WO1998026079A1 - Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods - Google Patents
Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods Download PDFInfo
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- WO1998026079A1 WO1998026079A1 PCT/NL1997/000688 NL9700688W WO9826079A1 WO 1998026079 A1 WO1998026079 A1 WO 1998026079A1 NL 9700688 W NL9700688 W NL 9700688W WO 9826079 A1 WO9826079 A1 WO 9826079A1
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- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
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- C12N15/00—Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
- C12N15/09—Recombinant DNA-technology
- C12N15/63—Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
- C12N15/79—Vectors or expression systems specially adapted for eukaryotic hosts
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Definitions
- the present invention relates to the field of biotechnology, in particular to the field of culturing micro-organisms, -in particular yeast.
- Culturing of micro-organisms is a relatively old technique which is well established and well understood by persons skilled in this art. It usually involves bringing a microorganism of interest into a culture medium wherein it can survive, grow and divide.
- the culture medium usually comprises all the necessary nutrients for the micro-organism to be able to do this .
- Micro-organisms are cultured for many different purposes. These include the production of biomass, the production of antibiotics, the production of useful proteins expressed by micro-organisms (be it naturally or through genetic engineering) , the production of micro-organisms useful themselves (for instance in brewing or baking bread, leavening of dough, etc.) Because of its relatively long history and its many uses the techniques for culturing microorganisms have been very well optimised, so that further gains in yield or growth rate of the micro-organism to be cultured are difficult to achieve. However, because of the cost of culturing micro-organisms and the large amounts needed, such improvements (however small percentage-wise) remain very desirable.
- One of the problems of culturing micro-organisms is that they often show preference for certain carbon sources, which carbon sources do not result in the best yields and/or growth rates of the micro-organism. Often the availability of such a preferred carbon source will lead to repression of the metabolism of other available carbon sources (which other carbon sources often do result in higher yields) .
- S. cerevisiae shows marked preferences for certain sources of carbon, nitrogen and energy.
- One such preference concerns the use of glucose above other fermentable and non-fermentable carbon compounds (see 1,2).
- This behaviour causes diauxic growth of this yeast when cultured on mixtures of carbon sources that include glucose.
- Yeast cells growing on glucose display high growth rates, presumably related to the ease with which intermediates can be derived from the catabolism of this sugar.
- Glucose has radical consequences for the enzyme complement and metabolic patterns in the yeast cell (Fig. 1) .
- enzymes required for metabolism of other carbon sources are either absent or strongly reduced in amount as a result of active degradation of mRNAs or proteins (catabolite inactivation) , repressed synthesis of mRNAs (catabolite repression) , or both.
- Such enzymes include permeases and key enzymes involved in the utilization of various sugars, enzymes of gluconeogenesis and the glyoxylate cycle.
- synthesis of components of the mitochondrial respiratory chain is repressed, resulting in a low respiratory capacity.
- Glucose-repressed cells, or cells pulsed briefly with excess glucose produce ethanol by decarboxylation of cytosolic pyruvate and subsequent action of alcohol dehydrogenase .
- the present invention provides a general mechanism by which such problems may be solved in that it provides a method for producing a micro-organism of which a metabolic pathway has been modulated, for instance a micro-organism of which the sugar/glucose metabolism has been shifted from aerobic fermentation towards oxidation, comprising providing said micro-organism with the capability of inhibition or circumvention of the repression of the oxidative metabolism of glucose induced by the availability for the micro-organism of said carbon source .
- the invention solves this problem when the preferred carbon source of the micro-organism is glucose, which is the case for many micro-organisms, in particular yeasts.
- yeasts One of the most important yeasts in industry is (of course) Saccharomyces cerevisiae. For that reason we have chosen this micro-organism as a model for explaining our invention. Because of its importance it is of course also a highly preferred embodiment of the present invention.
- Other well known -industrial yeast strains such as Hansenula, Kluyveromyces and other strains are of course also within the scope of the present invention.
- an important aspect of the present invention is to provide a method according whereby the repressed metabolism is restored to a significant extent by activation of the pathways for metabolism for the non-preferred carbon sources.
- said activation is achieved by providing the micro-organism with at least one transcriptional activator for at least one gene encoding an enzyme in said pathways .
- a very suitable and preferred way of achieving said activation is one whereby the transcriptional activator is provided by introduction into the micro-organism of a recombinant nucleic acid encoding said activator.
- Said recombinant nucleic acid is preferably an expression vector.
- Such a vector may be an autonomously replicating vector, but it is preferred to use vectors that integrate in the host genome. However, it may also be achieved by other means, such as mutation (site directed) .
- transcriptional activator is constitutively expressed by said micro-organism.
- transcriptional activator can be expressed by the micro-
- improved yeast has applications in all industrial processes in which optimal conversion of sugar into biomass is required. Use of these improved yeasts will lead to reduction of costs because of reduced process times and increased amounts of biomass per consumed glucose.
- This invention is well applicable in, for example, the (aerobic) production process of yeast for bakeries, or as source of flavour-enhancing yeast extracts. Furthermore this invention will lead to increased production of metabolites and heterologous gene products, such enzymes, precursors for chemicals, biosurfactants and fatty acids for application in pharmaceutical, agricultural or food sectors.
- the invention may also be applied with respect to manipulation of glucose repression or even glucose inactivation of processes not directly related to respiratory function of yeast.
- the uptake and metabolism of carbon sources other than glucose, such as galactose, sucrose or maltose is repressed by glucose.
- Yeast fermentation in lean dough depends on maltose as main substrate, which is produced in the dough from starch by action of amylases present in the flour.
- the flour contains in addition variable amounts of other sugars amongst which glucose.
- Maltose permease responsible for the translocation of maltose across the plasma membrane and maltase, the maltose metabolising enzyme, are both subject to glucose repression and inactivation (4) . Since this negatively affects CO2 production and thereby leavening activity, tools to reduce the glucose effect on maltose uptake and utilisation would be useful. Therefore it is noteworthy this invention will even improve leavening activity of said yeast strains.
- Saccharo yces cerevisiae a very important micro-organism is Saccharo yces cerevisiae.
- Saccharo yces cerevisiae a very important micro-organism.
- glucose Saccharomyces shows a "Crabtree" response and switches to ethanol production through aerobic fermentation.
- the present invention in one embodiment offers a solution to such problems by the construction of production strains of micro-organisms in particular yeasts, more specifically S. cerevisiae in which the Crabtree-effeet is reduced or absent.
- the principle of the approach is the controlled de-regulation of glucose-repressible genes by overexpression of a specific transcriptional activator from a promoter insensitive to glucose control. The resultant shift in balance from fermentative to oxidative metabolism leads to increased growth rates and reduced ethanol production.
- Glucose control of metabolism in S. cerevisiae The extensive changes in enzyme complement during a shift from oxidative/gluconeogenic to fermentative growth are, in the vast majority of cases, the result of induction or repression of transcription of the corresponding genes in response to glucose. Genes whose expression is repressed by this sugar can be divided into three groups :
- Snfl/Snf4 complex a protein serine/threonine kinase, which is thought to alleviate transcriptional repression and promote transcriptional activation at glucose-regulated promoters (5) .
- Snfl/Snf4 directly phosphorylates a transcriptional regulator
- genetic studies suggest that important direct or indirect targets for Snfl/Snf4 are the transcription factor Migl, Ssn6/Tupl and Hap2/3/4.
- Migl is a zinc-finger protein which acts as a transcriptional repressor at many glucose-repressible genes
- Ssn6/Tupl acts as a repressor of transcription at a large number of genes, probably in combination with gene- or family-specific transcription factors (7) .
- the Hap2/3/4 complex is, in contrast, an activator of transcription. It is required for induction of transcription by non-fermentable carbon sources of a limited number of genes encoding proteins involved mainly in mitochondrial electron transport, Krebs cycle, haem biosynthesis and gluconeogenesis (8, 9, 10, 11, 12) .
- Transcriptional regulation by the Hap2/3/4 complex is the main mechanism for coordinating the derepression of these enzymes in response to changes in carbon status of the medium (11, 13) .
- the activity of the Hap complex is controlled by the availability of the activator subunit Hap4 , whose synthesis is approximately 5-fold repressed by glucose (13) . Transcription and transcriptional control in yeast
- a typical yeast promoter consists of several cis-acting elements that function as target sites for regulatory proteins ( Figure 2) .
- the position of transcription initiation by the RNA polymerase II complex is located at the initiation site (I) .
- the TATA-box (T) has been shown to be essential in many promoters for transcription initiation to occur. It is the target site for the basal RNA polymerase II transcription factor TFIID, which nucleates the assembly of the other basal transcription factors and RNA polymerase II into a stable preinitiation complex.
- TFIID basal RNA polymerase II transcription factor
- UAS elements function as DNA- binding sites for transcriptional regulatory proteins, that are thought to interact with the basal transcriptional machinery to mediate specific regulation.
- yeast promoters consist of several TATA- and UAS-elements, which together determine the rate of transcription of the adjoining gene.
- yeast promoters may contain operators or upstream repressor sites (URS) and upstream induction sites (UIS) . By binding of specific proteins these elements contribute to the overall transcriptional regulation.
- URS upstream repressor sites
- UAS upstream induction sites
- Hap2 and Hap3 were first identified as proteins capable of binding to the UAS2 region of the gene encoding iso-1-cytochrome c in S. cerevisiae (14). This region, responsible for carbon source response, contains a sequence motif closely resembling the CCAAT box element found in many other eukaryotic promoters. The two proteins bind to DNA in an interdependent manner. Hap4 appears not to contact DNA directly, but is necessary for DNA binding of the other two proteins. Sequence analysis reveals a C-terminally located, highly acidic region whose presence is necessary for activity.
- Hap4 is the key component of the complex in terms of its ability to regulate transcriptional activity in response to carbon source.
- the HAP2 gene encodes a 265 residue protein, of which an evolutionarily-conserved 65 amino acid core in the highly basic C-terminal region is necessary and sufficient for both complex formation and binding to DNA (Fig. 4) .
- the HAP3 gene encodes a 144 residue protein, which contains a 90 amino acid core (B-domain) required for complex formation and DNA-binding (Fig. 5) .
- the HAP4 gene encodes a
- HAP2 and HAP3 have been isolated from a wide range of organisms (15) .
- the encoded proteins form a heteromeric complex called NF-Y, CBF or CP, which activates transcription by binding to the evolutionarily conserved CCAAT box element.
- Hap2- and Hap3 -homologous subunits make similar contacts with DNA.
- human CP1 complex it has been shown that the Hap2 and Hap3 homologues are exchangeable in vitro with those of yeast (16) .
- the human CP1 complex consists of more than two subunits, none of these appear to correspond to the S. cerevisiae Hap4 protein.
- Hap homologous complexes are not specifically involved in induction of genes under certain growth conditions, but function as general transcription factors required for basal level expression of a large number of genes.
- Hap complex in the yeast Saccharomyces cerevisiae
- modification of its expression has a profound effect on the cell's physiology.
- catabolic network that is, the energy conserving machinery
- synthesis of components of the respiratory chain is to a significant extent under control of the Hap2/3/4 complex. It seems justified to conclude that Hap-dependent regulation is at least involved in the physiological phenomenon known as the Crabtree effect. Its direct physiological impact is a catabolic shift from respiratory to fermentative catabolism whenever elevated levels of glucose are present.
- the yeast strains described in this invention comprise both laboratory strains and industrial production yeast strains.
- the overexpression of Hap4 was first achieved in a laboratory strain by means of introduction of a self-replicating plasmid harbouring the HAP4 gene under control of the ADH1 promoter.
- Saccharomyces cerevisiae strain DL1 has been transformed with YCplaclll : :ADH1 (without any gene placed behind the ADH promoter) or YCplaclll : :ADH1-HAP4 (expression of HAP4 under control of ADH1 promoter) . Transformation of the yeast strain with YCplaclll: :ADH1, the so-called "empty" plasmid is necessary to prevent any differences in physiology of the Hap4 overproducer and the wild type due to differences in e.g the plasmid encoded LEU2 marker gene.
- DL1 denotes strain Dll transformed with YCplaclll : :ADH1
- DL1HAP denotes DL1 transformed with YCplaclll : :ADH1-HAP4.
- Fig 9 Expression of HAP4 in Dll is strongly repressed by glucose.
- HAP4 under control of the ADH1 promoter leads to an increased expression level of HAP4 in DL1HAP which is grown on media containing 2% glucose. This level is comparable to the expression level of HAP4 in wildtype DL1 cells when grown on non-fermentable carbon- sources, which do not repress transcription of HAP4 and genes encoding respiratory components .
- V which summarizes carbon fluxes in both strains.
- the amount of CO2 produced via TCA cycle was calculated by the amount of oxygen consumed during the experiment .
- the integration plasmid is constructed in such a way that the promoter-HAP4 fusion is flanked by DNA sequences representing parts of the yeast SIT2 gene (see Fig 11 and 13) . Integration of the total plasmid including the promoter-HAP4 fusion can therefore take place at the SIT2 locus in the yeast genome .
- the presence of a gene encoding acetamidase (amdS) enables cells which have integrated the plasmid to grow on medium containing acetamide as a nitrogen source, in contrast to untransformed cells which are unable to grow on this medium. Since the plasmid does not contain any sequences which enable replication in yeast, integration of the plasmid in the genome is required to acquire the ability to grow on acetamide.
- Strains DS28911, DS18332 and DS19806 were transformed with the plasmid pKSP02-GPDHAP4 or pKSP02-TEFHAP4. Transformants with an integrated plasmid in the genome were selected on plates containing acetamide. Transformants containing pKSP02- GPDHAP4 were named DS28911GH, DS18332GH,or DS19806GH, transformants containing pKSP02-TEFHAP4 DS28911TH, DS18332TH or DS19806TH.
- (anaplo ⁇ d) transformants contain both one or more glucose repressed HAP4 genes and a HAP4 gene which is under control of a constitutively active promoter.
- mRNA was analysed of cells grown aerobically in media containing 2% glucose.
- the mRNA expression level of one selected transformant of every strain containing either the GPDHAP4 (GH) or the TEFHAP4 (TH) is shown in Figure 15.
- HAP4 Different levels of HAP4 mRNA were obtained in the different strains and with the two different promoters.
- PDA constitutively expressed gene
- As a loading control a constitutively expressed gene (PDA, encoding a subunit of pyruvate dehydrogenase, (24)) was visualized, showing that the higher expression of QCR8 is due to HAP4 overexpression.
- PDA constitutively expressed gene
- the integrated constitutively expressed HAP4 thus appears to result in alleviation of transcriptional repression of a respiratory component, analogous to the effect of the plasmid encoded HAP4 under control of the ADH1 promoter as described above.
- the modified industrial strains requires removal of any sequences that are not derived from yeast .
- the transformants contain the total plasmid pKSP02-GPDHAP4 or pKSP02-TEFHAP4 in the genome.
- the 'non-yeast' plasmid sequences can however be removed by homologous recombination of identical DNA segments in the genome, as depicted in Figure 13.
- Cells which are devoid of plasmid sequences can be selected by growth on medium containing fluoro-acetamide, which is toxic for cells still containing the gene encoding acetamidase .
- FIG 11B This led to a higher efficiency of integration at the SIT2 locus, as shown by Southern blot analysis.
- the expression levels of HAP4 , QCR8 and PDA1 were determined by northern blotting of mRNAs isolated from cells grown in medium containing 2% glucose.
- Figure 17A also in these strains the elevated expression of HAP4 resulted in alleviation of glucose repression of QCR8.
- the centromeric plasmids YCplaclll : :ADH1 and YCplaclll:: ADH1-HAP4 are capable of self-replicating in E. coli and in yeast and contains the ADH1 promoter region without (YCplaclll: :ADH1) or with the coding sequence of HAP4.
- the construction of YCplaclll : :ADH1-HAP4 is outlined in Figure 7.
- YCplaclll: :ADH1 is derived from YCplaclll (25) and contains between the BamHI and the Smal site a 723 bp EcoRV promoter fragment from pBPHl (26) .
- Vector pBPHl was derived from pACl (27) , which is a YCp50 derivative which carries the BamHI/Hindlll fragment from pMAC561 containing the yeast alcohol dehydrogenase I promoter (28) .
- HAP4 The coding region of HAP4 was cloned behind the ADH1 promoter in the former construct by isolation of HAP4 from pSLF406 (13) .
- pSLF406 was digested with BspHI , which cleaves HAP4 at position -1 relative to the start codon the coding sequence .
- the BspHI end was blunted and subsequently the HAP4 fragment obtained by cleavage of the DNA with PstI and isolation from agarose gel.
- YCPlaclll was cleaved with Smal and PstI and ligated with the HAP4 fragment to generate YCplaclll: :ADH1-HAP4.
- the plasmid pKSP02 is used for integration of a fusion of HAP4 and the GPD1 or TEF2 promoter. These fusions were first constructed in shuttle vectors containing either the GPD1 (p425GPD) or the TEF2 promoter region (p425TEF) (22) . A 2621 bp fragment from pSLF406 (13) , containing the HAP4 gene, was isolated after digestion with BspHI, blunting and digestion with PstI as described in the previous paragraph.
- This HAP4 fragment was cloned in Smal and PstI sites of the vectors 425GPD or p425TEF, resulting in the vectors p425-GPDHAP4 and p425-TEFHAP4 respectively.
- These shuttle vectors can self- replicate in E. coli and in yeast, but will only be maintained in yeast when selective pressure is present, i.e. when the recipient strain is LEU2 auxotrophic . In industrial strains without auxotrophic markers, integration of the GPDHAP or TEFHAP fusion is required to maintain the altered HAP gene stable in yeast. The promoter-HAP4 fragments were therefore recloned into the integration vector pKSP02
- Transformation of E. coli was carried out using the electroporation technique , using a Biorad E.Coli pulser according to the description of the manufacturer.
- Yeast cells were transformed according to the LiAc method described by Ito et al (29) .
- Transformants of strain DL1 with the plasmid YCplaclll : :ADH1-HAP4 were selected on plates containing 2% glucose, 2% agar, 0.67% Yeast Nitrogen Base (Difco) supplied with the required aminoacids but lacking leucine.
- the industrial strains DS28911, DS18332 and DS19806 were plated on medium consisting of 1.8% nitrogen- free agar (Oxoid) , 1.17% Yeast Carbon Base (Difco), 30 mM phosphte buffer pH 6.8 and 5mM acetamide (Sigma).
- Transformants were grown in YPD medium for 60 to 70 generations by daily dilution of the cultures for 3 to 4 days. Aliqouts of the cultures were plated on the fluoro- acetamide containing plates, which selects for cells which have recombined out the acetamidase gene . The presence of the GPDHAP4 or TEFHAP4 fusion was tested by Southern blot analysis . Growth of yeast in flask-batch cultures
- yeast cells were grown in either YPD (1% Yeast Extract, 1% BactoPeptone, 3% D-Glucose) , YPEG (Yeast Extract , 1% BactoPeptone, 2% Ethanol, 2% Glycerol), YPL (lactate medium: 1.5% lactic acid, 2% Na-lactate, 0.1% Glucose, 8mM MgS ⁇ 4 , 45 mM (NH)2HP ⁇ 4, 0.5% Yeast-extract) " or in mineral medium (0.67% Yeast Nitrogen Base) containing 3% D-glucose and supplemented with the appropiate aminoacids to obtain selective pressure for maintenaince of the transformed plasmid.
- YPD 1% Yeast Extract, 1% BactoPeptone, 3% D-Glucose
- YPEG Yeast Extract , 1% BactoPeptone, 2% Ethanol, 2% Glycerol
- YPL lactate medium
- All cultures were inoculated from precultures which were prepared by inoculation of 5 ml medium with a colony from a plate.
- the wild type and modified industrial yeast strains were precultured overnight in YPD and strain DL1 containing YCplaclll : :ADH1-HAP4 and Dll containing the empty YCplaclll vector were precultured overnight in mineral medium with additional amino acids .
- These cultures were used to inoculate 100ml YPEG and/or YPD medium and grown overnight at 28 "C to OD600 ⁇ l-5, after which cells were harvested by centrifugation.
- Transformed yeast cells were grown in selective mineral Evans medium containing 30 g I "1 D-Glucose and supplemented with 40 mg I "1 uracil and L-histidine.
- the mineral medium contained : NaH2P ⁇ 4.2H2 ⁇ , lOmM; KCl , 10 mM; MgCl2-6H2 ⁇ , 1.25 mM; NH4CI, 0.1 mM; Na2SC>4, 2 mM; C6H9NO6, 2 mM; CaCl2, 20 mM; ZnO, 25.3 mM; FeCl3.H2 ⁇ , 99.9 mM; MnCl2, 50.5 mM; CuCl2, 5 mM; C0CI2, 10 mM; H3B03, 5.2 mM; Na2Mo ⁇ 4.2H20, 0.08 mM.
- Optical cell density of cultures was measured in a spectrophotometer at 600nm.
- the dry weight of cultures was determined by centrifugation of 10.0 ml of culture, washing cells with demineralized H2O, and drying the cellpellet overnight at 80 °C. Parallel samples varied by less than 1%.
- Detection was by means of a 2142 refractive index detector (LKB) and SP4270 integrator of SpectraPhysics .
- oxygraph buffer 1% Yeast Extract, 0.1 % KH2PO4, 0.12 % (NH4)2S04, pH 4.5
- Oxygen consumption capacity of the cells was measured with a Clark electrode, with 0.1 mM ethanol as substrate.
- DNA fragments used as probes in this study include a 840 bp HindiII-SalI fragment from pJHl (30); a 1.6 kb BamHI-Kpnl fragment containing the yeast actin gene (24); ; a 2.5 kb Hindlll-Sall fragment from YE23SH containing the QCR2 gene (25) ; a 1333 bp Ncol-Hindlll fragment from pAZ6 containing the yeast PDA1 gene (24) and a 1.2 kb BamHI-Hindlll fragment from YE23R-SOD/SUC containing the SUC2 gene (26) . Fragments were labeled 3 P by nicktranslation as described by Maniatis et al .
- Chromosomal DNA isolation and Southern blotting Chromosomal DNA was isolated according to the method described by Hoffman and Winston (34) . 10 microliter of the chromosomal DNA was digested with either BamHI or EcoRI . The digested DNA was separated on a 1% agarose gel and transferred to nitrocellulose filter as described in Maniatis (31) Prehybridization of the filters was performed at 65°C in 6xSSC, 5xDenhardt, 0.5% SDS and 100 microgram/ml salmon sperm DNA. After 4 hours prehybridization, a radioactive labeled KpnI-Xbal fragment from pKSP02-GPDHAP (see Figure 11B and 13) was added and hybridization was continued overnight at 65°C.
- Blots were washed once with 2x SSC 0.1%SDS, twice with lxSSC, 0.1%SDS and finally with 0.5x SSC, 0.1%SDS. Blots were air- dried completely and radioactivity was visualised and analysed by a Storm 840 Molecular Dynamics Phosphorimager.
- ATG denotes the start codon of the corresponding translational open reading frame.
- UIS upstream induction site
- UAS upstream activation site
- URS upstream repressor site
- T TATA-box
- I initiation site.
- FIG. 3 Schematic representation of the regulatory pathways involved in glucose repression of a number of genes in yeast .
- Activating functions are denoted as (+)
- repressing/inactivating functions as (-)
- interactions which are not resolved yet are denoted as (?) .
- Figure 5 nucleotide and amino-acid sequence of the HAP3 gene
- Figure 6 nucleotide and amino-acid sequence of the HAP4 gene
- Figure 7 illustrates the construction of YCplaclll : :ADH1-HAP4 , a yeast shuttle vector where HAP4 is expressed from the ADH1 promoter. Plasmids are not drawn to scale.
- Figure 8 nucleotide and amino-acid sequence of the ADH1-HAP4 fusion
- FIG. 9 northern blot analysis of HAP4 overexpression.
- Dll containing YCplaclllADHl (WT) and DLl containing YCplaclll : :ADH1-HAP4 (+HAP4) were grown in medium containing 2% glucose (D) or 2% ethanol/2% glycerol (EG) .
- Total RNA was hybridized with probes specific for HAP4, actin (ACT) , QCR8, or SUC2 mRNA.
- fragments shown are the fragments as cloned into pKSP02 and represent the sequence as integrated in the genome Figure 13
- SITpr SIT2 promoter
- HAP4pr HAP4 promoter
- G/Tpr GPD or TEF promoter
- B BamHI
- E EcoRI
- K Kpnl
- X Xbal
- FacR fluoro-acetamide resistant.
- FIG. 14 Southern blot of chromosomal DNA digested with BamHI of transformants with pKSP02-GPDHAP (GH) or pKSP02-TEFHAP (TH) integrated at the HAP4 locus. The blot was hybridized with the KpnI-Xbal probe shown in Figure 12, visualizing fragments containing SIT2 and/or HAP4 sequences. Radioactivity was visualised and analysed by a Storm 840 Molecular Dynamics Phosphorimager.
- FIG. 16 Southern blot of chromosomal DNA digested with BamHI or EcoRI of transformants containing pKSP02 -GPDHAP (GH) or pKSP02- TEFHAP (TH) integrated at the SIT2 locus (A) and three clean transformants containing the GPDHAP4 or TEFHAP4 fusion after counterselection on fluoro-acetamide (B) .
- the blot was hybridized with the Kpnl -Xbal probe shown in Figure 12, visualizing fragments containing SIT2 and/or HAP4 sequences.
- Figure 17 Southern blot of chromosomal DNA digested with BamHI or EcoRI of transformants containing pKSP02 -GPDHAP (GH) or pKSP02- TEFHAP (TH) integrated at the SIT2 locus (A) and three clean transformants containing the GPDHAP4 or TEFHAP4 fusion after counterselection on fluoro-acetamide
- Table I Effect of induced expression of HAP4 on transcription gene protein functional expression expression HAP 4 in in binding wildtype HAP4 site on glucose overproducer on glucose
- CYC1 iso-1- repressed induced cytochrome c
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EP97950483A EP0944726A1 (en) | 1996-12-12 | 1997-12-12 | Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods |
CA002274150A CA2274150A1 (en) | 1996-12-12 | 1997-12-12 | Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods |
US09/319,989 US6190914B1 (en) | 1996-12-12 | 1997-12-12 | Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods |
JP52652598A JP2001505777A (en) | 1996-12-12 | 1997-12-12 | Method for modulating metabolic pathway of microorganism and microorganism obtained by this method |
AU53467/98A AU737640B2 (en) | 1996-12-12 | 1997-12-12 | Methods for modulating metabolic pathways of micro-organisms and micro-organisms obtainable by said methods |
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EP96203520 | 1996-12-12 | ||
EP96203520.0 | 1996-12-12 |
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EP (1) | EP0944726A1 (en) |
JP (1) | JP2001505777A (en) |
AU (1) | AU737640B2 (en) |
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Cited By (12)
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WO2000014258A1 (en) * | 1998-09-09 | 2000-03-16 | Novo Nordisk A/S | Method for the production of heterologous polypeptides in transformed yeast cells |
WO2000061722A1 (en) * | 1999-04-13 | 2000-10-19 | Universiteit Van Amsterdam | Process for the production of yeast biomass comprising functionally deleted $i(hxk2) genes |
WO2000071738A1 (en) * | 1999-05-21 | 2000-11-30 | Cargill Dow Llc | Methods and materials for the synthesis of organic products |
US6190883B1 (en) | 1998-09-09 | 2001-02-20 | Novo Nordisk A/S | Method for the production of heterologous polypeptides in transformed yeast cells |
WO2002044388A1 (en) * | 2000-11-30 | 2002-06-06 | Novo Nordisk A/S | Production of heterologous polypeptides in yeast |
US6861237B2 (en) | 2000-11-30 | 2005-03-01 | Novo Nordisk A/S | Production of heterologous polypeptides in yeast |
EP1728854A1 (en) * | 2005-06-03 | 2006-12-06 | DSM IP Assets B.V. | Process for the production of yeast biomass |
WO2009131179A1 (en) * | 2008-04-23 | 2009-10-29 | トヨタ自動車株式会社 | Yeast mutant and substance production process using the same |
WO2011041426A1 (en) | 2009-09-29 | 2011-04-07 | Butamax(Tm) Advanced Biofuels Llc | Improved yeast production host cells |
WO2011082248A1 (en) | 2009-12-29 | 2011-07-07 | Butamax(Tm) Advanced Biofuels Llc | Expression of hexose kinase in recombinant host cells |
US9850493B2 (en) | 2012-12-19 | 2017-12-26 | Verdezyne, Inc. | Biological methods for preparing a fatty dicarboxylic acid |
US9909151B2 (en) | 2012-12-19 | 2018-03-06 | Verdezyne, Inc. | Biological methods for preparing a fatty dicarboxylic acid |
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DE102007019184A1 (en) * | 2007-04-20 | 2008-10-23 | Organo Balance Gmbh | Microorganism for the production of succinic acid |
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US20160326552A1 (en) * | 2013-12-31 | 2016-11-10 | Butamax Advanced Biofuels Llc | Expression of a hap transcriptional complex subunit |
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-
1997
- 1997-12-12 US US09/319,989 patent/US6190914B1/en not_active Expired - Fee Related
- 1997-12-12 WO PCT/NL1997/000688 patent/WO1998026079A1/en not_active Application Discontinuation
- 1997-12-12 EP EP97950483A patent/EP0944726A1/en not_active Withdrawn
- 1997-12-12 CA CA002274150A patent/CA2274150A1/en not_active Abandoned
- 1997-12-12 AU AU53467/98A patent/AU737640B2/en not_active Ceased
- 1997-12-12 JP JP52652598A patent/JP2001505777A/en active Pending
Non-Patent Citations (8)
Cited By (20)
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US6190883B1 (en) | 1998-09-09 | 2001-02-20 | Novo Nordisk A/S | Method for the production of heterologous polypeptides in transformed yeast cells |
WO2000014258A1 (en) * | 1998-09-09 | 2000-03-16 | Novo Nordisk A/S | Method for the production of heterologous polypeptides in transformed yeast cells |
WO2000061722A1 (en) * | 1999-04-13 | 2000-10-19 | Universiteit Van Amsterdam | Process for the production of yeast biomass comprising functionally deleted $i(hxk2) genes |
US7700332B1 (en) | 1999-05-21 | 2010-04-20 | Cargill Inc. | Methods for the synthesis of lactic acid using crabtree-negative yeast transformed with the lactate dehydrogenase gene |
WO2000071738A1 (en) * | 1999-05-21 | 2000-11-30 | Cargill Dow Llc | Methods and materials for the synthesis of organic products |
US6485947B1 (en) | 1999-05-21 | 2002-11-26 | Cargill Dow Polymers, Llc | Production of lactate using crabtree negative organisms in varying culture conditions |
US7229805B2 (en) | 1999-05-21 | 2007-06-12 | Nature Work, Llp | Methods for the synthesis of lactic acid using crabtree-negative yeast transformed with the lactate dehydrogenase gene |
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WO2002044388A1 (en) * | 2000-11-30 | 2002-06-06 | Novo Nordisk A/S | Production of heterologous polypeptides in yeast |
US6861237B2 (en) | 2000-11-30 | 2005-03-01 | Novo Nordisk A/S | Production of heterologous polypeptides in yeast |
EP1728854A1 (en) * | 2005-06-03 | 2006-12-06 | DSM IP Assets B.V. | Process for the production of yeast biomass |
WO2009131179A1 (en) * | 2008-04-23 | 2009-10-29 | トヨタ自動車株式会社 | Yeast mutant and substance production process using the same |
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US9260708B2 (en) | 2009-09-29 | 2016-02-16 | Butamax Advanced Biofuels Llc | Yeast production host cells |
WO2011082248A1 (en) | 2009-12-29 | 2011-07-07 | Butamax(Tm) Advanced Biofuels Llc | Expression of hexose kinase in recombinant host cells |
US8637289B2 (en) | 2009-12-29 | 2014-01-28 | Butamax(Tm) Advanced Biofuels Llc | Expression of hexose kinase in recombinant host cells |
US9850493B2 (en) | 2012-12-19 | 2017-12-26 | Verdezyne, Inc. | Biological methods for preparing a fatty dicarboxylic acid |
US9909151B2 (en) | 2012-12-19 | 2018-03-06 | Verdezyne, Inc. | Biological methods for preparing a fatty dicarboxylic acid |
Also Published As
Publication number | Publication date |
---|---|
AU5346798A (en) | 1998-07-03 |
EP0944726A1 (en) | 1999-09-29 |
JP2001505777A (en) | 2001-05-08 |
US6190914B1 (en) | 2001-02-20 |
CA2274150A1 (en) | 1998-06-18 |
AU737640B2 (en) | 2001-08-23 |
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