Processing and secretion of barley (1-3,1-4)-beta-glucanase in yeast

Enhancing the performance of brewing yeasts

Beer production is one of the oldest known traditional biotechnological processes, but is nowadays facing increasing demands not only for enhanced product quality, but also for improved production economics. Targeted genetic modification of a yeast strain is one way to increase beer quality and to improve the economics of beer production. In this review we will present current knowledge on traditional approaches for improving brewing strains and for rational metabolic engineering. These research efforts will, in the near future, lead to the development of a wider range of industrial strains that should increase the diversity of commercial beers.

Construction of recombinant industrial Saccharomyces cerevisiae strain with bglS gene insertion into PEP4 locus by homologous recombination

The bglS gene encoding endo-l,3-1,4-beta-glucanase from Bacillus subtilis was cloned and sequenced in this study. The bglS expression cassette, including PGK1 promoter, bglS gene fused to the signal sequence of the yeast mating pheromone alpha-factor (MFalpha1(S)), and ADH1 terminator with G418-resistance as the selected marker, was constructed. Then one of the PEP4 allele of Saccharomyces cerevisiae WZ65 strain was replaced by bglS expression cassette using chromosomal integration of polymerase chain reaction (PCR)-mediated homologous recombination, and the bglS gene was expressed simultaneously. The recombinant strain S. cerevisiae (SC-betaG) was preliminarily screened by the clearing hydrolysis zone formed after the barley beta-glucan was hydrolyzed in the plate and no proteinase A (PrA) activity was measured in fermenting liquor. The results of PCR analysis of genome DNA showed that one of the PEP4 allele had been replaced and bglS gene had been inserted into the locus of PEP4 gene in recombinant strains. Different endo-l,3-1,4-beta-glucanase assay methods showed that the recombinant strain SC-betaG had high endo-l,3-1,4-beta-glucanase expression level with the maximum of 69.3 U/(h.ml) after 60 h of incubation. Meanwhile, the Congo Red method was suitable for the determination of endo-l,3-1,4-beta-glucanase activity during the actual brewing process. The current research implies that the constructed yeast strain could be utilized to improve the industrial brewing property of beer.

Improvement of Saccharomyces yeast strains used in brewing, wine making and baking

Yeast was the first microorganism domesticated by mankind. Indeed, the production of bread and alcoholic beverages such as beer and wine dates from antiquity, even though the fact that the origin of alcoholic fermentation is a microorganism was not known until the nineteenth century. The use of starter cultures in yeast industries became a common practice after methods for the isolation of pure yeast strains were developed. Moreover, effort has been undertaken to improve these strains, first by classical genetic methods and later by genetic engineering. In general, yeast strain development has aimed at improving the velocity and efficiency of the respective production process and the quality of the final products. This review highlights the achievements in genetic engineering of Saccharomyces yeast strains applied in food and beverage industry.

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.

Metabolic engineering of Saccharomyces cerevisiae

Comprehensive knowledge regarding Saccharomyces cerevisiae has accumulated over time, and today S. cerevisiae serves as a widley used biotechnological production organism as well as a eukaryotic model system. The high transformation efficiency, in addition to the availability of the complete yeast genome sequence, has facilitated genetic manipulation of this microorganism, and new approaches are constantly being taken to metabolicially engineer this organism in order to suit specific needs. In this paper, strategies and concepts for metabolic engineering are discussed and several examples based upon selected studies involving S. cerevisiae are reviewed. The many different studies of metabolic engineering using this organism illustrate all the categories of this multidisciplinary field: extension of substrate range, improvements of producitivity and yield, elimination of byproduct formation, improvement of process performance, improvements of cellular properties, and extension of product range including heterologous protein production.

Glycan modification of a thermostable recombinant (1-3, 1-4)-beta-glucanase secreted from Saccharomyces cerevisiae is determined by strain and culture conditions

High level biosynthesis and secretion of the thermostable hybrid (1-3, 1-4)- beta-glucanase H(A16-M) has been achieved in Saccharomyces cerevisiae by means of the yeast vacuolar endoprotease B promoter (PRB1P) and the Bacillus macerans (1-3, 1-4)-beta-glucanase signal peptide. The N-glycans present on the yeast-secreted H(A16-M), denoted H(A16-M)-Y, were released by endoglycosidase H, and identified by proton NMR spectroscopy to be a homologous series of Man8-13GlcNAc2, although only traces of Man9GlcNAc2 were found. Therefore, processing of N-glycans on H(A16-M)-Y is similar to that on homologous proteins. Most of the N-glycans (88%) were neutral while the remainder were charged due to phosphorylation. Site-directed mutagenesis of Asn to Gln in two of the N-glycosylation sequons, and subsequent analysis of the N-glycans on the yeast-secreted proteins together with analysis of the N-glycans from the individual sites of H(A16-M)-Y suggest the presence of steric hindrance to glycan modification by the glycans themselves. H(A16-M)-Y produced under control of either the yeast protease B or the yeast 3'-phosphoglycerate kinase promoter, each in two different Saccharomyces strains revealed a dependence of N-glycan profile on both strain and culture conditions. The extent of O-glycosylation was found to be nine mannose units per H(A16-M)-Y molecule. An attempt to identify the linkage-sites for the O-glycans by amino acid sequencing failed, suggesting non-stoichiometric or heterogeneous O-glycosylation. The possible modes in which N-glycans might contribute to resistance of H(A16-M)-Y to irreversible thermal denaturation are discussed with respect to structural information available for H(A16-M)-Y.

Expression and secretion of pea-seed lipoxygenase isoenzymes in Saccharomyces cerevisiae

Lipoxygenases (EC 1.13.11.12) catalyse the oxygenation of polyunsaturated fatty acids such as linoleic and arachidonic acid into reactive cis/trans hydroperoxidiene intermediates, which then serve as substrates for other enzymes leading to the production of a variety of secondary metabolites. In order to explore the characteristics of the individual lipoxygenase isoenzymes in more detail larger amounts of the pure enzymes are needed and their production in a heterologous host is therefore desirable. Full-length cDNAs encoding pea-seed lipoxygenase isoenzymes 2 and 3 were expressed in Saccharomyces cerevisiae with the aid of yeast-Escherichia coli shuttle vectors. Expression of the cDNA for lipoxygenase 2 under the control of the constitutive phosphoglycerate kinase (PGK) gene promoter yielded significant amounts of active enzyme inside the cell, both with yeast transformants carrying the cDNA gene on high-copy-number plasmids or integrated in chromosome V. Addition of the yeast invertase signal sequence in front of the pea lipoxygenase 3 yielded secreted active pea-seed lipoxygenase in the medium, but large amounts of inactive lipoxygenase 3 remained inside the yeast cell. Expression of the LOX3 cDNA can be achieved either constitutively with the PGK promoter or inducibly with the GAL1 promoter.

Expression of cDNAs encoding barley alpha-amylase 1 and 2 in yeast and characterization of the secreted proteins

Amylolytic strains of the yeast, Saccharomyces cerevisiae, were constructed by transformation with expression plasmids containing cDNAs encoding either AMY1 (clone E) or AMY2 (clone pM/C). The alpha-amylases were efficiently secreted into the culture medium directed by their own signal peptides. When clone E without its 5'-noncoding region was expressed from the yeast PGK promoter, AMY1 was produced as 1% of total cell protein and was thus the major protein secreted, whereas a similar construct derived from pM/C produced much less AMY2. This level is the highest reported for a plant protein secreted by yeast as mediated by the endogenous signal peptide. Production of AMY1 increased 25-fold when the 5'-noncoding part of clone E which contains a 12-bp dG.dC homopolymer tail had been removed. Moreover, expression was one to two orders of magnitude higher when genes encoding AMY1 or AMY2 were inserted between promoter and terminator of the yeast PGK gene in comparison to expression directed from the ADC1 or GAL1 promoters. Recombinant AMY1 and AMY2 had the same Mr and N-terminal sequence as the corresponding barley malt enzymes. Furthermore, none of the enzymes were found to be N-glycosylated. Isoelectric focusing indicated that transformed yeast cells secreted one major form of AMY2 and four dominant forms of AMY1. One AMY1 form corresponded to one of the major forms found in malt while the others, having either low activity or unusually high pI, probably reflect inefficient/incorrect processing. Enzyme kinetic properties and pH activity-dependence of recombinant AMY2 were essentially identical to those of malt AMY2.(ABSTRACT TRUNCATED AT 250 WORDS)