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.     

Physiological properties of Saccharomyces cerevisiae during sine-modulated and stepwise changes in the medium pH

The responses of a chemostat Saccharomyces cerevisiae culture (D = 0.1 h-1) to a stepwise increase or decrease in the pH of the medium were shown to be asymmetric. When the pH was lowered from 6.5 to a value above 0.3, the rates of oxygen uptake and carbon dioxide evolution rose for a sort period of time whereas the optical density of the culture fell down. The detected changes in the properties of the culture were identical with those which had been observed in the course of spontaneous undamped oscillations in the physiological parameters of the continuous C. cerevisiae culture. Apparently, in both cases, the energy status of cells changed when the oxidative type of metabolism was substituted by fermentation. When the pH of the medium was elevated within the same range (4.7-6.5), the response of the culture was three times as low and its properties changed in the opposite direction. When the pH of the medium was changed in a cyclic sinusoidal manner, oscillations in the physiological characteristics of the culture, identical with spontaneous oscillations were induced at certain values of the amplitude and the frequency of pH changes.     

Selection of Ethanol-Tolerant Yeast Hybrids in pH-Regulated Continuous Culture

Hybrids between naturally occurring wine yeast strains and laboratory strains were formed as a method of increasing genetic variability to improve the ethanol tolerance of yeast strains. The hybrids were subjected to competition experiments under continuous culture controlled by pH with increasing ethanol concentrations over a wide range to select the fastest-growing strain at any concentration of ethanol. The continuous culture system was obtained by controlling the dilution rate of a chemostat connected to a pH-meter. The nutrient pump of the chemostat was switched on and off in response to the pH of the culture, which was thereby kept near a critical value (pH_c). Under these conditions, when the medium was supplemented with ethanol, the ethanol concentration of the culture increased with each pulse of dilution. A hybrid strain was selected by this procedure that was more tolerant than any of the highly ethanol-tolerant wine yeast strains at any concentration of ethanol and was able to grow at up to 16% (vol/vol) ethanol. This improvement in ethanol tolerance led to an increase in both the ethanol production rate and the total amount of ethanol produced.     

Optimization and stability of glucoamylase production by recombinant strains of Aspergillus niger in chemostat culture

When grown on a medium containing 5 g maltodextrin L-1, Aspergillus niger transformant N402[pAB6-10]B1, which has an additional 20 copies of the glucoamylase (glaA) gene, produced 320 +/- 8 mg (mean +/- S.E.) glucoamylase (GAM) L-1 in batch culture and 373 +/- 9 mg GAM L-1 in maltodextrin-limited chemostat culture at a dilution rate of 0.13 h-1. These values correspond to specific production rates (qp) of 5.6 and 16.0 mg GAM [g biomass]-1 h-1, respectively. In maltodextrin-limited chemostat cultures grown at dilution rates from 0.06 to 0.14 h-1, GAM was produced by B1 in a growth-correlated manner, demonstrating that a continuous flow culture system operated at a high dilution rate is an efficient way of producing this enzyme. In chemostat cultures grown at high dilution rates, GAM production in chemostat cultures was repressed when the limiting nutrient was fructose or xylose, but derepressed when the limiting nutrient was glucose (qp, 12.0), potassium (6.2), ammonium (4.1), phosphate (2.0), magnesium (1.5) or sulphate (0.9). For chemostat cultures grown at a dilution rate of 0.13 h-1, the addition of 5 g mycopeptone L-1 to a glucose-mineral salts medium resulted in a 64% increase in GAM concentration (from 303 +/- 12 to 496 +/- 10 mg GAM L-1) and a 37% increase in specific production rate (from 12.0 +/- 0.4 to 16.4 +/- 1.6 mg GAM [g biomass]-1 h-1). However, although recombinant protein production was stable for at least 948 h (191 generations) when A. niger B1 was grown in chemostat culture on glucose-mineral salts medium, it was stable for less than 136 h (27 generations) on medium containing mycopeptone. The predominant morphological mutants occurring after prolonged chemostat culture were shown to have selective advantage in the chemostat over the parental strain. Compared to their parental strains, two morphological mutants had similar GAM production levels, while a third had a reduced production level. Growth tests and molecular analysis revealed that the number of glaA gene copies in this latter strain (B1-M) was reduced, which could explain its reduced GAM production. Shake-flask cultures carried out with the various morphological mutants revealed that in batch culture all three strains produced considerably less GAM than their parent strains and even less than N402. We show that physiological changes in these morphological mutants contribute to this decreased level of GAM production.     

Production of Thermostable alpha-Amylase, Pullulanase, and alpha-Glucosidase in Continuous Culture by a New Clostridium Isolate

The production of alpha-amylase, pullulanase, and alpha-glucosidase and the formation of fermentation products by the newly isolated thermophilic Clostridium sp. strain EM1 were investigated in continuous culture with a defined medium and an incubation temperature of 60 degrees C. Enzyme production and excretion were greatly influenced by the dilution rate and the pH of the medium. The optimal values for the formation of starch-hydrolyzing enzymes were a pH of 5.9 and a dilution rate of 0.075 to 0.10 per h. Increase of the dilution rate from 0.1 to 0.3 per h caused a drastic drop in enzyme production. The ethanol concentration and optical density of the culture, however, remained almost constant. Growth limitation in the chemostat with 1% (wt/vol) starch was found optimal for enzyme production. Under these conditions 2,800 U of pullulanase per liter and 1,450 U of alpha-amylase per liter were produced; the amounts excreted were 70 and 55%, respectively.     

Optimization of dilution rate, pH and oxygen supply on optical purity of 2, 3-butanediol produced by Paenibacillus polymyxa in chemostat culture

The optimum dilution rate for 2, 3-butanediol (BDL) production by Paenibacillus polymyxa was 0.2 h1 and the optical purity of BDL remained above 98 % at all dilution rates. With decreasing culture pH, ethanol and BDL production increased, whereas the optical purity of BDL decreased to 94 % at pH 5.7. In the chemostat culture at pH 6.3 and a 0.1 h1 dilution rate, the optimum air supply for BDL production was 200 ml min–1 in which the O2 uptake rate was 6.7 mmol l–1 h–1. Under this condition, the optical purity of BDL decreased to 93 %. © Rapid Science Ltd. 1998     

Production of Thermostable α-Amylase, Pullulanase, and α-Glucosidase in Continuous Culture by a New Clostridium Isolate

The production of α-amylase, pullulanase, and α-glucosidase and the formation of fermentation products by the newly isolated thermophilic Clostridium sp. strain EM1 were investigated in continuous culture with a defined medium and an incubation temperature of 60°C. Enzyme production and excretion were greatly influenced by the dilution rate and the pH of the medium. The optimal values for the formation of starch-hydrolyzing enzymes were a pH of 5.9 and a dilution rate of 0.075 to 0.10 per h. Increase of the dilution rate from 0.1 to 0.3 per h caused a drastic drop in enzyme production. The ethanol concentration and optical density of the culture, however, remained almost constant. Growth limitation in the chemostat with 1% (wt/vol) starch was found optimal for enzyme production. Under these conditions 2,800 U of pullulanase per liter and 1,450 U of α-amylase per liter were produced; the amounts excreted were 70 and 55%, respectively.     

Levels of cyclic-2,3-diphosphoglycerate in Methanobacterium thermoautotrophicum during phosphate limitation.

Batch-grown Methanobacterium thermoautotrophicum cells grew nonexponentially in the absence of exogenous Pi until intracellular cyclic-2,3-diphosphoglycerate (cyclic DPG) had fallen below 2 mumol/g (dry weight), the limit of detection. Growth resumed immediately upon transfer to medium containing Pi Cyclic DPG levels were also below detection in Pi-limited chemostat cultures operating at a dilution rate of 0.173 h-1 (4-h doubling time), with reservoir Pi concentrations below 200 microM. At this dilution rate, the Pi concentration in the culture was 4 microM. An H2-limited steady state was achieved with 400 microM Pi in the inflowing medium (67 microM in the culture). The cyclic DPG content of these cells was 72 to 74 mumol/g, about one-third the amount in batch-grown cells. The specific growth rate accelerated immediately to 0.36 h-1 (1.9-h doubling time) under washout conditions at high dilution rate. The cellular content of cyclic DPG declined over a 2-h period, and then increased rapidly as the Pi level in the medium approached 200 microM. Expansion of the cyclic DPG pool coincided with a marked increase in Pi assimilation. These results indicated that M. thermoautotrophicum accumulated cyclic DPG only when Pi and H2 were readily available.     

The segregation of the 2 mu-based yeast plasmid pJDB248 breaks down under conditions of slow, glucose-limited growth

The stability of the 2 mu-based yeast plasmid pJDB248 in Saccharomyces cerevisiae S150-2B(cir0) was investigated in glucose-limited chemostat culture. Plasmid-free cells were detected by loss of (plasmid-encoded) leucine prototrophy and confirmed by colony hybridization. The plasmid was considerably more stable at a high dilution rate (0.12 h-1) than at a lower dilution rate (0.05 h-1). The average plasmid copy number in the cells retaining the plasmid remained constant at approximately 50 in the high dilution rate culture whereas it rose to almost 600 in the slow dilution rate culture. However, in both cultures the overall plasmid level in the total population remained constant, indicating that plasmid segregation breaks down at the low growth rate. Similar experiments on the native 2 mu plasmid demonstrated high stability and no significant differences between the high and low growth rate cultures. It is postulated that the difference in behaviour between the native and chimeric plasmids is related to an interaction between the growth conditions and the loss of the D gene product.     

Dynamic analysis of a microbial process: A systems engineering approach

A general mathematical model of the chemostat system is developed in order to define an experimental program of dynamic testing. A glucose-limited culture ofSaccharomyces cerevisiae was grown in a chemostat using chemically defined medium. The chemostat was perturbed from an initial steady state by changes in input glucose concentration, dilution rate, pH, and temperature. Dynamic responses of cell mass, glucose, cell number, RNA, and protein concentrations were measured. A number of simulation techniques were used in developing a dynamic mathematical model and in comparing the developed model with experimental data as well as the Monod model. The resulting model was found to be quantitatively accurate and superior to the Monod model. The developed model was interpreted in the light of cell physiology. Adjustment of intracellular RNA fraction was found to be rate limiting in acceleration of cell specific growth rate.     

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 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.     

Kinetics of biphasic growth of yeast in continuous and fed-batch cultures

The influence of dilution rate on the production of biomass, ethanol, and invertase in an aerobic culture of Saccharomyces carlsbergensis was studied in a glucose-limited chemostat culture. A kinetic model was developed to analyze the biphasic growth of yeast on both the glucose remaining and the ethanol produced in the culture. The model assumes a double effect where glucose regulates the flux of glucose catabolism (respiration and aerobic fermentation) and the ethanol utilization in yeast cells. The model could successfully demonstrate the experimental results of a chemostat culture featuring the monotonic decrease of biomass concentration with an increase of dilution rate higher than 0.2 hr^?1 as well as the maximum ethanol concentration at a particular dilution rate around 0.5 hr^?1. Some supplementary data were collected from an ethanol-limited aerobic chemostat culture and a glucose-limited anaerobic chemostat culture to use in the model calculation. Some parametric constants of cell growth, ethanol production, and invertase formation were determined in batch cultures under aerobic and anaerobic states as summarized in a table in comparison with the chemostat data. Using the constants, a prediction of the optimal control of a glucose fed-batch yeast culture was conducted in connection with an experiment for harvesting a high yield of yeast cells with high invertase activity.     

Effect of oxygen supply on growth ofKlebsiella aerogenes in a multistage tower fermentor

The effect of the rate of oxygen supply on biomass growth, consumption of carbon source formation of metabolic by-products, biomass yeilds referred to C-source and oxygen, respiration rate and the respiratory quotient was studied in a multistage tower fermentor with an interstage backflow, i.e. with a continuous reinoculation of the preceding stages. Experiments were done with Klebsiella aerogenes CCM 2318 in a synthetic glucose medium with constant glucose concentration in the feed, at pH 7.0. temperature 30 degrees C, and dilution rates 0.6 and 0.178 h-1 (referred to one stage). Different behavior of the culture was found at different dilution rates both with oxygen and under oxygen limitation. As compared with the chemostat system, the regime with an interstage backflow exhibited differences in respiration rate and CO2 formation; this attests to a considerably different physiological state of the cells.     

Vancomycin production is enhanced in chemostat culture with biomass-recycle

Production of the glycopeptide antibiotic vancomycin by Amycolatopsis orientalis ATCC 19795 was examined in phosphate-limited chemostat cultures with biomass-recycle, employing an oscillating membrane separator, at a constant dilution rate (D= 0. 14 h-1). Experiments made under low agitation conditions (600 rpm) showed that the biomass concentration could be increased 3.9-fold with vancomycin production kinetics very similar to that of chemostat culture without biomass-recycle. The specific production rate (qvancomycin) was maximal when the biomass-recycle ratio (R) was 0.13 (D= 0.087 h-1). When the dissolved oxygen tension dropped below 20% (air saturation), the biomass and vancomycin concentrations decreased and an unidentified red metabolite was released into the culture medium. Using increased agitation (850 rpm), used to maintain the dissolved oxygen tension above 20% air saturation, maximum increases in biomass concentration (7.9-fold) and vancomcyin production 1.6-fold (0.6 mg/g dry weight/h) were obtained when R was 0.44 (D= 0.056 h -1) compared to chemostat culture without biomass-recycle. Moreover, at this latter recycle ratio the volumetric vancomycin production rate was 14.7 mg/L/h (a 7-fold increase compared to chemostat culture without biomass-recycle). These observations encourage further research on biomass-recycling as a means of optimising the production of antibiotics.     

The production of α-amylase in batch and chemostat culture by Bacillus stearothermophilus

The production of -amylase (-1,4-glucan 4-glucanohydrolase; EC. 3.2.1.1) by a strain of Bacillus stearothermophilus isolated from leaf litter was investigated in a tryptone-maltose medium at 55°C in batch and chemostat culture. Amylase production was growth-limited and restricted to the exponential phase in batch culture. The enzyme yield was reduced by 40% when the culture pH was maintained at pH 7.2. Amylase production in chemostat culture was influenced by the growth rate throughout the dilution rate range used.     

The effect of pH on the growth and metabolism of Streptococcus bovis in continuous culture

Streptococcus bovis H13/1 was grown anaerobically at pHs between 5.0 and 6.5 in a glucose-limited chemostat at a dilution rate of 0.05/h. The growth yield and the production of acetate, ethanol and formate decreased at pHs less than 6.5 whereas the production of lactate increased at the lower pH values. When a culture was subjected to sequential pH changes, growth yield and fermentation products were influenced not only by the pH existing in the culture medium but also by the metabolic activity of the cells at the preceding pHs in the sequence. The results are discussed in relation to the mechanisms available for the maintenance of pH homeostasis and for the metabolic control of fermentation pathways in Strep. bovis.     

The effect of pH on the growth and metabolism of Streptococcus bovis in continuous culture

Streptococcus bovis H13/1 was grown anaerobically at pHs between 5.0 and 6.5 in a glucose-limited chemostat at a dilution rate of 0.05/h. The growth yield and the production of acetate, ethanol and formate decreased at pHs less than 6.5 whereas the production of lactate increased at the lower pH values. When a culture was subjected to sequential pH changes, growth yield and fermentation products were influenced not only by the pH existing in the culture medium but also by the metabolic activity of the cells at the preceding pHs in the sequence. The results are discussed in relation to the mechanisms available for the maintenance of pH homeo-stasis and for the metabolic control of fermentation pathways in Strep. bovis.     

Kinetic analysis of batch and continuous culture of Streptococcus cremoris HP1.

The growth of Streptococcus cremoris on a semidefined medium was studied at initial lactose concentrations of 0.2-5.0% in batch culture, and in lactose-limited chemostat cultures at 0.5% lactose. Kinetic analysis of the batch data, using statisitcal techniques, indicated the importance of lactose limitation and lactic acid inhibition of the growth of S. cremoris. A model for the biomass production, lactose utilization, and lactic acid production in batch culture was proposed. In continuous culture, it was found that steady state populations were maintained at higher dilution rates (D = 0.6-0.7 h-1) than the maximum predicted by batch culture (0.56h-1). No evidence for a selection of fast growing mutants was obtained. Copious growth adhering to the walls of the fermentor (i.e. wall growth) occurred very rapidly at higher dilution rates and this undoubtedly affected steady-state growth and wash-out and, as a consequence, the apparent maximum dilution rate.     

Genetic transformation and cell morphology of Bacillus subtilis grown in Mg+(+)-limited chemostat culture

The rate and frequency of genetic transformation of Bacillus subtilis grown in Mg+(+)-limited chemostat culture are dependent on the dilution rate (D) of the system and achieved maximum values at D = 0.23 h-1. Mg+(+)-limitation induced a morphological change in the cells from their normal rod shape to extended helices. Although this change in shape was a transient phenomenon, under some conditions it persisted for several days and resulted in an apparent increase in the transformation frequency.