechol 1,2 dioxygenase per ml was obtained.     

Development of a fermentation process for production of an alginate G-lyase from Klebsiella pneumoniae

A high-density-cell fermentation process for production of an exracellular alginat lyase from Klebseilla pneumoniae on a defined medium has been developed. The process employs a strategy using two carbon sources. One low-molecular-mass, low-viscosity carbon source (sucrose) with high water solubililty is used as the main carbons source for growth, while the high-molecular-mass and viscoous alginate in low concentration is used as an inducer for enzyme synthesis. The repression of algiante lyase production by sucrose and the growth inhibition that we observed at increased levels of ammonia were circumvented by a computer-assisted fed-batch addition of the carbon sources (succrose and alginate) and by supplying nitrogen source as ammonia in the pH control. No enzyme production was observed when dissolved oxygen limited growth at an oxygen uptake rate of 40%–50% of the maximum uptake rate. An optimal composition of the feeding solution (12.5 g alginate and 587.5 g sucrose 1^–1) was found both for the maximum final concentration of enzyme (1330 U 1^–1) and for the maximum volumetric rate of enzyme production (67 U 1^–1 h^–1). The enzyme production dependes of the growth rate in the linear growth phase, giving a maximum enzyme concentration at the highest growth rate tested. The final enzyme concentration shows a fiveflod increase compare with previously reproted daata where alginate was used as a carbon source. In addition, the ratio of alginate lyase by a factor of apporximately 15. A doubling in extracellular specific activity of the enzyme was observed, a property of significant interest, especially for purification of the enzyme. On the othr hand, the final dry cell weight concentration of the bacteria also increased by a factor of 15–20 thus giving a relatively lower specific productivity of 0.4 U (g cell dry weight)^–1 h^–1.     

Enhanced production of recombinant galactose oxidase from <Emphasis Type="Italic">Fusarium graminearum</Emphasis> in <Emphasis Type="Italic">E. coli</Emphasis>

The gene gaoA encoding the copper-dependent enzyme galactose oxidase (GAO) from Fusarium graminearum PH-1 was cloned and successfully overexpressed in E. coli. Culture conditions for cultivations in shaken flasks were optimized, and optimal conditions were found to be double-strength LB medium, 0.5% lactose as inducer, and induction at the reduced temperature of 25°C. When using these cultivation conditions ~24 mg of active GAO could be produced in shaken flasks per litre medium. Addition of copper to the fermentation medium decreased the enzyme production significantly. The His-tagged recombinant enzyme could be purified conveniently with a single affinity chromatography step. The purified enzyme showed a single band on SDS–PAGE with an apparent molecular mass of 66 kDa and had kinetic properties similar to those of the fungal wild-type enzyme.     

Optimization of medium composition for lipase production by Candida rugosa NCIM 3462 using response surface methodology

A sequential optimization approach using statistical design of experiments was employed to enhance the lipase production by Candida rugosa in submerged batch fermentation. Twelve medium components were evaluated initially using the Plackett-Burman 2-level factorial design. The significant variables affecting lipase production were found to be glucose, olive oil, peptone, (NH4)2SO4, and FeCl3.6H2O. Various vegetable oils were tested in the second step, and among them, groundnut oil was found to be the best inducer for lipase production by C. rugosa. The third step was to identify the optimal values of the significant medium components with groundnut oil as the inducer using response surface methodology. The regression equation obtained from the experimental data designed using a central composite design was solved, and analyzing the response surface contour plots, the optimal concentrations of the significant variables were determined. A maximum lipase activity of 5.95 U.mL-1, which is 1.64 times the maximum activity obtained in the Plackett-Burman experimental trials, was observed. The optimum combination of medium constituents contained 19.604 g.L-1 glucose, 13.065 mL.L-1 groundnut oil, 7.473 g.L-1 peptone, 0.962 g.L-1 (NH4)2SO4, 0.0019 g.L-1 FeCl3.6H2O, and other insignificant components at the fixed level. A predictive model of the combined effects of the independent variables using response surface methodology and an artificial neural network was proposed. The unstructured kinetic models, logistic model, and Luedeking-Piret model were used to describe cell mass and lipase production. The parameters of the models were evaluated and the lipase production by C. rugosa was found to be growth associated.     

Cultivation of recombinant Escherichia coli to achieve high cell density with a high level of penicillin G acylase activity

A mutant strain of E. coli EP1 harbouring pGL-5 was employed to develop a process for producing penicillin G acylase (PGA). In comparison with different carbon sources in the medium, it was found that the specific levels of PGA activity obtained in the glucose medium were the lowest. which was likely due to catabolic repression. Phenylacetic acid (PAA) was previously reported to be an regulatory inducer for PGA production, whereas in this study, the addition of PAA repressed both cell growth and enzyme expression. In a fed-batch culture, the increase of specific PGA activity followed the pattern of the cell concentration during the early to middle cell growth phase. With application of pure oxygen aeration and an appropriate medium design, the cell concentration reached 162 (g wet weight/l), which was 2.4 times higher compared to that of the original operation, and a specific PGA activity of 37 (IU/g wet weight) was achieved after 12 h of cultivation.     

Leucine dehydrogenase from Bacillus sphaericus. Optimized production conditions and an efficient method for its large-scale purification

Summary To develop a large-scale isolation of leucine dehydrogenase (E.C. 1.4.1.9) as industrial catalyst we carried out a limited screening for microorganisms with high leucine dehydrogenase activity.Conditions for the growth and enzyme formation of Bacillus sphaericus (DSM 396) which proved to be the best enzyme producer were optimized. The highest yield in volume and specific activity were obtained using glucose and yeast-extract in the medium.The highest specific enzyme activity was found at the end of the exponential growth phase. Cultivation of Bacillus sphaericus under optimal conditions increased the yield to about 3 U mg^–1. The heat stability of the enzyme was exploited to develop a simple large-scale purification. Together with an ultrafiltration step, the enzyme could be enriched 9fold in a short time. After further purification using DE-cellulose an enzyme preparation (25fold enriched) was obtained; suitable as a technical catalyst in amino acid production.     

Effects of Octadecanoylsucrose Derivatives on the Production of Inulinase by Apergillus niger SL-09

Summary The effect of the addition of octadecanoylsucrose esters to the growth medium on the production of inulinase by Aspergillus niger SL-09 was studied in batch culture using shake flasks. The activities of inulinase in vitro and in vivo formed by Aspergillus niger SL-09 was enhanced dramatically by the addition of sucrose ester S-770 to the medium, and it was confirmed that sucrose ester acted as a very efficient inducer for inulinase production. As a result, with the addition of 6 g sucrose ester l⁻¹ at the beginning of the culture, the enzyme activities were enhanced near 7-fold higher than that obtained in the basal medium.     

Biochemical characterization and mutational analysis of the mononuclear non-haem Fe2+ site in Dke1, a cupin-type dioxygenase from Acinetobacter johnsonii

beta-diketone-cleaving enzyme Dke1 is a homotetrameric Fe2+-dependent dioxygenase from Acinetobacter johnsonii. The Dke1protomer adopts a single-domain beta-barrel fold characteristic of the cupin superfamily of proteins and features a mononuclear non-haem Fe2+ centre where a triad of histidine residues, His-62, His-64 and His-104, co-ordinate the catalytic metal. To provide structure-function relationships for the peculiar metal site of Dke1 in relation to the more widespread 2-His-1-Glu/Asp binding site for non-haem Fe2+,we replaced each histidine residue individually with glutamate and asparagine and compared binding of Fe2+ and four non-native catalytically inactive metals with purified apo-forms of wild-type and mutant enzymes. Results from anaerobic equilibrium microdialysis (Fe2+) and fluorescence titration (Fe2+, Cu2+, Ni2+, Mn2+ and Zn2+) experiments revealed the presence of two broadly specific metal-binding sites in native Dke1 that bind Fe2+ with a dissociation constant (Kd) of 5 microM (site I) and approximately 0.3 mM (site II). Each mutation, except for the substitution of asparagine for His-104, disrupted binding of Fe2+, but not that of the other bivalent metal ions, at site I,while leaving metal binding at site II largely unaffected. Dke1 mutants harbouring glutamate substitutions were completely inactive and not functionally complemented by external Fe2+.The Fe2+ catalytic centre activity (kcat) of mutants with asparagine substitution of His-62 and His-104 was decreased 140- and 220-fold respectively, compared with the kcat value of 8.5 s(-1) for the wild-type enzyme in the reaction with pentane-2,4-dione.The H64N mutant was not catalytically competent, except in the presence of external Fe2+ (1 mM) which elicited about 1/1000 of wild-type activity. Therefore co-ordination of Fe2+ by Dke1 requires an uncharged metallocentre, and three histidine ligands are needed for the assembly of a fully functional catalytic site. Oxidative inactivation of Dke1 was shown to involve conversion of enzyme-bound Fe2+ into Fe3+, which is then released from the metal centre.     

Metabolic roles of peptone and yeast extract for the culture of a recombinant strain ofEscherichia coli

Summary The influence of complex compounds on the growth of a recombinant strain ofEscherichia coli containing the gene encoding glyceraldehyde 3-phosphate dehydrogenase, as well as the production of this enzyme have been studied. Batchwise cultures led to an accumulation of acetate, which was not utilized in a yeast extract-free medium. After glucose exhaustion, growth stopped and enzyme activity decreased. Whereas yeast extract allowed acetate assimilation and growth, peptone stabilized the enzymatic activity. The addition of both compounds resulted in optimal performances for enzyme production.