Isolation and Characterization of Pichia heedii Mutants Defective in Xylose Uptake

To investigate the role of xylose uptake in xylose metabolism in yeasts, we isolated a series of mutated strains of the yeast Pichia heedii which are defective in xylose utilization. Four of these demonstrated defects in xylose uptake. Overlaps between the functional or regulatory mechanisms for glucose and xylose uptake may exist in this yeast since some of the mutants defective in xylose uptake were also defective in glucose transport. None of the mutants were defective in xylose reductase or xylitol dehydrogenase activities.     

Transport of xylose and glucose in the xylose-fermenting yeast Pichia stipitis

Summary A low-affinity and a high-affinity sylose proton symport operated simultaneously in both starved and non-starved cells of Pichia stipitis. Glucose competed with xylose for transport by the low-affinity system and inhibited xylose transport by the high-affinity system non-competitively. The low affinity system was subject to substrate inhibition when glucose but not when xylose was the substrate. The differences between the characteristics of monosaccharide transport by Pichia stipitis and its imperfect state, Candida shehatae, are discussed.     

A novel co-culture process with Zymomonas mobilis and Pichia stipitis for efficient ethanol production on glucose/xylose mixtures

An efficient conversion of glucose and xylose is a requisite for a profitable process of bioethanol production from lignocellulose. Considering the approaches available for this conversion, co-culture is a simple process, employing two different organisms for the fermentation of the two sugars. An innovative fermentation scheme was designed, co-culturing immobilized Zymomonas mobilis and free cells of Pichia stipitis in a modified fermentor for the glucose and xylose fermentation, respectively. A sugar mixture of 30 g/l glucose and 20 g/l of xylose was completely converted to ethanol within 19 h. This gave a volumetric ethanol productivity of 1.277 g/l/h and an ethanol yield of 0.49–0.50 g/g, which is more than 96% of the theoretical value. Extension of this fermentation scheme to sugarcane bagasse hydrolysate resulted in a complete sugar utilisation within 26 h; ethanol production peaked at 40 h with a yield of 0.49 g/g. These values are comparable to the best results reported. Cell interaction was observed between Z. mobilis and P. stipitis. Viable cells of Z. mobilis inhibited the cell activity of P. stipitis and the xylose fermentation. Z. mobilis showed evidence of utilising a source other than glucose for growth when co-cultured with P. stipitis.     

Physiological and enzymatic comparison between Pichia stipitis and recombinant Saccharomyces cerevisiae on xylose fermentation

In order to better understand the differences in xylose metabolism between natural xylose-utilizing Pichia stipitis and metabolically engineered Saccharomyces cerevisiae, we constructed a series of recombinant S. cerevisiae strains with different xylose reductase/xylitol dehydrogenase/xylulokinase activity ratios by integrating xylitol dehydrogenase gene (XYL2) into the chromosome with variable copies and heterogeneously expressing xylose reductase gene (XYL1) and endogenous xylulokinase gene (XKS1). The strain with the highest specific xylose uptake rate and ethanol productivity on pure xylose fermentation was selected to compare to P. stipitis under oxygen-limited condition. Physiological and enzymatic comparison showed that they have different patterns of xylose metabolism and NADPH generation.     

Mutational analysis of the role of the conserved lysine-270 in the Pichia stipitis xylose reductase

Xylose reductase catalyzes the NAD(P)H-dependent reduction of xylose to xylitol and is essential for growth on xylose by yeasts. To understand the nature of coenzyme binding to the Pichia stipitis xylose reductase, we investigated the role of the strictly conserved Lys270 in the putative IPKS coenzyme binding motif by site-directed mutagenesis. The Lys270Met variant exhibited lower enzyme activity than the wild-type enzyme. The apparent affinity of the variant for NADPH was decreased 5–16-fold, depending on the substrate used, while the apparent affinity for NADH, measured using glyceraldehyde as the substrate, remained unchanged. This resulted in 4.3-fold higher affinity for NADH over NADPH using glyceraldehyde as the substrate. The variant also showed a 14-fold decrease in K_m for xylose, but only small changes were observed in K_m values for glyceraldehyde. The wild-type enzyme, but not the Lys270Met variant, was susceptible to modification by the Lys-specific pyridoxal 5′-phosphate. Results of our chemical modification and site-directed mutagenesis study indicated that Lys270 is involved in both NADPH and d-xylose binding in the P. stipitis xylose reductase.     

Transport and Utilization of Hexoses and Pentoses in the Halotolerant Yeast Debaryomyces hansenii

Debaryomyces hansenii is a yeast species that is known for its halotolerance. This organism has seldom been mentioned as a pentose consumer. In the present work, a strain of this species was investigated with respect to the utilization of pentoses and hexoses in mixtures and as single carbon sources. Growth parameters were calculated for batch aerobic cultures containing pentoses, hexoses, and mixtures of both types of sugars. Growth on pentoses was slower than growth on hexoses, but the values obtained for biomass yields were very similar with the two types of sugars. Furthermore, when mixtures of two sugars were used, a preference for one carbon source did not inhibit consumption of the other. Glucose and xylose were transported by cells grown on glucose via a specific low-affinity facilitated diffusion system. Cells derepressed by growth on xylose had two distinct high-affinity transport systems for glucose and xylose. The sensitivity of labeled glucose and xylose transport to dissipation of the transmembrane proton gradient by the protonophore carbonyl cyanide m-chlorophenylhydrazone allowed us to consider these transport systems as proton symports, although the cells displayed sugar-associated proton uptake exclusively in the presence of NaCl or KCl. When the V_max values of transport systems for glucose and xylose were compared with glucose- and xylose-specific consumption rates during growth on either sugar, it appeared that transport did not limit the growth rate.     

Xylitol production by recombinant Saccharomyces cerevisiae expressing the Pichia stipitis and Candida shehatae XYL1 genes

The xylose reductase gene (XYL1) was isolated from Pichia stipitis and Candida shehatae, cloned into YEp-based vectors under the control of ADH2 and PGK1 promoter/terminator cassettes and introduced into Saccharomyces cerevisiae Y294 by electroporation. Shake-flask fermentations were carried out with 5% xylose and 1% galactose, glucose or maltose as co-substrates. Xylose uptake was similar in both the recombinant strains when different co-substrates were used and slowed once the co-substrate was depleted. The recombinant strains converted xylose to xylitol with yields approaching the theoretical maxima. Xylitol production was most rapid when the co-substrate was still present. Approximately 50% of the xylose was not metabolized due to the depletion of the co-substrate. Received: 23 December 1999 / Received revision: 30 June 2000 / Accepted: 1 July 2000     

Oxygen-dependent xylitol metabolism in Pichia stipitis

Pichia stipitis CBS 6054 was cultivated in chemostat cultures under aerobic and oxygen-limited conditions with xylitol alone, a mixture of xylitol and glucose and a mixture of xylitol and xylose. Xylitol metabolism was strictly respiratory and no ethanol was formed. Simultaneous feeding of xylitol and glucose and xylitol and xylose to oxygen-limited xylitol-pregrown cells resulted in ethanol formation. In vitro both pyruvate decarboxylase activity and alcohol dehydrogenase activity were present in cells metabolising xylitol under oxygen-limited conditions; however, this did not result in ethanol formation. Glucose, xylose and xylitol utilisation, respectively, were compared under anaerobic conditions with regard to growth rate, carbon source and oxygenation level during pre-cultivation. Irrespective of pre-growth conditions, xylitol was not metabolised under anaerobic conditions, whereas ethanol was formed from both xylose and glucose. Anaerobic xylose utilisation required induction of a xylose-utilising metabolic pathway during pre-cultivation. Received: 23 February 1999 / Received last revision: 20 July 1999 / Accepted: 1 August 1999     

Development of sequential-co-culture system (Pichia stipitis and Zymomonas mobilis) for bioethanol production from Kans grass biomass

Sequential-co-culture technique was investigated in this study for the production of bioethanol from relatively cheaper lignocellulosic biomass of Kans grass (Saccharum spontaneum). The consortium of Pichia stipitis and Zymomonas mobilis was used to develop a suitable sequential-co-culture system. The Kans grass biomass was hydrolyzed in such a manner that the two sugar fractions, xylose rich and glucose rich were generated (a separate study). The P. stipitis cells and respective fermentation media (xylose rich) were fed to the fermentation vessel, after the set fermentation time Z. mobilis cells and respective media were fed to the same vessel. Different strategies have been followed and experiments were conducted initially at flask level. The selected strategy was then applied at bioreactor level using both synthetic fermentation media and Kans grass hydrolysate media to compare the kinetic parameters. The sequential addition of cultures with their respective media and imposed process conditions, showed better utilization of total sugars added (>95%). Microaerobic condition for P. stipitis and strictly anaerobic condition for Z. mobilis fermentation were found significant. The average ethanol yield (Y_p/s) and overall volumetric productivity (r_po) were found as 0.453 g_p/g_s and 1.580 g/l/h respectively for Kans grass hydrolysate media and 0.474 g_p/g_s and 2.901 g/l/h respectively for synthetic fermentation media.     

Effects of culture conditions on the co-fermentation of a glucose and xylose mixture to ethanol by a mutant of Saccharomyces diastaticus associated with Pichia stipitis

Substrates that contain hexose as well as pentose sugars can form an interesting substrate for the production of ethanol. Pichia stipitis and a respiratory-deficient mutant of Saccharomyces diastaticus were used to convert such a substrate into ethanol under continuous culture conditions. With a sugar mixture (glucose 70%/xylose 30%) at 50 g/l, the xylose was entirely consumed when the dilution rate (D) did not exceed 0.006 h^–1 whereas the glucose was entirely consumed whatever the D. The study of influence of initial substrate concentration (S₀) was performed at D = 0.015 h^–1. Under these conditions the substrate was entirely consumed when its initial concentration did not exceed 20 g/l. With S₀ = 80 g/l the residual xylose concentration reached 20.5 g/l. At low D or at low S₀, P. stipitis was the dominant species in the fermentor. Increasing the D or S₀ resulted in the wash-out of P. stipitis mainly because of its low ethanol tolerance. Correspondence to: J. P. Delgenes     

Mutants of the pentose‐fermenting yeast Pichia stipitis with improved tolerance to inhibitors in hardwood spent sulfite liquor

Mutants of Pichia stipitis NRRL Y‐7124 able to tolerate and produce ethanol from hardwood spent sulfite liquor (HW SSL) were obtained by UV mutagenesis. P. stipitis cells were subjected to three successive rounds of UV mutagenesis, each followed by screening first on HW SSL gradient plates and then in diluted liquid HW SSL. Six third generation mutants with greater tolerance to HW SSL as compared to the wild type (WT) were isolated. The WT strain could not grow in HW SSL unless it was diluted to 65% (v/v). In contrast, the third generation mutants were able to grow in HW SSL diluted to 75% (v/v). Mutants PS301 and PS302 survived even in 80% (v/v) HW SSL, although there was no increase in cell number. All the third generation mutants exhibited higher growth rates but significantly lower growth yields on xylose or glucose compared to the WT. The mutants fermented 4% (w/v) glucose as efficiently as the WT and fermented 4% (w/v) xylose more efficiently with a higher ethanol yield than the WT. In a medium containing 4% (w/v) each of xylose and glucose, all the third generation mutants utilized glucose as efficiently and xylose more efficiently than the WT. This resulted in higher ethanol yield by the mutants. The mutants retained the ability to utilize galactose and mannose and ferment them to ethanol. Arabinose was consumed slowly by both the mutants and WT with no ethanol production. In 60% (v/v) HW SSL, the mutants utilized and fermented glucose, mannose, galactose and xylose while the WT could not ferment any of these sugars. Biotechnol. Bioeng. 2009; 104: 892–900. © 2009 Wiley Periodicals, Inc.     

Probing the bioethanol production potential of Scheffersomyces (Pichia) stipitis using validated genome-scale model

A detailed in silico analysis of different strategies for enhancement of bioethanol production by Scheffersomyces stipitis, = Pichia stipitis, using validated genome-scale metabolic model is presented. Glucose inhibition on xylose uptake is dominant in S. stipitis which makes fed-batch fermentation more effective for higher sugar concentrations. Bioethanol production potential of S. stipitis can be improved by growth media modification by introducing certain amino acids in small quantities. Slower sugar uptake by S. stipitis can be overcome by community-culture with recombinant Escherichia coli strain ZSC113, which has a higher xylose uptake rate. Ethanol yield and productivity of community-culture can be further enhanced by genetic modification of E. coli strain ZSC113.     

Effect of Oxygenation on Xylose Fermentation by Pichia stipitis

The effect of oxygen limitation on xylose fermentation by Pichia stipitis (CBS 6054) was investigated in continuous culture. The maximum specific ethanol productivity (0.20 g of ethanol g dry weight⁻¹ h⁻¹) and ethanol yield (0.48 g/g) was reached at an oxygen transfer rate below 1 mmol/liter per h. In the studied range of oxygenation, the xylose reductase (EC 1.1.1.21) and xylitol dehydrogenase (EC 1.1.1.9) activities were constant as well as the ratio between the NADPH and NADH activities of xylose reductase. No xylitol production was found. The pyruvate decarboxylase (EC 4.1.1.1) activity increased and the malate dehydrogenase (EC 1.1.1.37) activity decreased with decreasing oxygenation. With decreasing oxygenation, the intracellular intermediary metabolites sedoheptulose 7-phosphate, glucose 6-phosphate, fructose 1,6-diphosphate, and malate accumulated slightly while pyruvate decreased. The ratio of the xylose uptake rate under aerobic conditions, in contrast to that under anaerobic assay conditions, increased with increasing oxygenation in the culture. The results are discussed in relation to the energy level in the cell, the redox balance, and the mitochondrial function.     

Effect of pretreatment chemicals on xylose fermentation by Pichia stipitis

Pretreatment of biomass with dilute H₂SO₄ results in residual acid which is neutralized with alkalis such as Ca(OH)₂, NaOH and NH₄OH. The salt produced after neutralization has an effect on the fermentation of Pichia stipitis. Synthetic media of xylose (60 g total sugar/l) was fermented to ethanol in the presence and absence of the salts using P. stipitis CBS 6054. CaSO₄ enhanced growth and xylitol production, but produced the lowest ethanol concentration and yield after 140 h. Na₂SO₄ inhibited xylitol production, slightly enhanced growth towards the end of fermentation but had no significant effect on xylose consumption and ethanol concentration. (NH₄)₂SO₄ inhibited growth, had no effect on xylitol production, and enhanced xylose consumption and ethanol production.     

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.     

Effect of heterologous xylose transporter expression in Candida tropicalis on xylitol production rate

Xylose utilization is inhibited by glucose uptake in xylose-assimilating yeasts, including Candida tropicalis, resulting in limitation of xylose uptake during the fermentation of glucose/xylose mixtures. In this study, a heterologous xylose transporter gene (At5g17010) from Arabidopsis thaliana was selected because of its high affinity for xylose and was codon-optimized for functional expression in C. tropicalis. The codon-optimized gene was placed under the control of the GAPDH promoter and was integrated into the genome of C. tropicalis strain LXU1 which is xyl2-disrupted and NXRG (codon-optimized Neurospora crassa xylose reductase) introduced. The xylose uptake rate was increased by 37–73 % in the transporter expression-enhanced strains depending on the glucose/xylose mixture ratio. The recombinant strain LXT2 in 500-mL flask culture using glucose/xylose mixtures showed a xylose uptake rate that was 29 % higher and a xylitol volumetric productivity (1.14 g/L/h) that was 25 % higher than the corresponding rates for control strain LXU1. Membrane protein extraction and Western blot analysis confirmed the successful heterologous expression and membrane localization of the xylose transporter in C. tropicalis.     

Efficient production of L-lactic acid from xylose by Pichia stipitis

Microbial conversion of renewable raw materials to useful products is an important objective in industrial biotechnology. Pichia stipitis, a yeast that naturally ferments xylose, was genetically engineered for l-(+)-lactate production. We constructed a P. stipitis strain that expressed the l-lactate dehydrogenase (LDH) from Lactobacillus helveticus under the control of the P. stipitis fermentative ADH1 promoter. Xylose, glucose, or a mixture of the two sugars was used as the carbon source for lactate production. The constructed P. stipitis strain produced a higher level of lactate and a higher yield on xylose than on glucose. Lactate accumulated as the main product in xylose-containing medium, with 58 g/liter lactate produced from 100 g/liter xylose. Relatively efficient lactate production also occurred on glucose medium, with 41 g/liter lactate produced from 94 g/liter glucose. In the presence of both sugars, xylose and glucose were consumed simultaneously and converted predominantly to lactate. Lactate was produced at the expense of ethanol, whose production decreased to approximately 15 to 30% of the wild-type level on xylose-containing medium and to 70 to 80% of the wild-type level on glucose-containing medium. Thus, LDH competed efficiently with the ethanol pathway for pyruvate, even though the pathway from pyruvate to ethanol was intact. Our results show, for the first time, that lactate production from xylose by a yeast species is feasible and efficient. This is encouraging for further development of yeast-based bioprocesses to produce lactate from lignocellulosic raw material.     

Evolutionary Engineering of Saccharomyces cerevisiae for Anaerobic Growth on Xylose

Xylose utilization is of commercial interest for efficient conversion of abundant plant material to ethanol. Perhaps the most important ethanol-producing organism, Saccharomyces cerevisiae, however, is incapable of xylose utilization. While S. cerevisiae strains have been metabolically engineered to utilize xylose, none of the recombinant strains or any other naturally occurring yeast has been able to grow anaerobically on xylose. Starting with the recombinant S. cerevisiae strain TMB3001 that overexpresses the xylose utilization pathway from Pichia stipitis, in this study we developed a selection procedure for the evolution of strains that are capable of anaerobic growth on xylose alone. Selection was successful only when organisms were first selected for efficient aerobic growth on xylose alone and then slowly adapted to microaerobic conditions and finally anaerobic conditions, which indicated that multiple mutations were necessary. After a total of 460 generations or 266 days of selection, the culture reproduced stably under anaerobic conditions on xylose and consisted primarily of two subpopulations with distinct phenotypes. Clones in the larger subpopulation grew anaerobically on xylose and utilized both xylose and glucose simultaneously in batch culture, but they exhibited impaired growth on glucose. Surprisingly, clones in the smaller subpopulation were incapable of anaerobic growth on xylose. However, as a consequence of their improved xylose catabolism, these clones produced up to 19% more ethanol than the parental TMB3001 strain produced under process-like conditions from a mixture of glucose and xylose.     

Characterization of the sugar alcohol-producing yeast Pichia anomala

Sugar alcohols have been widely applied in the field of food and medicine for their unique properties. Compared to chemical production, microbial production of sugar alcohol has become attractive for its environmental and sustainable pattern. In this study, a potential yeast isolated from soil of Beijing suburbs was identified as Pichia anomala TIB-x229, and its key enzyme of d-arabitol dehydrogenase for microbial production of sugar alcohols was functionally characterized. This yeast could simultaneously produce d-arabitol, xylitol, and/or ribitol from a different ratio of sugar substrates at a high efficiency by bioconversion, and no glucose repression happened when mixed sugars of xylose and glucose were used as the substrates during the bioconversion. This yeast could also efficiently convert complicated feedstock such as xylose mother liquor to d-arabitol, xylitol, and ribitol with 55 % yields. To elucidate the conversion relationship of the sugar alcohols, especially d-arabitol and xylitol, the key d-arabitol dehydrogenase gene from P. anomala was cloned, expressed and purified for further in vitro characterization. The results showed that this d-arabitol dehydrogenase could catalyze arabitol to xylulose further, which is significant for xylitol production from glucose. Our study laid the foundation for improving the production of sugar alcohols by metabolic and fermentation engineering strategies.