产甘油假丝酵母与酿酒酵母胞浆3-磷酸甘油脱氢酶基因的功能比较

胞浆3-磷酸甘油脱氢酶(GPD)是酿酒酵母细胞甘油合成过程中的关键限速酶．尽管高产甘油菌株产甘油假丝酵母基因组中编码该酶的基因CgGPD已经被克隆出来,但是具体的功能,特别是与酿酒酵母GPD1和GPD2基因的功能比较值得进一步研究．以酿酒酵母渗透压敏感型的gpd1/gpd2和gpd1突变株为宿主,分别导入CgGPD、GPD1和GPD2基因,比较分析了CgGPD、GPD1和GPD2基因在高渗透压胁迫条件下和厌氧环境中的表达调控,及其对细胞甘油合成能力的影响．研究发现,GPD1基因受到渗透压诱导表达,GPD2基因在细胞厌氧条件下起着氧化还原平衡调节作用,而CgGPD基因不仅能够在渗透压胁迫条件下通过过量快速合成甘油调节渗透压平衡,而且能够在厌氧培养环境中互补GPD2基因的缺失,使gpd1/gpd2缺失突变株能够正常生长,同时提高了突变株的甘油合成能力．结果表明,CgGPD基因在gpd1/gpd2缺失突变株中既具有GPD1基因的功能,又能发挥GPD2基因的功能．     

Efficient, galactose-free production of Candida antarctica lipase B by GAL10 promoter in Δgal80 mutant of Saccharomyces cerevisiae

An efficient yeast gene expression system with GAL10 promoter that does not require galactose as an inducer was developed using Δgal80 mutant strain of Saccharomyces cerevisiae. We constructed several combinations of gal mutations (Δgal1, Δgal80, Δmig1, Δmig2, and Δgal6) of S. cerevisiae and tested for their effect on efficiency of recombinant protein production by GAL10 promoter using a lipase, Candida antarctica lipase B (CalB), as a reporter. While the use of Δgal1 mutant strain required the addition of a certain amount of galactose to the medium, Δgal80 mutant strain did not require galactose. Furthermore, it was found that the recombinant CalB could be produced more efficiently (1.6-fold at 5 L-scale fermentation) in Δgal80 mutant strain than in the Δgal1 mutant. The Δgal80 mutant strain showed glucose repressible mode of expression of GAL10 promoter. Using Δgal80 mutant strain of S. cerevisiae, CalB was efficiently produced in a glucose-only fermentation at volumes up to 500 L.     

Over-expressing <Emphasis Type="Italic">GLT1</Emphasis> in a <Emphasis Type="Italic">gpd2</Emphasis>Δ mutant of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> to improve ethanol production

We constructed two recombinant strains of Saccharomyces cerevisiae in which the GPD2 gene was deleted using a one-step gene replacement method to minimize formation of glycerol and improve ethanol production. In addition, we also over-expressed the GLT1 gene by a two-step gene replacement method to overcome the redox-imbalancing problem in the genetically modified strains. The result of anaerobic batch fermentations showed that the rate of growth and glucose consumption of the KAM-5 (MATα ura3 gpd2Δ::RPT) strain were slower than the original strain, and the KAM-13 (MATα ura3 gpd2Δ::RPT P _PGK -GLT1) strain, however, was indistinguishable compared to the original strain using the same criteria, as analyzed. On the other hand, when compared to the original strain, there were 32 and 38% reduction in glycerol formation for KAM-5 and KAM-13, respectively. Ethanol production increased by 8.6% for KAM-5 and 13.4% for KAM-13. Dramatic reduction in acetate and pyruvic acid was also observed in both mutants compared to the original strains. Although gene GPD2 is responsible for the glycerol synthesis, the mutant KAM-13, in which glycerol formation was substantially reduced, was able to cope and maintain osmoregulation and redox balance and have increased ethanol production under anaerobic fermentations. The result verified the proposed concept of increasing ethanol production in S. cerevisiae by genetic engineering of glycerol synthesis and over-expressing the GLT1 gene along with reconstituted nicotinamide adenine dinucleotide metabolism.     

Improved ethanol production by glycerol-3-phosphate dehydrogenase mutants of Saccharomyces cerevisiae

The anaerobic performance of gpd1Δ and gpd2Δ mutants of Saccharomyces cerevisiae was characterized and compared to that of a wild-type strain under well-controlled conditions by using a high-performance bioreactor. There was a 40% reduction in glycerol level in the gpd2Δ mutant compared to the wild-type. Also the gpd1Δ mutant showed a slight decrease in glycerol formation but to a much lesser degree. As a consequence, ethanol formation in the gpd2Δ mutant was elevated by 13%. In terms of growth, the gpd1Δ mutant and the wild-type were indistinguishable. The gpd2Δ mutant, on the other hand, displayed an extended lag phase as well as a reduced growth rate under the exponential phase. Even though glycerol-3-phosphate dehydrogenase 2 (GPD2) is the important enzyme under anaerobic conditions it can, at least in part, be substituted by GPD1. This was indicated by the higher expression level of GPD1 in the gpd2Δ mutant compared to the wild type. These results also show that the cells are able to cope and maintain redox balance under anaerobic conditions even if glycerol formation is substantially reduced, as observed in the gpd2Δ mutant. One obvious way of solving the redox problem would be to make a biomass containing less protein, since most of the excess NADH originates from amino acid biosynthesis. However, the gpd2Δ mutant did not show any decrease in the protein content of the biomass. Received: 16 February 1998 / Received revision: 16 March 1998 / Accepted: 1 June 1998     

Elimination of Glycerol Production in Anaerobic Cultures of a Saccharomyces cerevisiae Strain Engineered To Use Acetic Acid as an Electron Acceptor

In anaerobic cultures of wild-type Saccharomyces cerevisiae, glycerol production is essential to reoxidize NADH produced in biosynthetic processes. Consequently, glycerol is a major by-product during anaerobic production of ethanol by S. cerevisiae, the single largest fermentation process in industrial biotechnology. The present study investigates the possibility of completely eliminating glycerol production by engineering S. cerevisiae such that it can reoxidize NADH by the reduction of acetic acid to ethanol via NADH-dependent reactions. Acetic acid is available at significant amounts in lignocellulosic hydrolysates of agricultural residues. Consistent with earlier studies, deletion of the two genes encoding NAD-dependent glycerol-3-phosphate dehydrogenase (GPD1 and GPD2) led to elimination of glycerol production and an inability to grow anaerobically. However, when the E. coli mhpF gene, encoding the acetylating NAD-dependent acetaldehyde dehydrogenase (EC 1.2.1.10; acetaldehyde + NAD⁺ + coenzyme A ↔ acetyl coenzyme A + NADH + H⁺), was expressed in the gpd1Δ gpd2Δ strain, anaerobic growth was restored by supplementation with 2.0 g liter⁻¹ acetic acid. The stoichiometry of acetate consumption and growth was consistent with the complete replacement of glycerol formation by acetate reduction to ethanol as the mechanism for NADH reoxidation. This study provides a proof of principle for the potential of this metabolic engineering strategy to improve ethanol yields, eliminate glycerol production, and partially convert acetate, which is a well-known inhibitor of yeast performance in lignocellulosic hydrolysates, to ethanol. Further research should address the kinetic aspects of acetate reduction and the effect of the elimination of glycerol production on cellular robustness (e.g., osmotolerance).Bioethanol production by Saccharomyces cerevisiae is currently, by volume, the single largest fermentation process in industrial biotechnology. A global research effort is under way to expand the substrate range of S. cerevisiae to include lignocellulosic hydrolysates of nonfood feedstocks (e.g., energy crops and agricultural residues) and to increase productivity, robustness, and product yield (for reviews see references 20 and 35). A major challenge relating to the stoichiometry of yeast-based ethanol production is that substantial amounts of glycerol are invariably formed as a by-product (24). It has been estimated that, in typical industrial ethanol processes, up to 4% of the sugar feedstock is converted into glycerol (24). Although glycerol also serves as a compatible solute at high extracellular osmolarity (10), glycerol production under anaerobic conditions is primarily linked to redox metabolism (34).During anaerobic growth of S. cerevisiae, sugar dissimilation occurs via alcoholic fermentation. In this process, the NADH formed in the glycolytic glyceraldehyde-3-phosphate dehydrogenase reaction is reoxidized by converting acetaldehyde, formed by decarboxylation of pyruvate to ethanol via NAD⁺-dependent alcohol dehydrogenase. The fixed stoichiometry of this redox-neutral dissimilatory pathway causes problems when a net reduction of NAD⁺ to NADH occurs elsewhere in the metabolism. Such a net production of NADH occurs in assimilation when yeast biomass is synthesized from glucose and ammonia (34). Under anaerobic conditions, NADH reoxidation in S. cerevisiae is strictly dependent on reduction of sugar to glycerol (34). Glycerol formation is initiated by reduction of the glycolytic intermediate dihydroxyacetone phosphate to glycerol-3-phosphate, a reaction catalyzed by NAD⁺-dependent glycerol-3-phosphate dehydrogenase. Subsequently, the glycerol-3-phosphate formed in this reaction is hydrolyzed by glycerol-3-phosphatase to yield glycerol and inorganic phosphate.The importance of glycerol production for fermentative growth of yeasts was already observed in the 1960s during studies of non-Saccharomyces yeasts that exhibit a so-called “Custers effect.” In such yeast species, which are naturally unable to produce glycerol, fermentative growth on glucose is possible only in the presence of an external electron acceptor that can be reduced via an NADH-dependent reaction (e.g., the reduction of acetoin to butanediol via NAD⁺-dependent butanediol dehydrogenase) (29). It was later shown that gpd1Δ gpd2Δ strains of S. cerevisiae, which are also unable to produce glycerol, are similarly unable to grow under anaerobic conditions unless provided with acetoin as an external electron acceptor (8).In view of its large economic significance, several metabolic engineering strategies have been explored to reduce or eliminate glycerol production in anaerobic cultures of S. cerevisiae. Nissen et al. (25) changed the cofactor specificity of glutamate dehydrogenase, the major ammonia-fixing enzyme of S. cerevisiae, thereby increasing NADH consumption in biosynthesis. This approach significantly reduced glycerol production in anaerobic cultures grown with ammonia as the nitrogen source. Attempts to further reduce glycerol production by expression of a heterologous transhydrogenase, with the aim to convert NADH and NADP⁺ into NAD⁺ and NADPH, were unsuccessful (24) because intracellular concentrations of these pyridine nucleotide cofactor couples favor the reverse reaction (23).The goal of the present study was to investigate whether the engineering of a linear pathway for the NADH-dependent reduction of acetic acid to ethanol can replace glycerol formation as a redox sink in anaerobic, glucose-grown cultures of S. cerevisiae and thus provide a stoichiometric basis for elimination of glycerol production during industrial ethanol production. Significant amounts of acetic acid are released upon hydrolysis of lignocellulosic biomass, and, in fact, acetic acid is studied as an inhibitor of yeast metabolism in lignocellulosic hydrolysates (5, 7, 26). The S. cerevisiae genome already contains genes encoding acetyl coenzyme A (acetyl-CoA) synthetase (32) and NAD⁺-dependent alcohol dehydrogenases (ADH1-5 [12]). To complete the linear pathway for acetic acid reduction, we expressed an NAD⁺-dependent, acetylating acetaldehyde dehydrogenase (EC 1.2.1.10) from Escherichia coli into a gpd1Δ gpd2Δ strain of S. cerevisiae. This enzyme, encoded by the E. coli mhpF gene (15), catalyzes the reaction acetaldehyde + NAD⁺ + coenzyme A ↔ acetyl coenzyme A + NADH + H⁺. Growth and product formation of the engineered strain were then compared in the presence and absence of acetic acid and compared to those of a congenic reference strain.     

Effect of alternative NAD<Superscript>+</Superscript>-regenerating pathways on the formation of primary and secondary aroma compounds in a <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> glycerol-defective mutant

Saccharomyces cerevisiae maintains a redox balance under fermentative growth conditions by re-oxidizing NADH formed during glycolysis through ethanol formation. Excess NADH stimulates the synthesis of mainly glycerol, but also of other compounds. Here, we investigated the production of primary and secondary metabolites in S. cerevisiae strains where the glycerol production pathway was inactivated through deletion of the two glycerol-3-phosphate dehydrogenases genes (GPD1/GPD2) and replaced with alternative NAD⁺-generating pathways. While these modifications decreased fermentative ability compared to the wild-type strain, all improved growth and/or fermentative ability of the gpd1Δgpd2Δ strain in self-generated anaerobic high sugar medium. The partial NAD⁺ regeneration ability of the mutants resulted in significant amounts of alternative products, but at lower yields than glycerol. Compared to the wild-type strain, pyruvate production increased in most genetically manipulated strains, whereas acetate and succinate production decreased in all strains. Malate production was similar in all strains. Isobutanol production increased substantially in all genetically manipulated strains compared to the wild-type strain, whereas only mutant strains expressing the sorbitol producing SOR1 and srlD genes showed increases in isoamyl alcohol and 2-phenyl alcohol. A marked reduction in ethyl acetate concentration was observed in the genetically manipulated strains, while isobutyric acid increased. The synthesis of some primary and secondary metabolites appears more readily influenced by the NAD⁺/NADH availability. The data provide an initial assessment of the impact of redox balance on the production of primary and secondary metabolites which play an essential role in the flavour and aroma character of beverages.     

Elimination of glycerol and replacement with alternative products in ethanol fermentation by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>

Glycerol is a major by-product of ethanol fermentation by Saccharomyces cerevisiae and typically 2–3% of the sugar fermented is converted to glycerol. Replacing the NAD⁺-regenerating glycerol pathway in S. cerevisiae with alternative NADH reoxidation pathways may be useful to produce metabolites of biotechnological relevance. Under fermentative conditions yeast reoxidizes excess NADH through glycerol production which involves NADH-dependent glycerol-3-phosphate dehydrogenases (Gpd1p and Gpd2p). Deletion of these two genes limits fermentative activity under anaerobic conditions due to accumulation of NADH. We investigated the possibility of converting this excess NADH to NAD⁺ by transforming a double mutant (gpd1∆gpd2∆) with alternative oxidoreductase genes that might restore the redox balance and produce either sorbitol or propane-1,2-diol. All of the modifications improved fermentative ability and/or growth of the double mutant strain in a self-generated anaerobic high sugar medium. However, these strain properties were not restored to the level of the parental wild-type strain. The results indicate an apparent partial NAD⁺ regeneration ability and formation of significant amounts of the commodity chemicals like sorbitol or propane-1,2-diol. The ethanol yields were maintained between 46 and 48% of the sugar mixture. Other factors apart from the maintenance of the redox balance appeared to influence the growth and production of the alternative products by the genetically manipulated strains.     

Glycerol Production by Fermenting Yeast Cells Is Essential for Optimal Bread Dough Fermentation

Glycerol is the main compatible solute in yeast Saccharomyces cerevisiae. When faced with osmotic stress, for example during semi-solid state bread dough fermentation, yeast cells produce and accumulate glycerol in order to prevent dehydration by balancing the intracellular osmolarity with that of the environment. However, increased glycerol production also results in decreased CO₂ production, which may reduce dough leavening. We investigated the effect of yeast glycerol production level on bread dough fermentation capacity of a commercial bakery strain and a laboratory strain. We find that Δgpd1 mutants that show decreased glycerol production show impaired dough fermentation. In contrast, overexpression of GPD1 in the laboratory strain results in increased fermentation rates in high-sugar dough and improved gas retention in the fermenting bread dough. Together, our results reveal the crucial role of glycerol production level by fermenting yeast cells in dough fermentation efficiency as well as gas retention in dough, thereby opening up new routes for the selection of improved commercial bakery yeasts.     

Efficient production of 2,3-butanediol in Saccharomyces cerevisiae by eliminating ethanol and glycerol production and redox rebalancing

2,3-Butanediol is a promising valuable chemical that can be used in various areas as a liquid fuel and a platform chemical. Here, 2,3-butanediol production in Saccharomyces cerevisiae was improved stepwise by eliminating byproduct formation and redox rebalancing. By introducing heterologous 2,3-butanediol biosynthetic pathway and deleting competing pathways producing ethanol and glycerol, metabolic flux was successfully redirected to 2,3-butanediol. In addition, the resulting redox cofactor imbalance was restored by overexpressing water-forming NADH oxidase (NoxE) from Lactococcus lactis. In a flask fed-batch fermentation with optimized conditions, the engineered adh1Δadh2Δadh3Δadh4Δadh5Δgpd1Δgpd2Δ strain overexpressing Bacillus subtilis α-acetolactate synthase (AlsS) and α-acetolactate decarboxylase (AlsD), S. cerevisiae 2,3-butanediol dehydrogenase (Bdh1), and L. lactis NoxE from a single multigene-expression vector produced 72.9 g/L 2,3-butanediol with the highest yield (0.41 g/g glucose) and productivity (1.43 g/(L·h)) ever reported in S. cerevisiae.     

Using regulatory information to manipulate glycerol metabolism in Saccharomyces cerevisiae

Metabolic engineering has emerged as an attractive alternative to random mutagenesis and screening to design cell factories for industrial fermentation processes. The design of metabolic networks has been realized by gene deletions or strong overexpression of heterologous genes. There is an increasing body of evidence that indicates complete inactivation of native genes and high-level activity of heterologous enzymes may be deleterious to the cell. To moderately implement their expression, genes of interest are expressed under the control of promoters with different strengths. Constructing a promoter library is labor-intensive and requires precise quantification of the promoter strength. However, when the mechanisms of pathway regulation are known, it is possible to exploit this information to effect genetic changes efficiently. We report the implementation of this concept to reducing glycerol production during aerobic growth of Saccharomyces cerevisiae. Glycerol is produced to dispose excess cytosolic reduced nicotinamide adenine dinucleotide (NADH), and the regulating step in the pathway is mediated by glycerol 3-phosphate dehydrogenase (encoded by GPD1 and GPD2 genes). We expressed NADH oxidase in S. cerevisiae under the control of the GPD2 promoter to modulate the decrease in cytosolic NADH to the right level where the heterologous enzyme does not compete with oxidative phosphorylation while at the same time, decreasing glycerol production. This metabolic design resulted in substantially decreasing glycerol production and indeed, the excess carbon was redirected to biomass, resulting in a 14% increase in the specific growth rate. We believe that such strategies are more efficient than conventional methods and will find applications in bioprocesses.     

A metabolic engineering strategy for producing free fatty acids by the Yarrowia lipolytica yeast based on impairment of glycerol metabolism

In recent years, bio‐based production of free fatty acids from renewable resources has attracted attention for their potential as precursors for the production of biofuels and biochemicals. In this study, the oleaginous yeast Yarrowia lipolytica was engineered to produce free fatty acids by eliminating glycerol metabolism. Free fatty acid production was monitored under lipogenic conditions with glycerol as a limiting factor. Firstly, the strain W29 (Δgpd1), which is deficient in glycerol synthesis, was obtained. However, W29 (Δgpd1) showed decreased biomass accumulation and glucose consumption in lipogenic medium containing a limiting supply of glycerol. Analysis of substrate utilization from a mixture of glucose and glycerol by the parental strain W29 revealed that glycerol was metabolized first and glucose utilization was suppressed. Thus, the Δgpd1Δgut2 double mutant, which is deficient also in glycerol catabolism, was constructed. In this genetic background, growth was repressed by glycerol. Oleate toxicity was observed in the Δgpd1Δgut2Δpex10 triple mutant strain which is deficient additionally in peroxisome biogenesis. Consequently, two consecutive rounds of selection of spontaneous mutants were performed. A mutant released from growth repression by glycerol was able to produce 136.8 mg L^?1 of free fatty acids in a test tube, whereas the wild type accumulated only 30.2 mg L^?1. Next, an isolated oleate‐resistant strain produced 382.8 mg L^?1 of free fatty acids. Finely, acyl‐CoA carboxylase gene (ACC1) over‐expression resulted to production of 1436.7 mg L^?1 of free fatty acids. The addition of dodecane promoted free fatty acid secretion and enhanced the level of free fatty acids up to 2033.8 mg L^?1 during test tube cultivation.

     

Increasing ethanol titer and yield in a gpd1Δ gpd2Δ strain by simultaneous overexpression of GLT1 and STL1 in Saccharomyces cerevisiae

We have investigated whether simultaneous modification of cofactor metabolism and glycerol in a strain of Saccharomyces cerevisiae can eliminate glycerol synthesis during ethanol production. Two strains, S812 (gpd1Δ gpd2Δ PGK1p-GLT1) and LE17 (gpd1Δ gpd2Δ PGK1p-GLT1 PGKp-STL1) were generated that showed a 8 and 8.2 % increase in the ethanol yield, respectively, compared to the wild type KAM-2 strain. The ethanol titer was improved from 90.4 g/l for KAM-2 to 97.6 g/l for S812 and 97.8 g/l for LE17, respectively. These results provide a new insight into rationalization of metabolic engineering strategies for improvement of ethanol yield through elimination of glycerol production.     

A role for yeast glutaredoxin genes in selenite-mediated oxidative stress

Since the double Δgrx1Δgrx2 mutant is hypersensitive to selenite we decided to evaluate mechanisms underlying this phenomenon and establish the roles of other components of yeast glutaredoxin system, in particular glutaredoxin 5 in the selenite resistance. We found elevation in the intracellular and mitochondrial superoxide production in the Δgrx1Δgrx2 and Δgrx5 mutants after Se(IV) treatment. The last effect was more pronounced for cells lacking the mitochondrial Grx5 protein. We also recorded selenite-induced increase in the peroxide production in all strains tested. Nonfermentable carbon sources, glycerol and ethanol, augmented selenite toxicity. Hypo- and anoxia protected against the harmful effects of Se(VI). Augmentation of the intracellular levels of two endogenous antioxidants, erythroascorbic acid and glutathione confers resistance to selenite. We recorded a strain-unspecific, selenite-mediated decrease in the level of acid-soluble thiols. Collectively, our data demonstrate that hypersensitivity to the Δgrx1Δgrx2 and Δgrx5 disruptants to selenite is mediated by altered intracellular redox equilibrium.     

Heterologous expression of Zygosaccharomyces rouxii glycerol 3-phosphate dehydrogenase gene (ZrGPD1) and glycerol dehydrogenase gene (ZrGCY1) in Saccharomyces cerevisiae

We examined the effects of heterologous expression of the open reading frames (ORF) of two genes on salt tolerance and glycerol production in a Saccharomyces cerevisiae strain deficient in glycerol synthesis (gpd1Deltagpd2Delta). When the ORF of the Zygosaccharomyces rouxii glycerol 3-phosphate dehydrogenase gene (ZrGPD1) was expressed under the control of the GAL10 promoter, salt tolerance and glycerol production increased; when the ORF of the glycerol dehydrogenase gene (ZrGCY1) was expressed under the control of the GAL1 promoter, no such changes were observed. Zrgcy1p had a weak effect on glycerol production. These results suggest that Zrgpd1p is the primary enzyme involved in Z. rouxii glycerol production, following a mechanism similar to that of S. cerevisiae (Gpd1p). When the ORFs of the S. cerevisiae glycerol 3-phosphatase gene (GPP2) and ZrGPD1 were simultaneously expressed, glycerol production increased, compared with that in yeast expressing only ZrGPD1.     

Expression of hepatitis B surface antigen in <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> utilizing glyceraldeyhyde-3-phosphate dehydrogenase promoter of <Emphasis Type="Italic">Pichia pastoris</Emphasis>

An expression vector constructed from genes of Pichia pastoris was applied for heterologous gene expression in Saccharomyces cerevisiae. Recombinant hepatitis B surface antigen was synthesized by cloning hepatitis B virus ‘S’ gene under the control of glyceraldehyde-3-phosphate dehydrogenase (GAP) promoter of Pichia pastoris in Saccharomyces cerevisiae. Hepatitis B surface antigen was constitutively expressed, was stable and exhibited ∼20–22 nm particle formation. Stability and absence of toxicity to the host with the expression vector indicates the expression system can be applied for large-scale production.     

Effect of Salts on Growth and Pectinase Production by Halotolerant Yeast, <Emphasis Type="Italic">Debaryomyces nepalensis</Emphasis> NCYC 3413

In this study, Debaryomyces nepalensis NCYC 3413 isolated from rotten apple was studied for its halotolerance and its growth was compared with that of Saccharomyces cerevisiae in high salt medium. The specific growth rate of D. nepalensis was not affected by KCl even up to a concentration of 1 M, whereas NaCl and LiCl affected the growth of D. nepalensis. Among all tested salts, LiCl showed maximum inhibition on growth. At all conditions, halotolerance of D. nepalensis was much higher than that of S. cerevisiae. D. nepalensis showed maximum viability (80–100%) when grown in KCl, which was higher than with NaCl and LiCl. Pectinase production by D. nepalensis was noted at all high salt concentrations, namely, 2 M NaCl, 2 M KCl, and 0.5 M LiCl, and the maximum specific activity was observed when the strain was grown in 2 M NaCl.     

Stable continuous constitutive expression of a heterologous protein in Saccharomyces cerevisiae without selection pressure

The stability of heterologous protein expression in Saccharomyces cerevisiae during continuous culture without selection for plasmid-containing cells was investigated. The protein chosen was the leech thrombin inhibitor desulphato-hirudin, which is tolerated well by S. cerevisiae when over-expressed. Expression was from a 2- derived multicopy vector containing a synthetic hirudin gene under control of the constitutive glyceraldehyde-3-phosphate dehydrogenase derived GAPFL promoter. The behaviour of the system was studied at three dilution rates (D) corresponding to approximately 30% (0.06 h^–1), 60% (0.12 h^–1) and 90% (0.17 h^–1) of the estimated maximum D. The level of plasmid loss was low at all Ds, with only 5–10% plasmid-free cells observed at 75 generations. The plasmid was most stably maintained at the intermediate D of 0.12 h^–1, where the rate of loss was comparable to the loss of the native 2- plasmid. Hirudin expression was also highest at D=0.12 h^–1, possibly as a result of cell lysis at D=0.06 h^–1 and D=0.17 h^–1, leading to the release of vacuolar proteases and subsequent proteolysis of hirudin. Differences in expression levels were not a result of changes in plasmid copy number, which was in the range 40–60 throughout all three experiments. The high stability of this system at all Ds investigated shows that heterologous protein expression is not a burden to S. cerevisiae when the protein expressed is tolerated well. Correspondence to: M. Ibba