Xylitol does not inhibit xylose fermentation by engineered <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> expressing <Emphasis Type="Italic">xylA</Emphasis> as severely as it inhibits xylose isomerase reaction in vitro

Efficient fermentation of xylose, which is abundant in hydrolysates of lignocellulosic biomass, is essential for producing cellulosic biofuels economically. While heterologous expression of xylose isomerase in Saccharomyces cerevisiae has been proposed as a strategy to engineer this yeast for xylose fermentation, only a few xylose isomerase genes from fungi and bacteria have been functionally expressed in S. cerevisiae. We cloned two bacterial xylose isomerase genes from anaerobic bacteria (Bacteroides stercoris HJ-15 and Bifidobacterium longum MG1) and introduced them into S. cerevisiae. While the transformant with xylA from B. longum could not assimilate xylose, the transformant with xylA from B. stercoris was able to grow on xylose. This result suggests that the xylose isomerase (BsXI) from B. stercoris is functionally expressed in S. cerevisiae. The engineered S. cerevisiae strain with BsXI consumed xylose and produced ethanol with a good yield (0.31 g/g) under anaerobic conditions. Interestingly, significant amounts of xylitol (0.23 g xylitol/g xylose) were still accumulated during xylose fermentation even though the introduced BsXI might not cause redox imbalance. We investigated the potential inhibitory effects of the accumulated xylitol on xylose fermentation. Although xylitol inhibited in vitro BsXI activity significantly (K _I = 5.1 ± 1.15 mM), only small decreases (less than 10%) in xylose consumption and ethanol production rates were observed when xylitol was added into the fermentation medium. These results suggest that xylitol accumulation does not inhibit xylose fermentation by engineered S. cerevisiae expressing xylA as severely as it inhibits the xylose isomerase reaction in vitro.     

Physiological properties of Cellulomonas fermentans,a mesophilic cellulolytic bacterium

Summary The fermentation of cellobiose, glucose and cellulose MN 300 by Cellulomonas fermentans was studied. The molar growth yields (i.e. grams of cells per mole of hexose equivalent) were similar on cellobiose and cellulose at low sugar consumption levels (47.8 and 46.5 respectively), but was lower on glucose (38.0). The occurrence of cellobiose phosphorylase activity, detected in cellobiose- and cellulose-grown cells, might explain this result. The specific growth rates measured in cultures on cellobiose, glucose and cellulose were 0.055 h^-1, 0.040 h^-1 and 0.013 h^-1 respectively. Growth inhibition was observed, and a drop in Y_H occurred after relatively low but different quantities of hexose were consumed (2.2 mM, 5 mM and 8 mM hexose equivalent with cellulose, glucose and cellobiose respectively), which coincided with a change in the fermentative metabolism from a typical mixed acid metabolism (1 ethanol, 1 acetate and 2 formate synthesized by consumed hexose) to a more ethanolic fermentation. When growth ceased in cellulose cultures, consumption of cellulose continued, as did production of ethanol.Molar growth yields of C. fermentans were similar in anaerobic and aerobic cellobiose cultures (47.8 g/mol and 42.2 g/mol respectively). Specific growth rates were also quite similar under both culture conditions (0.055±0.013 h^-1 and 0.070±0.007 h^-1 respectively). Aerobic metabolism was studied using ¹⁴C glucose. During the exponential growth phase, acetate, succinate and nonidentified compound(s) accumulated in the supernatant, but no ¹⁴CO₂ was produced. During the stationary phase, acetate was oxidized and ¹⁴CO₂ produced, but without any further biomass synthesis. It seems that a blocking of metabolite oxidation may have occurred in C. fermentans except in the case of acetate, but acetate oxidation was apparently not coupled with production of energy utilizable in biosynthesis.     

Cloning,expression and characterization of xylose isomerase from the marine bacterium Fulvimarina pelagi in Escherichia coli

Production of a xylose isomerase (XI) with high tolerance to the inhibitors xylitol and calcium, and high activity at the low pH and temperature conditions characteristic of yeast fermentations, is desirable for a simultaneous isomerization/fermentation process for cellulosic ethanol production. A putative XI gene (xylA) from the marine bacterium Fulvimarina pelagi was identified by sequence analysis of the F. pelagi genome, and was PCR amplified, cloned, and expressed in Escherichia coli. The rXI was produced in shake flask and fed‐batch fermentations using glucose as the growth substrate. The optimum pH for rXI was approximately 7, although activity was evident at pH as low as 5.5. The purified rXI had a molecular weight in 160 kDA, a V_max of 0.142 U/mg purified rXI, and a K_M for xylose in the range of 1.75–4.17 mM/L at pH 6.5 and a temperature of 35°C. The estimated calcium and xylitol K_I values for rXI in cell‐free extracts were 2,500 mg/L and >50 mM, respectively. The low K_M of the F. pelagi xylose isomerase is consistent with the low nutrient conditions of the pelagic environment. These results indicate that Ca²⁺ and xylitol are not likely to be inhibitory in applications employing the rXI from F. pelagi to convert xylose to xylulose in fermentations of complex biomass hydrolysates. A higher V_max at low pH (<6) and temperature (30°C) would be preferable for use in biofuels production. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:1230–1237, 2016     

Identification of a Xylitol Dehydrogenase Gene from Kluyveromyces marxianus NBRC1777

Xylitol dehydrogenase (XDH) (EC 1.1.1.9) is one of the key enzymes in the xylose fermentation pathway in yeast and fungi. A xylitol dehydrogenase gene (XYL2) encoding a XDH was cloned from Kluyveromyces marxianus NBRC 1777, and the in vivo function was validated by disruption and complementation analysis. The highest activity of KmXDH could be observed at pH 9.5 during 55°C. The values of k _cat/K _m indicate that KmXDH prefers NAD⁺ to NADP⁺ (k _cat/K _{m NAD} ⁺ 3681/min mM and k _cat/K _{m NADP} ⁺ 1361/min mM). The different coenzyme preference between KmXR and KmXDH caused an accumulation of NADH in the xylose utilization pathway. The redox imbalance may be one of the reasons to cause the poor xylose fermentation under oxygen-limited conditions in K. marxianus NBRC1777.     

Heterologous production and biochemical characterization of a new highly glucose tolerant GH1 β-glucosidase from Anoxybacillus thermarum

The enzymatic lignocellulosic biomass conversion into value-added products requires the use of enzyme-rich cocktails, including β-glucosidases that hydrolyze cellobiose and cellooligosaccharides to glucose. During hydrolysis occurs accumulation of monomers causing inhibition of some enzymes; thus, glucose/xylose tolerant β-glucosidases could overcome this drawback. The search of new tolerant enzymes showing additional properties, such as high activity, wide-pH range, and thermal stability is very relevant to improve the bioprocess. We describe a novel β-glucosidase GH1 from the thermophilic Anoxybacillus thermarum (BgAt), which stood out by the robustness combination of great glucose/xylose tolerance, thermal stability, and high Vmax. The recombinant his-tagged-BgAt was overexpressed in Escherichia coli, was purified in one step, showed a high glucose/xylose tolerance, and activity stimulation (presence of 0.4 M glucose/1.0 M xylose). The optimal activity was at 65 °C - pH 7.0. BgAt presented an extraordinary temperature stability (48 h – 50 °C), and pH stability (5.5–8.0). The novel enzyme showed outstanding Vmax values compared to other β-glucosidases. Using p-nitrophenyl-β-d-glucopyranoside as substrate the values were Vmax (7614 U/mg), and K_M (0.360 mM). These values suffer a displacement in Vmax to 14,026 U/mg (glucose), 14,886 U/mg (xylose), and K_M 0.877 mM (glucose), and 1.410 mM (xylose).     

Comparing the xylose reductase/xylitol dehydrogenase and xylose isomerase pathways in arabinose and xylose fermenting Saccharomyces cerevisiae strains

Background

Ethanolic fermentation of lignocellulosic biomass is a sustainable option for the production of bioethanol. This process would greatly benefit from recombinant Saccharomyces cerevisiae strains also able to ferment, besides the hexose sugar fraction, the pentose sugars, arabinose and xylose. Different pathways can be introduced in S. cerevisiae to provide arabinose and xylose utilisation. In this study, the bacterial arabinose isomerase pathway was combined with two different xylose utilisation pathways: the xylose reductase/xylitol dehydrogenase and xylose isomerase pathways, respectively, in genetically identical strains. The strains were compared with respect to aerobic growth in arabinose and xylose batch culture and in anaerobic batch fermentation of a mixture of glucose, arabinose and xylose.

Results

The specific aerobic arabinose growth rate was identical, 0.03 h^-1, for the xylose reductase/xylitol dehydrogenase and xylose isomerase strain. The xylose reductase/xylitol dehydrogenase strain displayed higher aerobic growth rate on xylose, 0.14 h^-1, and higher specific xylose consumption rate in anaerobic batch fermentation, 0.09 g (g cells)^-1 h^-1 than the xylose isomerase strain, which only reached 0.03 h^-1 and 0.02 g (g cells)^-1h^-1, respectively. Whereas the xylose reductase/xylitol dehydrogenase strain produced higher ethanol yield on total sugars, 0.23 g g^-1 compared with 0.18 g g^-1 for the xylose isomerase strain, the xylose isomerase strain achieved higher ethanol yield on consumed sugars, 0.41 g g^-1 compared with 0.32 g g^-1 for the xylose reductase/xylitol dehydrogenase strain. Anaerobic fermentation of a mixture of glucose, arabinose and xylose resulted in higher final ethanol concentration, 14.7 g l^-1 for the xylose reductase/xylitol dehydrogenase strain compared with 11.8 g l^-1 for the xylose isomerase strain, and in higher specific ethanol productivity, 0.024 g (g cells)^-1 h^-1 compared with 0.01 g (g cells)^-1 h^-1 for the xylose reductase/xylitol dehydrogenase strain and the xylose isomerase strain, respectively.

Conclusion

The combination of the xylose reductase/xylitol dehydrogenase pathway and the bacterial arabinose isomerase pathway resulted in both higher pentose sugar uptake and higher overall ethanol production than the combination of the xylose isomerase pathway and the bacterial arabinose isomerase pathway. Moreover, the flux through the bacterial arabinose pathway did not increase when combined with the xylose isomerase pathway. This suggests that the low activity of the bacterial arabinose pathway cannot be ascribed to arabitol formation via the xylose reductase enzyme.     

Production and Purification of Extracellular D-Xylose Isomerase from an Alkaliphilic, Thermophilic Bacillus sp.

An alkaliphilic, thermophilic Bacillus sp. (NCIM 59) produced extracellular xylose isomerase at pH 10 and 50°C by using xylose or wheat bran as the carbon source. The distribution of xylose isomerase as a function of growth in comparison with distributions of extra- and intracellular marker enzymes such as xylanase and β-galactosidase revealed that xylose isomerase was truly secreted as an extracellular enzyme and was not released because of sporulation or lysis. The enzyme was purified to homogeneity by ammonium sulfate precipitation followed by gel filtration, preparative polyacrylamide gel electrophoresis, and ion-exchange chromatography. The molecular weight of xylose isomerase was estimated to be 160,000 by gel filtration and 50,000 by sodium dodecyl sulfate-polyacrylamide gel electrophoresis, indicating the presence of three subunits. The enzyme is most active at pH 8.0 and with incubation at 85°C for 20 min. Divalent metal ions Mg²⁺, Co²⁺, and Mn²⁺ were required for maximum activity of the enzyme. The K_m values for D-xylose and D-glucose at 80°C and pH 7.5 were 6.66 and 142 mM, respectively, while K_cat values were 2.3 × 10² s^-1 and 0.5 × 10² s^-1, respectively.     

Purification and characterization of thermostable xylose(glucose) isomerase from Bacillus thermoantarcticus

Xylose isomerase produced by Bacillus thermoantarcticus was purified 73-fold to homogeneity and its biochemical properties were determined. It was a homotetramer with a native molecular mass of 200 kDa and a subunit molecular mass of 47 kDa, with an isoelectric point at 4.8. The enzyme had a K _m of 33 mM for xylose and also accepted D-glucose as substrate. Arrhenius plots of the enzyme activity of xylose isomerase were linear up to a temperature of 85°C. Its optimum pH was around 7.0, and it had 80% of its maximum activity at pH 6.0. This enzyme required divalent cations for its activity and thermal stability. Mn²⁺, Co²⁺ or Mg²⁺ were of comparable efficiency for xylose isomerase reaction, while Mg²⁺ was necessary for glucose isomerase reaction. Journal of Industrial Microbiology & Biotechnology (2001) 27, 234–240. Received 18 March 2001/ Accepted in revised form 03 July 2001     

Purification and characterization of an extremely stable glucose isomerase from Geobacillus thermodenitrificans TH2

The D-glucose/D-xylose isomerase was purified from a thermophilic bacterium, Geobacillus thermodenitrificans TH2, by precipitating with heat shock and using Q-Sepharose ion exchange column chromatography, and then characterized. The purified enzyme had a single band having molecular weight of 49 kDa on SDS-PAGE. In the presence of D-glucose as a substrate, the optimum temperature and pH of the enzyme were found to be 80°C and 7.5, respectively. The purified xylose isomerase of G. thermodenitrificans TH2 was extremely stable at pH 7.5 after 96 h incubation at 4°C and 50°C. When the thermal stability profile was analyzed, it was determined that the purified enzyme was extremely stable during incubation periods of 4 months and 4 days at 4°C and 50°C, respectively. The K _m and V _max values of the purified xylose isomerase from G. thermodenitrificans TH2 were calculated as 32 mM and 4.68 μmol/min per mg of protein, respectively. Additionally, it was detected that some metal ions affected the enzyme activity at different ratios. The enzyme was active and stable at high temperatures and nearly neutral pHs which are desirable for the usage in the food and ethanol industry.     

Purification and characterization of carbonic anhydrase from bovine stomach and effects of some known inhibitors on enzyme activity

Carbonic anhydrase (CA) was purified from four different cell localisation (outer peripheral, cytosolic, inner peripheral and integral) in bovine stomach using affinity chromatography with Sepharose-4B-l-tyrosine sulphanilamide. During the purification steps, the activity of the enzyme was measured using p-nitrophenyl acetate at pH 7.4. Optimum pH and optimum temperature values for all CA samples were determined, and their K_m and V_max values for the same substrate by Lineweaver–Burk graphics. The extent of purification for all CA localizations was controlled by SDS-PAGE. The K_m values at optimum pH and 20°C were 0.625?mM, 0.541?mM, 0.785?mM and 0.862?mM with p-nitro phenyl acetate, for all CA localizations. The respective V_max values at optimum pH and 20°C were 0.875?μmol/L?min, 0.186?μmol/L?min, 0.214?μmol/L?min and 0.253?μmol/L?min with the same substrate. The K_i and I₅₀ values for the inhibitors sulphanilamide, KSCN, NaN₃ and acetazolamide were determined for all the CA localizations.     

Isolation and Characterization of a β-Glucosidase from a Clavispora Strain with Potential Applications in Bioethanol Production from Cellulosic Materials

We previously reported on a new yeast strain of Clavispora sp. NRRL Y-50464 that is capable of utilizing cellobiose as sole source of carbon and energy by producing sufficient native β-glucosidase enzyme activity without further enzyme supplementation for cellulosic ethanol production using simultaneous saccharification and fermentation. Eliminating the addition of external β-glucosidase reduces the cost of cellulosic ethanol production. In this study, we present results on the isolation and identification of a β-glucosidase protein from strain Y-50464. Using Matrix-assisted laser desorption/ionization time-of-flight mass spectrometry and blast search of the NCBInr database (National Center for Biotechnology Information nonredundant), the protein from Y-50464 was identified as a β-glucosidase (BGL1) with a molecular weight of 93.3 kDa. The BGL1 protein was purified through multiple chromatographic steps to a 26-fold purity (K _m?=?0.355 mM [pNPG]; K _i?=?15.2 mM [glucose]), which has a specific activity of 18.4 U/mg of protein with an optimal performance temperature at 45 °C and pH of 6.0. This protein appears to be intracellular although other forms of the enzyme may exist. The fast growth rate of Y-50464 and its capability to produce sufficient β-glucosidase activity for ethanol conversion from cellobiose provide a promising means for low-cost cellulosic ethanol production through a consolidated bioprocessing development.     

A Highly Efficient NADH-dependent Butanol Dehydrogenase from High-butanol-producing Clostridium sp. BOH3

Butanol has been considered as a better alternative fuel and it can be produced from anaerobic Clostridial fermentation. Though several enzymes are involved in the biosynthesis of butanol in Clostridia, butanol dehydrogenase (BDH) is understood to play a major role, which catalyzes the conversion of butyraldehyde into butanol at the expenditure of a cofactor NAD(P)H. Recently, the strain Clostridium sp. BOH3 is reported to generate high level of butanol from monosugars. To investigate the BDH activity at various stages of fermentation, BOH3 was cultured in reinforced Clostridial medium with 30 g/l of glucose at 35 °C and the cells were harvested periodically from acid production and solvent production phases. During acid production, NADPH-dependent BDH activity is higher than NADH dependent BDH. Conversely, NADH-BDH activity is predominant during solvent production phase. The optimum pHs for NADH and NADPH-BDH are estimated as pH?6 and 8, respectively. By employing three steps of purification, NADH-BDH is purified to 102-fold with 36 % yield. Subsequent characterization reveals that NADH-BDH is a dimer composed of two subunits depicting the molecular weight of 44 kDa. The peptide finger printing analysis (MS/MS) suggests that the purified protein has higher homology with bifunctional acetaldehyde-CoA and alcohol dehydrogenase of Clostridium acetobutylicum. The extensive kinetic studies show that NADH-BDH follows an ordered sequential bi bi mechanism. The calculated values of K _{butyraldehyde} and K _NADH are 8.35?±?0.25 and 0.076?±?0.02 mM, respectively, whereas V _max is 4.02?±?0.07 μmol/(mg protein. min). The purified NADH-BDH retains 70 % of its initial activity after 7 days at 4 °C.     

Comparative engineering of Escherichia coli for cellobiose utilization: Hydrolysis versus phosphorolysis

Microbial biocatalysts capable of cellobiose assimilation are of interest in bioconversion of cellulosic materials. This study provides a careful comparison in the two mechanisms of cellobiose assimilation, hydrolysis versus phosphorolysis, between two otherwise isogenic E. coli strains. Relative to cells assimilating cellobiose hydrolytically, phosphorolysis cells tolerated common inhibitors better under both anaerobic and aerobic conditions. Additionally, phosphorolysis cells were able to direct the favorable energy metabolism to recombinant protein production, resulting in up to five fold more recombinant proteins. In a mixed sugar fermentation (5% (w/v) cellobiose+5.0% (w/v) xylose), however, xylose utilization in phosphorolysis cells came to a complete halt after only about 60% consumption whereas the hydrolysis cells were able to ferment both sugars to near completion. These results provide insights into the new metabolic engineering strategy. To our best knowledge, this is the first comparison study in E. coli on the two cellobiose assimilation mechanisms.     

Ethanol Production by Thermophilic Bacteria: Fermentation of Cellulosic Substrates by Cocultures of Clostridium thermocellum and Clostridium thermohydrosulfuricum

The fermentation of various saccharides derived from cellulosic biomass to ethanol was examined in mono- and cocultures of Clostridium thermocellum strain LQRI and C. thermohydrosulfuricum strain 39E. C. thermohydrosulfuricum fermented glucose, cellobiose, and xylose, but not cellulose or xylan, and yielded ethanol/acetate ratios of >7.0. C. thermocellum fermented a variety of cellulosic substrates, glucose, and cellobiose, but not xylan or xylose, and yielded ethanol/acetate ratios of ~1.0. At nonlimiting cellulosic substrate concentrations (~1%), C. thermocellum cellulase hydrolysis products accumulated during monoculture fermentation of Solka Floc cellulose and included glucose, cellobiose, xylose, and xylobiose. A stable coculture that contained nearly equal numbers of C. thermocellum and C. thermohydrosulfuricum was established that fermented a variety of cellulosic substrates, and the ethanol yield observed was twofold higher than in C. thermocellum monoculture fermentations. The metabolic basis for the enhanced fermentation effectiveness of the coculture on Solka Floc cellulose included: the ability of C. thermocellum cellulase to hydrolyze α-cellulose and hemicellulose; the enhanced utilization of mono- and disaccharides by C. thermohydrosulfuricum; increased cellulose consumption; threefold increase in the ethanol production rate; and twofold decrease in the acetate production rate. The coculture actively fermented MN300 cellulose, Avicel, Solka Floc, SO₂-treated wood, and steam-exploded wood. The highest ethanol yield obtained was 1.8 mol of ethanol per mol of anhydroglucose unit in MN300 cellulose.     

Expression and characterization of GH3 β-Glucosidase from Aspergillus niger NL-1 with high specific activity, glucose inhibition and solvent tolerance

A β-glucosidase gene bglI from Aspergillus niger NL-1 was cloned and expressed in Pichia pastoris. The bglI gene consists of a 2583 bp open reading frame encoding 861 amino acids; the enzyme was classified into glycoside hydrolases 3. To improve the expression level of recombinant BGL in P. pastoris, fermentation conditions were optimized by the single-factor experiments. The optimal fermentation conditions were obtained: initial pH 5.0, methanol concentration 0.5% added into the culture every 24 h, and initial cell density (OD₆₀₀) of 10 for induction. The activity of BGL was increased from 4 U/mL to 45 U/mL in optimal conditions. The BGL was purified by ultrafiltration and (NH₄)₂SO₄ precipitation showing a single band on SDS-PAGE. The optimal activity was at pH 4.0 and 60°C. The recombinant enzyme was stable over a pH range of 3.0–7.0 and retained more than 85% activity after incubation at 60°C for 30 min. The kinetic experiments revealed K _m and V _max for p-nitrophenyl-β-D-glucoside of 0.64 mM and 370 U/mg, for cellobiose 8.59 mM and 1480 U/mg. The activity of BGL was not or only a little affected by many metal ions and EDTA and was enhanced by methanol or n-butyl alcohol. The BGL had a K _i of 48 mM for glucose and retained 76% activity in the presence of 50 mM glucose. The favorable properties of BGL offer the potential for industrial application.     

A novel xylose isomerase from Neurospora crassa

Summary Highest production of xylose Isomerase by Neurospora crassa grown with different carbon sources was at 0.014 U mg^-1 with D-xylose. The enzyme exhibited maximum activity at pH 8.0 and 70°C and retained 100% activity at 45°C for 30 min at pH 8.0. It was activated by 8 mM Mg²⁺ whereas 2 mM Co²⁺ afforded protection against inactivation by heat. The K _m for xylose was 10 mM and 22 mM for xylose Isomerase and xylose reductase respectively at 28°C and pH 7.0. This is the first report on the presence of xylose isomerase in N. crassa and the existence of two different pathways for the utilization of D-xylose.     

Characterization of Clostridium thermocellum JW20

Clostridium thermocellum JW20 (ATCC 31549), which was isolated from a Louisiana cotton bale, grew on cellulose, cellobiose, and xylooligomers and, after adaptation, on glucose, fructose, and xylose in the pH range of 7.5 to 6.1 with T_opt of 60°C, T_max of 69°C, and T_min of above 28°C. Doubling times during growth on cellulose and cellobiose were 6.5 and 2.5 h, respectively. The G+C content of the DNA was 40 mol% (chemical analysis). Growth on cellulose as substrate was totally inhibited in the presence of more than 125 mM sodium sulfate, 300 mM sodium chloride, 250 mM potassium chloride, 200 mM calcium chloride, 125 mM magnesium chloride, 40 mM lactate, or 250 mM acetate. The ratio of the fermentation products ethanol to acetate plus H₂ decreased when the culture was agitated. Agitation otherwise increased the rate of cellulose degradation in a growing culture but not under nongrowth conditions or with cell-free culture supernatant containing the extracellular cellulase. Shaking lowered the concentration of H₂ in the culture broth and thus minimized inhibition by the H₂ formed. Externally added H₂ caused an increased formation of ethanol during growth on cellulose or cellobiose. However, at an atmospheric pressure as high as 355 kPa (50 lb/in²), H₂ did not cause significant growth inhibition beyond an increasing lag phase (up to 24 h). Several criteria to specifically prove the purity of C. thermocellum cultures were suggested.     

Purification and characterization of trehalose phosphorylase from the commercial mushroom Agaricus bisporus

Trehalose phosphorylase (EC 2.4.1.64) from Agaricus bisporus was purified for the first time from a fungus. This enzyme appears to play a key role in trehalose metabolism in A. bisporus since no trehalase or trehalose synthase activities could be detected in this fungus. Trehalose phosphorylase catalyzes the reversible reaction of degradation (phosphorolysis) and synthesis of trehalose. The native enzyme has a molecular weight of 240 kDa and consists of four identical 61-kDa subunits. The isoelectric point of the enzyme was pH 4.8. The optimum temperature for both enzyme reactions was 30°C. The optimum pH ranges for trehalose degradation and synthesis were 6.0–7.5 and 6.0–7.0, respectively. Trehalose degradation was inhibited by ATP and trehalose analogs, whereas the synthetic activity was inhibited by P_i (K_i=2.0 mM). The enzyme was highly specific towards trehalose, P_i, glucose and α-glucose-1-phosphate. The stoichiometry of the reaction between trehalose, P_i, glucose and α-glucose-1-phosphate was 1:1:1:1 (molar ratio). The K_m values were 61, 4.7, 24 and 6.3 mM for trehalose, P_i, glucose and α-glucose-1-phosphate, respectively. Under physiological conditions, A. bisporus trehalose phosphorylase probably performs both synthesis and degradation of trehalose.     

Engineering and Two-Stage Evolution of a Lignocellulosic Hydrolysate-Tolerant Saccharomyces cerevisiae Strain for Anaerobic Fermentation of Xylose from AFEX Pretreated Corn Stover

The inability of the yeast Saccharomyces cerevisiae to ferment xylose effectively under anaerobic conditions is a major barrier to economical production of lignocellulosic biofuels. Although genetic approaches have enabled engineering of S. cerevisiae to convert xylose efficiently into ethanol in defined lab medium, few strains are able to ferment xylose from lignocellulosic hydrolysates in the absence of oxygen. This limited xylose conversion is believed to result from small molecules generated during biomass pretreatment and hydrolysis, which induce cellular stress and impair metabolism. Here, we describe the development of a xylose-fermenting S. cerevisiae strain with tolerance to a range of pretreated and hydrolyzed lignocellulose, including Ammonia Fiber Expansion (AFEX)-pretreated corn stover hydrolysate (ACSH). We genetically engineered a hydrolysate-resistant yeast strain with bacterial xylose isomerase and then applied two separate stages of aerobic and anaerobic directed evolution. The emergent S. cerevisiae strain rapidly converted xylose from lab medium and ACSH to ethanol under strict anaerobic conditions. Metabolomic, genetic and biochemical analyses suggested that a missense mutation in GRE3, which was acquired during the anaerobic evolution, contributed toward improved xylose conversion by reducing intracellular production of xylitol, an inhibitor of xylose isomerase. These results validate our combinatorial approach, which utilized phenotypic strain selection, rational engineering and directed evolution for the generation of a robust S. cerevisiae strain with the ability to ferment xylose anaerobically from ACSH.