Utilization of mixed sugars in continuous fermentation. II.

Batch growth characteristics of various organisms were determined on a number of pairs of sugars to find a stable system showing clear-cut classical diauxie. The system selected for further study was a strain of Klebsiella (Acrobacter) aerogenes, NCIB 8021 growing on a mixture of glucose and maltose in minimal salts medium at 30°C. This showed a specific growth rate (μ) of 1.19 ± 0.03 hr.^?1 on 0.01% (w/v) glucose, followed by a diauxie lag of 0.73 ± 0.04 hr and then further growth on 0.01% (w/v) maltose at μ = 0.60 ± 0.03 hr^?1. This system was applied to a two-stage continuous, stirred, aerated fermentor system, with working volumes of 1.85 and 2.77 liters, respectively, and growth was followed (mainly by optical density, referred to dry weights and viable counts) and also the concentrations of the sugars were measured. Except at the very highest flow rates, glucose was immediately and virtually completely consumed, but the utilization of maltose showed interesting variations: (a) At low feed rates between 0.09 and 0.4 vol./hr. exactly the same response was found with mixed sugars as with double concentration glucose, showing that the organism was able to metabolize maltose as well and as quickly as glucose. (b) At medium feed rates of 0.46 to 1.03 vol./hr. two deviations were observed, both of which increased as the dilution rate increased: the system showed a time lag on maltose before the cell population began to rise and the volume of medium used before the steady state was established was greater than predicted, (c) At fast feed rates, approaching “washout” condition of 1.055 to 1.135 vol./hr. the first culture vessel showed no reaction to a step change which included maltose, although, of course, with doubled glucose it responded immediately. The second vessel, however, quickly metabolized the overflow maltose, and showed a steady increase of cell population to the theoretical steady state. These results may have significance for industrial systems using complex commercial substrates.     

Cybernetic model of the growth dynamics of Saccharomyces cerevisiae in batch and continuous cultures.

Growth of Saccharomyces cerevisiae on glucose in aerobic batch culture follows the well-documented diauxic pattern of completely fermenting glucose to ethanol during the first exponential growth phase, followed by an intermediate lag phase and a second exponential growth phase consuming ethanol. In continuous cultures over a range of intermediate dilution rates, the yeast bioreactor exhibits sustained oscillations in all the measured concentrations, such as cell mass, glucose, ethanol, and dissolved oxygen, the amounts of intracellular storage carbohydrates, such as glycogen and trehalose, the fraction of budded cells as well as the culture pH. We present here a structured, unsegregated model for the yeast growth dynamics developed from the 'cybernetic' modeling framework, to simulate the dynamic competition between all the available metabolic pathways. This cybernetic model accurately predicts all the key experimentally observed aspects: (i) in batch cultures, duration of the intermediate lag phase, sequential production and consumption of ethanol, and the dynamics of the gaseous exchange rates of oxygen and carbon dioxide; and (ii) in continuous cultures, the spontaneous generation of oscillations as well as the variations in period and amplitude of oscillations when the dilution rate or agitatin rate are changed.     

Regulation of beta-D-galactosidase synthesis in Candida pseudotropicalis.

Regulation of lactose (beta-D-galactosidase) synthesis in the lactose-utilizing yeast Candida pseudotropicalis was studied. The enzyme was inducible by lactose and galactose. When grown on these sugars the enzyme level of the yeast was 20 times or higher than when grown on glycerol. The Km and optimal pH were similar for the lactase induced either by lactose or galactose. The hydrolysis of o-nitrophenyl-beta-D-galactopyranoside by the lactase was inhibited by galactose and several analogs and galactosides, but not by glucose. Lactose uptake activity observed in lactose-grown cells was very reduced in cells grown on glucose or galactose. Glucose repressed the induction of lactase, but not the metabolic system for galactose utilization. In continuous culture on lactose medium at dilution rates below 0.2 h-1 the specific lactase activity was higher than in batch cultures and decreased with increases in dilution rate. Lactase was induced by pulses of lactose and galactose in cells growing on glucose, but only at low dilution rates were the steady-state concentration of glucose was very low.     

Effect of temperature on diauxic growth with glucose and organic acids in Pseudomonas fluorescens

Growth of Pseudomonas fluorescens in batch culture with glucose and organic acids resulted in typical diauxic responses at 30° C but no detectable diauxic lag at 5° C.At 30° C, organic acids were preferentially utilized during the first growth phase. Glucose utilization was delayed unitl onset of the second growth phase. Systems involved in direct uptake and catabolism of glucose responded in a manner compatible with respression by malate and/or its metabolites and induction by glucose and/or its metabolites. The oxidative non-phosphorylated pathway, through gluconate and 2-ketogluconate (2-KG) as intermediates, was not induced during either growth phase.At 5° C, growth with glucose and organic acids was biphasic but without diauxic lag. Organic acids were preferentially utilized during the first growth phase. Although carbon from glucose was not fully catabolized until onset of the second growth phase, glucose was oxidized to and accumulated extracellularly as gluconate and 2-KG during the first growth phase. No significant repression of glucose-catabolizing enzymes was observed during growth with organic acids in the presence of glucose. However, uptake activities for gluconate and 2-KG did not increase significantly until onset of the second growth phase.Thus, at low temperatures, psychrotrophic P. fluorescens oxidized glucose to extracellular 2-KG, while growing on preferred carbon sources. The 2-KG was then catabolized after depletion of the organic acid.     

Control of mixed-substrate utilization in continuous cultures of Escherichia coli

The chemostat culture technique was used to study the control mechanisms which operate during utilization of mixtures of glucose and lactose and glucose and l-aspartic acid by populations of Escherichia coli B6. Constitutive mutants were rapidly selected during continuous culture on a mixture of glucose and lactose, and the beta-galactosidase level of the culture increased greatly. After mutant selection, the specific beta-galactosidase level of the culture was a decreasing function of growth rate. In cultures of both the inducible wild type and the constitutive mutant, glucose and lactose were simultaneously utilized at moderate growth rates, whereas only glucose was used in the inducible cultures at high growth rates. Catabolite repression was shown to be the primary mechanism of control of beta-galactosidase level and lactose utilization in continuous culture on mixed substrates. In batch culture, as in the chemostat, catabolite repression acting by itself on the lac enzymes was insufficient to prevent lactose utilization or cause diauxie. Interference with induction of the lac operon, as well as catabolite repression, was necessary to produce diauxic growth. Continuous cultures fed mixtures of glucose and l-aspartic acid utilized both substrates at moderate growth rates, even though the catabolic enzyme aspartase was linearly repressed with increasing growth rate. Although the repression of aspartase paralleled the catabolite repression of beta-galactosidase, l-aspartic acid could be utilized even at very low levels of the catabolic enzyme because of direct anabolic incorporation into protein.     

Glucose Utilization by Euglena gracilis var. bacillaris at Higher pH*

SYNOPSIS. Euglena gracilis var. bacillaris is able to grow luxuriantly on glucose in a mineral salts medium at pH 6.8–7.1 following an adaptation period of about 200 hr. If adapted cells are used as an inoculum or if 0.1% glycine is included in the medium, the lag is shortened to 70–100 hr. Inclusion of 0.1% acetate in the medium produces a diphasic growth pattern, with acetate being metabolized first, followed by the later (about 400 hr) utilization of the glucose. Glucose utilization was found to be sensitive to pH as compared to growth on ethyl alcohol. However, glycine partially overcame this sensitivity. Glycine is maximally stimulatory with regard to growth on glucose at pH 7.0 at a concentration of 0.03%, thus suggesting that it functions as a sparking substance. Glycine markedly stimulates the assimilation of ¹⁴C-glucose. A number of Krebs cycle acids and amino acids were also found to stimulate ¹⁴C-glucose assimilation at neutral pH. Adaptation to glucose utilization at neutral pH was due to the appearance of mutants able to grow more rapidly under these conditions. The nature of this mutation was not determined.     

Preferential use of glucose during diauxic growth of Carrot cells growing on glucose and malate

Suspension cells of carrot plants grown on mixed carbon sources of glucose (Glc) and malate preferentially used Glc. The cells started to utilize malate only after Glc was depleted from the medium, thus exhibiting a diauxic growth. The residual concentration of Glc decreased rapidly during the first growth phase, and that of malate decreased only during the second growth phase. Malate uptake was negligible throughout the diauxic growth, suggesting that malate was being utilized via another metabolite. An active metabolic flow from fumarate to pyruvate and oxaloacetate via malate was induced in cells during the second growth phase. These results strongly suggested that malate remained unused in the medium in the first phase, and in the second phase it was converted extracellularly into fumarate, which was subsequently transported into cells and metabolized into malate and further into pyruvate and oxaloacetate. This study presents the second case of diauxic growth in plants and the peculiar mode of malate utilization.     

Alcohol production by selected yeast strains in lactase-hydrolyzed acid whey

Ethanol production by Kluyveromyces fragilis and Saccharomyces cerevisiae was studied using cottage cheese whey in which 80 to 90% of the lactose present had been prehydrolyzed to glucose and galactose. Complete fermentation of the sugar by K. fragilis required 120 hr at 30°C in lactase-hydrolyzed whey compared to 72 hr in nonhydrolyzed whey. This effect was due to a diauxic fermentation pattern in lactase-hydrolyzed whey with glucose being fermented before galactose. Ethanol yields of about 2% were obtained in both types of whey when K. fragilis was the organism used for fermentation. Saccharomyces cerevisiae produced alcohol from glucose more rapidly than K. fragilis, but galactose was fermented only when S. cerevisiae was pregrown on galactose. Slightly lower alcohol yields were obtained with S. cerevisiae, owing to the presence of some lactose in the whey which was not fermented by this organism. Although prehydrolysis of lactose in whey and whey fractions is advantageous in that microbial species unable to ferment lactose may be utilized, diauxie and galactose utilization problems must be considered.     

Regulation of peptidoglycan biosynthesis in relA+ and relA- strains of Escherichia coli during diauxic growth on glucose and lactose.

In both relA+ and relA- derivatives, the biosynthesis of peptidoglycan, lipid intermediates, and nucleotide precursors abruptly halted at the onset of diauxic lag from glucose to lactose with a concomitant accumulation of guanosine 5'-diphosphate 3'-diphosphate (ppGpp). These results are consistent with the proposal that ppGpp is involved in inhibiting the incorporation of disaccharide-pentapeptide into peptidoglycan and in regulating nucleotide precursor synthesis.     

Regulation of Staphylococcal Enterotoxin B

Several factors influenced the formation of enterotoxin B by Staphylococcus aureus strain S-6. In the standard casein hydrolysate medium, toxin was not produced in detectable quantities during exponential growth; it was produced during the post-exponential phase when total protein synthesis was arithmetic. The rate of toxin synthesis was much greater than the rate of total protein synthesis. The appearance of enterotoxin was inhibited by chloramphenicol; thus, the presence of toxin was dependent on de novo protein synthesis. When low concentrations of glucose (<0.30%) were added to the casein hydrolysate medium, growth was diauxic; glucose was completely metabolized during the first growth period. During the second growth period, enterotoxin was synthesized. In unbuffered casein hydrolysate medium containing excess glucose, toxin synthesis was completely repressed. The absence of toxin production under such conditions might be explained by the low (4.6) pH resulting from the acid end products of glucose metabolism. At pH <5.0, little or no toxin was produced. Toxin synthesis was initiated in the presence of glucose when the medium were buffered at any pH above 5.6. In such media, the differential rates of toxin synthesis, with respect to the rates of total protein synthesis, were lower than the differential rates in casein hydrolysate medium alone. Addition of glucose to a culture synthesizing toxin resulted in an immediate decrease in the differential rate without any change in pH. Thus, toxin synthesis appeared to be regulated by catabolite repression.     

Metabolic regulation in Pseudomonas oxalaticus OX1. Diauxic growth on mixtures of oxalate and formate or acetate

Diauxic growth was observed in batch cultures of Pseudomonas oxalaticus when cells were pregrown on acetate and then transferred to mixtures of acetate and oxalate. In the first phase of growth only acetate was utilized. After the exhaustion of acetate from the medium enzymes involved in the metabolism of oxalate were synthesized during a lag phase of 2 h, followed by a second growth phase on oxalate. When the organism was pregrown on oxalate, oxalate utilization from the mixture with acetate completely ceased after a few hours during which acetate became the preferred substrate. Similar observations were made with formate/oxalate mixtures in which formate was the preferred substrate. Until formate was exhausted, it completely suppressed oxalate metabolism, again resulting in diauxic growth. However, when the organism was pregrown on oxalate and then transferred to mixtures of oxalate and formate, both substrates were utilized simultaneously although the initial rate of oxalate utilization from the mixture was strongly reduced as compared to growth on oxalate alone.Since both preferred substrates cross the cytoplasmic membrane by diffusion, whereas oxalate is accumulated by an inducible, active transport system, the effect of acetate and formate on oxalate transport was studied at different external pH values. At pH 5.5 both substrates completely inhibited oxalate transport. However, at pH 7.5, the pH at which the diauxic growth experiments were performed, formate and acetate did not affect oxalate transport. Growth patterns and enzymes profiles suggest that, at higher pH values, formate and acetate possibly affect oxalate utilization via an effect on the internal pool of oxalyl-CoA, the first product of oxalate metabolism.Abbreviations PMS phenazine methosulphate - RuBPCase ribulosebisphosphate carboxylase - DCPIP 2,6-dichlorophenolindophenol - FDH formate dehydrogenase - p.m.f. protonmotive force     

Regulation of beta-glucosidase in Bacteroides ruminicola by a different mechanism: growth rate-dependent derepression.

Bacteroides ruminicola B(1)4, a predominant ruminal and cecal bacterium, was grown in batch and continuous cultures, and beta-glucosidase activity was measured by following the hydrolysis of p-nitrophenyl-beta-glucopyranoside. Specific activity was high when the bacterium was grown in batch cultures containing cellobiose, mannose, or lactose (greater than 286 U/g of protein). Activity was reduced approximately 90% when the organism was grown on glucose, sucrose, fructose, maltose, or arabinose. The specific activity of cells fermenting glucose was initially low but increased as glucose was depleted. When glucose was added to cultures growing on cellobiose, beta-glucosidase synthesis ceased immediately. Catabolite repression by glucose was not accompanied by diauxic growth and was not relieved by cyclic AMP. Since glucose-grown cultures eventually exhibited high beta-glucosidase activity, cellobiose was not needed as an inducer. Catabolite repression explained beta-glucosidase activity of batch cultures and high-dilution-rate chemostats where glucose accumulated, but it could not account for activity at slow dilution rates. Maximal beta-glucosidase activity was observed at a dilution rate of approximately 0.35 h-1, and cellobiose-limited chemostats showed a 15-fold decrease in activity as the dilution rate declined. An eightfold decline was observed in glucose-limited chemostats. Since inducer availability was not a confounding factor in glucose-limited chemostats, the growth rate-dependent derepression could not be explained by other mechanisms.     

Role of inducer exclusion in preferential utilization of glucose over melibiose in diauxic growth of Escherichia coli

The role of inducer exclusion in diauxic growth of Escherichia coli on glucose and melibiose was investigated. The amounts of glucose and melibiose in the culture medium were determined during the diauxie. Glucose was consumed during the first growth cycle of the diauxie, and melibiose was consumed during the second cycle. The addition of adenosine 3',5'-cyclic monophosphate to the culture medium released both transient and catabolite repressions on the melibiose operon by glucose. Biphasic growth without a transient lag phase was observed in the presence of adenosine 3',5'-cyclic monophosphate. Preferential utilization of glucose over melibiose was observed even under such conditions. Thus, it is clear that inducer exclusion alone is sufficient to ensure the preferential utilization of glucose over melibiose. Similar results were obtained from a glucose-lactose diauxie. Inducer exclusion itself was not affected by adenosine 3',5'-cyclic monophosphate.     

Growth of Cephalotaxus harringtonia plant-cell cultures

Summary Cell cultures of Cephalotaxus harringtonia were examined to characterize growth kinetics. The requirement for an undefined medium supplement (coconut water) was eliminated by maintaining high cell concentrations in semicontinuous and batch growth. Sucrose fed to batch-cultured cells was completely hydrolyzed and a diauxic growth pattern was observed corresponding to first glucose and then fructose uptake. Examination of increases in cell concentrations on the basis of fresh and dry weight showed that a substantial lag period existed between the initiation of substrate uptake and increases in cell volume. Specific growth rates were highest during periods of glucose uptake, but cell yields were comparable for the two sugars. In contrast, studies with glucose or fructose as the sole carbon source indicated that cell yields were significantly lower with fructose but specific growth rates were comparable for the two sugars.Offprint requests to: P. J. Westgate     

Functional capacities and the adenylate energy charge in Escherichia coli under conditions of nutritional stress.

Functional capacities in Escherichia coli cells starved for glucose were examined by comparing protein synthesis, utilization of new substrates, and maintenance of viability with the adenylate energy charge of the culture. When growth ceased because of glucose exhaustion in an E. coli culture, the energy charge dropped from 0.90 to about 0.80. During this time, the viable-cell count and the capacity for protein synthesis and for induction of new enzymes were maintained only if other substrates were available in the medium. The culture could be maintained for many hours without growth or death if glucose was added slowly; the energy charge in this case stabilized at about 0.80. A consistent transient decrease in the energy charge to around 0.80, accompanied by a decrease in protein synthesis, was also observed during the adaptation from glucose to other substrates during diauxic growth on glucose and glycerol or lactose.     

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.     

Influence of dilution rate and induction of cloned gene expression in continuous fermentations of recombinant yeast

The effects of growth rate on cloned gene product synthesis in recombinant Saccharomyces cerevisiae have been studied in continuous culture. The plasmid employed contains a yeast GAL10-CYC1 hybrid promoter directing expression of the E. coli lacZ gene. beta-Galactosidase production was therefore controlled by the yeast galactose regulatory circuit, and the induction process and its effects were studied at the various dilution rates. At all dilution rates plasmid stability decreased with induction of lacZ gene expression. In some instances, two induced "steady states" were observed, the first 10-15 residence times after induction and the second after 40-50 residence times. The second induced steady state was characterized by greater biomass concentration and lower beta-galactosidase specific activity relative to the first induced "steady-state." beta-Galactosidase specific activity and biomass concentration increased as dilution rate was reduced, and despite lower flow rate and plasmid stability, overall productivity (activity/L/hr) was substantially higher at low dilution rate. Important factors influencing all of the trends were the glucose and galactose (inducer) concentrations in the vessel and inducer metabolism.     

Repression of xylose-specific enzymes by ethanol in Scheffersomyces (Pichia) stipitis and utility of repitching xylose-grown populations to eliminate diauxic lag

During the fermentation of lignocellulosic hydrolyzates to ethanol by native pentose-fermenting yeasts such as Scheffersomyces (Pichia) stipitis NRRL Y-7124 (CBS 5773) and Pachysolen tannophilus NRRL Y-2460, the switch from glucose to xylose uptake results in a diauxic lag unless process strategies to prevent this are applied. When yeast were grown on glucose and resuspended in mixed sugars, the length of this lag was observed to be a function of the glucose concentration consumed (and consequently, the ethanol concentration accumulated) prior to the switch from glucose to xylose fermentation. At glucose concentrations of 95 g/L, the switch to xylose utilization was severely stalled such that efficient xylose fermentation could not occur. Further investigation focused on the impact of ethanol on cellular xylose transport and the induction and maintenance of xylose reductase and xylitol dehydrogenase activities when large cell populations of S. stipitis NRRL Y-7124 were pre-grown on glucose or xylose and then presented mixtures of glucose and xylose for fermentation. Ethanol concentrations around 50 g/L fully repressed enzyme induction although xylose transport into the cells was observed to be occurring. Increasing degrees of repression were documented between 15 and 45 g/L ethanol. Repitched cell populations grown on xylose resulted in faster fermentation rates, particularly on xylose but also on glucose, and eliminated diauxic lag and stalling during mixed sugar conversion by P. tannophilus or S. stipitis, despite ethanol accumulations in the 60 or 70 g/L range, respectively. The process strategy of priming cells on xylose was key to the successful utilization of high mixed sugar concentrations because specific enzymes for xylose utilization could be induced before ethanol concentration accumulated to an inhibitory level.     

Catabolite regulation in a diauxic strain and a nondiauxic strain of Streptococcus bovis

Streptococcus bovis JB1 utilized glucose preferentially to lactose and grew diauxically, but S. bovis 581AXY2 grew nondiauxically and used glucose preferentially only when the glucose concentration was very high (greater than 5 mM). As little as 0.1 mM glucose completely inhibited the lactose transport of JB1. The lactose transport system of 581AXY2 was at least tenfold less sensitive to glucose, and 1 mM glucose caused only a 50% inhibition of lactose transport. Both strains had phosphotransferase systems (PTSs) for glucose and lactose. The glucose PTSs were constitutive, but little lactose PTS activity was detected unless lactose was the energy source for growth. JB1 had approximately threefold more glucose PTS activity than 581AXY2 (1600 versus 600 nmol glucose (mg protein)⁻¹(min)⁻¹. The glucose PTS of JB1 showed normal Michaelis Menten kinetics, and the affinity constant (K _s ) was 0.12 mM. The glucose PTS of 581AXY2 was atypical, and the plot of velocity versus velocity/substrate was biphasic. The low capacity system had a K_s of 0.20 mM, but the K_s of the high capacity system was greater than 6 mM. On the basis of these results, diauxic growth is dependent on the affinity of glucose enzyme II and the velocity of glucose transport. Received: 22 January 1996 / Accepted: 18 March 1996