The effect of growth rate and culturing conditions on the stability of plasmid pCJ55 and on the level of expression of a large fragment of DNA-polymerase I, cloned in Escherichia coli

Plasmid pCJ55 with a cloned gene for the large fragment of Escherichia coli DNA polymerase I is stable in the population of a recombinant strain under the conditions of batch and continuous cultivation at different dilution rates in the presence of ampicillin. The level of Klenow fragment expression is determined by at least two factors: the stability of the recombinant strain and its specific growth rate. The maximal activity of the Klenow fragment was found after thermoinduction of the culture growing at a rate of mu = 0.6 h-1 in a synthetic medium with bactopeptone and glucose as a carbon source.     

Effect of glucose metabolic products on the growth of a recombinant Escherichia coli strain--a superproducer of DNA-polymerase

The dynamics of glucose metabolites production by Escherichia coli CM 5199 was studied under the conditions of batch and continuous cultivation. Acetate and ethanol were shown to be accumulated in the cultural broth in considerable amounts, and the rate of their synthesis was directly proportional to the specific growth rate of the culture. Acetate inhibited E. coli growth as was found in experiments conducted in a turbidostat regimen. As a result, the specific growth rate of the strain decreased during both batch and continuous cultivation.     

Physiological regulation and optimization of lipase activity in Pseudomonas aeruginosa EF2.

Physiological regulation of extracellular lipase activity by a newly-isolated, thermotolerant strain of Pseudomonas aeruginosa (strain EF2) was investigated by growing the organism under various conditions in batch, fed-batch and continuous culture. Lipase activity, measured as the rate of olive oil (predominantly triolein) hydrolysis, was weakly induced by general carbon and/or energy limitation, strongly induced by a wide range of fatty acyl esters including triglycerides, Spans and Tweens, and repressed by long-chain fatty acids including oleic acid. The highest lipase activities were observed during the stationary phase of batch cultures grown on Tween 80, and with Tween 80-limited fed-batch and continuous cultures grown at low specific growth rates. The lipase activity of Tween 80-limited continuous cultures was optimized with respect to pH and temperature using response surface analysis; maximum activity occurred during growth at pH 6.5, 35.5 degrees C, at a dilution rate of 0.04 h-1. Under these conditions the culture exhibited a lipase activity of 39 LU (mg cells)-1 and a specific rate of lipase production (qLipase) of 1.56 LU (mg cells)-1 h-1 (1 LU equalled 1 mumol fatty acid released min-1). Esterase activity, measured with p-nitrophenyl acetate as substrate, varied approximately in parallel with lipase activity under all growth conditions, suggesting that a single enzyme may catalyse both activities.     

Biosynthesis of exopolysaccharide by Pseudomonas aeruginosa.

In batch cultures of Pseudomonas aeruginosa, the maximum rate of exopolysaccharide synthesis occurred during exponential growth. In nitrogen-limited continuous culture, the specific rate of exopolysaccharide synthesis increased from 0.27 g g of cell-1 h-1 at a dilution rate (D) of 0.05 h-1 to 0.44 g g of cells h-1 at D=0.1 H-1. The yield of exopolysaccharide on the basis of glucose used was in the range of 56 to 64%. Exopolysaccharide was also synthesized in carbon-limited cultures at 0.19 g g of cell-1 h-1 at D=0.05 h-1 in a 33% yield. Nonmucoid variants appeared after seven generations in continuous culture and rapidly increased in proportion to the total number of organisms present.     

Kinetics of Pseudomonas fluorescens growth under different conditions of culturing

The dynamics of Pseudomonas fluorescens VKM-1472 growth was studied under the conditions of batch and continuous cultivation, and the behaviour of the organism was investigated upon nutrition shifts and starvation. At D greater than 0.375 h-1, just as in the batch culture with a substrate excess, the strain realised excessive metabolism [15]: the yield in terms of the substrate fell down (38% for the batch culture and 40% for the continuous culture), the titre of viable cells decreased to a considerable extent, and maintenance expenditures increased (3 times for qgluc and 7.5 times for qO2). When the culture was incubated under the oligotrophous conditions, the biomass yield decreased fourfold within 8 days and the titre of viable cells dropped down twofold within the same period of time. However, the organism was still capable of oxidising a wide range of substrates (17 substrates were studied). As soon as a substrate was added, it was oxidised at a high rate and changes in the macromolecular composition were characteristic of an "up-jump" in the growth rate [11]. It is possible that the growth and behaviour of this organism are associated with its ecological niche occupied in natural systems.     

Metabolic limitation of DNA-polymerase I synthesis by Escherichia coli strain CM5199

The work was aimed at studying DNA polymerase I synthesis after induction of the vector prophage lambda polA (NM 964) in lysogenic Escherichia coli CM 5199 in the course of batch cultivation in different media and at various growth phases as well as upon "nutrient shifts" caused by adding organic compounds to the minimal medium. The enzyme activity was highest when the phage was induced at the exponential phase of growth and in media richer in their composition. The enzyme synthesis, the dynamics of protein and RNA content were studied after induction of the phage and enrichment of the medium; the studies have shown that synthesis of DNA polymerase I is influenced by limitation at two levels: (1) biosynthesis of amino acids and (2) biosynthesis of components of the protein-synthesizing apparatus. There is a direct correlation between DNA polymerase I biosynthesis under the control of vector DNA and the growth rate of the culture.     

Continuous cultivation in a chemostat of the phototrophic procaryote,anacystis nidulans,under nitrogen-limiting conditions

Anacystis nidulans was grown photoautotrophically in a chemostat in the presence of light, air and CO2 as the sole carbon source. Either the amount of the nitrogen source in the medium or light intensity were used as growth-limiting parameters. 1. Cells of high glycogen content obtained by pre-incubation under nitrogen starvation conditions maintained their glycogen content during continuous cultivation. Both growth rate and the amount of cell-mass and of glycogen depended on the nitrate content of the medium and the light intensity. The values for the growth rate, the maximal rates of glycogen synthesis and of cell mass formation were 0.1 h-1, 6 mg/l.h and 17 mg/l.h, respectively. 2. Cells without glycogen which had been transferred from an exponentially growing batch culture to chemostat conditions showed increasing rates of growth and of cell mass formation when the light intensity was increased. A determination of specific values resulted in 0.15 h-1 for growth rate and 23 mg/1.h for cell mass formation. 3. The chemostat apparatus is described in detail.     

Continuous cultivation of recombinant Escherichia coli: Existence of an optimum dilution rate for maximum plasmid and gene product concentration

Growth yield factors, plasmid stability, cellular plasmid content, and cloned gene product activity for Escherichia coli HB101 containing plasmid pDM246 were measured at several dilution rates in continuous culture. Cell mass yield per mass of glucose consumed declined with increasing dilution rate. There was no evidence of plasmid segregational instability in any experiments, none of which employed selective medium. Plasmid content per cell varied with population-specific growth rate as observed in earlier batch experiments with the same strain. Plasmid content declined with increasing specific growth rate following indication of a maximum number of plasmids per cell at specific growth rates of ca. 0.3 h(-1). Cloned gene product (beta-lactamase) activity exhibited a sharp maximum with respect to dilution rate in continuous culture. Qualitatively different results were observed in previous experiments in batch cultivation in which specific growth rate changes were effected by altering medium composition.     

Glucose repression of enterotoxins A, B and C and other extracellular proteins in staphlyococci in batch and continuous culture.

The production of enterotoxins, lipase and total extracellular protein by four strains of Staphylococcus aureus grown in batch culture at a controlled pH of 6.5 in a completely defined medium was markedly reduced by glucose or glycerol constantly maintained at 0.I M. A concomitant increase in the production of deoxyribonuclease, up to 13-fold, showed however that not all extracellular proteins are under the same control mechanism. The presence of glucose and glycerol in the medium also resulted in a rapid increase in the specific growth rate. However, growth of S. aureus s6 in Mgilimited continuous culture showed that glucose repression of enterotoxin B when the growth rate was held constant was more than twice that in batch culture. Therefore glucose repression can occur independently of an increase in growth rate. The specific rate of production of enterotoxin B, lipase, deoxyribonuclease, beta-haemolysin and total extracellular protein by S. aureus s6 increased as the growth rate increased from 0.07 to 0.24 h-1. Non-replicating cells grown in the absence of glucose produced considerable amounts of enterotoxin, and production was not repressed by the presence of glucose in the resuspension medium. In contrast, no enterotoxin B or C was obtained from nonreplicating cells grown in the presence of glucose. Chloramphenicol completely inhibited enterotoxin production by non-replicating cells, indicating that synthesis of new protein was required.     

Growth and physiology of a yeast cultivated in batch and continuous culture systems

Inoculum size has been found to affect significantly the maximum attainable specific growth rate during batch cultivation ofCandida utilis. Lower inoculum size resulted in an increased growth rate and relatively longer lag. The culture is found to be most active in the beginning of the exponential phase as regards its RNA synthesis rate. Batch data were used for predicting the conditions of the yeast population in single-stage continuous culture system. Predicted and the experimental values showed a reasonable agreement. In single-stage chemostat the physiology of the yeast was studied on the basis RNA, DNA and protein synthesis rates at various growth rates. The results indicate that the productivity of cells and the rate of synthesis of macromolecules is highest at the dilution rate values of 0.33 to 0.35 hr⁻¹. In order to attain so-called unrestricted conditions of growth a pluristage pluristream continuous system was employed. It is assumed that under such conditions the specific growth rate and the synthetic activity of yeasts may reach its maximum on a given medium. The results presented do not show such conditions of growth under the experimental conditions employed (D ₁=0.35 hr⁻¹ andD ₂=0.2 to 1.7 hr⁻¹) withCandida utilis cultivated on beet molasses medium. Second stage of a two-stage two-stream continuous system is constantly fed with the cells from the foregoing stage; this category of cells on entering the new conditions of the second stage is expected to show some adaptation period. Experiments are reported to this effect.     

Production of gramicidin S synthetases by Bacillus brevis in continuous culture.

The effects of different nutrient limitations on the production of the two enzymes of gramicidin S biosynthesis were studied during continuous culture of Bacillus brevis. Gramicidin S synthetases I and II were produced in the chemostat under carbon, nitrogen, phosphorus or sulphur limitation. The growth rate, rather than the nature of the limitation, was the major controlling factor in regulating the level of the gramicidin S synthetases. Synthetase production was low at high dilution rates (0.45 to 0.50 h-1) but increased as the dilution rate was lowered. The highest specific activities occurred at dilution rates that were different for each type of limitation: 0.40 h-1 for nitrogen, 0.32 h-1 for carbon, 0.24 h-1 for sulphur and 0.20 h-1 for phosphorus. Phosphorus limitation gave the highest specific activities. At low dilution rates (0.10 to 0.15 h-1), enzyme activities were again low. Sporulation occurred under carbon limitation, but at a lower dilution rate than that which supported optimal gramicidin S synthetase formation. The specific productivity of the synthetases in the chemostat was higher than the highest productivity obtained in batch growth.     

Continuous hydrogen production by the hyperthermophilic archaeon, Thermococcus kodakaraensis KOD1

The hydrogen (H2) production potential of the hyperthermophilic archaeon, Thermococcus kodakaraensis KOD1 was evaluated at 85 degrees C. In batch cultivation using a complex medium supplemented with elemental sulfur (S0), evolution of H2S and CO2 was observed in the gas phase. When S0 was omitted and pyruvate or starch was added in the medium, the cells produced H2 at high levels instead of H2S. As the level of H2 appeared to correlate with the specific growth rate, analysis in continuous cultures was performed to develop a continuous H2 production system. In a steady-state condition at a dilution rate of 0.2 h-1, a continuous H2 production rate (per gram dry weight, gdw) of 24.9 and 14.0 mmol gdw-1 h-1 was observed in media supplemented with pyruvate and starch, respectively. In both cultivations, a high accumulation of acetate and alanine was found as metabolites. When the dilution rates were elevated in the medium with pyruvate, steady-state growth was observed up to 0.8 h-1, and a maximum H2 production rate of 59.6 mmol gdw-1 h-1 was obtained. Based on the experimental results along with data of the entire genome sequence, the metabolic pathway of the strain relating to starch and pyruvate degradation is discussed.     

Production of the fimbrial adhesin 987P by enterotoxigenic Escherichia coli during growth under controlled conditions in a chemostat

The effects of growth conditions on the production of 987P fimbriae by the enterotoxigenic Escherichia coli strain 1592 were examined in steady state chemostat experiments at different specific growth rates. The amount of fimbriae produced by fimbriate cells (P+) was dependent on the specific growth rate (mu). Under aerobic growth conditions fimbriae production increased with higher mu values till mu = 0.40 h-1 and decreased again at mu values close to mu max (0.48 h-1). Under anaerobic growth conditions the maximal production was comparable to that under aerobic growth conditions, and was also maximal close to mu max (0.16 h-1). Phase variation, measured as the percentage of fimbriate cells in a particular population, was independent of mu. The composition of the growth medium influenced both phase variation and overall production of fimbriae. A shift from minimal to a complex medium induced a rapid reduction in the amount of fimbriae per P+ cell and a slower reduction in the percentage of P+ cells. A shift from complex to minimal medium resulted in an increase in the percentage of P+ cells and a constant amount of fimbriae per P+ cell. The frequency of the phase switch was calculated for different growth conditions. The frequency of the P+----P- switch between two steady states was 2.7 x 10(-2). In batch culture the frequency of the P(-)----P+ switch was minimally 2.9 x 10(-2). The results indicate that phase variation and the production of 987P fimbriae by fimbriate cells are under independent physiological control.     

Cultivation of Endomyces magnusii yeasts under batch and continuous conditions at an acid pH

The energy parameters of Endomyces magnusii cells and mitochondria were studied under the conditions of batch and continuous cultivation at different pH of the medium containing ethanol. The yeast was found to be capable of growth in the chemostat regime at D=0.2 h-1. Changes in the pH of the medium from 3.0 to 5.6 almost did not change the parameters characterizing oxidative phoshorylation of the mitochondria (the respiration chain contained three phosphorylation points). This correlated with the nearly identical biomass yield and economical coefficient. The content of RNA, DNA and protein remained unchanged at different pH values whereas the content of lipids increased at acid pH.     

Competition between different strains of Streptococcus cremoris

Abstract Streptococcus cremoris strain HP was found to grow poorly on agar plates under aerobic conditions in comparison to several other strains of S. cremoris (Wg2, ML1, AM1, E8). This made it possible to determine the numbers of strain HP in mixed cultures with other strains under different culture conditions. None of the mixtures was stable in batch cultures as a result of differences in the maximum specific growth rate. In continuous culture under lactose limitation strain HP outcompeted strains E8 and ML1 at low dilution rates, but at high dilution rates and in batch culture the reverse was observed. This represents another example of crossing μ-s curves in anaerobic bacteria.     

Oxygen requirements for growth and citric acid production of Yarrowia lipolytica

During continuous cultivation of Yarrowia lipolytica N 1, oxygen requirements for growth and citric acid synthesis were found to depend on the iron concentration in the medium. A coupled effect of oxygen and iron concentrations on the functioning of the mitochondrial electron transport chain in Y. lipolytica N 1 was established. Based on the results obtained in continuous culture, conditions for citric acid production in a batch culture of Y. lipolytica N 1 were proposed. At relatively low pO(2) value and a high iron concentration, citric acid accumulation was as high as 120 g l(-1); the specific rate of citric acid synthesis reached 120 mg citric acid (g cells h)(-1). The mass yield coefficient was 0.87 and the energy yield coefficient was 0.31.     

Growth characteristics of Escherichia coli HB101[pGEc47] on defined medium

This paper shows that differences in growth behavior of Escherichia coli strain HB101 and strain HB101[pGEc47] can be related to yeast extract-enriched medium rather than plasmid properties. An optimal medium for growth of E. coli HB101[pGEc47] was designed based on the individual yield coefficients for specific medium components (NH4+ 6 g g-1, PO43- 14 g g-1, SO42- 50 g g-1). The yield coefficient for L-leucine depends on the glucose content of the medium (20 g g-1 for 3% glucose, 40 g g-1 for 1% glucose) and the yield coefficient for L-proline depends on the cultivation mode (20 g g-1 for batch cultivation, 44 g g-1 for continuous cultivation). Growth on defined medium after medium optimization is as rapid as on complex medium (0. 42-0.45 h-1). The critical dilution rate (DR) in the defined medium above which undesired production of acetic acid occurs is in the range of 0.23-0.26 h-1.     

Expression of the multiple antibiotic resistance operon (mar) during growth of Escherichia coli as a biofilm

The multiple antibiotic resistance (mar) operon is a global regulator controlling the expression of various genes in Escherichia coli which constitutes the mar regulon. Upregulation of mar leads to a multi-drug resistant phenotype, which includes resistance towards structurally unrelated antibiotics, organic solvents and the disinfectant pine oil. Biofilms also display similar decreases in susceptibility to antimicrobial agents. A marOII-lacZ fusion strain (SPC105) of E. coli was used to monitor mar expression under various growth conditions including batch, continuous and biofilm culture. In chemically-defined media (CDM), mar expression was maximal in mid-log and declined in the stationary phase. Conversely, in rich media (Luria-Bertani broth), minimal expression in mid-log was followed by an increase in the stationary phase. In continuous culture, expression was inversely related to specific growth rate (mu = 0.05-0.4 h-1). LacZ expression by the marOII-lacZ fusion was generally low within the total biofilm population and equivalent to that of stationary phase cultures grown in batch culture. When the expression of mar in CDM batch culture was compared with that in biofilm populations, beta-galactosidase activity was generally higher throughout batch culture than in the attached population. Overall, these results suggest that while mar expression will be greatest within the depths of a biofilm where growth rates are suppressed, its probable induction within biofilms cannot explain the elevated levels of antibiotic resistance observed.     

Kinetic modeling of free fatty acid production in Escherichia coli based on continuous cultivation of a plasmid free strain

The microbial production of free fatty acids (FFAs) and reduced derivatives is an attractive process for the renewable production of diesel fuels. Toward this goal, a plasmid-free strain of Escherichia coli was engineered to produce FFAs by integrating three copies of a thioesterase gene from Umbellularia californica (BTE) under the control of an inducible promoter onto the chromosome. In batch culture, the resulting strain produced identical titers to a previously reported strain that expressed the thioesterase from a plasmid. The growth rate, glucose consumption rate, and FFA production rate of this strain were studied in continuous cultivation under carbon limitation. The highest yield of FFA on glucose was observed at a dilution rate of 0.05 h(-1) with the highest specific productivity observed at a dilution rate of 0.2 h(-1). The observed yields under the lowest dilution rate were 15% higher than that observed in batch cultures. An increase in both productivity and yield (≈ 40%) was observed when the composition of the nutrients was altered to shift the culture toward non-carbon limitation. A deterministic model of the production strain has been proposed and indicates that maintenance requirements for this strain are significantly higher than wild-type E. coli.