Xylulose fermentation by Saccharomyces cerevisiae and xylose-fermenting yeast strains

Xylulose fermentation by four strains of Saccharomyces cerevisiae and two strains of xylose-fermenting yeasts, Pichia stipitis CBS 6054 and Candida shehatae NJ 23, was compared using a mineral medium at a cell concentration of 10 g (dry weight)/l. When xylulose was the sole carbon source and fermentation was anaerobic, S. cerevisiae ATCC 24860 and CBS 8066 showed a substrate consumption rate of 0.035 g g cells^–1 h^–1 compared with 0.833 g g cells^–1 h^–1 for glucose. Bakers' yeast and S. cerevisiae isolate 3 consumed xylulose at a much lower rate although they fermented glucose as rapidly as the ATCC and the CBS strains. While P. stipitis CBS 6054 consumed both xylulose and glucose very slowly under anaerobic conditions, C. shehatae NJ 23 fermented xylulose at a rate of 0.345 g g cells^–1 h^–1, compared with 0.575 g g cells^–1 h^–1 for glucose. For all six strains, the addition of glucose to the xylulose medium did not enhance the consumption of xylulose, but increased the cell biomass concentrations. When fermentation was performed under oxygen-limited conditions, less xylulose was consumed by S. cerevisiae ATCC 24860 and C. shehatae NJ 23, and 50%–65% of the assimilated carbon could not be accounted for in the products determined.     

Xylulose fermentation by mutant and wild-type strains of Zygosaccharomyces and Saccharomyces cerevisiae

Anaerobic xylulose fermentation was compared in strains of Zygosaccharomyces and Saccharomyces cerevisiae, mutants and wild-type strains to identify host-strain background and genetic modifications beneficial to xylose fermentation. Overexpression of the gene (XKS1) for the pentose phosphate pathway (PPP) enzyme xylulokinase (XK) increased the ethanol yield by almost 85% and resulted in ethanol yields [0.61 C-mmol (C-mmol consumed xylulose)⁻¹] that were close to the theoretical yield [0.67 C-mmol (C-mmol consumed xylulose)⁻¹]. Likewise, deletion of gluconate 6-phosphate dehydrogenase (gnd1Δ) in the PPP and deletion of trehalose 6-phosphate synthase (tps1Δ) together with trehalose 6-phosphate phosphatase (tps2Δ) increased the ethanol yield by 30% and 20%, respectively. Strains deleted in the promoter of the phosphoglucose isomerase gene (PGI1) – resulting in reduced enzyme activities – increased the ethanol yield by 15%. Deletion of ribulose 5-phosphate (rpe1Δ) in the PPP abolished ethanol formation completely. Among non-transformed and parental strains S. cerevisiae ENY. WA-1A exhibited the highest ethanol yield, 0.47 C-mmol (C-mmol consumed xylulose)⁻¹. Other non-transformed strains produced mainly arabinitol or xylitol from xylulose under anaerobic conditions. Contrary to previous reports S. cerevisiae T23D and CBS 8066 were not isogenic with respect to pentose metabolism. Whereas, CBS 8066 has been reported to have a high ethanol yield on xylulose, 0.46 C-mmol (C-mmol consumed xylulose)⁻¹ (Yu et al. 1995), T23D only formed ethanol with a yield of 0.24 C-mmol (C-mmol consumed xylulose)⁻¹. Strains producing arabinitol did not produce xylitol and vice versa. However, overexpression of XKS1 shifted polyol formation from xylitol to arabinitol. Received: 2 July 1999 / Accepted in revised form: 12 October 1999     

Critical evaluation of sampling techniques for residual glucose determination in carbon-limited chemostat culture of Saccharomyces cerevisiae

In this paper, three sampling techniques for rapid quenching of cellular metabolism and subsequent separation of cells from fermentation broth are compared: (i) quick freezing of fermentation broth directly in liquid nitrogen; (ii) quenching metabolism by exposing the fermentation broth to stainless steel beads (4-mm diameter) in a filter syringe precooled to -18 degrees C; and (iii) withdrawal of the filtrate through a 0.45 microm filter attached to a syringe and a needle inserted directly into the fermentor. It was concluded that use of liquid nitrogen as a quenching method to rapidly arrest cellular metabolism, for quantitative analysis of extracellular glucose, is not a very reliable method and that the filter syringe steel beads work very well.     

Growth of Saccharomyces cerevisiae in a chemostat under high glucose conditions

Saccharomyces cerevisiae was grown in a chemostat under high glucose conditions (up to 300 g l^–1). The results support the view that higher glucose feed favors higher ethanol production regardless of the existence of osmotic stress. A low glucose utilization and yield coefficient provides an opportunity to improve continuous fermentation performance in the fuel alcohol industry. The possibility exists of reusing yeast cells and subsequently lower operating costs, and by using an optimal glucose feeding concentration between 100 and 200 g l^–1.     

Biosynthesis of superoxide dismutase and catalase in chemostat culture of Saccharomyces cerevisiae

Summary The effects of oxygen (100%), paraquat (0.5 mM), and copper (0.1 mM) on the growth and the biosynthesis of the antioxidant enzymes, superoxide dismutase (SOD) and catalase, were studied in Saccharomyces cerevisiae grown in glucose-limited chemostat cultures. The effect of dilution rates (D, h⁻¹) on cell mass, glucose consumption, ethanol production, oxygen uptake, and specific activities of SOD and catalase were also investigated at each steady state. SOD was optimally produced at D-values between 0.22 and 0.26 h⁻¹ in the presence of oxygen or paraquat, and at D-values greater than 0.17 h⁻¹ when copper was used. On the other hand, catalase activity decreased with increasing D-values. However, the presence of copper or 100% oxygen repressed catalase activity at low D-values (D<0.1 h⁻¹), and decreased the rate of oxygen uptake at all D-values tested. The presence of paraquat affected the rate of oxygen uptake only at high D-values (D>0.22 h⁻¹). We also studied the effect of oxygen concentration on the biosynthesis of SOD and catalase at D=0.1 h⁻¹. The data clearly show that synthesis of SOD and catalase, though correlated with changes in oxygen tension, are independent of one another. Paper Number 10871 of the Journal Series of North Carolina Agricultural Research Service, Raleigh, NC 27 695. The use of trade names in this publication does not imply endorsement by the North Carolina Agricultural Research Service of the products named, nor criticism of similar ones not mentioned     

The relationship between transport kinetics and glucose uptake by Saccharomyces cerevisiae in aerobic chemostat cultures

The steady-state residual glucose concentrations in aerobic chemostat cultures of Saccharomyces cerevisiae ATCC 4126, grown in a complex medium, increased sharply in the respiro-fermentative region, suggesting a large increase in the apparent k_s value. By contrast, strain CBS 8066 exhibited much lower steady-state residual glucose concentrations in this region. Glucose transport assays were conducted with these strains to determine the relationship between transport kinetics and sugar assimilation. With strain CBS 8066, a high-affinity glucose uptake system was evident up to a dilution rate of 0.41 h^–1, with a low-affinity uptake system and high residual glucose levels only evident at the higher dilution rates. With strain ATCC 4126, the high-affinity uptake system was present up to a dilution rate of about 0.38 h^–1, but a low-affinity uptake system was discerned already from a dilution rate of 0.27 h^–1, which coincided with the sharp increase in the residual glucose concentration. Neither of the above yeast strains had an absolute vitamin requirement for aerobic growth. Nevertheless, in the same medium supplemented with vitamins, no low-affinity uptake system was evident in cells of strain ATCC 4126 even at high dilution rates and the steady-state residual glucose concentration was much lower. The shift in the relative proportions of the high and low-affinity uptake systems of strain ATCC 4126, which might have been mediated by an inositol deficiency through its effect on the cell membrane, may offer an explanation for the unusually high steady-state residual glucose concentrations observed at dilution rates above 52% of the wash-out dilution rate.     

Maltotriose fermentation by Saccharomyces cerevisiae

Maltotriose, the second most abundant sugar of brewer's wort, is not fermented but is respired by several industrial yeast strains. We have isolated a strain capable of growing on a medium containing maltotriose and the respiratory inhibitor, antimycin A. This strain produced equivalent amounts of ethanol from 20 g l⁻¹ glucose, maltose, or maltotriose. We performed a detailed analysis of the rates of active transport and intracellular hydrolysis of maltotriose by this strain, and by a strain that does not ferment this sugar. The kinetics of sugar hydrolysis by both strains was similar, and our results also indicated that yeast cells do not synthesize a maltotriose-specific α-glucosidase. However, when considering active sugar transport, a different pattern was observed. The maltotriose-fermenting strain showed the same rate of active maltose or maltotriose transport, while the strain that could not ferment maltotriose showed a lower rate of maltotriose transport when compared with the rates of active maltose transport. Thus, our results revealed that transport across the plasma membrane, and not intracellular hydrolysis, is the rate-limiting step for the fermentation of maltotriose by these Saccharomyces cerevisiae cells. Journal of Industrial Microbiology & Biotechnology (2001) 27, 34–38. Received 13 January 2001/ Accepted in revised form 29 May 2001     

Xylose fermentation by Saccharomyces cerevisiae

We have performed a comparative study of xylose utilization in Saccharomyces cerevisiae transformants expressing two key enzymes in xylose metabolism, xylose reductase (XR) and xylitol dehydrogenase (XDH), and in a prototypic xylose-utilizing yeast, Pichia stipitis. In the absence of respiration (see text), baker's yeast cells convert half of the xylose to xylitol and ethanol, whereas P. stipilis cells display rather a homofermentative conversion of xylose to ethanol. Xylitol production by baker's yeast is interpreted as a result of the dual cofactor dependence of the XR and the generation of NADPH by the pentose phosphate pathway. Further limitations of xylose utilization in S. cerevisiae cells are very likely caused by an insufficient capacity of the non-oxidative pentose phosphate pathway, as indicated by accumulation of sedoheptulose-7-phosphate and the absence of fructose-1,6-bisphosphate and pyruvate accumulation. By contrast, uptake at high substrate concentrations probably does not limit xylose conversion in S. cerevisiae XYL1/XYL2 transformants. Correspondence to: M. Ciriacy     

Toxicity of hardwood extractives toward Saccharomyces cerevisiae glucose fermentation

The toxicity of oak and yellow-poplar wood extracts, as well as a first-stage hardwood hydrolyzate liquor prepared from a red oak:white oak:yellow-poplar (1:1:1) sawdust, on Saccharomyces cerevisiae D5A was examined. Acetone/water and hot methanol extracts of solid biomass samples from white oak, red oak, and yellow-poplar gave 88-94% of the ethanol produced with controls. The organism was tolerant to the compounds present in the xylose-rich hydrolyzate, with fermentation efficiency being improved to 97% of that obtained with controls by using an overliming/thermal conditioning protocol.     

Discrepancy in glucose and fructose utilisation during fermentation by Saccharomyces cerevisiae wine yeast strains

While unfermented grape must contains approximately equal amounts of the two hexoses glucose and fructose, wine producers worldwide often have to contend with high residual fructose levels (>2 gl(-1)) that may account for undesirable sweetness in finished dry wine. Here, we investigate the fermentation kinetics of glucose and fructose and the influence of certain environmental parameters on hexose utilisation by wine yeast. Seventeen Saccharomyces cerevisiae strains, including commercial wine yeast strains, were evaluated in laboratory-scale wine fermentations using natural Colombard grape must that contained similar amounts of glucose and fructose (approximately 110 gl(-1) each). All strains showed preference for glucose, but to varying degrees. The discrepancy between glucose and fructose utilisation increased during the course of fermentation in a strain-dependent manner. We ranked the S. cerevisiae strains according to their rate of increase in GF discrepancy and we showed that this rate of increase is not correlated with the fermentation capacity of the strains. We also investigated the effect of ethanol and nitrogen addition on hexose utilisation during wine fermentation in both natural and synthetic grape must. Addition of ethanol had a stronger inhibitory effect on fructose than on glucose utilisation. Supplementation of must with assimilable nitrogen stimulated fructose utilisation more than glucose utilisation. These results show that the discrepancy between glucose and fructose utilisation during fermentation is not a fixed parameter but is dependent on the inherent properties of the yeast strain and on the external conditions.     

Involvement of nitrogen metabolism in the triggering of ethanol fermentation in aerobic chemostat cultures of Saccharomyces cerevisiae.

We have investigated whether central nitrogen metabolism may influence the triggering of ethanol fermentation in Saccharomyces cerevisiae strain CEN.PK122 grown in the presence of different N-sources (ammonia, glutamate, or glutamine) under conditions in which the carbon to nitrogen (C : N) ratio was varied. An exhaustive quantitative evaluation of yeast physiology and metabolic behavior through metabolic flux analysis (MFA) was undertaken. It is shown that ethanol fermentation is triggered at dilution rates, D (growth rate), significantly lower (D=0.070 and 0.074 h(-1) for glutamate and glutamine, respectively, and D=0.109 h(-1) for ammonia) under N- than C-limitation (approximately 0.18 h(-1) for all N-sources). A characteristic specific rate of glucose influx, q(Glc), for each N-source at Dc, i.e., just before the onset of respirofermentative metabolism, was determined (approximately 2.0, 1.5, and 2.5, for ammonia, glutamate, and glutamine, respectively). This q(Glc) was independent of the nutritional limitation though dependent on the nature of the N-source. The onset of fermentation occurs when this "threshold q(Glc)" is overcome. The saturation of respiratory activity appears not to be associated with the onset of fermentation since q(O(2)) continued to increase after Dc. It was remarkable that under respirofermentative conditions in C-limited chemostat cultures, the glucose consumed was almost completely fermented with biomass being synthesized from glutamate through gluconeogenesis. The results obtained show that the enzyme activities involved in central nitrogen metabolism do not appear to participate in the control of the overflow in carbon catabolism, which is driven toward ethanol production. The role of nitrogen metabolism in the onset of ethanol fermentation would rather be realized through its involvement in setting the anabolic fluxes directed to nitrogenous macromolecules. It seems that nitrogen-related anabolic fluxes would determine when the threshold glucose consumption rate is achieved after which ethanol fermentation is triggered.     

Sequential inactivation of ammonium and glucose transport in Saccharomyces cerevisiae during fermentation

Abstract Ethanol at concentrations above 12% (v/v) in mineral medium with glucose and with ammonium as the only nitrogen source induced rapid inactivation of the ammonium transport system in the strain IGC 3507 of Saccharomyces cerevisiae terminating protein synthesis. Subsequently, when glucose was present, the glucose transport system was irreversibly inactivated. This two-step mechanism may play a decisive role when ethanol stops fermentation by S. cerevisiae , before all the fermentable sugar has been consumed.     

Dynamics of anaerobic growth of Saccharomyces cerevisiae in the chemostat.

A kinetic Monod model has been used to describe the dynamic response of a continuous stirred tank fermentor (CSTF) to changes in dilution rate. A general analytical solution of a linearized model was obtained. Experimental results (Vairo et al. 1977) of continuous anaerobic culture of Saccharomyces cerevisiae have verified the model quantitatively. For step disturbances on the dilution rate the responses of biomass concentration and the outlet substrate concentration were calculated on a digital computer and compared with the experimental data.     

Continuous and static fermentation of glucose to ethanol by immobilized Saccharomyces cerevisiae cells of different ages.

Glucose was converted to ethanol by calcium-alginate-entrapped Saccharomyces cerevisiae NRRL Y-2034 cells that were 24, 48, 72, and 96 h old in continuous-flow and static repeated-batch fermentors. In general, older yeast cells were more efficient than younger ones. In most cases, the continuous fermentations were better than the static ones in producing maximum ethanol yields (5.11 g/10 g of glucose) over extended time periods. The best static fermentation (with 24-h-old cells) converted 100% of the glucose to ethanol for about 12 days, whereas the best continuous fermentation (with 96-h-old cells) converted 100% of the glucose for a remarkable period of about 3 months.     

Evaluation of Saccharomyces cerevisiae grown in a multistage chemostat environment under increasing levels of glucose

The concept of net consumption and/or production rates of fermentation metabolites has been proposed and applied to evaluate the performance of Saccharomyces cerevisiae grown in a multistage chemostat environment under increasing glucose concentrations (increased gravity). Results show that both rates are strongly affected by high glucose doses (osmotic pressure) and that ethanol inhibition has a profound influence on the performance of yeast cells.     

Improvement of maltotriose fermentation by Saccharomyces cerevisiae

AIMS: To enhance the fermentation of maltotriose by industrial Saccharomyces cerevisiae strains. METHODS AND RESULTS: The capability to ferment maltotriose by an industrial yeast strain that uses this sugar aerobically was tested in shake flasks containing rich medium. While the presence of maltose in the medium did not improve maltotriose fermentation, enhanced and constitutive expression of the AGT1 permease not only increased the uptake of maltotriose, but allowed efficient maltotriose fermentation by this strain. Supplementation of the growth medium with 20 mmol magnesium l(-1) also increased maltotriose fermentation. CONCLUSIONS: Over expression of the AGT1 permease and magnesium supplementation improved maltotriose fermentation by an industrial yeast strain that respired but did not ferment this sugar. SIGNIFICANCE AND IMPACT OF THE STUDY: This work contributes to the elucidation of the roles of the AGT1 permease and nutrients in the fermentation of all sugars present in starch hydrolysates, a highly desirable trait for several industrial yeasts.     

Regulation of invertase synthesis by glucose in Saccharomyces cerevisiae.

Saccharomyces cerevisiae growing under repressible conditions (1% of glucose or more) produces a burst of external invertase when shifted to higher temperatures. The secretion of this invertase requires protein synthesis, but was found to be independent of RNA formation. The level of mRNA accumulated and translated was inversely proportional to the glucose present in the growth medium. These results are consistent with the hypothesis that invertase is continuously synthesized both in the presence and absence of glucose, but under repressible conditions is degraded before secretion takes place.