δ-Integration of endo/exo-glucanase and β-glucosidase genes into the yeast chromosomes for direct conversion of cellulose to ethanol

Simultaneous degradation of phytic acid and starch by an industrial strain of Saccharomyces cerevisiae producing phytase and alpha-amylase

Phytase liberates inorganic phosphate from phytic acid (myo-inositol hexakisphosphate) which is the major phosphate reserve in plant-derived foods and feeds. An industrial strain of Saccharomyces cerevisiae expressing the Debaryomyces castellii phytase gene (phytDc) and D. occidentalis alpha-amylase gene (AMY) was developed. The phytDc and AMY genes were constitutively expressed under the ADC1 promoter in S. cerevisiae by using the delta-integration system, which contains DNA derived exclusively from yeast. The recombinant industrial strain secreted both phytase and alpha-amylase for the efficient degradation of phytic acid and starch as main components of plant seeds. This new strain hydrolyzed 90% of 0.5% (w/v) sodium phytate within 5 days of growth and utilized 100% of 2% (w/v) starch within 48 h simultaneously.

Lactic fermentation of cellobiose by a yeast strain displaying beta-glucosidase on the cell surface

The Aspergillus aculeatus beta-glucosidase 1 (bgl1) gene was expressed in a lactic-acid-producing Saccharomyces cerevisiae strain to enable lactic fermentation with cellobiose. The recombinant beta-glucosidase enzyme was expressed on the yeast cell surface by fusing the mature protein to the C-terminal half region of the alpha-agglutinin. The beta-glucosidase expression plasmids were integrated into the genome. Three strong promoters of S. cerevisiae, the TDH3, PGK1, and PDC1 promoters, were used for beta-glucosidase expression. The specific beta-glucosidase activity varied with the promoter used and the copy number of the bgl1 gene. The highest activity was obtained with strain PB2 that possessed two copies of the bgl1 gene driven by the PDC1 promoter. PB2 could grow on cellobiose and glucose minimal medium at the same rate. Fermentation experiments were conducted in non-selective-rich media containing 95 g l(-1) cellobiose or 100 g l(-1) glucose as a carbon source under microaerobic conditions. The maximum rate of L-lactate production by PB2 on cellobiose (2.8 g l(-1) h(-1)) was similar to that on glucose (3.0 g l(-1) h(-1)). This indicates that efficient fermentation of cellobiose to L-lactate can be accomplished using a yeast strain expressing beta-glucosidase from a mitotically stable genomic integration plasmid.

Efficient one-step starch utilization by industrial strains of Saccharomyces cerevisiae expressing the glucoamylase and α-amylase genes from Debaryomyces occidentalis

Amylolytic industrial polyploid strains of Saccharomyces cerevisiae (ATCC 4126, ATCC 9763 and ATCC 24858) expressing a glucoamylase gene (GAM1) or an alpha-amylase gene (AMY) from Debaryomyces occidentalis were developed. The glucoamylase activity of S. cerevisiae ATCC 9763 expressing the GAM1 gene was 3.7-times higher than that of D. occidentalis. On the other hand, alpha-amylase activity in the corresponding strain expressing the D. occidentalis AMY gene increased 10-times relative to D. occidentalis. These two recombinant yeast strains expressing the GAM1 gene and AMY gene, respectively were cultured simultaneously to produce both glucoamylase and alpha-amylase for efficient one-step utilization of starch. Growth, substrate utilization and enzyme activity of these strains are described.

Development of stable flocculent Saccharomyces cerevisiae strain for continuous Aspergillus niger β-galactosidase production

A flocculent Saccharomyces cerevisiae strain was engineered to stably secrete Aspergillus niger beta-galactosidase in a continuous high-cell-density bioreactor. The delta-sequences from the yeast retrotransposon Ty1 were used as target sites for the integration of the beta-galactosidase expression cassette. High-copy-number transformants were successfully obtained using the delta-integration system together with the dominant selection antibiotic, G418. The integration of multiple copies was confirmed by genomic Southern blot analysis. Integrants with the highest beta-galactosidase levels (approximately eight gene copies) had similar beta-galactosidase activities as a recombinant strain carrying the beta-galactosidase expression cassette in a YEp-based vector. The beta-galactosidase expression cassettes integrated into the yeast genome were stably maintained after eight sequential batch cultures in a nonselective medium. In continuous high-cell-density culture under the same operating conditions, the integrant strain was more stable than the plasmid-carrying strain. To our knowledge, this is the first study of multicopy delta-integrant stability in a continuous bioreactor operating at different dilution rates.

Consolidated bioprocessing for bioethanol production using Saccharomyces cerevisiae

Consolidated bioprocessing (CBP) of lignocellulose to bioethanol refers to the combining of the four biological events required for this conversion process (production of saccharolytic enzymes, hydrolysis of the polysaccharides present in pretreated biomass, fermentation of hexose sugars, and fermentation of pentose sugars) in one reactor. CBP is gaining increasing recognition as a potential breakthrough for low-cost biomass processing. Although no natural microorganism exhibits all the features desired for CBP, a number of microorganisms, both bacteria and fungi, possess some of the desirable properties. This review focuses on progress made toward the development of baker's yeast (Saccharomyces cerevisiae) for CBP. The current status of saccharolytic enzyme (cellulases and hemicellulases) expression in S. cerevisiae to complement its natural fermentative ability is highlighted. Attention is also devoted to the challenges ahead to integrate all required enzymatic activities in an industrial S. cerevisiae strain(s) and the need for molecular and selection strategies pursuant to developing a yeast capable of CBP.

Purification and characterization of an intracellular beta-glucosidase from the methylotrophic yeast Pichia pastoris

Pichia pastoris beta-glucosidase was purified to apparent homogeneity by salting out with ammonium sulfate, gel filtration, and ion-exchange chromatography with Q-Sepharose and CM-Sepharose. The enzyme is a tetramer (275 kD) made up of four identical subunits (70 kD). The pH optimum is 7.3, and it is fairly stable in the pH range 5.5-9.5. The temperature optimum is 40 degrees C. The purified beta-glucosidase is effectively active on p-/o-nitrophenyl-beta-D-glucopyranosides (p-/o-NPG) and 4-methylumbelliferyl-beta-D-glucopyranoside (4-MUG) with Km values of 0.12, 0.22, and 0.096 mM and Vmax values of 10.0, 11.7, and 6.2 micromol/min per mg protein, respectively. It also exhibits different levels of activity against p-nitrophenyl-1-thio-beta-D-glucopyranoside, cellobiose, gentiobiose, amygdalin, prunasin, salicin, and linamarin. The enzyme is competitively inhibited by gluconolactone, p-/o-nitrophenyl-beta-D-fucopyranosides (p-/o-NPF), and glucose against p-NPG as substrate. o-NPF is the most effective inhibitor of the enzyme activity with Ki value of 0.41 mM. The enzyme is more tolerant to glucose inhibition with Ki value of 7.2 mM for p-NPG. Pichia pastoris has been employed as a host for the functional expression of heterologous beta-glucosidases and the risk of high background beta-glucosidase activity is discussed.

Stoichiometric network constraints on xylose metabolism by recombinant Saccharomyces cerevisiae

Metabolic pathway engineering is constrained by the thermodynamic and stoichiometric feasibility of enzymatic activities of introduced genes. Engineering of xylose metabolism in Saccharomyces cerevisiae has focused on introducing genes for the initial xylose assimilation steps from Pichia stipitis, a xylose-fermenting yeast, into S. cerevisiae, a yeast traditionally used in ethanol production from hexose. However, recombinant S. cerevisiae created in several laboratories have used xylose oxidatively rather than in the fermentative manner that this yeast metabolizes glucose. To understand the differences between glucose and engineered xylose metabolic networks, we performed a flux balance analysis (FBA) and calculated extreme pathways using a stoichiometric model that describes the biochemistry of yeast cell growth. FBA predicted that the ethanol yield from xylose exhibits a maximum under oxygen-limited conditions, and a fermentation experiment confirmed this finding. Fermentation results were largely consistent with in silico phenotypes based on calculated extreme pathways, which displayed several phases of metabolic phenotype with respect to oxygen availability from anaerobic to aerobic conditions. However, in contrast to the model prediction, xylitol production continued even after the optimum aeration level for ethanol production was attained. These results suggest that oxygen (or some other electron accepting system) is required to resolve the redox imbalance caused by cofactor difference between xylose reductase and xylitol dehydrogenase, and that other factors limit glycolytic flux when xylose is the sole carbon source.

Effects of xylulokinase activity on ethanol production from D-xylulose by recombinant Saccharomyces cerevisiae

AIMS

Recombinant Saccharomyces cerevisiae strains harbouring different levels of xylulokinase (XK) activity and effects of XK activity on utilization of xylulose were studied in batch and fed-batch cultures.

METHODS AND RESULTS

The cloned xylulokinase gene (XKS1) from S. cerevisiae was expressed under the control of the glyceraldehyde 3-phosphate dehydrogenase promoter and terminator. Specific xylulose consumption rate was enhanced by the increased specific XK activity, resulting from the introduction of the XKS1 into S. cerevisiae. In batch and fed-batch cultivations, the recombinant strains resulted in twofold higher ethanol concentration and 5.3- to six-fold improvement in the ethanol production rate compared with the host strain S. cerevisiae.

CONCLUSIONS

An effective conversion of xylulose to xylulose 5-phosphate catalysed by XK in S. cerevisiae was considered to be essential for the development of an efficient and accelerated ethanol fermentation process from xylulose.

SIGNIFICANCE AND IMPACT OF THE STUDY

Overexpression of the XKS1 gene made xylulose fermentation process accelerated to produce ethanol through the pentose phosphate pathway.

Purification and characterization of two beta-glucosidases from a thermo-tolerant yeast Pichia etchellsii

The thermo-tolerant yeast Pichia etchellsii produced two cell-wall-bound inducible beta-glucosidases, BGLI (molecular mass 186 kDa) and BGLII (molecular mass 340 kDa), which were purified by a simple, three-step method, comprising ammonium sulfate precipitation, ion-exchange and hydroxyapatite chromatography. The two enzymes exhibited a similar pH and temperature optima, inhibitory effect by glucose and gluconolactone, and stability in the pH range of 3.0-9.0. Placed in family 3 of glycosylhydrolase families, BGLI was more active on salicin, p-nitrophenyl beta-D-glucopyranoside and alkyl beta-D-glucosides whereas BGLII was most active on cellobiose. k(cat) and K(M) values were determined for a number of substrates and, for BGLI, it was established that the deglycosylation step was equally effective on aryl- and alkyl-glucosides while the glycosylation step varied depending on the substrate used. This information was used to synthesize alkyl-glucosides (up to a chain length of C(10)) using dimethyl sulfoxide stabilized single-phase reaction microenvironment. About 12% molar yield of octyl-glucoside was calculated based on a simple spectrophotometric method developed for its estimation. Further, detailed comparison of properties of the enzymes indicated these to be different from the previously cloned beta-glucosidases from this yeast.

Optimal growth and ethanol production from xylose by recombinant Saccharomyces cerevisiae require moderate D-xylulokinase activity

D-Xylulokinase (XK) is essential for the metabolism of D-xylose in yeasts. However, overexpression of genes for XK, such as the Pichia stipitis XYL3 gene and the Saccharomyces cerevisiae XKS gene, can inhibit growth of S. cerevisiae on xylose. We varied the copy number and promoter strength of XYL3 or XKS1 to see how XK activity can affect xylose metabolism in S. cerevisiae. The S. cerevisiae genetic background included single integrated copies of P. stipitis XYL1 and XYL2 driven by the S. cerevisiae TDH1 promoter. Multicopy and single-copy constructs with either XYL3 or XKS1, likewise under control of the TDH1 promoter, or with the native P. stipitis promoter were introduced into the recombinant S. cerevisiae. In vitro enzymatic activity of XK increased with copy number and promoter strength. Overexpression of XYL3 and XKS1 inhibited growth on xylose but did not affect growth on glucose even though XK activities were three times higher in glucose-grown cells. Growth inhibition increased and ethanol yields from xylose decreased with increasing XK activity. Uncontrolled XK expression in recombinant S. cerevisiae is inhibitory in a manner analogous to the substrate-accelerated cell death observed with an S. cerevisiae tps1 mutant during glucose metabolism. To bypass this effect, we transformed cells with a tunable expression vector containing XYL3 under the control of its native promoter into the FPL-YS1020 strain and screened the transformants for growth on, and ethanol production from, xylose. The selected transformant had approximately four copies of XYL3 per haploid genome and had moderate XK activity. It converted xylose into ethanol efficiently.

Direct and efficient production of ethanol from cellulosic material with a yeast strain displaying cellulolytic enzymes

For direct and efficient ethanol production from cellulosic materials, we constructed a novel cellulose-degrading yeast strain by genetically codisplaying two cellulolytic enzymes on the cell surface of Saccharomyces cerevisiae. By using a cell surface engineering system based on alpha-agglutinin, endoglucanase II (EGII) from the filamentous fungus Trichoderma reesei QM9414 was displayed on the cell surface as a fusion protein containing an RGSHis6 (Arg-Gly-Ser-His(6)) peptide tag in the N-terminal region. EGII activity was detected in the cell pellet fraction but not in the culture supernatant. Localization of the RGSHis6-EGII-alpha-agglutinin fusion protein on the cell surface was confirmed by immunofluorescence microscopy. The yeast strain displaying EGII showed significantly elevated hydrolytic activity toward barley beta-glucan, a linear polysaccharide composed of an average of 1,200 glucose residues. In a further step, EGII and beta-glucosidase 1 from Aspergillus aculeatus No. F-50 were codisplayed on the cell surface. The resulting yeast cells could grow in synthetic medium containing beta-glucan as the sole carbon source and could directly ferment 45 g of beta-glucan per liter to produce 16.5 g of ethanol per liter within about 50 h. The yield in terms of grams of ethanol produced per gram of carbohydrate utilized was 0.48 g/g, which corresponds to 93.3% of the theoretical yield. This result indicates that efficient simultaneous saccharification and fermentation of cellulose to ethanol are carried out by a recombinant yeast cells displaying cellulolytic enzymes.

Microbial cellulose utilization: fundamentals and biotechnology

Fundamental features of microbial cellulose utilization are examined at successively higher levels of aggregation encompassing the structure and composition of cellulosic biomass, taxonomic diversity, cellulase enzyme systems, molecular biology of cellulase enzymes, physiology of cellulolytic microorganisms, ecological aspects of cellulase-degrading communities, and rate-limiting factors in nature. The methodological basis for studying microbial cellulose utilization is considered relative to quantification of cells and enzymes in the presence of solid substrates as well as apparatus and analysis for cellulose-grown continuous cultures. Quantitative description of cellulose hydrolysis is addressed with respect to adsorption of cellulase enzymes, rates of enzymatic hydrolysis, bioenergetics of microbial cellulose utilization, kinetics of microbial cellulose utilization, and contrasting features compared to soluble substrate kinetics. A biological perspective on processing cellulosic biomass is presented, including features of pretreated substrates and alternative process configurations. Organism development is considered for "consolidated bioprocessing" (CBP), in which the production of cellulolytic enzymes, hydrolysis of biomass, and fermentation of resulting sugars to desired products occur in one step. Two organism development strategies for CBP are examined: (i) improve product yield and tolerance in microorganisms able to utilize cellulose, or (ii) express a heterologous system for cellulose hydrolysis and utilization in microorganisms that exhibit high product yield and tolerance. A concluding discussion identifies unresolved issues pertaining to microbial cellulose utilization, suggests approaches by which such issues might be resolved, and contrasts a microbially oriented cellulose hydrolysis paradigm to the more conventional enzymatically oriented paradigm in both fundamental and applied contexts.

Enhanced production of anticoagulant hirudin in recombinant Saccharomyces cerevisiae by chromosomal delta-integration

Recombinant Saccharomyces cerevisiae strains were developed to overproduce an anticoagulant hirudin. The delta-sequences of the yeast retrotransposon Ty1 and URA3 were used as target sites for a hirudin expression cassette. High copy-number transformants were successfully selected using a dominant selection antibiotic, G418. The copy numbers of the hirudin expression cassette integrated into delta-sequences of the yeast chromosome ranged from five to ten copies per cell. Production of hirudin in the delta-integrated recombinant S. cerevisiae system increased over two-fold compared with the YEp-based episomal hirudin expression system. A linear relationship between the copy number of the hirudin expression cassette and hirudin expression level was observed up to 10 copies. The hirudin expression cassettes integrated into the yeast chromosome were stably maintained in non-selective culture conditions.

Gene integration and expression and extracellular secretion of Erwinia chrysanthemi endoglucanase CelY (celY) and CelZ (celZ) in ethanologenic Klebsiella oxytoca P2

The development of methods to reduce costs associated with the solubilization of cellulose is essential for the utilization of lignocellulose as a renewable feedstock for fuels and chemicals. One promising approach is the genetic engineering of ethanol-producing microorganisms that also produce cellulase enzymes during fermentation. By starting with an ethanologenic derivative (strain P2) of Klebsiella oxytoca M5A1 with the native ability to metabolize cellobiose, the need for supplemental beta-glucosidase was previously eliminated. In the current study, this approach has been extended by adding genes encoding endoglucanase activities. Genes celY and celZ from Erwinia chrysanthemi have been functionally integrated into the chromosome of P2 using surrogate promoters from Zymomonas mobilis for expression. Both were secreted into the extracellular milieu, producing more than 20,000 endoglucanase units (carboxymethyl cellulase activity) per liter of fermentation broth. During the fermentation of crystalline cellulose with low levels of commercial cellulases of fungal origin, these new strains produced up to 22% more ethanol than unmodified P2. Most of the beneficial contribution was attributed to CelY rather than to CelZ. These results suggest that fungal enzymes with substrate profiles resembling CelY (preference for long-chain polymers and lack of activity on soluble cello-oligosaccharides of two to five glucosyl residues) may be limiting in commercial cellulase preparations.