Production and localization of beta-fructosidase in asynchronous and synchronous chemostat cultures of yeasts

In synchronized continuous cultures of Saccharomyces cerevisiae CBS 8066, the production of the extracellular invertase (EC 3.2.1.26) showed a cyclic behavior that coincided with the budding cycle. The invertase activity increased during bud development and ceased at bud maturation and cell scission. The cyclic changes in invertase production resulted in cyclic changes in amounts of invertase localized in the cell wall. However, the amount of enzyme invertase present in the culture liquid remained constant throughout the budding cycle. Also, in asynchronous continuous cultures of S. cerevisiae, the production and localization of invertase showed significant fluctuation. The overall invertase production in an asynchronous culture was two to three times higher than in synchronous cultures. This could be due to more-severe invertase-repressive conditions in a synchronous chemostat culture. Both the intracellular glucose-6-phosphate concentration and residual glucose concentration were significantly higher in synchronous chemostat cultures than in asynchronous chemostat cultures. In the asynchronous and synchronous continuous cultures of S. cerevisiae, about 40% of the invertase was released into the culture liquid; it has generally been believed that S. cerevisiae releases only about 5% of its invertase. In contrast to invertase production and localization in the chemostat cultures of S. cerevisiae, no significant changes in inulinase (EC 3.2.1.7) production and localization were observed in chemostat cultures of Kluyveromyces maxianus CBS 6556. In cultures of K. marxianus about 50% of the inulinase was present in the culture liquid.     

Buoyant density variation during the cell cycle of Saccharomyces cerevisiae

Cell buoyant densities of the budding yeast Saccharomyces cerevisiae were determined for rapidly growing asynchronous and synchronous cultures by equilibrium sedimentation in Percoll gradients. The average cell density in exponentially growing cultures was 1.1126 g/ml, with a range of density variation of 0.010 g/ml. Densities were highest for cells with buds about one-fourth the diameter of their mother cells and lowest when bud diameters were about the same as their mother cells. In synchronous cultures inoculated from the least-dense cells, there was no observable perturbation of cell growth: cell numbers increased without lag, and the doubling time (66 min) was the same as that for the parent culture. Starting from a low value at the beginning of the cycle, cell buoyant density oscillated between a maximum density near midcycle (0.4 generations) and a minimum near the end of the cycle (0.9 generations). The pattern of cyclic variation of buoyant density was quantitatively determined from density measurements for five cell classes, which were categorized by bud diameter. The observed variation in buoyant density during the cell cycle of S. cerevisiae contrasts sharply with the constancy in buoyant density observed for cells of Escherichia coli, Chinese hamster cells, and three murine cell lines.     

Regulation of trehalase activity during the cell cycle of Saccharomyces cerevisiae

Synchronous cultures of Saccharomyces cerevisiae prepared by selection of small unbudded cells from an elutriating rotor were used to measure trehalase activity during the cell cycle. After the small cells had been removed from the rotor, the remainder was used to prepare asynchronous control cultures. Both synchronous and control cultures were studied for two cell cycles. In asynchronous cultures the trehalase activity of crude cell lysates rose continuously. In synchronized populations trehalase activity increased from the beginning of budding onwards. However, around the period of cell division the enzyme activity dropped rapidly but transiently by more than 5-fold. The same changes were found during the second budding cycle. Measurements of invertase and glucose-6-phosphate dehydrogenase activities in the same synchronous and asynchronous cultures revealed a continuous increase for both enzymes. Incubation of cell lysates with cAMP-dependent protein kinase before assaying for trehalase resulted in a 2-fold enhancement of enzyme activity in asynchronous control cultures. In synchronized cells this treatment also led to a significant stimulation of trehalase activity, and largely abolished the cell-cycle-dependent oscillatory pattern of enzyme activity. These results suggest that the activity of trehalase during the cell cycle is regulated, presumably at the post-translational level, by a phosphorylation-dephosphorylation mechanism.     

Competition for glucose between the yeasts Saccharomyces cerevisiae and Candida utilis.

The competition between the yeasts Saccharomyces cerevisiae CBS 8066 and Candida utilis CBS 621 for glucose was studied in sugar-limited chemostat cultures. Under aerobic conditions, C. utilis always successfully completed against S. cerevisiae. Only under anaerobic conditions did S. cerevisiae become the dominant species. The rationale behind these observations probably is that under aerobic glucose-limited conditions, high-affinity glucose/proton symporters are present in C. utilis, whereas in S. cerevisiae, glucose transport occurs via facilitated diffusion with low-affinity carriers. Our results explain the frequent occurrence of infections by Crabtree-negative yeasts during bakers' yeast production.     

Production, Distribution, and Kinetic Properties of Inulinase in Continuous Cultures of Kluyveromyces marxianus CBS 6556

From a screening of several Kluyveromyces strains, the yeast Kluyveromyces marxianus CBS 6556 was selected for a study of the parameters relevant to the commercial production of inulinase (EC 3.2.1.7). This yeast exhibited superior properties with respect to growth at elevated temperatures (40 to 45°C), substrate specificity, and inulinase production. In sucrose-limited chemostat cultures growing on mineral medium, the amount of enzyme decreased from 52 U mg of cell dry weight⁻¹ at D = 0.1 h⁻¹ to 2 U mg of cell dry weight⁻¹ at D = 0.8 h⁻¹. Experiments with nitrogen-limited cultures further confirmed that synthesis of the enzyme is negatively controlled by the residual sugar concentration in the culture. High enzyme activities were observed during growth on nonsugar substrates, indicating that synthesis of the enzyme is a result of a derepression/repression mechanism. A substantial part of the inulinase produced by K. marxianus was associated with the cell wall. The enzyme could be released from the cell wall via a simple chemical treatment of cells. Results are presented on the effect of cultivation conditions on the distribution of the enzyme. Inulinase was active with sucrose, raffinose, stachyose, and inulin as substrates and exhibited an S/I ratio (relative activities with sucrose and inulin) of 15 under standard assay conditions. The enzyme activity decreased with increasing chain length of the substrate.     

Cloning and sequencing of the inulinase gene of Kluyveromyces marxianus var. marxianus ATCC 12424.

Cell wall inulinase (EC 3.2.1.7) was purified from Kluyveromyces marxianus var. marxianus (formerly K. fragilis) and its N-terminal 33-amino acid sequence was established. PCR amplification of cDNA with 2 sets of degenerate primers yielded a genomic probe which was then used to screen a genomic library established in the YEp351 yeast shuttle vector. One of the selected recombinant plasmids allowed an invertase-negative Saccharomyces cerevisiae mutant to grow on inulin. It was shown to contain an inulinase gene (INU 1) encoding a 555-amino acid precursor protein with a typical N-terminal signal peptide. The sequence of inulinase displays a high similarity (67%) to S. cerevisiae invertase, suggesting a common evolutionary origin for yeast beta-fructosidases with different substrate preferences.     

Use of chemostat data for modelling extracellular-inulinase production by Kluyveromyces marxianus in a high-cell-density fed-batch process

Production of extracellular inulinase by low-cell-density (2 kg dry weight·m⁻³) sucrose-limited chemostat cultures of Kluyveromyces marxianus obeyed saturated kinetics at dilution rates ranging from 0.02 to 0.5 h⁻¹. A non-structured Monod-type equation, describing the relation between specific growth rate and specific extracellular-inulinase production rate, was used to fit experimental data. THis equation was subsequently incorporated in a model for the production of biomass and extracellular inulinase in a high-cell-density (> 100 kg dry weight·m⁻³) fed-batchculture of K. marxianus grown on sucrose. The model adequately described biomass production in the fed-batch culture. However, the production of extracellular inulinase in the fed-batch process was slightly higher than predicted by the model. This observation may be related to differences in growth conditions between in the chemostat and fed-batch cultures.     

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.     

The effect of vitamins and amino acids on glucose uptake in aerobic chemostat cultures of three Saccharomyces cerevisiae strains

In the respiro-fermentative region of aerobic chemostat cultures at steady state, Saccharomyces cerevisiae CBS 8066 produced high concentrations of ethanol with concomitant low levels of residual glucose which followed Monod kinetics. By contrast, very high residual glucose concentrations were observed in cultures of S. cerevisiae strains ATCC 4126 and NRRL Y132 at dilution rates above 60% of the washout dilution rate, resulting in much lower ethanol concentrations, even though clearly glucose-limited at lower dilution rates in the respiratory region. The addition of a vitamin mixture resulted in decreased residual glucose concentrations in respiro-fermentative cultures of all three strains, but the effect was much more pronounced with strains ATCC 4126 and NRRL Y132. Meso-inositol was mainly responsible for this effect, although with strain ATCC 4126 other vitamins as well as an amino acid mixture were also required to minimise the steady-state residual glucose levels. The residual glucose concentration in continuous culture was, therefore, greatly dependent on the growth factor requirements of the particular yeast strain, which apparently increased on increasing the dilution rate into the respiro-fermentative region. The strain differences with respect to growth factor requirements at high dilution rates, which were not evident at low dilution rates, had a profound effect on the kinetics of glucose assimilation in aerobic chemostat culture.     

Synchronous cell growth occurs upon synchronizing the two regulatory steps of the Saccharomyces cerevisiae cell cycle

There are two known asynchronous steps in the budding yeast Saccharomyces cerevisiae cell cycle, where an asynchronous step is one which is completed in different lengths of time by different cells in an isogenic population. It is shown here that elimination of the asynchrony due to cell size by preincubation of cells with the mating pheromone alpha-factor, and decreasing the asynchrony in the cdc28 'start' step by lowering the pH, yields highly synchronous cell growth measured as the time period between the emergence of buds. In one experiment, cell budding for 92% of cells occurred within a 12-min period for at least two generations. Under identical conditions, cell number increase is not as synchronous as bud emergence indicating that there is a third asynchronous step, which is concluded to be at cell separation. These results are consistent with there being two--and only two--asynchronous steps in the cell cycle, measured from bud emergence to bud emergence. Surprisingly, these two steps are also the two major regulatory steps of the cell cycle. It is concluded that asynchrony may be a general feature of cell cycle regulatory steps. The asynchrony in the completion of the cdc28 'start' step which occurs in the first cell cycle after alpha-factor washout is shown here to be almost or entirely eliminated for the second passage through this step after alpha-factor washout. The 'true' time between the onset of budding and the point where 50% of cells have budded (called t50BE) is 17 and less than or equal to 2 min for the first and second budding, respectively, after alpha-factor washout. The cell cycle models requiring a transition probability, or asynchrony, at 'start' for every cell cycle are therefore incorrect.     

Changes in carbohydrate composition and trehalase-activity during the budding cycle of Saccharomyces cerevisiae

Summary The carbohydrate composition and the specific activity of the trehalase of cyclic partially synchronised yeast populations have been investigated. Under glucose limitation and appropriate cultural conditions synchronous growth in a chemostat was achieved. The cells accumulated the reserve carbohydrates during the single cell phase between two buddings. The rapid degradation of part of these reserves began shortly before the swelling of the bud. The importance of the mobilisation of endogenous reserves for the development of the cell is discussed.The specific activity of the trehalase changed during the budding cycle. The result gives rise to the assumption that the synthesis of this enzyme is linked to the growth cycle.     

Localization of inulinase and invertase in Kluyveromyces species

In vivo hydrolysis of inulin and sucrose was examined in selected yeasts of the genus Kluyveromyces. Cells, grown in sucrose-limited chemostat cultures, were subjected to treatments for the removal of inulinase, the enzyme responsible for the hydrolysis of both inulin and sucrose. The effects of these treatments were studied by measurement of inulin-dependent and sucrose-dependent oxygen consumption by cell suspensions. In Kluyveromyces marxianus var. marxianus, inulinase was partially secreted into the culture fluid. Removal of culture fluid inulinase by washing had no effect on sucrose-dependent oxygen consumption by this yeast. However, this treatment drastically reduced inulin-dependent oxygen consumption. Treatment of washed cells with sulfhydryls removed part of the cell wall-retained inulinase and reduced inulin-dependent oxygen consumption by another 80%. Sucrose-dependent oxygen consumption was less affected, decreasing by 40%. Cell suspensions of K. marxianus var. drosophilarum, K. marxianus var. vanudenii, and Saccharomyces kluyveri rapidly utilized sucrose but not inulin. This is in accordance with the classification of these yeasts as inulin negative. Supernatants of cultures grown at pH 5.5 did not catalyze the hydrolysis of inulin and sucrose. This suggested that these yeasts contained a strictly cell-bound invertase, an enzyme not capable of inulin hydrolysis. However, upon washing, cells became able to utilize inulin. The inulin-dependent oxygen consumption further increased after treatment of the cells with sulfhydryls. These treatments did not affect the sucrose-dependent oxygen consumption of the cells. Apparently, these treatments removed a permeability barrier for inulin that does not exist for sucrose.(ABSTRACT TRUNCATED AT 250 WORDS)     

腐皮镰孢菌壳聚糖酶的酶学性质研究及其在酿酒酵母工业菌株中的表达

摘要：【目的】本研究旨在了解腐皮镰孢菌（Fusarium solani）壳聚糖酶的基本酶学性质及其在壳寡糖生产中的应用,构建能高效分泌表达壳聚糖酶的酿酒酵母工业菌株。【方法】采用RT-PCR扩增腐皮镰孢菌壳聚糖酶的cDNA序列;通过组氨酸标签,纯化得到E. coli表达的重组壳聚糖酶,并进行基本酶学性质研究;以薄层层析、高效液相色谱等技术对该酶的酶解产物进行分析;通过马克斯克鲁维酵母（Kluyveromyces marxianus）菊粉酶信号肽（INU1A）实现壳聚糖酶在酿酒酵母工业菌株N-27中的分泌表     

Oxygen, pH value, and carbon source induced changes of the mode of oscillation in synchronous continuous culture of Saccharomyces cerevisiae

Oscillations of measured process parameters occur in continuous cultures of Saccharomyces cerevisiae owing to a partial synchronization of budding. Intentional changes of the oxygen concentration, pH value, and carbon source cause effects on the period length similar to those known from variations of the dilution rate. The generation times of parent and daughter cells frequently differ in synchronous culture. To analyze the oscillation the term mode IJ of oscillation is used, which is defined as the ratio IJ of the generation times of parent and daughter cells. When the dissolved oxygen concentration was reduced to zero, the mode of oscillation changed within two periods from mode 12 to mode 11, caused by a decrease of the generation time of daughter cells and an increase of that of the parent cells. When the pH value was slowly reduced from 5.0 to 3.9, a change from mode 112 to mode 13 was observed. Mode 13, representing one parent and three daughter cell populations (the start of budding of each of the three being delayed by one period), denotes an elongated generation time of the daughter cells compared to mode 112, marked by one parent and two different daughter cell classes. When the carbon source galactose was replaced by glucose a mode change from mode 12 to mode 11 was observed. This alteration of the mode was found to be dependent on the status of the cell cycle at the time when the carbon source is changed. The population distribution in batch cultures with glucose or galactose as a substrate was analysed by dyeing the DNA and counting the bud scars. Galactose provoked higher growth rates for the older cells. According to the model for stationary synchronous growth parameters like DO, pH value or the type of carbon source can be varied within a certain range without effecting the period length. If the variation imposes a certain stress, the culture switches to a new mode. These kinds of parameters therefore provide selective measures to influence the period lengths and the modes of oscillation.     

Studies on the stability of solvent production by Clostridium acetobutylicum in continuous culture

Various methods of continuous flow culture of Clostridium acetobutylicum NCIB 8052 were investigated, with the aim of obtaining prolonged production of acetone and butanol. In ammonia-limited chemostat culture, maximal concentrations of solvents were obtained at pH 5–5 at a relatively high biomass concentration of 1.3–2.0 g/1 dry weight maintained at a dilution rate of 0.06/h. Similar dependence of solvent production on the sustenance of a relatively high cell density was observed in magnesium- or phosphate-limited chemostat cultures. Solvent production was always transient, however, with a shift to production of only acetic and butyric acids being observed after 4–16 volume changes. Longer term solvent production was obtainable under conditions of glucose limitation but the solvent yield was low. Cultivation in a pH-auxostat permitted solvent production in reasonably high yield over at least 70 volume changes with no signs of culture degeneration. Although none of the continuous flow cultures achieved a true steady state, we conclude that turbidostat or pH-auxostat culture are the methods of choice for continuous solvent production by Cl. acetobutylicum NCIB 8052.     

Regulation of septin organization and function in yeast

Septins are a conserved eukaryotic family of GTP-binding filament-forming proteins with functions in cytokinesis and other processes. In the budding yeast Saccharomyces cerevisiae, septins initially localize to the presumptive bud site and then to the cortex of the mother-bud neck as an hourglass structure. During cytokinesis, the septin hourglass splits and single septin rings partition with each of the resulting cells. Septins are thought to function in diverse processes in S. cerevisiae, mainly by acting as a scaffold to direct the neck localization of septin-associated proteins.     

Cell cycle phase expansion in nitrogen-limited cultures of Saccharomyces cerevisiae

The time and coordination of cell cycle events were examined in the budding yeast Saccharomyces cerevisiae. Whole-cell autoradiographic techniques and time-lapse photography were used to measure the duration of the S, G1, and G2 phases, and the cell cycle positions of "start" and bud emergence, in cells whose growth rates were determined by the source of nitrogen. It was observed that the G1, S, and G2 phases underwent a proportional expansion with increasing cell cycle length, with the S phase occupying the middle half of the cell cycle. In each growth condition, start appeared to correspond to the G1 phase/S phase boundary. Bud emergence did not occur until mid S phase. These results show that the rate of transit through all phases of the cell cycle can vary considerably when cell cycle length changes. When cells growing at different rates were arrested in G1, the following synchronous S phase were of the duration expected from the length of S in each asynchronous population. Cells transferred from a poor nitrogen source to a good one after arrest in G1 went through the subsequent S phase at a rate characteristic of the better medium, indicating that cells are not committed in G1 to an S phase of a particular duration.     

Secretion and localization of invertase and inulinase in recombinant Saccharomyces cerevisiae

Summary Secretion of invertase and inulinase produced by recombinant Saccharomyces cerevisiae cells were investigated under derepression conditions of GALI promoter. Secreted invertase mainly localized in the periplasmic space, but most of inulinase was found in the extracellular culture medium. This high level of extracellular secretion of inulinase was not dependent on the growth phase in which derepression of GALI promoter occurs. Our results indicate that the inulinase polypeptide itself may have a function for the protein secretion into the culture medium.     

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.