YEAST STRAINS

Abstract: Reduction (preferably elimination) of the HSP150 protein in a yeast used to produce desired foreign proteins, especially human albumin, facilitates subsequent purification of the protein.

Description: YEAST STRAINS Field of the Invention The present invention relates to the production of heterologous proteins by yeast species and more particularly to an adaptation of the yeast in which the protein is produced. Background and Prior Art In recent years, yeasts have been widely used as host organisms for the production of heterologous proteins (reviewed by Romanos et al, 1992), including recombinant human albumin (rHA) (Sleep et al, 1990, 1991; Fleer et al, 1991). Yeasts are readily amenable to genetic manipulation, can be grown to high cell density on simple media, and as eukaryotes are suitable for the production of secreted as well as cytosolic proteins. When yeasts are utilised to produce a desired heterologous protein by secretion into the growth medium, a large number of host-derived proteins may also be present, including other proteins secreted by the host but also intracellular proteins present in the supernatant as the result of leakage from cells or cell lysis. In processes in which the protein is not secreted, there is of course an even higher level of contamination with intracellular yeast proteins. It is necessary to purify the desired protein and to remove these contaminating proteins from the preparation; such methods have been disclosed in WO 92/04367 and EP 524 681. The majority of contaminating proteins will have physicochemical properties sufficiently different from the desired protein to permit efficient separation by standard techniques, such as ion exchange or size exclusion chromatography. The prior art gives the impression that such proteins can be satisfactorily removed by such techniques; see, for example EP 524 681 (Gist-brocades), EP 570 916 (Green Cross) and EP 464 590 (Green Cross). Indeed, we have developed sophisticated chromatographic techniques (unpublished) to remove contaminating proteins from desired proteins. Summary of the Invention We have now also adopted a different approach and have identified the gene responsible for a protein, namely the HSP150 gene, which co-purifies with recombinant human albumin (rHA) and, in principle, with other desired proteins. In accordance with the invention, we eliminate the contaminating protein from the initial fermentation, rather than develop highly sophisticated and complex means of removal during purification. This protein was not previously known to be a co-purifying contaminant. In one aspect of the invention, the HSP150 gene is functionally deleted from the genome of the host. This has not caused any detrimental effects on production of the desired protein and removes a potential contaminant that has proven difficult to remove by standard purification techniques. Despite the presence of at least two closely related genes encoding proteins very similar to Hspl50, PIRl and PIR3, in such modified yeast, rHA purified from these organisms does not contain detectable levels of any protein from this family. The S. cerevisiae Hspl50 protein was originally described by Russo et al (1992) and was shown to be produced constitutively, to be extensively O- glycosylated and to be secreted efficiently into the growth medium. A 7-fold increase in the level of Hspl50 protein was seen when cells grown at 28 °C were shifted to 37°C. Makarow has proposed preparing fusions of Hspl50 (or fragments thereof) and a desired protein, in order to achieve enhanced, controllable secretion (WO 93/18167). The HSP150 gene encodes a primary translation product of 413 amino acids, including an N-terminal secretion signal sequence of 18 amino acids that is not present in the mature protein. A further post-translational processing event occurs C-terminal to a pair of basic residues to yield two subunits of 54 and 341 amino acids which remain associated. The 341 amino acid subunit contains 11 tandem repeats of a 19 amino acid sequence, the function of which is unknown. Homologues of the HSP150 gene were found in Torulaspora delbrueckii, Kluyveromyces marxianus and Schizosaccharomyces pombe (Russo et al, 1992). The same protein has been designated the PIR2 protein by Toh-e et al (1993). The HSP150/PIR2 gene was shown to be a member of a family of at least three genes (PIRl, PIRl and PIR3) all of which contain similar internal tandem repeats of approximately 19 amino acids. Homologues of the PIR genes were shown to be present also in Kluyveromyces lactis and Zygosaccharomyces rouxii (Toh-e et al, 1993). Disruption of the HSP150/PIR2 gene showed that this is not an essential gene (Russo et al, 1992; Toh-e et al, 1993). In this specification we refer to rHA as the desired protein. However, it is to be understood that the problem addressed by the invention will, in principle, be encountered with any other protein which has similar properties to those of rHA and which is therefore purified in the same way. Thus, the solution provided by the invention, namely elimination of Hspl50, is applicable also to the production of such other proteins. Our studies have revealed that the Hspl50 protein is inefficiently separated from rHA by ion exchange chromatography. Surprisingly, however, Hspl50 does not appear in the fraction equivalent to the rHA fraction when rHA is absent. For example, when rHA-containing culture supernatant is passed through a cation exchange column under conditions which ensure binding of the rHA to the column (eg pH4.5, conductivity < 7mS), Hspl50 also binds to the column and is eluted under the same conditions as rHA and thus contaminates the rHA preparation. However, when culture supernatant from a yeast that does not secrete rHA is passed through such a column under the same conditions, the Hspl50 protein does not bind to the matrix but passes straight through the column. The eluate fraction does not contain Hspl50 in the absence of rHA. Similarly, the Hspl50 protein does not bind to an anion exchange column run under conditions which would result in binding of albumin (eg pH5.5, 1.5mS) in the absence of rHA, but is present in the rHA eluate fraction when rHA is present. Surprisingly, we have found that the presence of rHA in culture supernatant significantly alters the behaviour of some yeast proteins during chromatographic purification of the rHA such that proteins with physico-chemical properties which indicate that they would be separated from albumin by, for instance, ion exchange chromatography in fact contaminate the rHA preparation and are difficult to remove. One aspect of the invention provides a process for preparing a desired protein from yeast, comprising culturing the yeast and obtaining the protein, characterised in that the yeast is deficient in heat shock protein 150 (Hspl50). The most convenient way of achieving this is to create a yeast which has a defect in its genome such that a reduced level of the Hspl50 protein is produced. For example, there may be a deletion, insertion or transposition in the coding sequence or the regulatory regions (or in another gene regulating the expression of the Hspl50 gene) such that little or no Hspl50 protein is produced. Alternatively, the yeast could be transformed to produce an anti- Hspl50 agent, such as an anti-Hspl50 antibody. To modify the HSP150 gene so that a reduced level of co-purifying protein is produced, site-directed mutagenesis or other known techniques can be employed to create single or multiple mutations, such as replacements, insertions, deletions, and transpositions, as described in Botstein and Shortle, "Strategies and Applications of In Vitro Mutagenesis", Science, 229: 193-210 (1985), which is incorporated herein by reference. Suitable mutations include chain termination mutations (clearly stop codons introduced near the 3' end might have insufficient effect on the gene product to be of benefit; the person skilled in the art will readily be able to create a mutation in, say, the 5' three quarters of the coding sequence), point mutations that alter the reading frame, small to large deletions of coding sequence, mutations in the promoter or terminator that affect gene expression and mutations that de-stabilize the mRNA. Some desirable point mutations or specific amino acid substitutions may affect chromatographic behaviour by altering the charge distribution. Hence, the protein produced has a similar primary amino acid sequence to that of native Hspl50, but is functionally distinct such that it will not co-purify with the desired protein. Such a modified protein is not regarded as being Hspl50. Specific mutations can be introduced by an extension of * the gene disruption technique known as gene transplacement (Winston, F. et al (1983) Methods Enzymol. 101, 211-228). Any polypeptides inserted into the Hspl50 protein should not be, and should not create, ligands for the desired protein. Those skilled in the art can readily determine, by simple binding assays, whether a ligand has been used or created. Generally one uses a selectable marker to disrupt a gene sequence, but this need not be the case, particularly if one can detect the disruption event phenotypically. In many instances the insertion of the intervening sequence will be such that a stop codon is present in frame with the Hspl50 sequence and the inserted coding sequence is not translated. Alternatively the inserted sequence may be in a different reading frame to Hspl50. The gene may have one or more portions (optionally including regulatory regions, up to the whole gene) excised or inverted, or it may have a portion inserted, in order to result either in no production of protein from the HSP150 locus or in the production of protein from the HSP150 locus which does not co- purify with the desired protein. Preferably, the yeast secretes the desired protein, which is then purified from the fermentation medium. The purification may take place elsewhere; hence, production of culture medium, containing desired protein, in which the level of Hspl50 protein is low or zero is an end in itself. A protein is generally regarded as co-purifying with Hspl50 if the two are still associated after two dissimilar chromatographic separation techniques (one of which is affinity chromatography for the desired protein) or, if affinity chromatography is not used, if the proteins are still associated after three dissimilar steps (for example an anion exchange, a cation exchange and a gel permeation step). Essentially, the identity of the desired protein is self-defined: if a person skilled in die art finds that his desired protein is, after an otherwise suitable purification process, contaminated with a yeast protein, he can determine (using known methods, which are explained in more detail below) whether that yeast protein is Hspl50 and, if it is, use the yeasts and methods of the invention; if the desired protein is not contaminated with Hspl50, then the need for the present invention will not arise. We have found the process of the invention to be particularly applicable to albumins and to other proteins which have similar physico-chemical properties to albumins, such that they are purified by similar chromatographic techniques. Preferably, the desired protein is a human albumin. Human serum albumin (HSA) is a protein of 585 amino acids that is present in human serum at a concentration of 35-45g L "1 and represents about 60% of the total serum protein. HSA is responsible for a significant proportion of the osmotic pressure of serum, and also functions as a carrier of endogenous and exogenous ligands. It is used clinically in the treatment of patients with severe burns, shock, or blood loss, and at present is produced commercially by extraction from human blood. The production of recombinant human albumin (rHA) in microorganisms has been disclosed in EP 330 451 and EP 361 991. The albumin may be a variant of normal HSA/rHA. By "variants" we include insertions, deletions and substitutions, either conservative or non-conservative, where such changes do not substantially alter the oncotic, useful ligand-binding or non-immunogenic properties of albumin. In particular, we include naturally- occurring polymorphic variants of human albumin; fragments of human albumin, for example those fragments disclosed in EP 322 094 (namely HSA (1-n), where n is 369 to 419); and fusions of albumin with other proteins, for example the kind disclosed in WO 90/13653. By "conservative substitutions" is intended swaps within groups such as Gly, Ala; Val, He, Leu; Asp, Glu; Asn, Gin; Ser, Thr; Lys, Arg; and Phe, Tyr. A second main aspect of the invention provides a yeast transformed to express a desired protein which will co-purify with Hspl50 in chromatographic techniques, characterised in that the yeast is deficient in such Hspl50. In addition to the transformed host cells themselves, the present invention also contemplates a culture of those cells, preferably a monoclonal (clonally homogeneous) culture, or a culture derived from a monoclonal culture, in a nutrient medium. The desired protein is produced in conventional ways, for example from a coding sequence inserted in the yeast chromosome or on a free plasmid. The yeasts are transformed with a coding sequence for the desired protein in any of the usual ways, for example electroporation. Methods for transformation of yeast by electroporation are disclosed in Becker & Guarente (1990) Methods Enzymol. 194, 182. Successfully transformed cells, ie cells that contain a DNA construct of the present invention, can be identified by well known techniques. For example, cells resulting from the introduction of an expression construct can be grown to produce the desired polypeptide. Cells can be harvested and lysed and their DNA content examined for the presence of the DNA using a method such as that described by Southern (1975) J. Mol. Biol. 98, 503 or Berent et al (1985) Biotech. 3, 208. Alternatively, the presence of the protein in the supernatant can be detected using antibodies. Useful yeast plasmid vectors include pRS403-406 and pRS413-416 and are generally available from Stratagene Cloning Systems, La Jolla, CA 92037, USA. Plasmids ρRS403, pRS404, ρRS405 and pRS406 are Yeast Integrating plasmids (Yips) and incorporate the yeast selectable markers HIS3, TRP1, LEU2 and URA3. Plasmids pRS413-416 are Yeast Centromere plasmids (YCps). A variety of methods have been developed to operably link DNA to vectors via complementary cohesive termini. For instance, complementary homopolymer tracts can be added to the DNA segment to be inserted to the vector DNA. The vector and DNA segment are then joined by hydrogen bonding between the complementary homopolymeric tails to form recombinant DNA molecules. Synthetic linkers containing one or more restriction sites provide an alternative method of joining the DNA segment to vectors. The DNA segment, generated by endonuclease restriction digestion as described earlier, is treated with bacteriophage T4 DNA polymerase or E. coli DNA polymerase I, enzymes that remove protruding, 3 '-single-stranded termini with their 3'-5'-exonucleolytic activities, and fill in recessed 3'-ends with their polymerizing activities. The combination of these activities therefore generates blunt-ended DNA segments. The blunt-ended segments are then incubated with a large molar excess of linker molecules in the presence of an enzyme that is able to catalyze the ligation of blunt-ended DNA molecules, such as bacteriophage T4 DNA ligase. Thus, the products of the reaction are DNA segments carrying polymeric linker sequences at their ends. These DNA segments are then cleaved with the appropriate restriction enzyme and ligated to an expression vector that has been cleaved with an enzyme that produces termini compatible with those of the DNA segment. Synthetic linkers containing a variety of restriction endonuclease sites are commercially available from a number of sources including International Biotechnologies Inc, New Haven, CN, USA. A desirable way to modify the DNA in accordance with the invention is to use the polymerase chain reaction as disclosed by Saiki et al (1988) Science 239, 487-491. In this method the DNA to be enzymatically amplified is flanked by two specific oligonucleotide primers which themselves become incorporated into the amplified DNA. The said specific primers may contain restriction endonuclease recognition sites which can be used for cloning into expression vectors using methods known in the art. Any yeast which produces an Hspl50 protein can be modified in accordance with the invention. Exemplary genera of yeast contemplated to be useful in the practice of the present invention are Pichia (Hansenula), Saccharomyces , Kluyveromyces, Candida, Torulopsis, Torulaspora, Schizosaccharomyce , Citeromyces, Pachysolen, Debaromyces, Metschunikowia, Rhodosporidium, Leucosporidium, Botryoascus, Sporidiobolus, Endomycopsis, and the like. Preferred genera are those selected from the group consisting of Saccharomyces, Schizosaccharomyces, Kluyveromyces, and Torulaspora. Examples of Saccharomyces spp. are S. cerevisiae, S. italicus and S. rouxii. Examples of Kluyveromyces spp. are K fragilis, K. lactis and K. marxianus. A suitable Torulaspora species is T. delbrueckii. Examples of Pichia (Hansenula) spp. are P. angusta (formerly H. polymorpha), P. anomala (formerly H. anomala) and P. pastoris. Homologues of HSP 150 have already been shown to be present in a wide range of different yeast genera: Torulaspora sp., Kluyveromyces sp., Schizosaccharomyces sp. and Zygosaccharomyces sp. (Russo et al, 1992; Toh-e et al, 1993). In addition, our own studies have shown by Southern blotting that Pichia sp. possess a homologue of HSP 150. Methods for the transformation of S. cerevisiae are taught generally in EP 251 744, EP 258 067 and WO 90/01063, all of which are incorporated herein by reference. Suitable promoters for S. cerevisiae include those associated with the PGK1 gene, GALl or GAL10 genes, CYCl, PH05, TRPl, ADHl, ADH2, the genes for glyceraldehyde-3-phosphate dehydrogenase, hexokinase, pyruvate decarboxylase, phosphofructokinase, triose phosphate isomerase, phosphoglucose isomerase, glucokinase, α-mating factor pheromone, a-mating factor pheromone, the PRB1 promoter, the GUT2 promoter, the GPD1 promoter, and hybrid promoters involving hybrids of parts of 5' regulatory regions with parts of 5' regulatory regions of other promoters or with upstream activation sites (eg the promoter of EP-A-258 067). Convenient regulatable promoters for use in Schizosaccharomyces pombe are the thiamine-repressible promoter from the nmt gene as described by Maundrell (1990) J. Biol. Chem. 265, 10857-10864 and the glucose-repressibleybpi gene promoter as described by Hoffman & Winston (1990) Genetics 124, 807-816. Methods of transforming Pichia for expression of foreign genes are taught in, for example, Cregg et al (1993), and various Phillips patents (eg US 4 857 467, incorporated herein by reference), and Pichia expression kits are commercially available from Invitrogen BV, Leek, Netherlands, and Invitrogen Corp., San Diego, California. Suitable promoters include AOX1 and AOX2. The Gellissen et al (1992) paper mentioned above and Gleeson et al (1986) J. Gen. Microbiol. 132, 3459-3465 include information on Hansenula vectors and transformation, suitable promoters being MOX1 and FMD1; whilst EP 361 991, Fleer et al (1991) and other publications from Rhδne-Poulenc Rorer teach how to express foreign proteins in Kluyveromyces spp., a suitable promoter being PGK1. The transcription termination signal is preferably the 3' flanking sequence of a eukaryotic gene which contains proper signals for transcription termination and polyadenylation. Suitable 3' flanking sequences may, for example, be those of the gene naturally linked to the expression control sequence used, ie may correspond to the promoter. Alternatively, they may be different in which case the termination signal of the S. cerevisiae ADHl gene is preferred. The desired protein may be initially expressed with a secretion leader sequence, which may be any leader effective in the yeast chosen. Leaders useful in S. cerevisiae include that from the mating factor polypeptide (MFa-l) and the hybrid leaders of EP-A-387 319. Such leaders (or signals) are cleaved by the yeast before the mature albumin is released into the surrounding medium. Further such leaders include those of S. cerevisiae invertase (SUC2) disclosed in JP 62-096086 (granted as 91/036516), acid phosphatase (PH05), the pre- sequence of MFα-1, β-glucanase (BGL2) and killer toxin; S. diastaticus glucoamylase II; S. carlsbergensis α-galactosidase (MEL1); K. lactis killer toxin; and Candida glucoamylase. Detailed Description of the Invention Preferred aspects of the invention will now be described in more detail, with reference to the accompanying drawings, in which Figure 1 is a scheme showing the preparation of an EcoRl HSP150-URA3- HSP150 fragment used to transform a yeast strain (DBU3) and disrupt the HSP 150 gene (Example 1); and Figure 2 is a scheme showing the preparation of a further EcoRl fragment used to remove the HSP 150 coding sequence altogether (Example 2). All standard recombinant DNA procedures are as described in Sambrook et al (1989) unless otherwise stated. The DNA sequences encoding rHA are derived from the cDNA disclosed in EP 201 239. Example 1 The HSP150 gene was mutated by the process of gene disruption (Rothstein, 1983) which effectively deleted part of the HSP150 coding sequence, thereby preventing the production of Hspl50. Four oligonucleotides suitable for the PCR amplification of the 5' and 3' ends of the HSP 150 gene (Russo et al, 1992) were synthesized using an Applied Biosystems 380B Oligonucleotide Synthesizer. 5' End LRE45 : 5 ' -CTATTTCCTATTTCGGGAATTCTTAAAGACAAAAAAGCTC-3 ' LRE46: 5 ' -GGCTGTGGTGCTGCAGATGATGCGCTGG-3 ' 3' End LRE47: 5 '-GCTACTTCCGCTTCTGCAGCCGCTACCTCC-3' LRE48: 5'-GCCGTGTAGCGAGGGAATTCTGTGGTCACGATCACTCG-3' Note, LRE45 and LRE48 contain changes in the HSP150 gene sequence so as to introduce EcøRI sites into the 5' or the 3' end of the HSP 150 gene PCR products. LRΕ46 and LRE47 both contain Pst I sites naturally present in the HSP 150 gene sequence (SEQ 1). PCR was carried out to amplify individually the 5' and 3' ends of the HSP 150 gene, using LRE45 and LRE46 or LRE47 and LRE48 respectively, from the DNA from S. cerevisiae genomic DNA (Clontech Laboratories, Inc.). Conditions were as follows: lμg/ml genomic DNA, = 1.2xl0 "10 moles of each primer, denature at 94°C for 61 seconds, anneal at 37°C for 121 seconds, DNA synthesis at 72 °C for 181 seconds for 30 cycles, with a 10 second extension to the DNA synthesis step after each cycle, followed by a 4°C soak. PCR was carried out using a Perkin-Elmer-Cetus Thermal cycler and a Perkin- Elmer-Cetus PCR kit was used according to the manufacturer's recommendations. PCR products were analysed by gel electrophoresis and were found to be of the expected size. Each PCR product was digested with EcøRI and Pstl and cloned into EcoRl/Pstl digested pUC19 (Yanisch-Perron et al, 1985) to form pAYΕ503 (containing the 5' end of the HSP150 gene) and pAYE504 (containing the 3' end of the HSP150 gene) (see Fig. 1). Plasmid DNA sequencing was carried out on pAYE503 and pAYE504 to confirm that the inserts were the desired sequences. pAYE503 and pAYE504 were digested with EcoRl and HmdIII and the HSP150 gene fragments were isolated and cloned together into pUC19XΗ (a derivative of pUC19 lacking a HmdIII site in its polylinker) to form pAYΕ505. The URA3 gene was isolated from YEp24 (Botstein et al, 1979) as a HmdIII fragment and cloned into the HmdIII site of pAYE505 to form pAYE506 (Fig. 1). pAYE506 contains a selectable marker (URA3) flanked by 5' and 3' regions of the HSP 150 gene. To construct a strain lacking the capacity to produce ΗSP150, a ura3 derivative of DB1 cir° pAYE316 (Sleep et al, 1991) was obtained by random chemical mutagenesis and selection for resistance to 5-fluoro-orotic acid (Boeke et al, 1987). Plasmid pAYE316 is based on the 2 μm plasmid and contains a coding sequence for human albumin under the control of the yeast PRB1 promoter, with an ADHl terminator and a LEU2 selectable marker. The strain was grown overnight in lOOmL buffered minimal medium (Yeast Nitrogen Base [without amino acids, without ammonium sulphate, Difco], (NH 4 ) 2 S0 4 5g/L, citric acid monohydrate 6.09g/L, NaHP0 4 20.16g/L, sucrose 20g/L, pH6.5) and the cells were collected by centrifugation and then washed once with sterile water. The cells were then resuspended in lOmL sterile water and 2mL aliquots were placed in separate 15mL Falcon tubes. A 5mg/mL solution of N-methyl-N'-nitro-N-nitrosoguanidine (NTG) was then added to the tubes as follows: OμL, 20/xL, 40μL, 80μL or 160μL. The cells were then incubated at 30 °C for 20 min and then centrifuged and washed three times with sterile water. Finally, the cells were resuspended in ImL YEP (1 % W / V yeast extract, 2% w / v Bacto peptone) and stored at 4°C. The percentage of cells that survived the mutagenic treatment was determined by spreading dilutions of the samples on YEP plates containing 2% / v sucrose and incubating at 30°C for 3 days. Cells from the treatment which gave approximately 50% survival were grown on YEP plates containing 2% / v sucrose and then replica-plated onto YNB minimal medium containing 2% w / v sucrose and supplemented with 5- fluoro-orotic acid (lmg/mL) and uracil (50μg/mL). Colonies able to grow on this medium were purified, tested to verify that they were unable to grow in the absence of uracil supplementation and that this defect could be corrected by introduction of the URA3 gene by transformation. The ura3 strain, DBU3 cir° (pAYE316), was transformed with EcoRl digested pAYΕ506 and Ura + transformants were selected. The disruption of the HSP150 gene in these transformants was confirmed by Southern blot analysis using a fragment comprising the 5' and 3 ' ends of the HSP 150 gene (the EcoRl fragment from pAYE505) as a probe. The yeast was then grown to high cell density by fed batch culture in minimal medium in a fermenter (Collins, 1990). Briefly, a fermenter of 10L working volume was filled to 5L with an initial batch medium containing 50 mL/L of a concentrated salts mixture (Table 1), 10 mL/L of a trace elements solution (Table 2), 50 mL/L of a vitamins mixture (Table 3) and 20 g/L sucrose. An equal volume of feed medium containing 100 mL/L of the salts mixture, 20 mL/L of the trace elements mixture, 100 mL/L of vitamins solution and 500 g/L sucrose was held in a separate reservoir connected to the fermenter by a metering pump. The pH was maintained at 5.7 ± 0.2 by the automatic addition of ammonium hydroxide or sulphuric acid, and the temperature was maintained at 30°C. The stirrer speed was adjusted to give a dissolved oxygen tension of > 20% air saturation at 1 v/v/min air flow rate. Table 1. Salts Mixture Chemical Concentration (g/L) KH 2 P0 4 114.0 MgS0 4 12.0 CaCl 2 .6H 2 0 3.0 Na 2 EDTA 2.0 Table 2. Trace Elements Solution Chemical Concentration (g/L) ZnS0 4 .7H 2 0 3.0 FeS0 4 .7H 2 0 10.0 MnS0 4 .4H 2 0 3.2 CuS0 4 .5H 2 0 0.079 H 3 BO 3 1.5 KI 0.2 Na 2 Mo0 4 .2H 2 0 0.5 CoCl 2 .6H 2 0 0.56 H 3 P0 4 75mL/L Table 3. Vitamins Solution Chemical Concentration (g/L) Ca pantothenate 1.6 Nicotinic acid 1.2 -inositol 12.8 Thiamine HC1 0.32 Pyridoxine HC1 0.8 Biotin 0.008 The fermenter was inoculated with 100 mL of an overnight culture of S. cerevisiae grown in buffered minimal medium (Yeast nitrogen base [without amino acids, without ammonium sulphate, Difco] 1.7 g/L, (NH 4 ) 2 S0 4 5 g/L, citric acid monohydrate 6.09 g/L, Na 2 HP0 4 20.16 g/L, sucrose 20 g/L, pH6.5). The initial batch fermentation proceeded until the carbon source had been consumed, at which point the metering pump was switched on and the addition of feed was computer controlled (the micro MFCS system, B. Braun, Melsungen, Germany) using an algorithm based on that developed by Wang et al (1979). A mass spectrometer was used in conjunction with the computer control system to monitor the off gases from the fermentation and to control the addition of feed to maintain a set growth rate (eg 0.1 h "1 ). Maximum conversion of carbon substrate into biomass is achieved by maintaining the respiratory coefficient below 1.2 (Collins, 1990) and, by this means, cell densities of approximately 100 g/L cell dry weight can be achieved. The fermentation broth was centrifuged to remove the cells and then subjected to affinity chromatographic purification as follows. The culture supernatant was passed through a Cibacron Blue F3GA Sepharose column (Pharmacia) which was then washed with 0.1M phosphate glycine buffer, pH8.0. The rHA was then eluted from the column with 2M NaCl, 0.1M phosphate glycine, pH8.0. The albumin may alternatively be purified from the culture medium by any of the variety of known techniques for purifying albumin from serum or fermentation culture medium, for example those disclosed in WO 92/04367, Maurel et al (1989), Curling (1980) and EP 524 681. Analysis of rHA purified from HsplSO strains revealed that no HSP150 protein was present in these samples. HSP150 protein is determined using prior art techniques such as ELISA or Western blotting. Anti-HSP150 antibodies are disclosed in Russo et al (1992) Proc. Nat. Acad. Sci. (USA) 89, 3671-3675. Example 2 The HSP150 protein coding sequence was deleted by using alternative fragments of the cloned HSP 150 sequences as follows. The URA3 HmdIII fragment from YEp24 (see Example 1) was cloned into pIC19R (Marsh J.L. et al (1984) Gene 32, 481-485) at HmdIII to form pAYE601 and then excised as a SaWClal fragment and inserted into pAYE505 at the Xhol and Clal sites to form pAYE602 (Fig 2). This plasmid was digested with EcoRl and then used to transform DBU3 cir° (pAYΕ316), selecting for Ura + transformants. The disruption of the HSP 150 gene in these transformants was confirmed by Southern blot analysis as described in Example 1. Thus, in this example, the whole of the HSP150 coding sequence is removed, whereas in Example 1 the sequence is disrupted to yield non-functional protein. Example 3 Southern blotting has revealed an Ηspl50 homologue in Hansenula polymorpha (now called Pichia angusta). The P. angusta gene may be functionally deleted by ways analogous to those in Examples 1 and 2. References Boeke, J. D. et al (1987) Methods Enzymol. 154, 164-175. Botstein, D. et al (1979) Gene 8, 17-24. Collins, S.H. (1990) In Protein Production by Biotechnology (Harris, T.J.R., ed.) pp 61-77, Elsevier, Barking, Essex. Curling (1980) "Albumin Purification by Ion Exchange Chromatography", in "Methods of Plasma Protein Purification", Ed. Curling, J.M., Academic Press, London. Fleer, R. et al (1991) Bio/Technology 9, 968-975. Maurel et al (1989) "Biotechnology of Plasma Proteins", Colloque INSERM 175, 19-24. Romanos, M. et al (1992) Yeast 8, 423-488. Rothstein, R. J. (1983) Methods Enzymol. 101, 202-211. Russo, P. et al (1992) Proc. Nad. Acad. Sci. USA 89, 3671-3675. Sambrook, J. et al (1989) Molecular Cloning: a Laboratory Manual, 2nd edition. Cold Spring Harbor Laboratory Press, Cold Spring Harbor, NY. Sleep, D. et al (1991) Bio /Technology 9, 183-187. Toh-e et al (1993) Yeast 9, 481-494. Wang, H.Y. et al (1979) Biotechnology & Bioeng. 21, 975 Yanisch-Perron, C. et al (1985) Gene 33, 103-119. SEQUENCE LISTING (1) GENERAL INFORMATION: (i) APPLICANT: (A) NAME: Delta Biotechnology Limited (B) STREET: Castle Court, Castle Boulevard (C) CITY: Nottingham (E) COUNTRY: United Kingdom (F) POSTAL CODE (ZIP): NG7 1FD (ii) TITLE OF INVENTION: Yeast Strains (iii) NUMBER OF SEQUENCES: 6 (iv) COMPUTER READABLE FORM: (A) MEDIUM TYPE: Floppy disk (B) COMPUTER: IBM PC compatible (C) OPERATING SYSTEM: PC-DOS/MS-DOS (D) SOFTWARE: Patentln Release #1.0, Version #1.25 (EPO) (vi) PRIOR APPLICATION DATA: (A) APPLICATION NUMBER: GB 9411356.0 (B) FILING DATE: 07-JUN-1994 (2) INFORMATION FOR SEQ ID NO: 1 : (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 40 base pairs (B) TYPE: nucleic acid (C) STRANDEDNESS: single (D) TOPOLOGY: linear (ii) MOLECULE TYPE: cDNA (iii) HYPOTHETICAL: NO (ix) FEATURE: (A) NAME/KEY: misc_feature (B) LOCATION: 1..40 (D) OTHER INFORMATION: /note= "Oligonucleotide for PCR amplification of 5' end of Hspl50 gene." (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 1 : CTATTTCCTA TTTCGGGAAT TCTTAAAGAC AAAAAAGCTC 40 (2) INFORMATION FOR SEQ ID NO: 2: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 28 base pairs (B) TYPE: nucleic acid (C) STRANDEDNESS: single (D) TOPOLOGY: linear (ii) MOLECULE TYPE: cDNA (iii) HYPOTHETICAL: NO (ix) FEATURE: (A) NAME/KEY: misc eature (B) LOCATION: 1..28 (D) OTHER INFORMATION: /note= "Oligonucleotide for PCR amplification of the 5' end of the Hspl50 gene. " (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 2: GGCTGTGGTG CTGCAGATGA TGCGCTGG 28 (2) INFORMATION FOR SEQ ID NO: 3: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 30 base pairs (B) TYPE: nucleic acid (C) STRANDEDNESS: single (D) TOPOLOGY: linear (ii) MOLECULE TYPE: cDNA (iii) HYPOTHETICAL: NO (ix) FEATURE: (A) NAME/KEY: miscjeature (B) LOCATION: 1..30 (D) OTHER INFORMATION: /note= "Oligonucleotide for PCR amplification of 3' end of the Hspl50 gene. " (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 3: GCTACTTCCG CTTCTGCAGC CGCTACCTCC 30 (2) INFORMATION FOR SEQ ID NO: 4: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 38 base pairs (B) TYPE: nucleic acid (C) STRANDEDNESS: single (D) TOPOLOGY: linear (ii) MOLECULE TYPE: cDNA (iii) HYPOTHETICAL: NO (ix) FEATURE: (A) NAME/KEY: miscjeature (B) LOCATION: 1..38 (D) OTHER INFORMATION: /note= "Oligonucleotide for PCR amplification of the 3' end of the Hspl50 gene. " (xi) SEQUENCEDESCRIPTION: SEQ ID NO: 4: GCCGTGTAGC GAGGGAATTC TGTGGTCACG ATCACTCG 38 (2) INFORMATION FOR SEQ ID NO: 5: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 2048 base pairs (B) TYPE: nucleic acid (C) STRANDEDNESS: single (D) TOPOLOGY: linear (ii) MOLECULE TYPE: DNA (genomic) (iii) HYPOTHETICAL: NO (vi) ORIGINAL SOURCE: (A) ORGANISM: Saccharomyces cerevisiae (ix) FEATURE: (A) NAME/KEY: CDS (B) LOCATION: 397..1638 (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 5: AGTGATCTTA CTATTTCCTA TTTCGGAAAT TATTAAAGAC AAAAAAGCTC ATTAATGGCT 60 TTCCGTCTGT AGTGATAAGT CGCCAACTCA GCCTAATTTT TCATTTCTTT ACCAGATCAG 120 GAAAACTAAT AGTACAAATG AGTGTTTTCT CAAGCGGAAC ACCACATTTT GAGCTAAATT 180 TAGATTTTGG TCAAAATAAG AAAGATCCTA AAAAAGGAAT GGTTGGTGAA AAATTTATTA 240 GCTTGAATGG TAGGAATCCT CGAGATATAA AAGGAACACT TGAAGTCTAA CGACAATCAA 300 TTTCGATTAT GTCCTTCCTT TTACCTCAAA GCTCAAAAAA ATATCAATAA GAAACTCATA 360 TTCCTTTTCT AACCCTAGTA CAATAATAAT AATATA ATG CAA TAC AAA AAG ACT 414 Met Gin Tyr Lys Lys Thr 1 5 TTG GTT GCC TCT GCTTTG GCC GCT ACTACATTG GCC GCC TATGCT CCA 462 Leu Val Ala Ser Ala Leu Ala Ala Thr Thr Leu Ala Ala Tyr Ala Pro 10 15 20 TCTGAG CCTTGG TCC ACTTTG ACTCCA ACA GCC ACTTAC AGC GGTGGT 510 Ser Glu Pro Tip Ser Thr Leu Thr Pro Thr Ala Thr Tyr Ser Gly Gly 25 30 35 GTTACC GACTAC GCTTCC ACC TTC GGTATTGCC GTTCAA CCAATC TCC 558 Val Thr Asp Tyr Ala Ser Thr Phe Gly He Ala Val Gin Pro He Ser 40 45 50 ACTACATCC AGC GCATCA TCTGCA GCC ACCACA GCC TCA TCTAAGGCC 606 Thr Thr Ser Ser Ala Ser Ser Ala Ala Thr Thr Ala Ser Ser Lys Ala 55 60 65 70 AAGAGAGCTGCTTCC CAA ATTGGTGATGGTCAA GTC CAA GCTGCTACC 654 Lys Arg Ala Ala Ser Gin He Gly Asp Gly Gin Val Gin Ala Ala Thr 75 80 85 ACTACTGCTTCTGTC TCTACC AAGAGTACC GCTGCC GCC GTTTCTCAG 702 Thr Thr Ala Ser Val Ser Thr Lys Ser Thr Ala Ala Ala Val Ser Gin 90 95 100 ATC GGTGATGGTCAAATCCAA GCTACTACTAAGACTACC GCTGCTGCT 750 He Gly Asp Gly Gin He Gin Ala Thr Thr Lys Thr Thr Ala Ala Ala 105 110 115 GTC TCTCAA ATTGGTGATGGTCAA ATTCAA GCTACC ACC AAGACTACC 798 Val Ser Gin He Gly Asp Gly Gin He Gin Ala Thr Thr Lys Thr Thr 120 125 130 TCTGCTAAGACTACC GCC GCTGCC GTTTCTCAAATCAGT GATGGTCAA 846 Ser Ala Lys Thr Thr Ala Ala Ala Val Ser Gin He Ser Asp Gly Gin 135 140 145 150 ATC CAA GCTACC ACC ACTACTTTA GCC CCA AAG AGC ACC GCTGCTGCC 894 He Gin Ala Thr Thr Thr Thr Leu Ala Pro Lys Ser Thr Ala Ala Ala 155 160 165 GTTTCTCAA ATC GGTGATGGTCAA GTTCAA GCTACCACC 26 ACT ACT TTA 942 Val Ser Gin He Gly Asp Gly Gin Val Gin Ala Thr Thr Thr Thr Leu 170 175 180 GCC CCA AAG AGC ACC GCTGCTGCC GTTTCT CAA ATC GGT GATGGT CAA 990 Ala Pro Lys Ser Thr Ala Ala Ala Val Ser Gin He Gly Asp Gly Gin 185 190 195 GTTCAA GCTACTACTAAGACTACC GCTGCT GCT GTC TTT CAAATTGGT 1038 Val Gin Ala Thr Thr Lys Thr Thr Ala Ala Ala Val Phe Gin He Gly 200 205 210 GATGGT CAA GTT CTTGCTACC ACC AAG ACTACT CGTGCC GCC GTTTCT 1086 Asp Gly Gin Val Leu Ala Thr Thr Lys Thr Thr Arg Ala Ala Val Ser 215 220 225 230 CAAATC GGTGATGGTCAAGTTCAAGCTACTACC AAGACT ACC GCTGCT 1134 Gin He Gly Asp Gly Gin Val Gin Ala Thr Thr Lys Thr Thr Ala Ala 235 240 245 GCT GTC TCTCAA ATC GGTGATGGTCAA GTTCAA GCA ACT ACC AAA ACC 1182 Ala Val Ser Gin He Gly Asp Gly Gin Val Gin Ala Thr Thr Lys Thr 250 255 260 ACT GCC GCA GCT GTTTCC CAA ATTACT GAC GGTCAA GTT CAA GCC ACT 1230 Thr Ala Ala Ala Val Ser Gin He Thr Asp Gly Gin Val Gin Ala Thr 265 270 275 ACA AAA ACC ACTCAA GCA GCC AGC CAA GTA AGC GATGGC CAA GTC CAA 1278 Thr Lys Thr Thr Gin Ala Ala Ser Gin Val Ser Asp Gly Gin Val Gin 280 285 290 GCTACTACT GCTACTTCC GCTTCT GCA GCC GCTACC TCC ACTGAC CCA 1326 Ala Thr Thr Ala Thr Ser Ala Ser Ala Ala Ala Thr Ser Thr Asp Pro 295 300 305 310 GTC GAT GCT GTC TCC TGT AAG ACT TCT GGT ACC TTA GAA ATG AAC TTA 1374 Val Asp Ala Val Ser Cys Lys Thr Ser Gly Thr Leu Glu Met Asn Leu 315 320 325 AAG GGC GGTATC TTA ACTGAC GGT AAG GGT AGA ATTGGT TCTATTGTT 1422 Lys Gly Gly He Leu Thr Asp Gly Lys Gly Arg He Gly Ser He Val 330 335 340 GCT AAC AGA CAA TTC CAA TTT GAC GGT CCA CCA CCA CAA GCT GGT GCC 1470 Ala Asn Arg Gin Phe Gin Phe Asp Gly Pro Pro Pro Gin Ala Gly Ala 345 350 355 ATCTAC GCT GCT GGTTGGTCT ATA ACT CCA GAC GGTAAC TTG GCTATT 1518 He Tyr Ala Ala Gly Tip Ser He Thr Pro Asp Gly Asn Leu Ala He 360 365 370 GGTGAC AAT GAT GTC TTC TAC CAATGTTTGTCC GGTACT TTC TAC AAC 1566 Gly Asp Asn Asp Val Phe Tyr Gin Cys Leu Ser Gly Thr Phe Tyr Asn 375 380 385 390 TTGTAC GAC GAA CAC ATT GGTAGTCAATGTACTCCA GTC CAC TTGGAA 1614 Leu Tyr Asp Glu His He Gly Ser Gin Cys Thr Pro Val His Leu Glu 395 400 405 GCT ATC GAT TTG ATA GAC TGT TAAGCAGAAA ACTATTAGTT CTTTTATCCT 1665 Ala He Asp Leu He Asp Cys 410 GATGACTTTT TCTCATTTGC ATTGATTAGA AAGGAAAAAA AGAAGTGTCC TTTTCTACTA 1725 CTACTCTAGT CGCATCCATT CCTTTGCATT TATCTTTTCT GCGGTTGGCC AATCCATTCT 1785 TCCGAGAATT TGGCTAGCCA TACTTGATGT TTTCCCATTA TTGGTTCGTT TGGCAATGCT 1845 AATTTTCTTA ATTGCCCCTT ATATACTCTT CCATAAAATG TTTTTTTTAT AACTAATTTT 1905 CTGTATATCA TTATCTAATA ATCTTATAAA ATGTTAAAAA GACTTGGAAA GCAACGAGTG 1965 ATCGTGACCA CATAATTGCC TCGCTACACG GCAAAAATAA GCCAGTCCTA ATGTGTATAT 2025 TAAAGGCTGC ATGTGGCTAC GTC 2048 (2) INFORMATION FOR SEQ ID NO: 6: (i) SEQUENCE CHARACTERISTICS: (A) LENGTH: 413 amino acids (B) TYPE: amino acid (D) TOPOLOGY: linear (ii) MOLECULE TYPE: protein (xi) SEQUENCE DESCRIPTION: SEQ ID NO: 6: Met Gin Tyr Lys Lys Thr Leu Val Ala Ser Ala Leu Ala Ala Thr Thr 1 5 10 15 Leu Ala Ala Tyr Ala Pro Ser Glu Pro Trp Ser Thr Leu Thr Pro Thr 20 25 30 Ala Thr Tyr Ser Gly Gly Val Thr Asp Tyr Ala Ser Thr Phe Gly He 35 40 45 Ala Val Gin Pro He Ser Thr Thr Ser Ser Ala Ser Ser Ala Ala Thr 50 55 60 Thr Ala Ser Ser Lys Ala Lys Arg Ala Ala Ser Gin He Gly Asp Gly 65 70 75 80 Gin Val Gin Ala Ala Thr Thr Thr Ala Ser Val Ser Thr Lys Ser Thr 85 90 95 Ala Ala Ala Val Ser Gin He Gly Asp Gly Gin He Gin Ala Thr Thr 100 105 110 Lys Thr Thr Ala Ala Ala Val Ser Gin He Gly Asp Gly Gin He Gin 115 120 125 Ala Thr Thr Lys Thr Thr Ser Ala Lys Thr Thr Ala Ala Ala Val Ser 130 135 140 Gin He Ser Asp Gly Gin He Gin Ala Thr Thr Thr Thr Leu Ala Pro 145 150 155 160 Lys Ser Thr Ala Ala Ala Val Ser Gin He Gly Asp Gly Gin Val Gin 165 170 175 Ala Thr Thr Thr Thr Leu Ala Pro Lys Ser Thr Ala Ala Ala Val Ser 180 185 190 Gin He Gly Asp Gly Gin Val Gin Ala Thr Thr Lys Thr Thr Ala Ala 195 200 205 Ala Val Phe Gin He Gly Asp Gly Gin Val Leu Ala Thr Thr Lys Thr 210 215 220 Thr Arg Ala Ala Val Ser Gin He Gly Asp Gly Gin Val Gin Ala Thr 225 230 235 240 Thr Lys Thr Thr Ala Ala Ala Val Ser Gin He Gly Asp Gly Gin Val 245 250 255 Gin Ala Thr Thr Lys Thr Thr Ala Ala Ala Val Ser Gin He Thr Asp 260 265 270 Gly Gin Val Gin Ala Thr Thr Lys Thr Thr Gin Ala Ala Ser Gin Val 275 280 285 Ser Asp Gly Gin Val Gin Ala Thr Thr Ala Thr Ser Ala Ser Ala Ala 290 295 300 Ala Thr Ser Thr Asp Pro Val Asp Ala Val Ser Cys Lys Thr Ser Gly 305 310 315 320 Thr Leu Glu Met Asn Leu Lys Gly Gly He Leu Thr Asp Gly Lys Gly 325 330 335 Arg He Gly Ser He Val Ala Asn Arg Gin Phe Gin Phe Asp Gly Pro 340 345 350 Pro Pro Gin Ala Gly Ala He Tyr Ala Ala Gly Tφ Ser He Thr Pro 355 360 365 Asp Gly Asn Leu Ala He Gly Asp Asn Asp Val Phe Tyr Gin Cys Leu 370 375 380 Ser Gly Thr Phe Tyr Asn Leu Tyr Asp Glu His He Gly Ser Gin Cys 385 390 395 400 Thr Pro Val His Leu Glu Ala He Asp Leu He Asp Cys 405 410

Claims: CLAIMS 1. A process for preparing a desired protein from yeast, comprising culturing the yeast and obtaining the desired protein, characterised in that the yeast is deficient in heat shock protein 150 (Hspl50). 2. A process according to Claim 1 wherein the yeast has a defect in its genome such that a reduced level of the Hspl50 protein is produced. 3. A process according to Claim 2 wherein substantially no Hspl50 protein is produced. 4. A process according to any one of the preceding claims wherein the desired protein is an albumin. 5. A process according to Claim 4 wherein the desired protein is a human albumin. 6. A process according to any one of the preceding claims wherein the yeast is a Torulaspora, Kluyveromyces, Schizosaccharomyces, Pichia or Saccharomyces species. 7. A process according to Claim 6 wherein the yeast is S. cerevisiae. 8. A process according to any one of the preceding claims wherein the desired protein is secreted from the yeast into the surrounding medium and purified therefrom. 9. A protein prepared by a process according to any one of the preceding claims. 10. A culture medium containing a desired protein and prepared by a process according to any one of Claims 1 to 7. 11. A yeast transformed to express a desired protein which will co-purify with Hspl50 in chromatographic techniques, characterised in that the yeast is deficient in Hspl50. 12. A yeast according to Claim 11 wherein the yeast has a defect in its genome such that a reduced level of the Hspl50 protein is produced. 13. A yeast according to Claim 11 wherein substantially no Hspl50 protein is produced by the yeast. 14. A yeast according to any one of Claims 11 to 13 wherein the desired protein is an albumin. 15. A yeast according to Claim 14 wherein the desired protein is a human albumin. 16. A yeast according to any one of Claims 11 to 15 wherein the yeast is Torulaspora, Kluyveromyces, Schizosaccharomyces or Saccharomyces species. 17. A yeast according to Claim 16 wherein the yeast is S. cerevisiae. 18. A yeast according to any one of Claims 11 to 17 wherein the yeast is transformed with a DNA construct such that the desired protein is secreted from the yeast during culturing thereof. 19. A method of preparing a yeast according to any one of Claims 11 to 18 comprising the steps of (i) transforming the yeast with a coding sequence for expression of the desired protein, and (ii) disrupting the genome of the yeast such that the yeast has an abnormally low level of Hspl50, wherein steps (i) and (ii) may be carried out in either order or simultaneously.

Inventors: QUIRK ALAN VICTOR, WOOD PATRICIA CAROL, QUIRK, ALAN, VICTOR, WOOD, PATRICIA, CAROL
Applicants: DELTA BIOTECHNOLOGY LTD, QUIRK ALAN VICTOR, WOOD PATRICIA CAROL, DELTA BIOTECHNOLOGY LIMITED, QUIRK, ALAN, VICTOR, WOOD, PATRICIA, CAROL
Application year: 1995
Main classification: C12N15
IPC codes: C07K14, C12N1, C12N15, C12P21, C12R1