Xylose fermentation by Candida shehatae and Pichia stipitis: effects of pH,temperature and substrate concentration

The effects of temperature, pH and xylose concentration on the fermentation parameters of Candida shehatae and Pichia stipitis were evaluated. The optimum pH was in the region of pH 4–5.5, with an optimum fermentation temperature of 30°C. Maximum fermentation rates were reached at 50 g l⁻¹ xylose. A maximum volumetric ethanol productivity of about 0.9 g (l h)⁻¹ was obtained with both yeast strains. The ethanol yield of C. shehatae decreased considerably when cultivated above 30°C or when the xylose concentration was increased. Xylitol accumulated concomitantly. Xylitol production by P. stipitis was observed only during cultivation at 36°C. Whereas the ethanol yield of C. shehatae was usually about 75% of the theoretical maximum, it was 85–90% with P. stipitis.     

Relationship Between Effect of Ethanol on Proton Flux Across Plasma Membrane and Ethanol Tolerance, inPichia stipitis

Pichia stipitisefficiently converts glucose or xylose into ethanol but is inhibited by ethanol concentrations exceeding 30 g/L. InSaccharomyces cerevisiae, ethanol has been shown to alter the movement of protons into and out of the cell. InP. stipitisthe passive entry of protons into either glucose- or xylose-grown cells is unaffected at physiological ethanol concentrations. In contrast, active proton extrusion is affected differentially by ethanol, depending on the carbon source catabolized. In fact, in glucose-grown cells, the H⁺-extrusion rate is reduced by low ethanol concentrations, whereas, in xylose-grown cells, the H⁺-extrusion rate is reduced only at non-physiological ethanol concentrations. Thus, the ethanol inhibitory effect on growth and ethanol production, in glucose-grown cells, is probably caused by a reduction in H⁺-extrusion. Comparison of the rates of H⁺-flux with the relatedin vitroH⁺-ATPase activity suggests a new mechanism for the regulation of the proton pumping plasma membrane ATPase (EC 3.6.1.3) ofP. stipitis, by both glucose and ethanol. Glucose activates both the ATP hydrolysis and the proton-pumping activities of the H⁺-ATPase, whereas ethanol causes an uncoupling between the ATP hydrolysis and the proton-pumping activities. This uncoupling may well be the cause of ethanol induced growth inhibition of glucose grownP. stipitiscells.     

Genome-Scale NAD(H/+) Availability Patterns as a Differentiating Feature between Saccharomyces cerevisiae and Scheffersomyces stipitis in Relation to Fermentative Metabolism

Scheffersomyces stipitis is a yeast able to ferment pentoses to ethanol, unlike Saccharomyces cerevisiae, it does not present the so-called overflow phenomenon. Metabolic features characterizing the presence or not of this phenomenon have not been fully elucidated. This work proposes that genome-scale metabolic response to variations in NAD(H/⁺) availability characterizes fermentative behavior in both yeasts. Thus, differentiating features in S. stipitis and S. cerevisiae were determined analyzing growth sensitivity response to changes in available reducing capacity in relation to ethanol production capacity and overall metabolic flux span. Using genome-scale constraint-based metabolic models, phenotypic phase planes and shadow price analyses, an excess of available reducing capacity for growth was found in S. cerevisiae at every metabolic phenotype where growth is limited by oxygen uptake, while in S. stipitis this was observed only for a subset of those phenotypes. Moreover, by using flux variability analysis, an increased metabolic flux span was found in S. cerevisiae at growth limited by oxygen uptake, while in S. stipitis flux span was invariant. Therefore, each yeast can be characterized by a significantly different metabolic response and flux span when growth is limited by oxygen uptake, both features suggesting a higher metabolic flexibility in S. cerevisiae. By applying an optimization-based approach on the genome-scale models, three single reaction deletions were found to generate in S. stipitis the reducing capacity availability pattern found in S. cerevisiae, two of them correspond to reactions involved in the overflow phenomenon. These results show a close relationship between the growth sensitivity response given by the metabolic network and fermentative behavior.     

Ethanol tolerance of Pichia stipitis and Candida shehatae strains in fed-batch cultures at controlled low dissolved oxygen levels

Summary Fed-batch cultivations of Pichia stipitis and strains of Candida shehatae with d-xylose or d-glucose were conducted at controlled low dissolved oxygen tension (DOT) levels. There were some marked differences between the strains. In general growth was inhibited at lower ethanol concentrations than fermentation, and ethanol levels of up to 47 g·l^-1 were produced at 30°C. Ethanol production was mainly growth associated. The yeast strains formed small amounts of monocarboxylic acids and higher alcohols, which apparently did not enhance the ethanol toxicity. The maximum ethanol concentration obtained on d-xylose could not be increased by using a high cell density culture, nor by using d-glucose as substrate. The latter observation suggested that the low ethanol tolerance of these xylose-fermenting yeast strains was not a consequence of the metabolic pathway used during pentose fermentation. In contrast with the C. shehatae strains, it was apparent with P. stipitis CSIR-Y633 that when the ethanol concentration reached about 28 g·l^-1, ethanol assimilation exceeded ethanol production, despite cultivation at a low DOT of 0.2% of air saturation. Discontinuing the aeration enabled ethanol accumulation to proceed, but with concomitant xylitol production and cessation of growth.     

Enhanced ethanol production by fermentation of rice straw hydrolysate without detoxification using a newly adapted strain of Pichia stipitis

An enhanced inhibitor-tolerant strain of Pichia stipitis was successfully developed through adaptation to acid-treated rice straw hydrolysate. The ethanol production obtained by fermentation of NaOH-neutralized hydrolysate without detoxification using the adapted P. stipitis was comparable to fermentation of overliming-detoxified hydrolysate. The ethanol yield using the adapted P. stipitis with both types of hydrolysate at pH 5.0 achieved 0.45 g_p g_s⁻¹, which is equivalent to 87% of the maximum possible ethanol conversion. Furthermore, the newly adapted P. stipitis demonstrated significantly enhanced tolerance to sulfate and furfural despite the fact that both inhibitors had not been removed from the hydrolysate by NaOH neutralization. Finally, the ethanol conversion could be maintained at 60% and above when the neutralized hydrolysate contained 3.0% sulfate and 1.3 g L⁻¹ furfural.     

Ethanol production by In situ xylose isomerization using recombinant Escherichia coli and fermentation using conventional Saccharomyces cerevisiae

Xylose isomerase from Geobacillus kaustophilus HTA426 was functionally expressed in Escherichia coli BL21 (DE3) and the recombinant E. coli cells were used together with conventional Saccharomyces cerevisiae to produce ethanol from xylose by simultaneous xylose isomerisation and fermentation. When recombinant E. coli cells were used as the source of xylose isomerase, a significant amount of ethanol was produced from xylose, whereas the control without recombinant E. coli cells did not produce any detectable amount of ethanol from xylose. Ethanol production was increased by 38% by feeding more recombinant E. coli at 48 h compared to adding recombinant E. coli only in the beginning, resulting in more ethanol production than P. stipitis CBS6054 under the same conditions. The xylitol accumulation by the in situ process was only 57% of that produced by the P. stipitis CBS6054.     

Evaluation of hardboard manufacturing process wastewater as a feedstream for ethanol production

Waste streams from the wood processing industry can serve as feedstream for ethanol production from biomass residues. Hardboard manufacturing process wastewater (HPW) was evaluated on the basis of monomeric sugar recovery and fermentability as a novel feedstream for ethanol production. Dilute acid hydrolysis, coupled with concentration of the wastewater resulted in a hydrolysate with 66 g/l total fermentable sugars. As xylose accounted for 53 % of the total sugars, native xylose-fermenting yeasts were evaluated for their ability to produce ethanol from the hydrolysate. The strains selected were, in decreasing order by ethanol yields from xylose (Y _p/s, based on consumed sugars), Scheffersomyces stipitis ATCC 58785 (CBS 6054), Pachysolen tannophilus ATCC 60393, and Kluyveromyces marxianus ATCC 46537. The yeasts were compared on the basis of substrate utilization and ethanol yield during fermentations of the hydrolysate, measured using an HPLC. S. stipitis, P. tannophilus, and K. marxianus produced 0.34, 0.31, and 0.36 g/g, respectively. The yeasts were able to utilize between 58 and 75 % of the available substrate. S. stipitis outperformed the other yeast during the fermentation of the hydrolysate; consuming the highest concentration of available substrate and producing the highest ethanol concentration in 72 h. Due to its high sugar content and low inhibitor levels after hydrolysis, it was concluded that HPW is a suitable feedstream for ethanol production by S. stipitis.     

Construction of xylose-assimilating Saccharomyces cerevisiae

The xylose reductase gene originating from Pichia stipitis was subcloned on an expression vector with the enolase promoter and terminator from Saccharomyces cerevisiae. The transformants of S. cerevisiae harboring the resultant plasmids produced xylose reductase constitutively at a rate about 3 times higher than P. stipitis, but could not assimilate xylose due to the deficient conversion of xylitol to xylulose. The xylitol dehydrogenase gene was also isolated from the gene library of P. stipitis by plaque hybridization using a probe specific for its N-terminal amino acid sequence. The gene transferred into S. cerevisiae was well expressed. Furthermore, high expressions of the xylose reductase and xylitol dehydrogenase genes in S. cerevisiae were achieved by introducing both genes on the same or coexisting plasmids. The transformants could grow on a medium containing xylose as the sole carbon source, but ethanol production from xylose was less than that by P. stipitis and a significant amount of xylitol was excreted into the culture broth.     

An investigation of d-{1-13C} xylose metabolism in Pichia stipitis under aerobic and anaerobic conditions

Summary The uptake of d-{1-¹³C} xylose, the accumulation of intermediates and the distribution of the label in ethanol in Pichia stipitis under aerobic and anaerobic conditions were investigated by nuclear magnetic resonance spectroscopy. The rate-limiting step of d-xylose metabolism under aerobic conditions appeared to be uptake, whereas under anaerobic conditions it was the conversion of xylitol to xylulose. The yeast showed no preference to either the alpha-or beta-forms of d-xylose. Under anaerobic conditions only {2-¹³C{ ethanol was detected and this suggests that NADH but not NADPH was used as cofactor in the conversion of xylose to xylitol. d-Xylose is most likely metabolised by the pentose phosphate pathway in this yeast.     

Ethanol fermentation characteristics of Thermoanaerobacter ethanolicus

Thermoanaerobacter ethanolicus is an extreme thermophilic non-spore forming ethanol-producing anaerobic bacterium. Minimum nutrient requirements and optimum growth conditions have been established. An optimum yeast extract-glucose ratio for ethanol yield has also been determined. Initial medium pH, optimally 7.5–8.0, significantly affected the amount of ethanol formed. Maximum specific growth rate was found to be 0.22 h^?1at pH 7.5 and 69°C. Ethanol concentration up to 11 g l^?1at pH 7.5 and 69°C was used to characterize ethanol inhibition. The growth kinetics of T. ethanolicus were characterized in terms of environmental parameters. Substrate utilization, ethanol formation and inhibition by both sugar and ethanol were also quantified.     

Ethanol production from pentoses by immobilized microorganisms

The capabilities of immobilized Fusarium oxysporum f. sp. lini, Mucor sp., and Saccharomyces cerevisiae in fermenting pentose to ethanol have been compared. S. cerevisiae was found to have the best fermentation rate on d-xylulose of 0.3 g l^?1 h^?1. By using a separate isomerase column for converting d-xylose to d-xylulose and a yeast column for converting d-xylulose to ethanol, an ethanol concentration of 32 g l^?1 was obtained from 10% d-xylose. The ethanol yield was calculated to be 64% of the theoretical yield.     

Ethanol-Induced Leakage in Saccharomyces cerevisiae: Kinetics and Relationship to Yeast Ethanol Tolerance and Alcohol Fermentation Productivity

Ethanol stimulated the leakage of amino acids and 260-nm-light-absorbing compounds from cells of Saccharomyces cerevisiae. The efflux followed first-order kinetics over an initial period. In the presence of lethal concentrations of ethanol, the efflux rates at 30 and 36°C were an exponential function of ethanol concentration: k_e^X = k_e^Xme^{E (X-X_m)}, where k_e^X and k_e^Xm are the efflux rate constants, respectively, in the presence of a concentration X of ethanol or the minimal concentration of ethanol, X_m, above which the equation was applicable, coincident with the minimal lethal concentration of ethanol. E is the enhancement constant. At 36°C, as compared with the corresponding values at 30°C, the efflux rates were higher and the minimal concentration of ethanol (X_m) was lower. The exponential constants for the enhancement of the rate of leakage (E) had similar values at 30 or 36°C and were of the same order of magnitude as the corresponding exponential constants for ethanol-induced death. Under isothermic conditions (30°C) and up to 22% (vol/vol) ethanol, the resistance to ethanol-induced leakage of 260-nm-light-absorbing compounds was found to be closely related with the ethanol tolerance of three strains of yeasts, Kluyveromyces marxianus, Saccharomyces cerevisiae, and Saccharomyces bayanus. The resistance to ethanol-induced leakage indicates the possible adoption of the present method for the rapid screening of ethanol-tolerant strains. The addition to a fermentation medium of the intracellular material obtained by ethanol permeabilization of yeast cells led to improvements in alcohol fermentation by S. cerevisiae and S. bayanus. The action of the intracellular material, by improving yeast ethanol tolerance, and the advantages of partially recycling the fermented medium after distillation were discussed.     

The fermentation of hexose and pentose sugars by Candida shehatae and Pichia stipitis

Summary The fermentation by Candida shehatae and Pichia stipitis of xylitol and the various sugars which are liberated upon hydrolysis of lignocellulosic biomass was investigated. Both yeasts produced ethanol from d-glucose, d-mannose, d-galactose and d-xylose. Only P. stipitis fermented d-cellobiose, producing 6.5 g·l^-1 ethanol from 20 g·l^-1 cellobiose within 48 h. No ethanol was produced from l-arabinose, l-rhamnose or xylitol. Diauxie was evident during the fermentation of a sugar mixture. Following the depletion of glucose, P. stipitis fermented galactose, mannose, xylose and cellobiose simultaneously with no noticeable preceding lag period. A similar fermentation pattern was observed with C. shehatae, except that it failed to utilize cellobiose even though it grew on cellobiose when supplied as the sole sugar. P. stipitis produced considerably more ethanol from the sugar mixture than C. shehatae, primarily due to its ability to ferment cellobiose. In general P. stipitis exhibited a higher volumetric rate and yield of ethanol production. This yeast fermented glucose 30–50% more rapidly than xylose, whereas the rates of ethanol production from these two sugars by C. shehatae were similar. P. stipitis had no absolute vitamin requirement for xylose fermentation, but biotin and thiamine enhanced the rate and yield of ethanol production significantly.Nomenclature _max Maximum specific growth rate, h^-1 - Q _p Maximum volumetric rate of ethanol production, calculated from the slope of the ethanol vs. time curve, g·(l·h)^-1 - q _p Maximum specific rate of ethanol production, g·(g cells·h) - Y _p/s Ethanol yield coefficient, g ethanol·(g substrate utilized)^-1 - Y _x/s Cell yield coefficient, g biomass·(g substrate utilized)^-1 - E Efficiency of substrate utilization, g substrate consumed·(g initial substrate)^-1·100     

Production of ethanol and xylanolytic enzymes by yeasts inhabiting rotting wood isolated in sugarcane bagasse hydrolysate

Yeasts associated with rotting wood from four Atlantic Rain forest sites in Brazil were investigated using a culture medium based on sugarcane bagasse hydrolysate. A total of 330 yeast strains were isolated. Pichia manshurica, Candida pseudolambica, and Wickerhamomyces sp. 3 were the most frequently isolated species. Fourteen novel species were obtained in this study. All isolates were tested for their ability to ferment d-xylose and to produce xylanases. In the fermentation assays using d-xylose (30 g L⁻¹), the main ethanol producers were Scheffersomyces stipitis (14.08 g L⁻¹), Scheffersomyces sp. (7.94 g L⁻¹) and Spathaspora boniae (7.16 g L⁻¹). Sc. stipitis showed the highest ethanol yield (0.42 g g⁻¹) and the highest productivity (0.39 g L⁻¹h⁻¹). The fermentation results using hemicellulosic hydrolysate showed that Sc. stipitis was the best ethanol producer, achieving a yield of 0.32 g g⁻¹, while Sp. boniae and Scheffersomyces sp. were excellent xylitol producers. The best xylanase-producing yeasts at 50 °C belonged to the species Su. xylanicola (0.487 U mg⁻¹) and Saitozyma podzolica (0.384 U mg⁻¹). The results showed that rotting wood collected from the Atlantic Rainforest is a valuable source of yeasts able to grow in sugarcane bagasse hydrolysate, including species with promising biotechnological properties.     

Biological treatment of eucalypt spent sulphite liquors: a way to boost the production of second generation bioethanol

The fermentation of reducing sugars from hardwood (eucalypt) spent sulphite liquor (HSSL) into ethanol by Pichia (Scheffersomyces) stipitis is hindered by concomitant inhibitors of microbial metabolism. The conditions for the HSSL biological treatment step by Paecilomyces variotii were evaluated and optimised. Two different strategies of reactor operation were compared using single batch (B) and sequential batch reactor (SBR). Biological treatment of HSSL in the SBR revealed the best results with respect to the removal of microbial inhibitors. Also, most of inhibitory compounds, acetic acid, gallic acid, pyrogallol, amongst others, were removed from HSSL by P. variotii before the ethanol fermentation. The bio-detoxified HSSL was subjected to a successful fermentation by P. stipitis, attaining a maximum ethanol concentration of 2.4 g L⁻¹ with a yield of 0.24 g ethanol g sugars⁻¹.     

Optimization of enzymatic hydrolysis of pretreated rice straw and ethanol production

Cellulase, Tween 80, and β-glucosidase loading were studied and optimized by response surface methodology to improve saccharification. Microwave alkali-pretreated rice straw used as substrate for onsite enzyme production by Aspergillus heteromorphus and Trichoderma reesei. The highest enzymatic hydrolysis (84%) was obtained from rice straw at crude enzyme loading of 10 FPU/gds of cellulase, 0.15% Tween 80, and 100 international unit/g dry solids of β-glucosidase activities. Enzymatic hydrolyzate of pretreated rice straw was used for ethanol production by Saccharomyces cerevisiae, Scheffersomyces stipitis, and by co-culture of both. The yield of ethanol was 0.50, 0.47, and 0.48 g_p/g_s by S. cerevisiae, S. stipitis, and by co-culture, respectively, using pretreated rice straw hydrolyzate. The co-culture of S. cerevisiae and S. stipitis produced 25% more ethanol than S. cerevisiae alone and 31% more ethanol than S. stipitis alone. During anaerobic fermentation 65.08, 36.45, and 50.31 μmol/ml CO₂ released by S. cerevisiae, S. stipitis, and by co-culture, respectively. The data indicated that saccharification efficiency using optimized crude enzyme cocktail was good, and enzymatic hydrolyzate could be fermented to produce ethanol.     

NADH-linked aldose reductase: the key to anaerobic alcoholic fermentation of xylose by yeasts

Summary The kinetics and enzymology of d-xylose utilization were studied in aerobic and anaerobic batch cultures of the facultatively fermentative yeasts Candida utilis, Pachysolen tannophilus, and Pichia stipitis. These yeasts did not produce ethanol under aerobic conditions. When shifted to anaerobiosis cultures of C. utilis did not show fermentation of xylose; in Pa. tannophilus a very low rate of ethanol formation was apparent, whereas with Pi. stipitis rapid fermentation of xylose occurred. The different behaviour of these yeasts ist most probably explained by differences in the nature of the initial steps of xylose metabolism: in C. utilis xylose is metabolized via an NADPH-dependent xylose reductase and an NAD⁺-linked xylitol dehydrogenase. As a consequence, conversion of xylose to ethanol by C. utilis leads to an overproduction of NADH which blocks metabolic activity in the absence of oxygen. In Pa. tannophilus and Pi. stipitis, however, apart from an NADPH-linked xylose reductase also an NADH-linked xylose reductase was present. Apparently xylose metabolism via the NADH-dependent reductase circumvents the imbalance of the NAD⁺/NADH redox system, thus allowing fermentation of xylose to ethanol under anaerobic conditions. The finding that the rate of xylose fermentation in Pa. tannophilus and Pi. stipitis corresponds with the activity of the NADH-linked xylose reductase activity is in line with this hypothesis. Furthermore, a comparative study with various xylose-assimilating yeasts showed that significant alcoholic fermentation of xylose only occurred in those organisms which possessed NADH-linked aldose reductase.     

Temperature profiles of growth and ethanol tolerance of the xylose-fermenting yeasts Candida shehatae and Pichia stipitis

Summary The effect of different ethanol concentrations on the growth of Candida shehatae and Pichia stipitis with xylose as substrate was evaluated in a temperature gradient incubator. The upper limit of the temperature profiles of ethanol tolerance of both yeast strains were similar, although P. stipitis appeared to have a slightly higher ethanol tolerance in the higher temperature range. An increase in the ethanol concentration severely depressed the maximum growth temperature, and also increased the minimum growth temperature slightly. The ethanol tolerance limit of 46–48 g·l^-1 occurred within a narrow temperature plateau of 11 to 22° C. The low ethanol tolerance of these pentose fermenting yeasts is detrimental for commercial ethanol production from hemicellulose hydrolysates.     

Anaerobic Xylose Fermentation by Recombinant Saccharomyces cerevisiae Carrying XYL1, XYL2, and XKS1 in Mineral Medium Chemostat Cultures

For ethanol production from lignocellulose, the fermentation of xylose is an economic necessity. Saccharomyces cerevisiae has been metabolically engineered with a xylose-utilizing pathway. However, the high ethanol yield and productivity seen with glucose have not yet been achieved. To quantitatively analyze metabolic fluxes in recombinant S. cerevisiae during metabolism of xylose-glucose mixtures, we constructed a stable xylose-utilizing recombinant strain, TMB 3001. The XYL1 and XYL2 genes from Pichia stipitis, encoding xylose reductase (XR) and xylitol dehydrogenase (XDH), respectively, and the endogenous XKS1 gene, encoding xylulokinase (XK), under control of the PGK1 promoter were integrated into the chromosomal HIS3 locus of S. cerevisiae CEN.PK 113-7A. The strain expressed XR, XDH, and XK activities of 0.4 to 0.5, 2.7 to 3.4, and 1.5 to 1.7 U/mg, respectively, and was stable for more than 40 generations in continuous fermentations. Anaerobic ethanol formation from xylose by recombinant S. cerevisiae was demonstrated for the first time. However, the strain grew on xylose only in the presence of oxygen. Ethanol yields of 0.45 to 0.50 mmol of C/mmol of C (0.35 to 0.38 g/g) and productivities of 9.7 to 13.2 mmol of C h⁻¹ g (dry weight) of cells⁻¹ (0.24 to 0.30 g h⁻¹ g [dry weight] of cells⁻¹) were obtained from xylose-glucose mixtures in anaerobic chemostat cultures, with a dilution rate of 0.06 h⁻¹. The anaerobic ethanol yield on xylose was estimated at 0.27 mol of C/(mol of C of xylose) (0.21 g/g), assuming a constant ethanol yield on glucose. The xylose uptake rate increased with increasing xylose concentration in the feed, from 3.3 mmol of C h⁻¹ g (dry weight) of cells⁻¹ when the xylose-to-glucose ratio in the feed was 1:3 to 6.8 mmol of C h⁻¹ g (dry weight) of cells⁻¹ when the feed ratio was 3:1. With a feed content of 15 g of xylose/liter and 5 g of glucose/liter, the xylose flux was 2.2 times lower than the glucose flux, indicating that transport limits the xylose flux.