Metabolic Engineering of a Phosphoketolase Pathway for Pentose Catabolism in Saccharomyces cerevisiae

Low ethanol yields on xylose hamper economically viable ethanol production from hemicellulose-rich plant material with Saccharomyces cerevisiae. A major obstacle is the limited capacity of yeast for anaerobic reoxidation of NADH. Net reoxidation of NADH could potentially be achieved by channeling carbon fluxes through a recombinant phosphoketolase pathway. By heterologous expression of phosphotransacetylase and acetaldehyde dehydrogenase in combination with the native phosphoketolase, we installed a functional phosphoketolase pathway in the xylose-fermenting Saccharomyces cerevisiae strain TMB3001c. Consequently the ethanol yield was increased by 25% because less of the by-product xylitol was formed. The flux through the recombinant phosphoketolase pathway was about 30% of the optimum flux that would be required to completely eliminate xylitol and glycerol accumulation. Further overexpression of phosphoketolase, however, increased acetate accumulation and reduced the fermentation rate. By combining the phosphoketolase pathway with the ald6 mutation, which reduced acetate formation, a strain with an ethanol yield 20% higher and a xylose fermentation rate 40% higher than those of its parent was engineered.     

A genome shuffling-generated <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> isolate that ferments xylose and glucose to produce high levels of ethanol

Genome shuffling is an efficient approach for the rapid improvement of industrially important microbial phenotypes. This report describes optimized conditions for protoplast preparation, regeneration, inactivation, and fusion using the Saccharomyces cerevisiae W5 strain. Ethanol production was confirmed by TTC (triphenyl tetrazolium chloride) screening and high-performance liquid chromatography (HPLC). A genetically stable, high ethanol-producing strain that fermented xylose and glucose was obtained following three rounds of genome shuffling. After fermentation for 84 h, the high ethanol-producing S. cerevisiae GS3-10 strain (which utilized 69.48 and 100% of the xylose and glucose stores, respectively) produced 26.65 g/L ethanol, i.e., 47.08% higher than ethanol production by S. cerevisiae W5 (18.12 g/L). The utilization ratios of xylose and glucose were 69.48 and 100%, compared to 14.83 and 100% for W5, respectively. The ethanol yield was 0.40 g/g (ethanol/consumed glucose and xylose), i.e., 17.65% higher than the yield by S. cerevisiae W5 (0.34 g/g).     

Evaluation of Simultaneous Saccharification and Ethanol Fermentation of Undetoxified Steam-Exploded Corn Stover by Saccharomyces cerevisiae Y5

Toxin-tolerant yeast strains that produce high ethanol yield are inevitably requited for cost-effective ethanol production from undetoxified steam-exploded corn stover. To verify the ethanol-producing capability of the strain Saccharomyces cerevisiae Y5 developed in our laboratory, simultaneous saccharification and fermentation of undetoxified steam-exploded corn stover with solids loading of 30 % (w/v) was carried out in different-sized flasks and an automatic fermenter. After 96 h, the ethanol concentrations had reached 50, 47.8, and 47.5 g/L in the 100-mL flask, 3,000-mL flask, and 5-L automatic fermenter, respectively. The experiment demonstrates that ethanol production from undetoxified steam-exploded corn stover using S. cerevisiae Y5 simplifies the production process, reduces equipment investment and water consumption, and generates highly concentrated ethanol. S. cerevisiae Y5 is a promising strain that could reduce the cost of producing ethanol from steam-exploded corn stover.     

Effect of C/N ratio and starch concentration on ethanol production from sago starch using recombinant yeast

Recombinant Saccharomyces cerevisiae YKU 131 (capable of expressing glucoamylase) was used to produce ethanol from sago starch. The optimum C/N ratio for ethanol production by the recombinant yeast was 7.9, where 4.7 and 10.1 g/l ethanol was produced from 20 and 40 g/l sago starch, respectively. At sago starch concentration higher than 40 g/l and C/N ratio higher than 10.4, glucoamylase production and rate of starch hydrolysis were reduced, which in turn, reduced ethanol production significantly. The theoretical yield of ethanol based on sago starch consumed in fermentation using 40 g/l was 72.6%. This yield was slightly lower than those obtained in fermentation using soluble starch such as potato and corn starch, which ranged from 80–90% as reported in the literature. However, S. cerevisiae YKU 131 could only utilize 62% of the total amount of starch added to a medium.     

Engineering of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> to utilize xylan as a sole carbohydrate source by co-expression of an endoxylanase,xylosidase and a bacterial xylose isomerase

Xylan represents a major component of lignocellulosic biomass, and its utilization by Saccharomyces cerevisiae is crucial for the cost effective production of ethanol from plant biomass. A recombinant xylan-degrading and xylose-assimilating Saccharomyces cerevisiae strain was engineered by co-expression of the xylanase (xyn2) of Trichoderma reesei, the xylosidase (xlnD) of Aspergillus niger, the Scheffersomyces stipitis xylulose kinase (xyl3) together with the codon-optimized xylose isomerase (xylA) from Bacteroides thetaiotaomicron. Under aerobic conditions, the recombinant strain displayed a complete respiratory mode, resulting in higher yeast biomass production and consequently higher enzyme production during growth on xylose as carbohydrate source. Under oxygen limitation, the strain produced ethanol from xylose at a maximum theoretical yield of ~90 %. This study is one of only a few that demonstrates the construction of a S. cerevisiae strain capable of growth on xylan as sole carbohydrate source by means of recombinant enzymes.     

Reduced Oxidative Pentose Phosphate Pathway Flux in Recombinant Xylose-Utilizing Saccharomyces cerevisiae Strains Improves the Ethanol Yield from Xylose

In recombinant, xylose-fermenting Saccharomyces cerevisiae, about 30% of the consumed xylose is converted to xylitol. Xylitol production results from a cofactor imbalance, since xylose reductase uses both NADPH and NADH, while xylitol dehydrogenase uses only NAD⁺. In this study we increased the ethanol yield and decreased the xylitol yield by lowering the flux through the NADPH-producing pentose phosphate pathway. The pentose phosphate pathway was blocked either by disruption of the GND1 gene, one of the isogenes of 6-phosphogluconate dehydrogenase, or by disruption of the ZWF1 gene, which encodes glucose 6-phosphate dehydrogenase. Decreasing the phosphoglucose isomerase activity by 90% also lowered the pentose phosphate pathway flux. These modifications all resulted in lower xylitol yield and higher ethanol yield than in the control strains. TMB3255, carrying a disruption of ZWF1, gave the highest ethanol yield (0.41 g g⁻¹) and the lowest xylitol yield (0.05 g g⁻¹) reported for a xylose-fermenting recombinant S. cerevisiae strain, but also an 84% lower xylose consumption rate. The low xylose fermentation rate is probably due to limited NADPH-mediated xylose reduction. Metabolic flux modeling of TMB3255 confirmed that the NADPH-producing pentose phosphate pathway was blocked and that xylose reduction was mediated only by NADH, leading to a lower rate of xylose consumption. These results indicate that xylitol production is strongly connected to the flux through the oxidative part of the pentose phosphate pathway.     

Simultaneous Saccharification and Ethanol Fermentation of Corn Stover at High Temperature and High Solids Loading by a Thermotolerant Strain Saccharomyces cerevisiae DQ1

The thermotolerant strain Saccharomyces cerevisiae DQ1 was applied to the simultaneous saccharification and fermentation (SSF) at high temperature and high solids loading of the dilute acid-pretreated corn stover in the present study. The SSF using S. cerevisiae DQ1 was operated at 30?% solids loading of the pretreated corn stover with three-step SSF mode and achieved up to ethanol titer of 48?g/L and yield of 65.6?%. S. cerevisiae DQ1 showed strong thermotolerance in both the regular one-step SSF and the three-step SSF with changing temperature in each step. The three-step SSF at 40°C using S. cerevisiae DQ1 tolerated the greater cellulase dosage and solids loading of the pretreated corn stover and resulted in increased ethanol production. The present study provided a practical potential for the future SSF of lignocellulose feedstock at high temperature to reach high ethanol titer.     

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.     

Effect of nickel oxide nanoparticles on bioethanol production: Process optimization,kinetic and metabolic studies

The present study optimized ethanol yield using nickel oxide (NiO) nanoparticles (NPs) as a biocatalyst. Additionally, Saccharomyces cerevisiae BY4743 cell growth and the bioethanol production kinetics were assessed. The Response Surface Methodology (RSM) model showed a coefficient of determination (R²) value of 0.93. The optimized process gave a biomass concentration and ethanol yield of 2.04 g/L and 0.26 g/g (1.03 and 1.19-fold increment compared to the control experiment), respectively. The process kinetic data showed that the inclusion of NiO NPs improved the affinity of S. cerevisiae BY4743 to glucose consumption, carbohydrate and protein accumulation. A significant reduction in volatile fatty acid (VFA) was observed in the presence of NiO NPs. The application of nano biocatalyst in simultaneous saccharification and fermentation of potato peel waste, meaningfully enhanced bioethanol production (>65 %). The study provided major insights into the use of NiO NPs to enhance the bioprocess of ethanol production.     

Improve carbon metabolic flux in Saccharomyces cerevisiae at high temperature by overexpressed TSL1 gene

This study describes a novel strategy to improve the glycolysis flux of Saccharomyces cerevisiae at high temperature. The TSL1 gene-encoding regulatory subunit of the trehalose synthase complex was overexpressed in S. cerevisiae Z-06, which increased levels of trehalose synthase activity in extracts, enhanced stress tolerance and glucose consuming rate of the yeast cells. As a consequence, the final ethanol concentration of 185.5 g/L was obtained at 38 °C for 36 h (with productivity up to 5.2 g/L/h) in 7-L fermentor, and the ethanol productivity was 92.7 % higher than that of the parent strain. The results presented here provide a novel way to enhance the carbon metabolic flux at high temperature, which will be available for the purposes of producing other primary metabolites of commercial interest using S. cerevisiae as a host.     

Implementation of a transhydrogenase-like shunt to counter redox imbalance during xylose fermentation in Saccharomyces cerevisiae

Three enzymes responsible for the transhydrogenase-like shunt, including malic enzyme (encoded by MAE1), malate dehydrogenase (MDH2), and pyruvate carboxylase (PYC2), were overexpressed to regulate the redox state in xylose-fermenting recombinant Saccharomyces cerevisiae. The YPH499XU/MAE1 strain was constructed by overexpressing native Mae1p in the YPH499XU strain expressing xylose reductase and xylitol dehydrogenase from Scheffersomyces stipitis, and native xylulokinase. Analysis of the xylose fermentation profile under semi-anaerobic conditions revealed that the ethanol yield in the YPH499XU/MAE1 strain (0.38?±?0.01 g g^?1 xylose consumed) was improved from that of the control strain (0.31?±?0.01 g g^?1 xylose consumed). Reduced xylitol production was also observed in YPH499XU/MAE1, suggesting that the redox balance was altered by Mae1p overexpression. Analysis of intracellular metabolites showed that the redox imbalance during xylose fermentation was partly relieved in the transformant. The specific ethanol production rate in the YPH499XU/MAE1–MDH2 strain was 1.25-fold higher than that of YPH499XU/MAE1 due to the additional overexpression of Mdh2p, whereas the ethanol yield was identical to that of YPH499XU/MAE1. The specific xylose consumption rate was drastically increased in the YPH499XU/MAE1–MDH2–PYC2 strain. However, poor ethanol yield as well as increased production of xylitol was observed. These results demonstrate that the transhydrogenase function implemented in S. cerevisiae can regulate the redox state of yeast cells.     

A high-throughput transient gene expression system for switchgrass (Panicum virgatum L.) seedlings

Background

Fermentations using Escherichia coli KO11, Saccharomyces cerevisiae 424A(LNH-ST), and Zymomonas mobilis AX101 are compared side-by-side on corn steep liquor (CSL) media and the water extract and enzymatic hydrolysate from ammonia fiber expansion (AFEX)-pretreated corn stover.

Results

The three ethanologens are able produce ethanol from a CSL-supplemented co-fermentation at a metabolic yield, final concentration and rate greater than 0.42 g/g consumed sugars, 40 g/L and 0.7 g/L/h (0-48 h), respectively. Xylose-only fermentation of the tested ethanologenic bacteria are five to eight times faster than 424A(LNH-ST) in the CSL fermentation. All tested strains grow and co-ferment sugars at 15% w/v solids loading equivalent of ammonia fiber explosion (AFEX)-pretreated corn stover water extract. However, both KO11 and 424A(LNH-ST) exhibit higher growth robustness than AX101. In 18% w/w solids loading lignocellulosic hydrolysate from AFEX pretreatment, complete glucose fermentations can be achieved at a rate greater than 0.77 g/L/h. In contrast to results from fermentation in CSL, S. cerevisiae 424A(LNH-ST) consumed xylose at the greatest extent and rate in the hydrolysate compared to the bacteria tested.

Conclusions

Our results confirm that glucose fermentations among the tested strains are effective even at high solids loading (18% by weight). However, xylose consumption in the lignocellulosic hydrolysate is the major bottleneck affecting overall yield, titer or rate of the process. In comparison, Saccharomyces cerevisiae 424A(LNH-ST) is the most relevant strains for industrial production for its ability to ferment both glucose and xylose from undetoxified and unsupplemented hydrolysate from AFEX-pretreated corn stover at high yield.     

The effect of xylose reductase genes on xylitol production by industrial Saccharomyces cerevisiae in fermentation of glucose and xylose

The co-production of xylitol and ethanol from agricultural straw has more economic advantages than the production of ethanol only. Saccharomyces cerevisiae, the most widely used ethanol-producing yeast, can be genetically engineered to ferment xylose to xylitol. In the present study, the effects of xylose-specificity, cofactor preference, and the gene copy number of xylose reductase (XR; encoding by XYL1 gene) on xylitol production of S. cerevisiae were investigated. The results showed that overexpression of XYL1 gene with a lower xylose-specificity and a higher NADPH preference favored the xylitol production. The copy number of XYL1 had a positive correlation with the XR activity but did not show a good correlation with the xylitol productivity. The overexpression of XYL1 from Candida tropicalis (CtXYL1) achieved a xylitol productivity of 0.83 g/L/h and a yield of 0.99 g/g-consumed xylose during batch fermentation with 43.5 g/L xylose and 17.0 g/L glucose. During simultaneous saccharification and fermentation (SSF) of pretreated corn stover, the strain overexpressing CtXYL1 produced 45.41 g/L xylitol and 50.19 g/L ethanol, suggesting its application potential for xylitol and ethanol co-production from straw feedstocks.     

Changes in intracellular metabolism underlying the adaptation of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> strains to ethanol stress

Saccharomyces cerevisiae is often stressed by the ethanol which accumulates during the production of bioethanol by the fermentation process. The study of ethanol-adapted S. cerevisiae strains provide an opportunity to clarify the molecular mechanism underlying the adaptation or tolerance of S. cerevisiae to ethanol stress. The aim of this study was to clarify this molecular mechanism by investigating the ethanol adaptation-associated intracellular metabolic changes in S. cerevisiae using a gas chromatography–mass spectrometry-based metabolomics strategy. A partial least-squares-discriminant analysis between the parental strain and ethanol-adapted strains identified 12 differential metabolites of variable importance with a projection value of >1. The ethanol-adapted strains had a more activated glycolysis pathway and higher energy production than the parental strain, suggesting the possibility that an increased energy production and energy requirement might be partly responsible for an increased ethanol tolerance. An increased glycine content also partly contributed to the higher ethanol tolerance of the ethanol-adapted strains. The decreased oleic acid content may be a self-protection mechanism of ethanol-adapted strains to maintain membrane integrity through decreasing membrane fluidity. We suggest that while being exposed to ethanol stress, ethanol-adapted S. cerevisiae cells may remodel their metabolic phenotype and the composition of their cell membrane to adapt to ethanol stress and acquire higher ethanol tolerance.     

Improved ethanol production of a newly isolated thermotolerant Saccharomyces cerevisiae strain after high-energy-pulse-electron beam

Aims: To isolate thermotolerant Saccharomyces cerevisiae with high‐energy‐pulse‐electron (HEPE) beam, to optimize the mutation strain fermentation conditions for ethanol production and to conduct a preliminary investigation into the thermotolerant mechanisms. Methods and Results: After HEPE beam radiation, the thermotolerant S. cerevisiae strain Y43 was obtained at 45°C. Moreover, the fermentation conditions of mutant Y43 were optimized by L3³ orthogonal experiment. The optimal glucose content and initial pH for fermentation were 20% g l^?1 and 4·5, respectively; peptone content was the most neglected important factor. Under this condition, ethanol production of Y43 was 83·1 g l^?1 after fermentation for 48 h at 43°C, and ethanol yield was 0·42 g g^?1, which was about 81·5% of the theoretical yield. The results also showed that the trehalose content and the expression of the genes MSN2, SSA3 and TPS1 in Y43 were higher than those in the original strain (YE0) under the same stress conditions. Conclusions: A genetically stable mutant strain with high ethanol yield under heat stress was obtained using HEPE. This mutant may be a suitable candidate for the industrial‐scale ethanol production. Significance and Impact of the Study: High‐energy‐pulse‐electron radiation is a new efficient technology in breeding micro‐organisms. The mutant obtained in this work has the advantages in industrial ethanol production under thermostress.     

不同信号肽对酿酒酵母蔗糖转化酶Suc2分泌表达水平的影响

目前，绝大多数酿酒酵母（Saccharomyces cerevisiae）菌株利用菊糖生产乙醇的能力有限，而蔗糖转化酶Suc2是酿酒酵母水解菊糖的关键酶，其分泌水平直接影响酿酒酵母转化菊糖为乙醇的性能。为提高酿酒酵母中蔗糖转化酶Suc2的分泌表达水平，利用生物信息学的分析方法选择出11种不同的分泌信号肽，包括酿酒酵母内源性、其他菌株来源以及已报道序列优化改造的信号肽，将它们融合至Suc2并构建了相应的酿酒酵母BY4741重组菌。其中，酿酒酵母内源分泌信号肽AGA2能使蔗糖转化酶Suc2更有效的分泌，含有信号肽AGA2的重组菌BY-AG的蔗糖酶酶活和菊糖酶酶活相对于含有天然信号肽的原始菌BY-S分别提高42%和26%，其利用菊糖产乙醇能力较原始菌提高了32%，乙醇产量达到78.11 g/L。在使用毕赤酵母（Pichia pastoris）分泌信号肽MSB2时，蔗糖转化酶Suc2的分泌水平也有提高，含有信号肽MSB2的重组菌BY-MS较原始菌BY-S的蔗糖酶酶活和菊糖酶酶活分别提高了80%和74%，同时，利用菊糖产乙醇能力也提高了56%，产量达到86.31 g/L。最后，对重组菌BY-MS摇瓶发酵过程中的生物量、蔗糖酶酶活、残糖总量和乙醇产量进行了监测，结果表明，重组菌BY-MS的发酵性能较原始菌BY-S有显著提高。本研究为提高蔗糖转化酶Suc2的分泌水平、构建高效菊糖基乙醇生产菌株提供参考。     

Expression of aldehyde dehydrogenase 6 reduces inhibitory effect of furan derivatives on cell growth and ethanol production in Saccharomyces cerevisiae

Yeast dehydrogenases and reductases were overexpressed in Saccharomyces cerevisiae D452-2 to detoxify 2-furaldehyde (furfural) and 5-hydroxymethyl furaldehyde (HMF), two potent toxic chemicals present in acid-hydrolyzed cellulosic biomass, and hence improve cell growth and ethanol production. Among those enzymes, aldehyde dehydrogenase 6 (ALD6) played the dual roles of direct oxidation of furan derivatives and supply of NADPH cofactor to their reduction reactions. Batch fermentation of S. cerevisiae D452-2/pH-ALD6 in the presence of 2 g/L furfural and 0.5 g/L HMF resulted in 20-30% increases in specific growth rate, ethanol concentration and ethanol productivity, compared with those of the wild type strain. It was proposed that overexpression of ALD6 could recover the yeast cell metabolism and hence increase ethanol production from lignocellulosic biomass containing furan-derived inhibitors.     

Development of new unstructured model for simultaneous saccharification and fermentation of starch to ethanol by recombinant strain

The development of simultaneous saccharification and fermentation of starch to ethanol (SSFSE) by genetically modified microbial strains has been studied intensively [M.M. Altintas, B. Kirdar, Z.Ï. Önsan, K.Ö. Ülgen, Cybernetic modelling of growth and ethanol production in a recombinant Saccharomyces cerevisiae strain secreting a bifunctional fusion protein, Process Biochem. 37 (2002) 1439–1445; G. Birol, Z.Ï. Önsan, B. Kirdar, S.G. Oliver, Ethanol production and fermentation characteristics of recombinant Saccharomyces cerevisiae strains grown on starch, Enzyme Microb. Technol. 22 (1998) 672–677; F. Kobayashi, Y. Nakamura, Effect of repressor gene on stability of bioprocess with continuous conversion of starch into ethanol using recombinant yeast, Biochem. Eng. J. 18 (2004) 133–141; F. Kobayashi, Y. Nakamura, Mathematical model of direct ethanol production from starch in immobilized recombinant yeast culture, Biochem. Eng. J. 21 (2004) 93–101; M.M. Altintas, K.Ö. Ülgen, B. Kirdar, Z.Ï. Önsan, S.G. Oliver, Improvement of ethanol production from starch by recombinant yeast through manipulation of environmental factors, Enzyme Microb. Technol. 31 (2002) 640–647; K.Ö. Ülgen, B. Saygili, Z.Ï. Önsan, B. Kirdar, Bioconversion of starch into ethanol by a recombinant Saccharomyces cerevisiae strain YPG-AB, Process Biochem. 37 (2002) 1157–1168]. Saccharomyces cerevisiae YPB-G strain secretes a bifunctional fusion protein containing enzymatic activity of the B. subtilis alpha-amylase and of the Aspergillus awamori glucoamylase [M.M. Altintas, B. Kirdar, Z.Ï. Önsan, K.Ö. Ülgen, Cybernetic modelling of growth and ethanol production in a recombinant Saccharomyces cerevisiae strain secreting a bifunctional fusion protein, Process Biochem. 37 (2002) 1439–1445], and therefore is distinguished in relation to SSFSE step. In this work we have used the experimental data, presented in the paper [M.M. Altintas, B. Kirdar, Z.Ï. Önsan, K.Ö. Ülgen, Cybernetic modelling of growth and ethanol production in a recombinant Saccharomyces cerevisiae strain secreting a bifunctional fusion protein, Process Biochem. 37 (2002) 1439–1445] to develop two-hierarchic-level unstructured mathematical model describing kinetics of direct bioconversion of starch to ethanol. The first level has modeled enzymatic hydrolysis of starch to glucose by bifunctional protein and the second level includes utilization and bioconversion of glucose to ethanol by yeasts. The second level has unified the enzymatic degradation of starch, and glucose metabolization to ethanol by microorganisms. The response surface analysis was used to develop the rates models. A hybrid genetic algorithm and a decomposition approach were used in the nonlinear parameters identification procedure. The proposed model demonstrated excellent flexibility for different operational conditions of SSFSE process, and can be used successfully to describe microbial physiology of genetically modified strains.     

Expression of bacterial xylose isomerase in Saccharomyces cerevisiae under galactose supplemented condition

We constructed recombinant Saccharomyces cerevisiae harboring the xylose isomerase (XI) gene isolated from Clostridium phytofermentans to metabolize xylose and use it as a carbon and energy source. In this study, the effect of supplementation using co-substrate such as glucose or galactose on xylose utilization was studied in recombinant S. cerevisiae. Glucose, which is transported with high affinity by the same transport system as is xylose, was not affected by the heterologous expression of XI, thus xylose utilization was not observed in recombinant S. cerevisiae. However, supplemental galactose added to the recombinant S. cerevisiae stimulated xylose utilization as well as the expression of XI protein. Recombinant S. cerevisiae consumed up to 23.48 g/L of xylose when grown in media containing 40 g/L of xylose and supplemented with 20 g/L of galactose. These cells also produced 15.89 g/L of ethanol. Therefore, expression of the bacterial XI in recombinant S. cerevisiae was highly induced by the addition of supplemental galactose as a co-substrate with xylose, and supplemented galactose enabled the yeast strain to grow on xylose and ferment xylose to ethanol.