Efficient secretion of human parathyroid hormone by Saccharomyces cerevisiae

A cDNA encoding mature human parathyroid hormone (hPTH) was expressed in Saccharomyces cerevisiae, after fusion to the prepro region of yeast mating factor alpha (MF alpha). Radioimmunoassay showed high levels of hPTH immunoreactive material in the growth medium (up to 10 micrograms/ml). More than 95% of the immunoreactive material was found extracellularly as multiple forms of hormone peptides. Three internal cleavage sites were identified in the hPTH molecule. The major cleavage site, after a pair of basic amino acids (aa) (Arg25Lys26 decreases Lys27), resembles that recognized by the KEX2 gene product on which the MF alpha expression-secretion system depends. The use of a protease-deficient yeast strain and the addition of high concentrations of aa to the growth medium, however, not only changed the peptide pattern, but also resulted in a significant increase in the yield of intact hPTH (1-84) (more than 20% of the total amount of immunoreactive material). The secreted hPTH (1-84) migrates like a hPTH standard in two different gel-electrophoretic systems, co-elutes with standard hPTH on reverse-phase high-performance liquid chromatography, reacts with two hPTH antibodies raised against different parts of the peptide, has a correct N-terminal aa sequence, and has full biological activity in a hormone-sensitive osteoblast adenylate cyclase assay.     

Use of high culture pH for the decreased proteolysis of human parathyroid hormone secreted by Saccharomyces cerevisiae

Human parathyroid hormone (hPTH) was expressed and secreted in Saccharomyces cerevisiae. In batch fermentations performed at pH = 5.6, 6.5, 7.2 and 7.5, optimal production of hPTH (12.1 mg/l) was obtained at pH 7.2 after 24 h of culture. At pH 5.6, most of secreted hPTH was degraded. Proteolysis of hPTH was significantly decreased by increasing the culture pH.     

Expression of human pancreatic secretory trypsin inhibitor in Saccharomyces cerevisiae

Human pancreatic secretory trypsin inhibitor (PSTI) cDNA was expressed in Saccharomyces cerevisiae using the yeast acid phosphatase PHO5 promoter. The product encoded by the PSTI-coding cDNA was correctly processed in yeast cells, and the PSTI molecules were efficiently secreted into the medium. The amino acid composition and the N-terminal amino acid sequence of the secreted PSTI molecules were identical to those of the authentic PSTI polypeptides from human pancreas, and the product exhibited trypsin-inhibitory activity.     

Two different modes of cyclin clb2 proteolysis during mitosis in Saccharomyces cerevisiae

Sister chromatid separation and mitotic exit are triggered by the anaphase-promoting complex (APC/C) which is a multi-subunit ubiquitin ligase required for proteolytic degradation of various target proteins. Cdc20 and Cdh1 are substrate-specific activators of the APC/C. It was previously proposed that Cdh1 is essential for proteolysis of the yeast mitotic cyclin Clb2. We show that Clb2 proteolysis is triggered by two different modes during mitosis. A fraction of Clb2 is degraded during anaphase in the absence of Cdh1. However, a second fraction of Clb2 remains stable during anaphase and is degraded in a Cdh1-dependent manner as cells exit from mitosis. Most of cyclin Clb3 is degraded independently of Cdh1. Our data imply that degradation of mitotic cyclins is initiated by a Cdh1-independent mechanism.     

Process development for high-level secretory production of carboxypeptidase Y by Saccharomyces cerevisiae

In order to develop a production process for carboxypeptidase Y (CPY, yeast vacuolar protease) secreted by Saccharomyces cerevisiae KS58-2D, medium composition, culture conditions, and expression systems were investigated. We found that the addition of histidine to thiamine-free medium, in which CPY production was almost negligible, raised the intracellular thiamine level, resulting in the increase of CPY production. On the basis of the choice of an expression system that uses an inducible GAL10 promoter, reassessment of histidine concentration in the medium, and optimization of the pH level during cultivation (pH 6.5), active CPY was secreted in a quantity of over 400 mg/l, which was more than tenfold that higher than that previously reported. The process developed could be easily scaled-up to industrial-scale fermentation. Received: 16 January 1998 / Received revision: 16 February 1998 / Accepted: 27 February 1998     

Degradation signals for ubiquitin system proteolysis in Saccharomyces cerevisiae.

Combinations of different ubiquitin-conjugating (Ubc) enzymes and other factors constitute subsidiary pathways of the ubiquitin system, each of which ubiquitinates a specific subset of proteins. There is evidence that certain sequence elements or structural motifs of target proteins are degradation signals which mark them for ubiquitination by a particular branch of the ubiquitin system and for subsequent degradation. Our aim was to devise a way of searching systematically for degradation signals and to determine to which ubiquitin system subpathways they direct the proteins. We have constructed two reporter gene libraries based on the lacZ or URA3 genes which, in Saccharomyces cerevisiae, express fusion proteins with a wide variety of C-terminal extensions. From these, we have isolated clones producing unstable fusion proteins which are stabilized in various ubc mutants. Among these are 10 clones whose products are stabilized in ubc6, ubc7 or ubc6ubc7 double mutants. The C-terminal extensions of these clones, which vary in length from 16 to 50 amino acid residues, are presumed to contain degradation signals channeling proteins for degradation via the UBC6 and/or UBC7 subpathways of the ubiquitin system. Some of these C-terminal tails share similar sequence motifs, and a feature common to almost all of these sequences is a highly hydrophobic region such as is usually located inside globular proteins or inserted into membranes.     

A process for the production of human proinsulin in Saccharomyces cerevisiae

In order to develop a large-scale fermentation process for the production of human proinsulin in yeast, the intra-cellular expression of a human superoxide dismutase-human proinsulin fusion product (SOD-PI) has been studied. The expression of SOD-PI in Saccharomyces cerevisiae is regulated by a hybrid alcohol dehydrogenase 2/glyceraldehyde-3-phosphate dehydrogenase promoter. The promoter is repressed by glucose and derepressed by depletion of glucose. Although the genetic stability of the construction is shown to be poor under product-inducing conditions, it is demonstrated in shake flask experiments that a stable expression potential can be maintained in a complex medium for more than 60 generations by maintaining excess glucose throughout the cultivations. These results have been confirmed in continuous cultures in chemostat and turbidostat experiments. Addition of the glucose analogs glucosamine, 2-desoxyglucose, methylglucose, and thioglucose also leads to repression of SOD-PI formation. The analogs, however, are not suitable for improving genetic stability during propagation because of growth inhibition. In batch fermentation experiments in a complex medium at 30 degrees C, it has been demonstrated that initial glucose concentrations up to 50 g/L result in high specific SOD-PI yields giving an overall yield of up to 700 mg SOD-PI/L whereas higher glucose concentrations lead to both lower specific and overall yields due to depletion of critical medium components in the production period. In fed-batch experiments at 30 degrees C it has been possible to obtain high specific SOD-PI yields even at high biomass concentrations by feeding glucose at a constant rate of 1.5 g/L/h for 40 h followed by a feeding of ethanol at 1.0 g/L/h for 24 h, thus giving an overall yield of 1200 mg/L. Decreasing the temperature from 30 to 26 degrees C leads to improved yields in batch as well as fed-batch experiments. The optimized fed-batch fermentation process which is suitable to be scaled up to the cubic meter level has been tested in 200-L fermentations resulting in yields of more than 1500 mg/L of the fusion protein which conveniently can be used as a precursor in the production of recombinant human proinsulin.     

Protein oxidation, repair mechanisms and proteolysis in Saccharomyces cerevisiae

Reactive oxygen species, generated as normal by-products of aerobic metabolism or due to cellular stress, oxidize molecules and cause cell death by apoptosis. The accumulation of oxidized proteins is a hallmark of aging and a number of aging diseases. Oxidation can impair protein function as the proteins are unfolded leading to an increase of protein hydrophobicity and often resulting in the formation of toxic aggregates. The yeast Saccharomyces cerevisiae has been used as a eukaryotic model system to analyze the molecular mechanisms of oxidative stress protection. This paper reviews how the identification in yeast of specific damaged proteins has provided new insights into mechanisms of cytotoxicity and highlights the role of repair and degradative processes, including vacuolar/lysosomal and proteasomal proteolysis, in housekeeping after protein oxidative damage.     

Fatty acid-acylated proteins in secretory mutants of Saccharomyces cerevisiae.

Yeast secretory (sec) mutants that are blocked in the transport of secretory proteins and accumulate membrane organelles were used to study the biosynthesis of fatty acid-acylated proteins. Four proteins were labeled with [3H]palmitate in sec mutants accumulating endoplasmic reticulum membranes. Three of these (molecular weights approximately equal to 20,000, 50,000, and 120,000) were N-linked glycoproteins, based on their ability to be labeled with [3H]mannose and their sensitivity to endoglycosidase H. The fourth protein (molecular weight approximately equal to 30,000) also was labeled with [3H]mannose but was insensitive to endoglycosidase H; it appeared to contain O-linked sugars. In sec mutants accumulating Golgi membranes or post-Golgi vesicles, a 35-kilodalton protein was labeled with [3H]palmitate. Analysis of Staphylococcus aureus protease V8 digests and pulse-chase experiments indicated that the 30-kilodalton protein was a precursor of 35 kilodaltons. None of these proteins was labeled with [3H]palmitate in a sec mutant that blocked the penetration of nascent polypeptides into endoplasmic reticulum; thus, acylation occurred in endoplasmic reticulum. All four proteins could be recovered from fractions enriched for yeast membranes. Fatty acids were not released from proteins by boiling in sodium dodecyl sulfate or extraction with organic solvents but were recovered as methyl esters after proteins were treated with KOH-methanol, a reaction characteristic of an acyl ester linkage.     

Comparison of three different promoter systems for secretory alpha-amylase production in fed-batch cultures of recombinant Saccharomyces cerevisiae

Cloned gene expression in recombinant Saccharomyces cerevisiae 20B-12 containing three different plasmids was compared in batch and fed-batch cultures. The plasmids pNA3, pNA7, and pNA9 contain the alpha-amylase gene under the control of SUC2, PGK, and GAL7 Promoters, respectively. The synthesis of alpha-amylase was therefore induced by low glucose concentration for the SUC2 and PGK promoters, and by galactose for GAL7 promoter. The specific cell growth rates were similar among cells harboring the three different plasmids; they decreased from 0.35 to 0.38 h(-1) during the cell growth phase to 0.03 to 0.06h(-1) during the production phase. The secretory alpha-amylase activity of cells harboring plasmid pNA7 was 129 U/mL in fed-batch culture, which was 1.4 and 2 times as high as the activities of cells harboring plasmids pNA3 and pNA9, respectively. The secretion ratios (amount of extracellular alpha-amylase activity/amounts of total alpha-amylase activity) of cells harboring plasmids pNA3, pNA7, and pNA9 were 91.4%, 94.5%, and 95.3%, respectively. (c) 1993 Wiley & Sons, Inc.     

Acetoin production in Saccharomyces cerevisiae wine yeasts

Abstract One hundred strains of Saccharomyces cerevisiae were examined for the capacity to produce acetoin in synthetic medium and in grape must. The low production of acetoin was found to be the more common pattern in this species. Most strains exhibited a similar distribution in both media, production ranging from non-detectable amounts to 12 mg 1⁻¹. Only four strains produced high quantities of acetoin, up to 29.5 mg l⁻¹ in synthetic medium and up to 194.6 mg l⁻¹ in grape must. This biometric study showed the existence of two phenotypes, "low and high acetoin production", that could be selected for conferring a desirable flavour of the final product.     

Acetaldehyde production in Saccharomyces cerevisiae wine yeasts

Abstract Eighty-six strains of Saccharomyces cerevisiae were investigated for their ability to produce acetaldehyde in synthetic medium and in grape must. Acetaldehyde production did not differ significantly between the two media, ranging from a few mg/l to about 60 mg/l, and was found to be a strain characteristic. The fermentation temperature of 30°C considerably increased the acetaldehyde produced. This study allowed us to assign the strains to different phenotypes: low, medium and high acetaldehyde producers. The low and high phenotypes differed considerably also in the production of acetic acid, acetoin and higher alcohols and can be useful for studying acetaldehyde production in S. cerevisiae , both from the technological and genetic point of view.     

Regulation of Saccharomyces cerevisiae nicotinamide adenine dinucleotide phosphate-dependent glutamate dehydrogenase by proteolysis during carbon starvation.

Inactivation of the nicotinamide adenine dinucleotide phosphate-dependent glutamate dehydrogenase from Saccharomyces cerevisiae during carbon starvation occurs with a simultaneous loss of enzyme protein and enzyme activity.     

Manganese ion concentration affects production of human core 3 O-glycan in Saccharomyces cerevisiae

BackgroundProduction of various mucin-like glycoproteins could be useful for development of antibodies specific to disease-related glycoproteins as well as for the biosynthesis of clinically useful glycoproteins. A Saccharomyces cerevisiae strain capable of in vivo production of mucin-type core 1 structure (Galβ1-3GalNAcα1-O-Ser/Thr) has been reported, but a strain producing core 3 structure (GlcNAcβ1-3GalNAcα1-O-Ser/Thr) has not been constructed.MethodsTo generate core 3-producing strain, genes encoding uridine diphosphate (UDP)-Gal-4-epimerase, UDP-GalNAc transporter, UDP-GlcNAc transporter, and two glycosyltransferases were integrated into the genome. A Mucin-1-derived acceptor peptide (MUC1ap) was expressed as an acceptor. The amount of the resulting modified peptide was analyzed by HPLC.ResultsIntroduction of a codon-optimized UDP-GlcNAc:βGal β-1,3-N-acetylglucosaminyltransferase 6 (β3Gn-T6) gene yielded increases in β3Gn-T6 activity but did not alter the level of core 3 production. The highest in vitro activity of β3Gn-T6 was observed at Mn^2 + concentrations of 10 mM and above. Supplementation of MnCl₂ to the culture medium yielded increases of up to 25% in the accumulation of core 3 on the MUC1ap. The yeast invertase from the core 3-producing strain was less extensively N-glycosylated; however, it was partially restored by the addition of MnCl₂ to the medium.ConclusionsPhysiological Mn^2 + concentration in S. cerevisiae was insufficient to facilitate optimal synthesis of core 3. Mn^2 + supplementation led to up-regulation of reaction of glycosylation in the Golgi, resulting in increases of core 3 production.General significanceThis study reveals that control of Mn^2 + concentration is important for production of specific mammalian-type glycans in S. cerevisiae.