Continuous fermentation process

Abstract

A fermentation assembly comprising: (a) a vessel for culturing living cells; (b) at least two storage flasks in fluid communication with the vessel for supply of liquids and a first transport means for transferring the liquids from the storage flasks to the vessel; (c) individual appliances operably connected to the transport means for monitoring the supply of the contents of the storage flasks to the vessel; (d) a harvest flask in fluid communication with the vessel and a second transport means for transferring the fermentation broth from the vessel to the harvest flask; and (e) a device operably connected to the first transport means for controlling and maintaining a constant dilution rate in the vessel with varying rates of individual supply of liquid from the storage flasks to the vessel is disclosed.

Description

FIELD OF THE INVENTION

[0001] The present invention relates to a continuous process for the manufacture of proteins. In particular, the invention relates to fermentation assemblies and processes for manufacturing proteins.

SUMMARY OF THE INVENTION

[0002] In accordance with the present invention it has been found that splitting of cultivation media used in a continuous fermentation process allows one to study the influence on growth and metabolite-production of microorganisms, and thus to determine optimal conditions for the fermentation process. A continuously delivered fermentation medium can generally be split into as many fractions as it contains ingredients. Examples of such ingredients are carbon, nitrogen, phosphorus, and sulfur sources as well as vitamins and complex substrates such as corn steep, yeast extract, and other natural products. Furthermore, every required mineral, micro- or trace element can be provided separately as a solution of a water-soluble salt, such as a chloride, sulfate or nitrate. In this manner, a fermentation medium of any desired composition can be obtained, provided that the desired amounts of the ingredients are (water)-soluble and no disturbing interactions (e.g., precipitation, reaction) occur in the individual feed solutions or in the fermentation medium.

[0003] One embodiment of the invention is a fermentation assembly containing a vessel for culturing living cells, at least two storage flasks in fluid communication with the vessel for supply of liquids and a first transport means for transferring the liquids from the storage flasks to the vessel, individual appliances operably connected to the transport means for monitoring the supply of the contents of the storage flasks to the vessel, a harvest flask in fluid communication with the vessel and a second transport means for transferring the fermentation broth from the vessel to the harvest flask, and a device operably connected to the first transport means for controlling and maintaining a constant dilution rate in the vessel with varying rates of individual supply of liquid from the storage flasks to the vessel.

[0004] Another embodiment of the invention is a process for the manufacture of a protein. This process includes providing a continuous culture of living cells in a fermentation reactor; and individually feeding nutrients and other agents required for the growth of the cells into the reactor at a constant dilution rate to achieve optimal production of the protein.

[0005] A further embodiment of the invention is a fermentation assembly. This fermentation assembly includes a fermentor 1 equipped with inlet tubes 2a in fluid communication with a storage flask 2 for supply of liquids to the fermentor, a pump 3 operably connected to the inlet tubes for transporting liquids from the storage flask 2 to the fermentor 1, a scale 4 in contact with each storage flask for monitoring the amount of liquid supplied to and discharged from the fermentor, a gas inlet 9 and outlet tubes 10 in communication with the fermentor for introducing and removing gas therefrom, a pump 6 operably connected to an outlet tube 5a which is in fluid connection with the fermentor, wherein the pump discharges fermentation broth from the fermentor to a harvest flask 5, a main controlling unit 7 operably connected to the fermentation assembly for overall process monitoring and steering, a controlling unit 11 operably connected to individual control systems 17 for monitoring and steering temperature, pH, gas pressure, fermentor content, and antifoam agents, a circuit 12 for monitoring gas supply and taking samples including an outlet tube from the fermentor, which circuit is operably connected to the outlet to be pump 13, and gas inlet and outlet flow control devices 14 and 15 operably connected to the gas inlet and outlet tubes 9, 10.

BRIEF DESCRIPTION OF DRAWINGS

[0006] FIG. 1 is a diagram depicting a fermentation assembly according to the present invention.

[0007] FIG. 2 depicts the design of a consensus phytase amino acid sequence.

[0008] FIG. 3 depicts the nucleotide sequence of the consensus phytase-1 gene (fcp) and of the primers used to construct it.

[0009] FIG. 4 depicts the alignment and consensus sequences of five Basidiomycetes phytases.

[0010] FIG. 5 depicts the design of the consensus phytase-10 amino acid sequence.

[0011] FIG. 6 depicts the nucleotide and amino acid sequences of consensus phytase-10.

[0012] FIG. 7 depicts the amino acid alignment for the design of consensus phytase-11.

[0013] FIG. 8 depicts the nucleotide and amino acid sequence of phytase-1-thermo[8]-Q50T-K91A.

[0014] FIG. 9 depicts the nucleotide and amino acid sequence of consensus phytase-10-thermo[3]-Q50T-K91A.

[0015] FIG. 10 depicts the nucleotide and amino acid sequence of A. fumigatus ATCC 13073 phytase &agr;-mutant.

[0016] FIG. 11 depicts the nucleotide and amino acid sequence of consensus phytase-7.

[0017] FIG. 12 depicts a differential scanning calorimetry (DSC) of consensus phytase-10 (12A) and consensus phytase-1 (12B).

[0018] FIG. 13 depicts DSC of consensus phytase-10-thermo[3]-Q50T (13A) and consensus phytase-10-thermo-[3]-Q50T-K91A (13B).

[0019] FIG. 14 is a graph comparing the temperature optima between consensus phytase-1, consensus phytase-10, and consensus phytase-10-thermo[3]-Q50TF.

[0020] FIG. 15 is a graph depicting the pH 1-dependent activity profile (15A) and substrate specificity (15B) of consensus phytase 10, consensus phytase-10-thermo[3]-Q50T, and consensus phytase-10-thermo[3]-Q50T-K91A.

[0021] FIG. 16 depicts the, pH-dependent activity profile (16A) and substrate specificity (16B) of consensus phytase-1-thermo[g]-Q50T and consensus phytase-1-thermo[8]-Q50T-K91A.

[0022] FIG. 17 depicts DSC of consensus phytase-1-thermo[8]-Q50T (17A) and consensus phytase-1-thermo[8]-Q50T-K91A (17B).

[0023] FIG. 18 is a graph comparing the temperature optima between consensus phytase-1, consensus phytase-1-thermo[3], and consensus phytase-1-thermo[8].

[0024] FIG. 19 depicts the pH-dependent activity profile (19A) and substrate specificity (19B) of consensus phytase-1, consensus phytase-7, and the phytase from A. niger NRRL 3135.

[0025] FIG. 20 depicts DSC of the phytase from A. fumigatus ATCC 13073 (20B) and of its stabilized &agr;-mutant (20A).

[0026] FIG. 21 is a graph depicting the temperature optima of A. fumigatus ATCC 13073 wild type phytase, its &agr;-mutant, and a further stabilized &agr;-mutant.

[0027] FIG. 22 depicts the amino acid sequence of consensus phytase-12 (consphy 12).

DETAILED DESCRIPTION OF THE INVENTION

[0028] In one aspect, the present invention is a continuous process for the manufacture of proteins by means of a protein-producing microorganism.

[0029] More particularly, the invention is a continuous process for the manufacture of a protein using a protein-producing microorganism that may be immobilized on a solid carrier and/or the nutrients and other agents required for growth of the microorganism and optimal production of protein therefrom are fed into a reactor individually at a constant dilution rate.

[0030] In a preferred aspect, the invention is a process for the manufacture of a protein using a fermentation assembly that includes (a) a vessel suitable for carrying out reactions with living or inactivated cells; (b) at least two storage flasks connected to the vessel for supply of liquids and means to transport the liquids from the storage flasks to the vessel; (c) individual appliances monitoring the supply of the contents of the storage flasks to the vessel; (d) a harvest flask connected to the vessel and means to transport fermentation broth from the vessel to the harvest flask; and (e) a device for controlling and maintaining a constant dilution rate in the vessel with varying rates of supply of individual liquids from the storage flasks to the vessel.

[0031] Any conventional fermentation vessel can be used as the vessel in step (a) above for the purpose of this invention. The vessel may be made of materials such as stainless steel, glass or ceramics, and may have a volume of from e.g., 100 ml to 2500 m3 although these figures are not critical to the invention. For continuous operation, the inside of the vessel is optionally equipped with a receptacle or sieve plate for uptake of immobilized living cells. These cells may be present in the vessel as a bed of immobilized cells, such as one selected from the group consisting of a fixed bed, an expanded bed, a moving bed, and combinations thereof.

[0032] Further, the fermentation vessel is connected to a series of storage flasks that contain nutrient solutions and solutions for maintaining and controlling a desired pH and other parameters, such as foam formation, redox potential, etc., in the fermentation broth. Depending on the particular needs of the fermentation, there may be separate storage flasks for individual supply of substrates to the vessel, which substrates serve as the carbon, nitrogen or mineral source for the living cells in the vessel. In a particular embodiment, at least one of the at least two storage flasks contains a controlling agent. Said controlling agent has the purpose of regulating the pH of the contents of the flask containing it, and may be an acid, e.g., hydrochloric acid, or a base, e.g., sodium hydroxide.

[0033] The present process is advantageously carried out at a constant dilution rate in the fermentation vessel. As used herein, the term “dilution rate” means the total volume of liquids supplied to the fermentation vessel per volume of the fermentation vessel per hour (h−1).

[0034] Accordingly, it is a particular feature of the present invention to carry out the fermentation process at a constant dilution rate in the fermentation vessel while varying the supply of individual nutrient components or other additives during the fermentation process. To facilitate this task, a storage flask containing an inert component, e.g., water is optionally provided in the fermentation vessel to complement the supply of liquids added to the fermentation vessel, thus keeping the total supply of liquid constant in the fermentation vessel.

[0035] The assembly that is preferably used to carry out the process of this invention further includes means to transport the individual components of the fermentation medium from the storage flasks to the fermentation vessel, and appliances for monitoring the amount of liquid supplied to the fermentation vessel. Every combination of measuring instruments (e.g., volumetric or mass flow rate by either gravimetric, anemometric, magnetic, ultrasonic, Venturi, J. cross-relation, thermal, Coriolis, or radiometric) and transfer units (e.g., pumps or pressure difference) can be used for this purpose. Additionally, every transfer unit can be applied as a dosing unit (e.g., gear, peristaltic, piston, membrane or excenter pump). For operation on a small scale, the supply is suitably monitored by weighing the storage flasks that contain nutrient or additive solutions in a predetermined concentration.

[0036] As used herein, the “means to transport” individual components of the fermentation medium from the storage flasks to the fermentation vessel includes tubing, piping, and other types of conventional liquid transfer apparatus.

[0037] The device for controlling and maintaining a constant dilution rate in the fermentation vessel is suitably a system containing a measuring instrument that monitors the flow from the storage flasks and a controlling unit, e.g., a computer-software control that calculates the actual mass flow rates, compares them to the desired value, and adjusts the pump setting accordingly. An appropriate system is, e.g., the Process Automation System, National Instruments, Bridge View, USA, for Windows NT 4.0 (represented by National Instruments, Sonnenbergstrasse 53, 5408 Ennetbaden, Switzerland) that is connected to the various operating units (scales, pumps) through a serial-interface box (Rocket Port, Comtrol Europe Ltd, Great Britain, represented by Technosoftware AG Rothackerstrasse 13, 5702 Niederlenz, Switzerland).

[0038] An assembly that can be used in the process of this invention is depicted in FIG. 1. As FIG. 1 shows, the fermentation vessel 1 (Fermentor) is equipped with inlet tubes 2a from storage flasks 2 (e.g., suitably equipped with a stirrer) for supply of salt solution (Salts), nutrient solution (Nutrients), particular substrates (e.g., Substrate 1 and Substrate 2) for supply of, e.g., distinct carbon sources, agents for controlling the pH (Base), water for controlling a constant dilution rate, and antifoam agents. Pumps 3 transport liquids from the storage flasks 2 to the fermentor 1. Scales 4 monitor the amount of liquids supplied to and discharged from the fermentor. Further, the fermentor has inlet tubes 9 for oxygen supply and outlet tubes 10 for exhaust controlled by units 14 and 15, respectively. Pump 6 discharges fermentation broth via outlet tubes 5a to a harvest flask 5. A main controlling unit 7 monitors and steers the overall process. Controlling unit 11 monitors and steers individual control systems 17 for temperature, pH, gas pressure, fermentor content, and supply of antifoam agents. Circuit 12 including pump 13 is used for taking samples from the fermentation broth and for providing a controlled gas flow for moving the fermentation broth. Inlet and outlet gas flow is controlled by flow control 14 and 15. Sterile filters 16 are provided optionally. Optionally, the fermentation vessel 1 is equipped with a thermostating unit 8.

[0039] In the process of the present invention, any protein-producing microorganism either of natural origin, e.g. naturally occurring fungal or bacterial microorganisms or microorganisms which have been transformed by protein encoding DNA whereby such transformed microorganisms can be bacteria, fungi or yeast, preferably from the genus Peniophora, Aspergillus, Hansenula or Pichia, especially Aspergillus niger, Aspergillus awanari, Aspergillus sojae, Aspergillus oryzae, Hansenula polymorpha or Pichia pastoris.

[0040] In this context, the skilled person in the art selects such a protein-producing microorganism which is known to be useful for the production of a desired protein.

[0041] In a preferred embodiment of the present invention the protein has the activity of an enzyme such as catalase, lactase, phenoloxidase, oxidase; oxidoreductase, glucanase cellulase, xylanase and other polysaccharides, peroxidase, lipase, hydrolase, esterase, cutinase, protease and other proteolytic enzymes, aminopeptidase, carboxypeptidase, phytase, lyase, pectinase and other pectinolytic enzymes, amylase, glucosidase, mannosidase, isomerase, invertase, transferase, ribonuclease, chitinase, and desoxyribonuclease. In another preferred embodiment of the present invention, the protein is a therapeutic protein such as an antibody, a vaccine, an antigen, or an antibacterial and/or a health-beneficial protein such as lactoternin, lactoperoxidase or lysozyme.

[0042] It will be understood by those skilled in the art that the term “activity” includes not only native activities referring to naturally occurring enzymes or therapeutic functions, but also those activities or functions which have been modified by amino acid substitutions, deletions, additions or other modifications which may be made to enhance or modify the desired activity, the thermostability, pH tolerance, and/or further properties.

[0043] In a most preferred embodiment of the invention, the selected protein is a protein having the activity of a phytase. Examples of proteins having the activity of a phytase are described in EP 684 313, EP 897 010, EP 897 985 or in Examples 6 to 16 and FIGS. 2-22 of the present invention.

[0044] FIG. 2: Design of the consensus phytase sequence. The letters represent the amino acid residues in the one-letter code. The following sequences were used for the alignment: phyA from Aspergillus terreus 9A-1 (Mitchell et al, 1997; from amino acid (aa) 27), phyA from A. terreus cbs116.46; (van Loon et al., 1998; from aa 27), phyA from Aspergillus niger var. awamori (Piddington et al, 1993; from aa 27), phyA from A. niger T213; Mitchell et al. 1997 from aa 27), phyA from A. niger strain NRRL3135 (van Hartingsveldt et al, 1993; from aa 27), phyA from Aspergillus fumigatus ATCC 13073 (Pasamontes et al, 1997; from aa 25), phyA from A. fumigatus ATCC 32722 (EP 897 985; FIG. 1; from aa 27), phyA from A. fuimigatus ATCC 58128 (EP 897 985; FIG. 1; from aa 27), phyA from A. fumigatus ATCC 26906 (EP 897 985, FIG. 1; from aa 27), phyA from A. fumigatus ATCC 32239 (EP 897 985; FIG. 1; from aa 30), phyA from Emericella nidulans (Pasamontes et al, 1997a; from aa 25), phyA from Talaromyces thermophilus (Pasamontes et al, 1997a; from aa 24), and phyA from Myceliophthora thermophila (Mitchell et al, 1997; from aa 19). As used herein, the phrase “from aaX” means that the sequence used to generate a consensus sequence began at amino acid number X counting from the start codon. The alignment was calculated using the program PILEUP (program menu for the Wisconsin Package, version 8, September 1994, Genetics Computer Group, 575 Science Drive, Madison, Wis., USA 53711; see also Devereux et al., 1984). The location of the gaps was refined by hand. Capitalized amino acid residues in the alignment at a given position belong to the amino acid coalition that establish the consensus residue. In bold, beneath the calculated consensus sequence, the amino acid sequence of the finally constructed consensus phytase (Fcp) is shown. The gaps in the calculated consensus sequence were filled by hand according to principals stated in Example 6.

[0045] FIG. 3: DNA sequence of the consensus phytase-1 gene (fcp) and of the primers used for the gene construction. The calculated amino acid sequence (FIG. 2) was converted into a DNA sequence using the program BACKTRANSLATE (Devereux et al., 1984) and the codon frequency table of highly expressed yeast genes (GCG program package, 9.0). The signal peptide of the phytase from A. terreus cbs.116.46 was fused to the N-terminus. The bold bases represent the sequences of the oligonucleotides used to generate the gene. The names of the respective oligonucleotides are alternately noted above or below the sequence. The underlined bases represent the start and stop codon of the gene. The bases written in italics show the two introduced Eco RI sites.

[0046] FIG. 4: Alignment and consensus sequence of five Basidiomycetes phytases. The letters represent the amino acid residues in the one-letter code. The amino acid sequences of the phytases from Paxillus involutus, phyA1 (from aa 21) and phyA2 (from aa 21, WO 98/28409), Trametes pubescens (from aa 24, WO 98/28409), Agrocybe pediades (from aa 19, WO 98/28409), and Peniophora lycii (from aa 21, WO 98/28409) starting with the amino acid residues mentioned in parentheses, were used for the alignment and the calculation of the corresponding consensus sequence called “Basidio” (Example 7). The alignment was performed by the program PILEUP. The location of the gaps was refined by hand. The consensus sequence was calculated by the program PRETTY from the Sequence Analysis Package Release 9.0 (Devereux et al., 1984). PRETTY prints sequences with their columns alligned and can display a consensus sequence for the alignment. While a vote weight of 0.5 was assigned to the two P. involutus phytases, all other genes were used with a vote weight of 1.0 for the consensus sequence calculation. At positions where the program was not able to determine a consensus residue, the Basidio sequence contains a dash. Capitalized amino acid residues in the alignment at a given position belong to the amino acid coalition that establish the consensus residue.

[0047] FIG. 5: Design of consensus phytase-10 amino acid sequence. Adding the phytase sequence of Thermomyces lanuginosus (Berka et al., 1998) and the consensus sequence of the phytases from five Basidiomycetes (FIG. 4) to the alignment of FIG. 2, an improved consensus sequence was calculated by the program PRETTY. Additionally, the amino acid sequence of A. niger T213 was omitted; therefore, a vote weight of 0.5 was used for the remaining A. niger phytase sequences. For further information see Example 8.

[0048] FIG. 6: DNA and amino acid sequence of consensus phytase-10. The amino acid sequence is written above the corresponding DNA sequences using the one-letter code. The sequence of the oligonucleotides which were used to assemble the gene are in bold letters. The labels of oligonucleotides and the amino acids which were changed compared to those for consensus phytase-1 are underlined. The fcp10 gene was assembled from the following oligonucleotides: CP-1, CP-2, CP-3.10, CP-4.10, CP-5.10, CP-6, CP-7.10, CP-8.10, CP-9.10, CP-10.10, CP-11.10, CP-12.10, CP-13.10, CP-14.10, CP-15.10, CP-16.10, CP-17.10, CP18.10, CP-19.10, CP-20.10, CP-21.10, and CP-22.10. The newly synthesized oligonucleotides are additionally marked by the number 10. The phytase contains the following 32 exchanges relative to consensus phytase-1: Y54F, E58A, D69K, D70G, A94K, N134Q, 1158V, S187A, Q188N, D197N, S204A, T214L, D220E, L234V, A238P, D246H, T251N, Y259N, E267D, E277Q, A283D, R291I, A320V, R329H, S364T, 1366V, A379K, S396A, G404A, Q415E, A437G, A463E. The mutations accentuated in bold letters revealed a stabilizing effect on consensus phytase-1 when tested as single mutations in consensus phytase-1.

[0049] FIG. 7: Alignment for the design of consensus phytase-11. In contrast to the design of consensus phytase-10, for the design of the amino acid sequence of consensus phytase-11, all Basidiomycete phytases (FIG. 4) were used as independent sequences using an assigned vote weight of 0.2 for each Basidiomycete sequence. Additionally, the amino acid sequence of A. niger T213 phytase was used in that alignment, again.

[0050] FIG. 8: DNA and amino acid sequence of consensus phytase-1-thermo[8]-Q50T-K91A. The amino acid sequence is written above the corresponding DNA sequence using the one-letter code. The replaced amino acid residues are underlined. The stop codon of the gene is marked by a star (*).

[0051] FIG. 9: DNA and amino acid sequence of consensus phytase-10-thermo[3]-Q50T-K91A. The amino acid sequence is written above the corresponding DNA sequence using the one-letter code. The replaced amino acid residues are underlined. The stop codon of the gene is marked by a star (*).

[0052] FIG. 10: DNA and amino acid sequence of A. fumigatus ATCC 13073 phytase &agr;-mutant. The amino acid sequence is written above the corresponding DNA sequence using the one-letter code. The replaced amino acid residues are underlined. The stop codon of the gene is marked by a star (*).

[0053] FIG. 11: DNA and amino acid sequence of consensus phytase-7. The amino acids are written above the corresponding DNA sequence using the one-letter code. The sequences of the oligonucleotides used to assemble the gene are in bold letters. Oligonucleotides and amino acids that were exchanged are underlined and their corresponding triplets are highlighted in small cases. The fcp7 gene was assembled from the following oligonucleotides: CP-1, CP-2, CP-3, CP-4.7, CP-5.7, CP-6, CP-7, CP-8.7, CP-9, CP-10.7, CP-11.7, CP-12.7, CP-13.7, CP-14.7, CP-15.7, CP-16, CP-17.7, CP-18.7, CP-19.7, CP-20, CP-21, and CP-22. The newly synthesized oligonucleotides are additionally marked by number 7. The phytase contains the following 24 exchanges in comparison to the original consensus phytase-1: S89D, S92G, A94K, D164S, P201S, G203A, G205S, H212P, G224A, D226T, E255T, D256E, V258T, P265S, Q292H, G300K, Y305H, A314T, S364G, M365I, A397S, S398A, G404A, and A405S.

[0054] FIG. 12: Differential scanning calorimetry (DSC) of consensus phytase-1 and consensus phytase-10. The protein samples were concentrated to about 50-60 mg/ml and extensively dialyzed against 10 mM sodium acetate, pH 5.0. A constant heating rate of 10° C./min was applied up to 95° C. DSC of consensus phytase-10 (12A) yielded a melting temperature of 85.4° C., which is 7.3° C. higher than the melting point of consensus phytase-1 (78.1° C., 12B).

[0055] FIG. 13: Differential scanning calorimetry (DSC) of consensus phytase-1-thermo[3]-Q50T and consensus phytase-10-thermo[3]-Q50T-K91A. The protein samples were concentrated to about 50-60 mg/ml and extensively dialyzed against 10 mM sodium acetate, pH 5.0. A constant heating rate of 10° C./min was applied up to 95° C. DSC of consensus phytase-10-thermo-[3]-Q50T (13A) yielded a melting temperature of 88.6° C., while the melting point of consensus phytase-10-thermo[3]-Q50T-K91A was found at: 89.25° C. (13B).

[0056] FIG. 14: Comparison of the temperature optimum between consensus phytase-1, consensus phytase-10 and consensus phytase-10-thermo[3]-Q50T. For the determination of the temperature optimum, the phytase standard assay was performed at a series of temperatures between 37° C. and 86° C. (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). The diluted supernatant of transformed S. cerevisiae strains was used for the determination. The other components of the supernatant showed no influence on the determination of the temperature optimum: &Dgr;, consensus phytase-1; ⋄, consensus phytase-10; ▪, consensus phytase 10-thermo[3]-Q50T.

[0057] FIG. 15: pH-dependent activity profile and substrate specificity of consensus phytase-10 and its variants thermo[3]-Q50T and thermo[3]-Q50T-K91A. FIG. 15A) shows the pH-dependent activity profile of consensus phytase-10 (□), consensus phytase-10-thermo[3]-Q50T (&Dgr;), and consensus phytase-10-thermo[3]-Q50T-K91A (&Dgr;).The phytase activity was determined using a standard assay in appropriate buffers (see Example 15) at different pH-values (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). FIG. 15B) shows the corresponding substrate specificity tested by replacement of phytate by the indicated compounds in a standard assay; open bars, consensus phytase-10 (white bars, consensus phytase-10-thermo-Q50T; dark bars, consensus phytase-10-thermo-Q50T-K91A). The numbers correspond to the following compounds: 1, phytate; 2, p-nitrophenyl phosphate; 3, phenyl phosphate; 4, fructose-1,6-bisphosphate; 5, fructose-6-phosphate; 6, glucose-6-phosphate; 7, ribose-5-phosphate; 8, DL-glycerol-3-phosphate; 9, glycerol-2-phosphate; 10, 3-phosphoglycerate; 11, phosphoenolpyruvate; 12, AMP; 13, ADP; 14, ATP.

[0058] FIG. 16: pH-dependent activity profile and substrate specificity of consensus phytase-1-thermo[8]-Q50T and of consensus phytase-1-thermo[8]-Q50T-K91A. FIG. 16A) shows the pH-dependent activity profile of the Q50T-(▪) and the Q50T-K91A-variant (&Dgr;). The phytase activity was determined using the standard assay in appropriate buffers (see Example 15) at different pH-values (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). FIG. 16B) shows the corresponding substrate specificities tested by replacement of phytate by the indicated compounds in the standard assay (open bars, consensus phytase-1-thermo[8]-Q50T; filled bars, consensus phytase-1-thermo[8]-Q50T-K91A). The substrates are listed in the legend of FIG. 15.

[0059] FIG. 17: Differential scanning calorimetry (DSC) of consensus phytase-1-thermo[8]-Q50T (FIG. 17A) and consensus phytase-1-thermo[8]-Q50T-K91A (FIG. 17B). The protein samples were concentrated to about 50-60 mg/mT. and extensively dialyzed against 10 mM sodium acetate, pH 5.0. A constant heating rate of 10° C./min was applied up to 95° C. DSC of consensus phytase-1-thermo[8]-Q50T (FIG. 17A) showed a melting temperature of 84.72° C., while the melting point of consensus phytase-1-thermo[8]-Q50T-K91A (FIG. 17B) was found at 85.70° C.

[0060] FIG. 18: Comparison of the temperature optimum between consensus phytase-1, consensus phytase-1-thermo[3] and consensus phytase-1-thermo[8]. For the determination of the temperature optimum, the phytase standard assay was performed at a series of temperatures between 37° C. and 86° C. (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). Purified protein from the supernatant of transformed S. cerevisiae strains was used for the determination. O, consensus phytase-1; □, consensus phytase-1-thermo[3]; &Dgr;, consensus phytase-1-thermo[8].

[0061] FIG. 19: Comparison of the pH-dependent activity profile (FIG. 19A) and substrate specificity (FIG. 19B) of consensus phytase-1, consensus phytase-7, and of the phytase from A. niger NRRL 3135. FIG. 19A) shows the pH-dependent activity profile of consensus phytase-1 (▪), the phytase, from A. niger NRRL 3135 (O), and of consensus phytase-7 (&Dgr;).The phytase activity was determined using the standard assay in appropriate buffers (see Example 15) at different pH-values (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). FIG. 19B) shows the corresponding substrate specificity tested by replacement of phytate by the indicated compounds in the standard assay (black bars, A. niger NRRL 3135 phytase; grey bars, consensus phytase-1, dashed bars, consensus phytase-7). The substrates are listed in the legend of FIG. 15.

[0062] FIG. 20: Differential scanning calorimetry (DSC) of the phytase from A. fumigatus ATCC 13073 (FIG. 20B) and of its stabilized &agr;-mutant (FIG. 20A), which contains the following amino acid exchanges: F55Y, V100I, F114Y, A243L, S265P, N294D.

[0063] The protein samples were concentrated to about 50-60 mg/ml and extensively dialyzed against 10 mM sodium acetate, pH 5.0. A constant heating rate of 10° C./min was applied up to 95° C. DSC of consensus A. fumigatus 13073 phytase (FIG. 20B) revealed a melting temperature of 62.50° C., while the melting point of the &agr;-mutant (FIG. 20A) was found at 67.02° C.

[0064] FIG. 21: Comparison of the temperature optimum of A. fumigatus 13073 wild-type phytase, its &agr;-mutant, and a further stabilized &agr;-mutant (E59A-S126N-R329H-S364T-G404A). For the determination of the temperature optimum, the phytase standard assay was performed at a series of temperatures between 37° C. and 75° C. (see Mitchell et al., 1997, Lehmann et al., 2000 and further references mentioned therein). The diluted supernatants of transformed S. cerevisiae strains were used for the determination. The other components of the supernatant showed no influence on the determination of the temperature optimum. O, A. fumigatus ATCC 13073 phytase; &Dgr;, A. fumigatus ATCC 13073 &agr;-mutant; □, A. fumigatus ATCC 13073 alpha-mutant-59A-S126N-R29H-S364T-G404A)-Q27T; ▪, A. fumigatus ATCC 13073 &agr;-mutant-(E59A-S126N-R329H-S364T-G404A)-Q27T-K68A. The mutations Q51T and K92A in the A. fumigatus a-mutants correspond to −1 Q50T and K91A in consensus phytase, respectively.

[0065] FIG. 22: Amino acid sequence of consensus phytase-12 (consphy12), which contains a number of active site residues transferred from the “basidio” consensus sequence (FIG. 4) to consensus phytase-10-thermo[3]-Q50T-K91A.

[0066] The culture medium used in the fermentation process in accordance with the present invention includes nutrients for the cells or microorganisms such as digestible nitrogen sources and inorganic substances, vitamins, micro- and trace elements and other growth-promoting factors. In addition, the culture medium contains a carbon source. Various organic or inorganic substances may be used as nitrogen sources in the fermentation process, such as nitrates, ammonium salts, yeast extract, meat extract, peptone, casein, cornsteep liquor, amino acids and urea. Typical inorganic substances that can be used in the fermentation are calcium, iron, zinc, nickel, manganese, cobalt, copper, molybdenum, and alkali salts such as chlorides, sulfates and phosphates as well as boric acid. As a carbon source, glycerol or sugar-like mono-, di-, oligo- or polysaccharides, e.g., glucose, fructose, sucrose, maltose, starch, glycogen, cellulose or substrates containing such substances, e.g., molasses, glucose syrups and fructose syrups can be used. The concentration of glucose and/or methanol in the total feed stream may vary from about 10 to about 500 g/l for each component, and is preferably from about 200 to about 300 g/l. While the fermentation medium is principally an aqueous medium, such medium may contain organic solvents such as alcohols, e.g. methanol, ethanol or isopropanol. Further, the fermentation medium may also be a dispersion or suspension, in which case the fermentation is suitably carried out with stirring.

[0067] For continuous operation, the cells are optionally immobilized on a solid porous carrier. Any solid porous carrier with any porosity, size and geometry conventionally used in fermentation processes and exerting no toxic effects on the particular cell or microorganism which is to be immobilized can be used for the purpose of this invention. Examples of such carriers are those made from inorganic material and having a pore diameter of from about 0.5 to about 100 &mgr;m, preferably from about 10 to about 30 &mgr;m diameter. Examples of inorganic materials are ceramics and natural minerals such as steatite, zeolite, bentonite, silicates (glasses), aluminum silicates, aluminum oxide, magnesium aluminum silicates and magnesium aluminum oxides. Such carriers are commercially available, e.g., from Ceramtec, Marktredwitz, Germany, Schott Engineering GmbH, Mainz, Germany and others. Preferably, the carriers are spherical with a mean diameter of from about 0.2 to about 20 mm diameter. The carriers can be loaded with the living cells in a manner known per se by contacting the carrier particles with an appropriate cell culture. If desired, the carrier particles loaded with the cells can be further processed by applying a membrane-type coating layer, such as described in German Offenlegungsschrift DE 3421049. Suitably, the carrier is present in the fermentation vessel on a fixed bed. Further, the culture medium, its components and their containments, respectively are suitably sterilized prior to use if autosterilization (e.g., by methanol, ethanol, ammonia) cannot be guaranteed. Heat sterilization with steam (e.g., at 121° C. and 1 bar pressure for 20 minutes) and filtration (0.2 &mgr;m) for sensitive components are preferred. Alternative sterilization methods may be applied. Media components need not necessarily be sterilized when running the process in continuous mode.

[0068] Depending on the particular cell or organism used, the fermentation may be carried out at a pH between about 2 and about 11. In a preferred aspect of the invention, the fermentation process for the manufacture of phytase is carried out using the microorganism, Hansenula polymorpha transformed by a phytase encoding DNA sequence as described in EP 897 010, EP 897 985, or Example 11 of the present case. According to that particular aspect of the invention, the preferred carbon source is a mixture of glucose and methanol. Further, in accordance with that particular aspect of the invention, the fermentation may be carried out at a pH between about 4 and 5, preferably at about pH 4.6. A preferred temperature range for carrying out such fermentation process is between about 10° C. and 50° C., more preferably the fermentation temperature is about 30° C. The aeration rate is preferably adjusted to between about 0.01 and about 1.5 volume of gas per volume of liquid with a dissolved oxygen concentration (DO) of between 0.01% and about 500%. A DO of 100% denotes oxygen saturation of the solution at atmospheric pressure (1 bar) and reactor temperature. The fermentation can be carried out at a pressure of from about 0.1 to about 100 bar, preferably, the fermentation is carried out at atmospheric pressure, i.e., at about 1 bar. The dilution rate can vary from about 0.001 to about 0.5 per hour.

[0069] The following examples are provided to further illustrate the process of the present invention. These examples are illustrative only and are not intended to limit the scope of the invention in any way.

EXAMPLES

Example 1

[0070] Storage solutions for feed medium were prepared as follows: 1 1.1 CaCl2/H3BO3 Solution CaCl2.2H2O  18.75 g/l H3BO3 0.0125 g/l

[0071] This solution was sterilized at 121° C. for 20 minutes. 2 1.2 Microelements Solution (NH4)2Fe(SO4)2.6H2O  2.5 g/l CuSO4.5H2O  0.2 g/l ZnSO4.7H2O 0.75 g/l MnSO4.5H2O  1.0 g/l Na-EDTA  2.5 g/l

[0072] This solution was sterilized at 121° C. for 20 minutes. 3 1.3 Trace Elements Solution NiSO4.6H2O 0.025 g/l CoCl2.6H2O 0.025 g/l Na2MoO4.2H2O 0.025 g/l KI 0.025 g/l

[0073] This solution was sterilized at 121° C. for 20 minutes. 4 1.4 Salts + Vitamin Solution KH2PO4 50.0 g/l NH4H2PO4 100.0 g/l MgSO4.7H2O 45.0 g/l (NH4)2SO4 50.0 g/l KCl 23.0 g/l NaCl 5.0 g/l vitamin solution 5.0 ml/l

[0074] (D-biotin, 600 mg/l and thiamin.HCl 200 g/l in 50% isopropanol/water)

[0075] The vitamin solution was sterilized by filtration (0.2 &mgr;m), and added to the salt solution that was sterilized at 121° C. for 20 minutes.

[0076] 1.5 Glucose Solution

[0077] 770 g of D-glucose.H2O were dissolved in 480 g of water and sterilized (121° C., 20 minutes) to yield a 1 liter solution containing 57% (by weight) of D-glucose.

[0078] 1.6 Methanol

[0079] Pure methanol was assumed to be sterile and poured into a sterilized flask.

[0080] 1.7 Antifoam

[0081] A sterilized (121° C., 20 minutes) solution of 10 antifoam (STRUKTOL J 673, Schill & Seilacher, Hamburg, Germany) was provided for supply on demand by foam-control.

[0082] 1.8 Base

[0083] A solution of about 12.5% (by weight) of ammonia in sterile water was poured into a sterilized flask.

EXAMPLE 2

[0084] A fixed bed bioreactor (1 liter) was set up following the principle illustrated in FIG. 1 with individual storage flasks provided for solutions 1.1 to 1.8 of Example 1. The fixed bed of porous steatite spheres (4 mm diameter, pore diameter 10-30 &mgr;m, 280 pores per ml, CeramTec, Marktredwitz, Germany) was contained by a sieve plate at the top. The reactor was sterilized (121° C., 20 minutes), and thereafter filled with an inoculum culture of Hansenula polymorpha transformed with a phytase encoding DNA as described, e.g. in EP 897 010, EP 897 985 or Example 11. EP 897010 and EP 897985 are incorporated by reference as if recited in full herein. Then the connection to the storage flasks was established. The inoculum culture was grown on a medium containing glycerol as a carbon source instead of glucose. The reactor was switched to batch operation until all glycerol was consumed, which was determined by a rise of the dissolved oxygen concentration. Then the feed stream was turned on and the fermentation was run under process conditions as given below: 5 Temperature 30° C. pH 4.6 Diluted oxygen concentration 52-62 % oxotal 105 N/m2 PO2 105 N/m2 Dilution rate 0.0067 h−1 Aeration rate 100 ml/min Vfluid 1190 ml−1 Vfixed bed 950 ml−1

[0085] Substrate composition as provided by storage flasks 1-8; (actual concentrations in feed stream given): 6 D-glucose  305 g/l Methanol  264 g/l CaCl2/H3BO3 Solution 12.2 g/l Microelement Solution 20.9 g/l Trace Element Solution 17.2 g/l Salts + vitamin Solution 44.7 g/l

[0086] Analytics:

[0087] Bio-Rad Protein Assay Kit I (Bio-Rad, Glattbrugg, Switzerland) was used to determine the total protein concentration. A factor for the calculation of phytase concentration (cphyt) from total protein concentration (ctp) was determined as Cphyt=0.76 ctp.

[0088] To determine the biomass in the medium two samples of 1 ml were centrifuged, washed with 1 ml of water, centrifuged again, dried at 85° C. for two days and weighed.

[0089] Results:

[0090] Under the above process conditions, the biomass was 59 g/l. Given a dilution rate of 0.0067 per hour the productivity was 0.078 g of phytase per liter per hour.

[0091] In a fermentation that was run fed-batch-wise, the biomass was 125 g/l; the productivity, however, was calculated to 0.054 g phytase per liter per hour.

Example 3

[0092] A fermentation was carried out as set forth in Example 2 but omitting the steatite spheres (i.e., without immobilization of the microorganism). A nutrient and a salt and vitamin solution of the following composition were pumped into the reactor separately: 7 Nutrient Solution: NiSO4.6H2O 8.33 mg/l CoCl26.H2O 8.33 mg/l Na2MoO4.2H2O 8.33 mg/l KI 8.33 mg/l (NH4)2Fe(SO4)2.6H2O 833.33 mg/l CuSO 66.67 mg/l ZnSO4.7H2O 250 mg/l MnSO4.5H2O 333.33 mg/l Na-EDTA 833.33 mg/l CaCl2.2H2O 6250 mg/l H3BO3 4.17 mg/l

[0093] 8 Salts + Vitamins Solution: KH4PO4 50.0 g/l NH4H2PO4 100.0 g/l MgSO4.7H2O 45.0 g/l (NH4)2Fe(SO4) 50.0 g/l KCl 23.0 g/l NaCl 5.0 g/l vitamin solution 5.0 ml/l

[0094] (D-biotin, 600 mg/l and thiamin.HCl 200 g/l in 50% isopropanol/water)

[0095] The supply of these two solutions was adjusted to provide in the feed stream a concentration of 51 g/l of the Nutrient Solution and 61 g/l of the Salts+Vitamins Solution. The dilution rate was adjusted to 0.009 h−1. The pH was kept at 4.6 by addition of 12.5 wt % ammonium hydroxide. Glucose Solution as in Example 1 and methanol were fed into the reactor separately to maintain a glucose concentration of 275 g/l and a methanol concentration of 260 g/l in the feed stream.

[0096] The productivity of this fermentation was 0.088 g phytase per liter per hour. Biomass in outflow was 58 g/l.

Example 4

[0097] A fermentation process as set forth in Example 3 was carried out, but adjusting glucose concentration to 290 g/l and methanol concentration to 260 g/l, and keeping the dilution rate constant at 0.009 h−1, the productivity was 0.092 g phytase per liter per hour. Biomass in outflow was 60.4 g/l.

Example 5

[0098] A fermentation process as set forth in Example 3 was carried out, but adjusting glucose concentration to 270 g/l and methanol concentration to 280 g/l, and keeping the dilution rate constant at 0.009 h−1, the productivity was 0.094 g phytase per liter per hour. Biomass in outflow was 56.8 g/l.

Example 6

Design of the Amino Acid Sequence of Consensus Phytase-1

[0099] Alignment of the Amino Acid Sequences

[0100] The alignment was calculated using the program PILEUP from the GCG Sequence Analysis Package Release 9.0 (Devereux et al., 1984) with the standard parameters (gap creation penalty 12, gap extension penalty 4). The location of the gaps was refined using a text editor. Table 1 shows the sequences (see FIG. 2), without the signal sequence, that were used for the performance of the alignment starting with the amino acid (aa) as mentioned in Table 1, e.g., “aa 27” means that the alignment began at the 27 amino acid from the start codon. 9 TABLE 1 Origin and vote weight of the phytase amino acid sequences used for the design of consensus phytase-1 phyA from Aspergillus terreus 9A-1, aa 27, vote weight 0.5 (Mitchell et al., 1997) phyA from Aspergillis terreus cbs 116.46, aa 27, vote weight 0.5 (EP 897 985; HG. 1) phyA from Aspergillus niger var. awamori, aa 27, vote weight 0.33 (Piddington et al., 1993) phyA from Aspergillus niger T213, aa 27, vote weight 0.33 phyA from Aspergillus niger strain NRRL3135, aa 27, vote weight 0.33 (van Hartingsveldt et al., 1993) phyA from Aspergillus fumigatus ATCC 13073, aa 26, vote weight 0.2 (Pasamontes et al., 1997) phyA from Aspergillus fumigatus ATCC 32722, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 58128, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 26906, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 32239, aa 30, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Emericella nidulans, aa 25, vote weight 1.0 (Pasamontes et al., 1997a) phyA from Talaromyces thermophilus ATCC 20186, aa 24, vote weight 1.0 (Pasamontes et al., 1997a) phyA from Myceliophthora thermophila, aa 19, vote weight 1.0 (Mitchell et al., 1997)

[0101] Calculation of the Amino Acid Sequence of Consensus Phytase-1

[0102] Using the refined alignment as input, the consensus sequence was calculated by the program PRETTY from the GCG Sequence Analysis Package Release 9.0 (Devereux et al., 1984). PRETTY prints sequences with their columns aligned and can display a consensus sequence for an alignment. A vote weight that pays regard to the similarity between the amino acid sequences of the aligned phytases was assigned to all sequences. The vote weight was set in such a way that the combined impact of all phytases from one sequence subgroup (same species, but from different strains), e.g. the amino acid sequences of all phytases from A. fumigatus, on the election was set one, that means that each sequence contributes a value of 1 divided by the number of strain sequences (see Table 1). By this means, it was possible to prevent very similar amino acid sequences, e.g. of the phytases from different A. fumigatus strains, from dominating the calculated consensus sequence.

[0103] The program PRETTY was started with the following parameters: The plurality defining the number of votes below which there is no consensus was set on 2.0. The threshold, which determines the scoring matrix value below which an amino acid residue may not vote for a coalition of residues, was set on 2. PRETTY used the PrettyPep.Cmp consensus scoring matrix for peptides.

[0104] Ten positions of the alignment (positions 46, 66, 82, 138, 162, 236, 276, 279, 280, 308; FIG. 2), for which the program was not able to determine a consensus residue, were filled by hand according to the following rules: if a most frequent residue existed, this residue was chosen (positions 138, 236, 280); if a prevalent group of similar equivalent residues occurred, the most frequent or, if not available, one residue of this group was selected (positions 46, 66, 82, 162, 276, 308). If there was neither a prevalent residue nor a prevalent group, one of the occurring residues was chosen according to common assumptions on their influence on the protein stability (position 279). Eight other positions (positions 132, 170, 204, 211, 275, 317, 384, 447; FIG. 2) were not filled with the amino acid residue selected by the program but normally with amino acids that occur with the same frequency as the residues that were chosen by the program. In most cases, the slight underrating of the three A. niger sequences (sum of the vote weights: 0.99) was eliminated by this correction.

[0105] Conversion of the Consensus Phytase-1 Amino Acid Sequence to a DNA Sequence

[0106] The first 26 amino acid residues of the A. terreus cbs116.46 phytase were used as a signal peptide and, therefore, fused to the N-terminus of all consensus phytases. For this stretch, we used a special method to calculate the corresponding DNA sequence. Purvis et al (1987) proposed that the incorporation of rare codons in a gene has an influence on the folding efficiency of the protein. The DNA sequence for the signal sequence was calculated using the approach of Purvis et al (1987), which is hereby incorporated by reference as if recited in full herein, and optimized for expression in S. cerevisiae. For the remaining parts of the protein, we used the codon frequency table of highly expressed S. cerevisiae genes, obtained from the GCG program package, to translate the calculated amino acid sequence into a DNA sequence.

[0107] The resulting sequence of the fcp gene is shown in FIG. 3.

[0108] Construction and Cloning of the Consensus Phytase-1 Gene

[0109] The calculated DNA sequence of consensus phytase-1 (fcp) was divided into oligonucleotides of 85 bp, alternately using the sequence of the sense and the anti-sense strand. Every oligonucleotide overlaps 20 bp with its previous and its following oligonucleotide of the opposite strand. The location of all primers, purchased from Microsynth, Balgach (Switzerland) and obtained in a PAGE-purified form, is indicated in FIG. 3.

[0110] PCR-Reactions

[0111] In three PCR reactions, the synthesized oligonucleotides were composed to the entire gene. For the PCR, the High Fidelity Kit from Boehringer Mannheim (Boehringer Mannheim, Germany) and the thermo cycler The Protokol (TM) from AMS Biotechnology (Europe) Ltd. (Lugano, Switzerland) were used.

[0112] Oligonucleotides CP-1 to CP-10 (Mix 1, FIG. 3) were mixed to a concentration of 0.2 pmol/&mgr;l of each oligonucleotide. A second oligonucleotide mixture (Mix 2) was prepared with CP-9 to CP-22 (0.2 pmol/&mgr;l of each oligonucleotide). Additionally, four short primers were used in the PCR reactions: 10                Eco RI CP-a: 5′-TATATGAATTCATGGGCGTGTTCGTC-3′ (SEQ ID No. 1) CP-b: 5′-TGAAAAGTTCATTGAAGGTTTC-3′ (SEQ ID No. 2) CP-c: 5′-TCTTCGAAAGCAGTACAAGTAC-3′ (SEQ ID No. 5)                 Eco RI CP-e: 5′-TATATGAATTCTTAAGCGAAAC-3′ (SEQ ID No. 4)

[0113] 11 PCR reaction a: 10 &mgr;l Mix 1 (2.0 pmol of each oligonucleotide) 2 &mgr;l nucleotides (10 mM each nucleotide) 2 &mgr;l primer CP-a (10 pmol/&mgr;l) 2 &mgr;l primer CP-c (10 pmo/&mgr;l) 10.0 &mgr;l PCR buffer 0.75 &mgr;l polymerase mixture (2.6 U) 73.25 &mgr;l H2O PCR reaction b: 10 &mgr;l Mix 2 (2.0 pmol of each oligonucleotide) 2 &mgr;l nucleotides (10 mM each nucleotide) 2 &mgr;l primer CP-b (10 pmol/&mgr;l) 2 &mgr;l primer CP-e (10 pmol/&mgr;l) 10.0 &mgr;l PCR buffer 0.75 &mgr;l polymerase mixture (2.6 U) 73.25 &mgr;l H2O

[0114] Reaction conditions for PCR reactions a and b: 12 step 1  2 minutes - 45° C. step 2 30 seconds - 72° C. step 3 30 seconds - 94° C. step 4 30 seconds - 52° C. step 5  1 minute - 72° C.

[0115] Steps 3 to 5 were repeated 40 times.

[0116] The PCR products (670 and 905 bp) were purified by an agarose gel electrophoresis (0.9% agarose) and subsequently subjected to gel extraction (QIAEX II Gel Extraction Kit, Qiagen, Hilden, Germany). The purified DNA fragments were used for the PCR reaction c. 13 PCR reaction C: 6 &mgr;l PCR product of reaction a (≈50 ng) 6 &mgr;l PCR product of reaction b (≈50 ng) 2 &mgr;l primer CP-a (10 pmol/&mgr;l) 2 &mgr;l primer CP-e (10 pmol/&mgr;l) 10.0 &mgr;l PCR buffer 0.75 &mgr;l polymerase mixture (2.6 U) 73.25 &mgr;l H2O

[0117] Reaction conditions for PCR reaction c: 14 step 1  2 minutes - 94° C. step 2 30 seconds - 94° C. step 3 30 seconds - 55° C. step 4  1 minutes - 72° C.

[0118] Steps 2 to 4 were repeated 31-times.

[0119] The resulting PCR product (1.4 kb) was purified as mentioned above, digested with Eco RI, and ligated in an Eco RI-digested and dephosphorylated pBsk(−)-vector (Stratagene, La Jolla, Calif., USA). 1 &mgr;l of the ligation mixture was used to transform E. coli XL-1 competent cells (Stratagene, La Jolla, Calif., USA). All standard procedures were carried out as described by Sambrook et al. (1987). The DNA sequence of the constructed consensus phytase gene (fcp, FIG. 3) was controlled by sequencing as known in the art.

Example 7

Design of an Improved Consensus Phytase (Consensus Phytase-10) Amino Acid Sequence

[0120] The alignments used for the design of consensus phytase-10 were calculated using the program PILEUP from the GCG Sequence Analysis Package Release 9.0 (Devereux et al., 1984) with the standard parameters (gap creation penalty 12, gap extension penalty 4). The location of the gaps was refined using a text editor.

[0121] The following sequences were used for the alignment of the Basiodiomycete phytases starting with the amino acid (aa) mentioned in Table 2: 15 TABLE 2 Origin and vote weight of five Basidiomycete phytases used for the calculation of the corresponding amino acid consensus sequence (basidio) phyA1 from Paxillus involutus NN005693, aa 21, vote weight 0.5 (WO 98/28409) phyA2 from Paxillus involutus NN005693, aa 21, vote weight 0.5 (WO 98/28409) phyA from Trametes pubescens NN9343, aa 24, vote weight 1.0 (WO 98/28409) phyA from Agrocybe pediades NN009289, aa 19, vote weight 1.0 (WO 98/28409) phyA from Peniophora lycii NN006113, aa 21, vote weight 1.0 (WO 98/28409)

[0122] The alignment is shown in FIG. 4.

[0123] In Table 3 the genes, which were used for the performance of the final alignment, are arranged. The first amino acid (aa) of the sequence, which is used in the alignment is mentioned behind the organism's designation. 16 TABLE 3 Origin and vote weight of the phytase sequences used for the design of consensus phytase 10 phyA from Aspergillus terreus 9A-1, aa 27, vote weight 0.5 (Mitchell et al., 1997) phyA from Aspergillus terreus cbs116.46, aa 27, vote weight 0.5 (EP 897 985; FIG. 1) phyA from Aspergillus niger var. awamori, aa 27, vote weight 0.5 (Piddington et al., 1993) phyA from Aspergillus niger strain NRRL3135, aa 27, vote weight 0.5 (van Hartingsveldt et al., 1993) phyA from Aspergillus fumigatus ATCC 13073, aa 26, vote weight 0.2 (Pasamontes et al., 1997) phyA from Aspergillus fumigatus ATCC 32722, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 58128, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 26906, aa 26, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Aspergillus fumigatus ATCC 32239, aa 30, vote weight 0.2 (EP 897 985; FIG. 1) phyA from Emericella nidulans, aa 25, vote weight 1.0 (Pasamontes et al., 1997a) phyA from Talaromyces thermophilus ATCC 20186, aa 24, vote weight 1.0 (Pasamontes et al., 1997a) phyA from Myceliopthora thermophila, aa 19, vote weight 1.0 (Mitchell et al., 1997) phyA from Thermomyces lanuginosa, aa 36, vote weight 1.0 (Berka et al., 1998) Consensus sequence of five Basidiomycete phytases, vote weight 1.0 (Basidio, FIG. 4)

[0124] The corresponding alignment is shown in FIG. 5.

[0125] Calculation of the Amino Acid Sequence of Consensus Phytase-10

[0126] To improve the alignment, we combined the consensus sequence of five phytases from four different Basidiomycetes, called Basidio, still containing the undefined sequence positions (see FIG. 4), nearly all phytase sequences used for calculation of the original consensus phytase, and one new phytase sequence from the Ascomycete Thermomyces lanuginosus to a larger alignment. We set plurality on 2.0 and threshold on 3. The vote weights used are listed in Table 3. The alignment and the corresponding consensus sequence are presented in FIG. 5. The new consensus phytase-10 sequence has 32 different amino acids in comparison to the original consensus phytase (consensus phytase-1). Positions for which the program PRETTY was not able to calculate a consensus amino acid residue were filled according to rules mentioned in Example 6. None of the residues suggested by the program was replaced.

[0127] We included all Basidiomycete phytases as single amino acid sequences but assigning a vote weight of 0.2 in the alignment. The corresponding alignment is shown in FIG. 7. he calculated consensus amino acid sequence (consensus phytase-11) has the following differences to the sequence of consensus phytase-10: D35X, X(K)69K, X(E)100E, A101R, Q134N, X(K)153N, X(H)190H, X(A)204S, X(E)220D, E222T, V227A, X(R)271R, H287A, X(D)288D, X(K)379K, X(I)3891, E390X, X(E)415E, X(A)416A, X(R)446L, E463A, where the numbering is as in FIG. 6.

[0128] As used herein, “X” means that the program was not able to calculate a consensus amino acid; the amino acid in parenthesis corresponds to the amino acid finally included in the consensus phytase-10.

[0129] We also checked single amino acid replacements suggested by the improved consensus phytase sequences 10 and 11 on their influence on the stability of the original consensus phytase-1. The approach is described in Example 8.

[0130] Conversion of Consensus Phytase-0 Amino Acid Sequence to a DNA Sequence

[0131] The first 26 amino acid residues of A. terreus cbs116.46 phytase were used as a signal peptide and, therefore, fused to the N-terminus of consensus phytase-10. The procedure used is further described in Example 6.

[0132] The resulting sequence of the fcp10 gene is shown in FIG. 6.

[0133] Construction and Cloning of the Consensus Phytase-10 Gene (fcp10)

[0134] The calculated DNA sequence of fcp10 was divided into oligonucleotides of 85 bp, alternately using the sequence of the sense and the anti-sense strand. Every oligonucleotide overlaps 20 bp with its previous and its following oligonucleotide of the opposite strand. The location of all primers, purchased from Microsynth, Balgach (Switzerland) and obtained in a PAGE-purified form, is indicated in FIG. 6.

[0135] PCR-Reactions

[0136] In three PCR reactions, the synthesized oligonucleotides were composed to the entire gene. For the PCR, the High Fidelity Kit from Boehringer Mannheim (Boehringer Mannheim, Mannheim; Germany) and the thermocycler The Protokol™ from AMS Biotechnology (Europe) Ltd. (Lugano, Switzerland) were used. The following oligonucleotides were used in a concentration of 0.2 pmol/ml.

[0137] Mix 1.10: CP-1, CP-2, CP-3.10, CP-4.10, CP-5.10, CP-6, CP-7.10, CP-8.10, CP-9.10, CP-10.10

[0138] Mix 2.10: CP-9.10, CP-10.10, CP-11.10, CP-12.10, CP-13.10, CP-14.10, CP-15.10, CP-16.10, CP-17.10, CP-18.10, CP-19.10, CP-20.10, CP-21.10, CP-22.10

[0139] The newly synthesized oligonucleotides are marked by number 10. The phytase contains the following 32 exchanges, which are underlined in FIG. 6, in comparison to the original consensus phytase-1: Y54F, E58A, D69K, D70G, A94K, N134Q, I158V, S187A, Q188N, D197N, S204A, T214L, D220E, L234V, A238P, D246H, T251N, Y259N, E267D, E277Q, A283D, R291I, A320V, R329H, S364T, 1366V, A379K, S396A, G404A, Q415E, A437G, A463E.

[0140] Four short PCR primers were used for the assembling of the oligonucleotides: 17      Eco RI CP-a: 5′-TATATGAATTCATGGGCGTGTTCGTC-3′ (SEQ ID No. 1) CP-b: 5′-TGAAAAGTTCATTGAAGGTTTC-3′ (SEQ ID No. 2) CP-c.10: 5′-TCTTCGAAAGCAGTACACAAAC-3′ (SEQ ID No. 5)      Eco RI CP-e: 5′-TATATGAATTCTTAAGCGAAAC-3′ (SEQ ID No. 4)

[0141] 18 PCR reaction a: 10 &mgr;l Mix 1.10 (2.0 pmol of each oligonucleotide) 2 &mgr;l nucleotides (10 mM each nucleotide) 2 &mgr;l primer CP-a(10 pmol/ml) 2 &mgr;l primer CP-c.10 (10 pmol/ml) 10.0 &mgr;l PCR buffer 0.75 &mgr;l polymerase mixture (2.6 U) 73.25 &mgr;l H2O PCR reaction b: 10 &mgr;l Mix 2.10 (2.0 pmol of each oligonucleotide) 2 &mgr;l nucleotides (10 mM each nucleotide) 2 &mgr;l primer CP-b (10 pmol/ml) 2 &mgr;l primer CP-e (10 pmol/ml) 10.0 &mgr;l PCR buffer 0.75 &mgr;l polymerase mixture (2.6 U) 73.25 &mgr;l H2O

[0142] Reaction conditions for PCR reactions a and b: 19 step 1  2 minutes - 45° C. step 2 30 seconds - 72° C. step 3 30 seconds - 94° C. step 4 30 seconds - 52° C. step 5  1 minutes - 72° C.

[0143] Steps 3 to 5 were repeated 40 times.

[0144] The PCR products (670 and 905 bp) were purified by an agarose gel electrophoresis (0.9% agarose) subsequently followed by gel extraction (QIAEX II Gel Extraction Kit, 2 Qiagen, Hilden, Germany). The purified DNA fragments were used for the PCR reaction c.

[0145] PCR reaction c:

[0146] 6 &mgr;l PCR product of reaction a (≈50 ng)

[0147] 6 &mgr;l PCR product of reaction b (≈50 ng)

[0148] 2 &mgr;l primer CP-a (10 pmol/ml)

[0149] 2 &mgr;l primer CP-e (10 pmol/ml).

[0150] 10.0 &mgr;l PCR buffer

[0151] 0.75 &mgr;l polymerase mixture (2.6 U)

[0152] 73.25 &mgr;l H2O

[0153] Reaction conditions for PCR reaction c: 20 step 1  2 minutes - 94° C. step 2 30 seconds - 94° C. step 3 30 seconds - 55° C. step 4  1 minute - 72° C.

[0154] Steps 2 to 4 were repeated 31 times.

[0155] The resulting PCR product (1.4 kb) was purified as mentioned above, digested with Eco RI, and ligated in an Eco RI-digested and dephosphorylated pBsk(−)-vector (Stratagene, La Jolla, Calif., USA). 1 &mgr;l of the ligation mixture was used to transform E. coli XL-1 competent cells (Stratagene, La Jolla, Calif., USA). All standard procedures were carried out as described by Sambrook et al. (1987). The DNA sequence of the constructed gene (fcp10) was checked by sequencing as known in the art.

Example 8

Increasing the Thermostability of Consensus Phytase-1 by Introduction of Single Mutations Suggested by the Amino Acid Sequence of Consensus Phytase-10 and/or Consensus Phytase-11

[0156] To increase the thermostability of homologous genes, it is also possible to test the stability effect of each differing amino acid residue between the protein of interest and the calculated consensus sequence, and to combine all stabilizing mutations into the protein of interest. We used the consensus phytase-1 as the protein of interest, and tested the effect on the protein stability of 34 amino acids, which differed between consensus phytase-1 on one hand and consensus phytases-10 and/or -11 on the other hand, by single mutation.

[0157] To construct muteins for expression in A. niger, S. cerevisiae, or H. polymorpha, the corresponding expression plasmid containing the consensus phytase gene was used as template for site-directed mutagenesis (see Examples 11-13). Mutations were introduced using the “quick exchange™ site-directed mutagenesis kit” from Stratagene (La Jolla, Calif., USA) following the manufacturer's protocol, and using the corresponding primers. All mutations made and their corresponding primers are summarized in Table 4. Plasmids harboring the desired mutation were identified by DNA sequence analysis as known in the art. 21 TABLE 4 Primers used for site-directed mutagenesis of consensus phytases (Exchanged bases are highlighted in bold. The introduction of a restriction site is marked above the sequence. When a restriction site is written in parenthesis, the mentioned site was destroyed by introduction of the mutation.) mutation Primer set             Kpn I Q50T 5′-CACTTGTGGGGTACCTACTCTCCATACTTCTC-3′ (SEQ ID No. 6) 5′-GAGAAGTATGGAGAGTAGGTACCCCACAAGTG-3′ (SEQ ID No. 7) Y54F 5′-GGTCAATACTCTCCATTCTTCTCTTTGGAAG-3′ (SEQ ID No. 8) 5′-CTTCCAAAGAGAAGAATGGAGAGTATTGACC-3′ (SEQ ID No. 9) E58A 5′-CATACTTCTCTTTGGCAGACGAATCTGC-3′ (SEQ ID No. 10) 5′-GCAGATTCGTCTGCCAAAGAGAAGTATG-3′ (SEQ ID No. 11)                            Aat II D69K 5′-CTCCAGACGTCCCAAAGGACTGTAGAGTTAC-3′ (SEQ ID No. 12) 5′-GTAACTCTACAGTCCTTTGGGACGTCTGGAG-3′ (SEQ ID No. 13)                            Aat II D70G 5′-CTCCAGACGTCCCAGACGGCTGTAGAGTTAC-3′ (SEQ ID No. 14) 5′-GTAACTCTACAGCCGTCTGGGACGTCTGGAG-3′ (SEQ ID No. 15) K91A 5′-GATACCCAACTTCTTCTGCGTCTAAGGCTTACTCTG-3′ (SEQ ID No. 16) 5′-CAGAGTAAGCCTTAGACGCAGAAGAAGTTGGGTATC-3′ (SEQ ID No. 17)                                Sca I A94K 5′-CTTCTAAGTCTAAGAAGTACTCTGCTTTG-3′ (SEQ ID No. 18) 5′-CAAAGCAGAGTACTTCTTAGACTTAGAAG-3′ (SEQ ID No. 19) A101R 5′-GCTTACTCTGCTTTGATTGAACGGATTCAAAAGAACGCTAC-3′ (SEQ ID No. 20) 5′-GTAGCGTTCTTTTGAATCCGTTCAATCAAAGCAGAGTAAGC-3′ (SEQ ID No. 21) N134Q 5′-CCATTCGGTGAACAGCAAATGGTTAACTC-3′ (SEQ ID No. 22) 5′-GAGTTAACCATTTGCTGTTCACCGAATGG-3′ (SEQ ID No. 23)                               Nru I K153N 5′-GATACAAGGCTCTCGCGAGAAACATTGTTC-3′ (SEQ ID No. 24) 5′-GGAACAATGTTTCTCGCGAGAGCCTTGTATC-3′ (SEQ ID No. 25)                               Bss HI I158V 5′-GATTGTTCCATTCGTGCGCGCTTCTGGTTC-3′ (SEQ ID No. 26) 5′-GAACCAGAAGCGCGCACGAATGGAACAATC-3′ (SEQ ID No. 27)                                 Bcl I D197N 5′-CTCCAGTTATTAACGTGATCATTCCAGAAGG-3′ (SEQ ID No. 28) 5′-CCTTCTGGAATGATCACGTTAATAACTGGAG-3′ (SEQ ID No. 29)                            Apa I S187A 5′-GGCTGACCCAGGGGCCCAACCACACCAAGC-3′ (SEQ ID No. 30) 5′-GCTTGGTGTGGTTGGGCCCCTGGGTCAGCC-3′ (SEQ ID No. 31)                             Nco I T214L 5′-CACTTTGGACCATGGTCTTTGTACTGCTTTCG-3′ (SEQ ID No. 32) 5′-CGAAAGCAGTACAAAGACCATGGTCCAAAGTG-3′ (SEQ ID No. 33)                                  Avr II E222T 5′-GCTTTCGAAGACTCTACCCTAGGTGACGACGTTG-3′ (SEQ ID No. 34) 5′-CAACGTCGTCACCTAGGGTAGAGTCTTCGAAAGC-3′ (SEQ ID No. 35) V227A 5′-GGTGACGACGCTGAAGCTAACTTCAC-3′ (SEQ ID No. 36) 5′-GTGAAGTTAGCTTCAGCGTCGTCACC-3′ (SEQ ID No. 37)                            Sac II L234V 5′-CTAACTTCACCGCGGTGTTCGCTCCAG-3′ (SEQ ID No. 38) 5′-CTGGAGCGAACACCGCGGTGAAGTTAG-3′ (SEQ ID No. 39) A238P 5′-GCTTTGTTCGCTCCACCTATTAGAGCTAGATTGG-3′ (SEQ ID No. 40) 5′-CCAATCTAGCTCTAATAGGTGGAGCGAACAAAGC-3′ (SEQ ID No. 41)                          Hpa I T251N 5′-GCCAGGTGTTAACTTGACTGACGAAG-3′ (SEQ ID No. 42) 5′-TTCGTCAGTCAAGTTAACACCTGGC-3′ (SEQ ID No. 43)                          Aat II Y259N 5′-GACGAAGACGTCGTTAACTTGATGGAC-3′ (SEQ ID No. 44) 5′-GTCCATCAAGTTAACGACGTCTTCGTC-3′ (SEQ ID No. 45)                            Asp I E267D 5′-GTCCATTCGACACTGTCGCTAGAACTT C-3′ (SEQ ID No. 46) 5′-GAAGTTCTAGCGACAGTGTCGAATGGAC-3′ (SEQ ID No. 47) E277Q 5′-CTGACGCTACTCAGCTGTCTCCATTC-3′ (SEQ ID No. 48) 5′-GAATGGAGACAGCTGAGTAGCGTCAG-3′ (SEQ ID No. 49) A283D 5′-GTCTCCATTCTGTGATTTGTTCACTCAC-3′ (SEQ ID No. 50) 5′-GTGAGTGAACAAATCACAGAATGGAGAC-3′ (SEQ ID No. 51)                           Ksp I H287A 5′-GCTTTGTTCACCGCGGACGAATGGAG-3′ (SEQ ID No. 52) 5′-CTCCATTCGTCCGCGGTGAACAAAGC-3′ (SEQ ID No. 53)                           Bam HI R291I 5′-CACGACGAATGGATCCAATACGACTAC-3′ (SEQ ID No. 54) 5′-GTAGTCGTATTGGATCCATTCGTCGTG-3′ (SEQ ID No. 55)                             Bsi WI Q292A 5′-GACGAATGGAGAGCGTACGACTACTTG-3′ (SEQ ID No. 56) 5′-CAAGTAGTCGTACGCTCTCCATTCGTC-3′ (SEQ ID No. 57)                              Hpa I A320V 5′-GGTGTTGGTTTCGTTAACGAATTGATTGC-3′ (SEQ ID No. 58) 5′-GCAATCAATTCGTTAACGAAACCAACACC-3′ (SEQ ID No. 59)                             (Bgl II) R329H 5′-GCTAGATTGACTCACTCTCCAGTTCAAG-3′ (SEQ ID No. 60) 5′-CTTGAACTGGAGAGTGAGTCAATCTAGC-3′ (SEQ ID No. 61)                                 Eco RV S364T 5′-CTCACGACAACACTATGATATCTATTTTCTTC-3′ (SEQ ID No. 62) 5′-GAAGAAAATAGATATCATAGTGTTGTCGTGAG-3′ (SEQ ID No. 63)                            Nco I I366V 5′-CGACAACTCCATGGTTTCTATTTTCTTCGC-3′ (SEQ ID No. 64) 5′-GCGAAGAAAATAGAAACCATGGAGTTGTCG-3′ (SEQ ID No. 65)                         Kpn I A379K 5′-GTACAACGGTACCAAGCCATTGTCTAC-3′ (SEQ ID No. 66) 5′-GTAGACAATGGCTTGGTACCGTTGTAC-3′ (SEQ ID No. 67) S396A 5′-CTGACGGTTACGCTGCTTCTTGGAC-3′ (SEQ ID No. 68) 5′-GTCCAAGAAGCAGCGTAACCGTCAG-3′ (SEQ ID No. 69) G404A 5′-CTGTTCCATTCGCTGCTAGAGCTTAC-3′ (SEQ ID No. 70) 5′-GTAAGCTCTAGCAGCGAATGGAACAG-3′ (SEQ ID No. 71) Q415E 5′-GATGCAATGTGAAGCTGAAAAGGAACC-3′ (SEQ ID No. 72) 5′-GGTTCCTTTTCAGCTTCACATTGCATC-3′ (SEQ ID No. 73)                             Sal I A437G 5′-CACGGTTGTGGTGTCGACAAGTTGGG-3′ (SEQ ID No. 74) 5′-CCCAACTTGTCGACACCACAACCGTG-3′ (SEQ ID No. 75)                              Mun I A463E 5′-GATCTGGTGGCAATTGGGAGGAATGTTTCG-3′ (SEQ ID No. 76) 5′-CGAAACATTCCTCCCAATTGCCACCAGATC-3′ (SEQ ID No. 77)

[0158] and accordingly for other mutations.

[0159] The temperature optimum of the purified phytases, expressed in Saccharomyces cerevisiae (Example 14), was determined as outlined in Example 14. Table 5 shows the effect on the stability of consensus phytase-1 for each mutation introduced.

[0160] Table 5: Stability Effect of the Individual Amino Acid Replacements in Consensus Phytase-1

[0161] (+or − means a positive, respectively, negative effect on the protein stability up to 1° C., ++ and − means a positive, respectively, negative effect on the protein stability between 1° C. and 3° C.; the number 10 or 11 corresponds to the consensus phytase sequence that suggested the amino acid replacement.) 22 TABLE 5 stabilizing neutral destabilizing mutation effect Mutation effect Mutation effect E58A (10) + D69A ± Y54F (10) − D69K (11) + D70G (10) ± V73I − D197N (10) + N134Q (10) ± A94K (10) − T214L (10) ++ G186H ± A101R (11) − E222T (11) ++ S187A (10) ± K153N (11) − E267D (10) + T214V ± I158V (10) −− R291I* + T251N (10) ± G203A −− R329H (10) + Y259N (10) ± G205S − S364T (10) ++ A283D (10) ± A217V − A379K (11) + A320V (10) ± V227A (11) −− G404A (10) ++ K445T ± L234V (10) − A463E (10) ± A238P (10) −− E277Q (10) −− H287A (11) −− Q292A (10) −− I366V (10) −− S396A (10) −− Q415E (11) −− A437G (10) −− E451R −− *This amino acid replacement was found in another round of mutations.

[0162] We combined eight positive mutations (E58A, D197N, E267D, R291I, R329H, S364T, A379K, G404A) in consensus phytase-1 using the primers and the technique mentioned above in this example. Furthermore, the mutations Q50T and K91A were introduced which mainly influence the catalytical characteristics of the phytase (see EP 897 985 as well as Example 14). The DNA and amino acid sequence of the resulting phytase gene (consensus phytase-1-thermo[8]-Q50T-K91A) is shown in FIG. 8. In this way, the temperature optimum and the melting point of the consensus phytase was increased by 7° C. (FIGS. 16, 17, 18).

[0163] Using the results of Table 5, we further improved the thermostability of consensus phytase 10 by the back mutations K94A, V158I, and A396S that revealed a strong negative influence on the stability of consensus phytase-1. The resulting protein is consensus phytase-10-thermo [3]. We also introduced the mutations Q50T and K91A which mainly influence the catalytical characteristics of consensus phytase (see EP 897 485 as well as Example 14 and FIGS. 15 and 16). The resulting DNA and amino acid sequence is shown in FIG. 9. The optimized phytase showed a 4° C. higher temperature optimum and melting point than consensus phytase-10 (FIGS. 13 and 14). The phytase also had a strongly increased specific activity with phytate as substrate of 250 U/mg at pH 5.5 (FIG. 15).

Example 9

Stabilization of the Phytase of A. fumigatus ATCC 13073 by Replacement of Amino Acid Residues with the Corresponding Consensus Phytase-1 and Consensus Phytase-10 Residues

[0164] At six typical positions where the A. fumigatus 13073 phytase is the only or nearly the only phytase in the alignment of FIG. 2 that does not contain the corresponding consensus phytase amino acid residue, the non-consensus amino acid residue was replaced by the consensus one. In a first round, the following amino acids were substituted in A. fumigatus 13073 phytase, containing the Q51T substitution and the signal sequence of A. terreus cbs. 116.46 phytase (see FIG. 10):

[0165] F55(28)Y, V100(73)I, F114(87)Y, A243(220)L, S265(242)P, N294(282)D.

[0166] The numbers in parentheses refer to the numbering of FIG. 2.

[0167] In a second round, four of the seven stabilizing amino acid exchanges (E59A, R329H, S364T, G404A) found in the consensus phytase-10 sequence and, tested as single mutations in consensus phytase-1 (Table 5), were additionally introduced into the A. fumigatus &agr;-mutant. The amino acid replacement S154N, shown to reduce the protease susceptibility of the phytase, was also introduced.

[0168] The mutations were introduced as described in example 8 (see Table 6), and expressed as described in Examples 11 to 13. The resulting A. fumigatus 13073 phytase variants were called &agr;-mutant and &agr;-mutant-E59A-S154N—R329H—S364T-G404A.

[0169] The temperature optimum (60° C., FIG. 21) and the melting point (67.02° C., FIG. 20) of the A. fumigatus 13073 phytase &agr;-mutant were increased by 5-7° C. in comparison to the values of the wild-type (temperature optimum: 55° C., Tm: 60° C.). The five additional amino acid replacements further increased the temperature optimum by 3° C. (FIG. 21). 23 TABLE 6 Mutagenesis primers for stabilization of A. fumigatus phytase ATCC 13073 Mutation Primer F55Y 5′-CACGTACTCGCCATACTTTTCGCTCGAG-3′ (SEQ ID No. 78) 5′-CTCGAGCGAAAAGTATGGCGAGTACGTG-3′ (SEQ ID No. 79)                            (Xho I) E58A 5′-CCATACTTTTCGCTCGCGGACGAGCTGTCCGTG-3′ (SEQ ID No. 80) 5′-CACGGACAGCTCGTCCGCGAGCGAAAAGTAGG-3′ (SEQ ID No. 81) V100I 5′-GTATAAGAAGCTTATTACGGCGATCCAGGCC-3′ (SEQ ID No. 82) 5′-GGCCTGGATCGCCGTAATAAGCTTCTTATAC-3′ (SEQ ID No. 83) F114Y 5′-CTTCAAGGGCAAGTACGCCTTTTTGAAGACG-3′ (SEQ ID No. 84) 5′-CGTCTTCAAAAAGGCGTACTTGCCCTTGAAG-3′ (SEQ ID No. 85) A243L 5′-CATCCGAGCTCGCCTCGAGAAGCATCTTC-3′ (SEQ ID No. 86) 5′-GAAGATGCTTCTCGAGGCGAGCTCGGATG-3′ (SEQ ID No. 87) S265P 5′-CTAATGGA TGTGTCCGTTTGATACGGTAG-3′ (SEQ ID No. 88) 5′-CTACCGTATCAAACGGACACATGTCCATTAG-3′ (SEQ ID No. 89) N294D 5′-GTGGAAGAAGTACGACTACCTTCAGTC-3′ (SEQ ID No. 90) 5′-GACTGAAGGTAGTCGTACTTCTTCCAC-3′ (SEQ ID No. 91)                            (Mlu I) R329H 5′-GCCCGGTTGACGCATTCGCCAGTGCAGG-3′ (SEQ ID No. 92) 5′-CCTGCACTGGCGAATGCGTCAACCGGGC-3′ (SEQ ID No. 93)                              Nco I S364T 5′-CACACGACAACACCATGGTTTCCATCTTC-3′ (SEQ ID No. 94) 5′-GAAGATGGAAACCATGGTGTTGTCGTGTG-3′ (SEQ ID No. 95)                              (Bss HI) G404A 5′-GTGGTGCCTTTCGCCGCGCGAGCCTACTTC-3′ (SEQ ID No. 96) 5′-GAAGTAGGCTCGCGCGGCGAAAGGCACCAC-3′ (SEQ ID No. 97)

Example 10

Introduction of the Active Site Amino Acid Residues of the A. niger NRRL 3135 Phytase into the Consensus Phytase-1

[0170] We used the crystal structure of the Aspergillus niger NRRL 3135 phytase to define all active site amino acid residues (see Reference Example and EP 897 010, which is hereby incorporated by reference as if recited in full herein). Using the alignment of FIG. 2, we replaced the following active site residues and additionally the non-identical adjacent residues of the consensus phytase-1 by those of the A. niger phytase:

[0171] S89D, S92G, A94K, D164S, P201S, G203A, G205S, H212P, G224A, D226T, E255T, D256E, V258T, P265S, Q292H, G300K, Y305H, A314T, S364G, M365I, A397S, S398A, G404A, and A405S

[0172] The new protein sequence, consensus phytase-7, was backtranslated into a DNA sequence (FIG. 11) as described in Example 6. The corresponding gene (fcp7) was generated as described in Example 6 using the following oligonucleotide mixes:

[0173] Mix 1.7: CP-1, CP-2, CP-3, CP-4.7, CP-5.7, CP-6, CP-7, CP-8.7, CP-9, CP-10.7

[0174] Mix 2.7: CP-9, CP-10.7, CP-11.7, CP-12.7, CP-13.7, CP-14.7, CP-15.7, CP-16, CP-17.7, CP-18.7, CP-19.7, CP-20, CP-21, CP-22.

[0175] The DNA sequences of the oligonucleotides are indicated in FIG. 11. The newly synthesized oligonucleotides are additionally marked by the number “7.” After assembling of the oligonucleotides using the same PCR primers as set forth in Example 6, the gene was cloned into an expression vector as described in Examples 11-13.

[0176] The pH-profile of consensus phytase-7, purified after expression in Hansenula polymorpha, was very similar to that of A. niger NRRL 3135 phytase (see FIG. 19).

Example 11

Expression of the Consensus Phytase Genes in Hansenula olymorpha

[0177] The phytase expression vectors, used to transform H. polymorpha RB11 (Gellissen et al., 1994), were constructed by inserting the Eco RI fragment of pBsk−fcp or variants thereof into the multiple cloning site of the H. polymorpha expression vector pFPMT121, which is based on an ura3 selection marker from S. cerevisiae, a formate dehydrogenase (FMD) promoter element and a methanol oxidase (MO) terminator element from H. polymorpha. The 5′ end of the fcp gene is fused to the FMD promoter, and the 3end to the MOX terminator (Gellissen et al., 1996;, EP 0299 108 B). The resulting expression vectors were designated pFPMTfcp, pFPMTfcp10, pFPMTfcp7.

[0178] The constructed plasmids were propagated in E. coli. Plasmid DNA was purified using standard state of the art procedures (see, for example, EP 897 985, Example 5). The expression plasmids were transformed into'the H. polymorpha strain RP11 deficient in orotidine-5′-phosphate decarboxylase (ura3) using the procedure for preparation of competent cells and for transformation of yeast as described in Gelissen et al. (1996). Each transformation mixture was plated on YNB (0.14% w/v Difco YNB and 0.5% ammonium sulfate),containing 2% glucose and 10.8% agar and incubated at 37° C. After 4 to 5 days, individual transformant colonies were picked and grown in the liquid medium described above for 2 days at 37° C. Subsequently, an aliquot of this culture was used to inoculate fresh vials With YNB-medium containing 2% glucose. After seven further passages in selective medium, the expression vector is integrated into the yeast genome in multimeric form. Subsequently, mitotically stable transformants were obtained by two additional cultivation steps in 3 ml non-selective liquid medium (YPD, 2% glucose, 10 g yeast extract, and 20 g peptone). To obtain genetically homogeneous recombinant strains, an aliquot from the last stabilization culture was plated on a selective plate. Single colonies were isolated for analysis of phytase expression in YNB containing 2% glycerol instead of glucose to derepress the fmd promoter. Purification of the consensus phytases was done as described in Example 12.

Example 12

Expression of the Consensus Phytase Genes in Saccharomyces cerevisiae and Purification of the Phytases from Culture Supernatant

[0179] The consensus phytase genes were isolated from the corresponding Bluescript-plasmid (pBsk−fcp, pBSK−fcp10, pBsk−fcp7), and ligated into the Eco RI sites of the expression cassette of the Saccharomyces cerevisiae expression vector pYES2 (Invitrogen, San Diego, Calif., USA) or subcloned between the shortened GAPFL (glyceraldhyde-3-phosphate dehydrogenase) promoter and the phos terminator as described by Janes et al. (1990). The correct orientation of the gene was checked by PCR. Transformation of S. cerevisiae strains e.g. INVSc1 (Invitrogen, San Diego, Calif., USA) was done according to Hinnen et al. (1978). Single colonies harboring the phytase gene under the control of the GAPFL promoter were picked and cultivated in 5 ml selection medium (SD-uracil, Sherman et al., 1986) at 30° C. under vigorous shaking (250 rpm) for one day. The preculture was then added to 500 ml YPD medium (Sherman et al., 1986) and grown under the same conditions. Induction of the gall promoter was done according to the manufacturer's (Invitrogen) instructions. After four days of incubation, cell broth was centrifuged (7000 rpm, GS3 rotor, 15 min, 5° C.) to remove the cells and the supernatant was concentrated by way of ultrafiltration in Amicon 8400 cells (PM30 membranes) and ultrafree-15 centrifugal filter devices (Biomax-30K, Millipore, Bedford, Mass., USA). The concentrate (10 ml) was desalted on a 40 ml Sephadex G25 Superfine column (Pharmacia Biotech, Freiburg, Germany), with 10 mM sodium acetate, pH 5.0, serving as elution buffer. The desalted sample was brought to 2 M (NH4)2SO4 and directly loaded onto a 1 ml Butyl Sepharose 4 Fast Flow hydrophobic interaction chromatography column (Pharmacia Biotech, Freiburg, Germany) which was eluted with a linear gradient from 2 M to 0 M (NH4)2SO4 in 10 mM sodium acetate, pH 5.0. Phytase was eluted in the break-through, concentrated and loaded on a 120 ml Sephacryl S-300 gel permeation chromatography column (Pharmacia Biotech, Freiburg, Germany). Consensus phytase-1 and consensus phytase-7 eluted as a homogeneous symmetrical peak and was shown by SDS-PAGE to be approximately 95% pure.

Example 13

Expression of the Consensus Phytase Genes in Aspergillus niger

[0180] The Bluescript-plasmids pBsk−fcp, pBSK−fcp10, and pBsk−fcp7 were used as template for the introduction of a Bsp HI-site upstream of the start codon of the genes and an Eco RV-site downstream of the stop codon. The Expand™ High Fidelity PCR Kit (Boehringer Mannheim, Mannheim, Germany) was used with the following primers: 24 Primer Asp-1: (SEQ ID No. 98)        Bsp HI 5′-TATATCATGAGCGTGTTCGTCGTGCTACTGTTC-3′ Primer Asp-2 used for cloning of fcp and fcp7: (SEQ ID No. 99)                           Eco RV 3′-ACCCGACTTACAAAGCGAATTCTATAGATATAT-5′ Primer Asp-3 used for cloning of fcp10: (SEQ ID No. 100)                           Eco RV 3′-ACCCTTCTTACAAAGCGAATTCTATAGATATAT-5′

[0181] The reaction was performed as described by the supplier. The PCR-amplified fcp-genes had a new Bsp HI site at the start codon, introduced by primer Asp-1, which resulted in a replacement of the second amino acid residue glycine by serine. Subsequently, the DNA-fragment was digested with Bsp HI and Eco RV and ligated into the Nco I site downstream of the glucoamylase promoter of Aspergillus niger (glaA) and the Eco RV site upstream of the Aspergillus nidulans tryptophan C terminator (trpC) (Mullaney et al., 1985). After this cloning step, the genes were sequenced to detect possible failures introduced by PCR. The resulting expression plasmids which basically correspond to the pGLAC vector as described in Example 9 of EP 684 313 contained the orotidine-5′-phosphate decarboxylase gene (pyr4) of Neurospora crassa as a selection marker. Transformation of Aspergillus niger and expression of the consensus phytase genes was done as described in EP 684 313. The consensus phytases were purified as described in Example 12.

Example 14

Determination of Phytase Activity and of Temperature Optimum

[0182] Phytase activity was determined basically as described by Mitchell et al. (1997). The activity was measured in an assay mixture containing 0.5% phytic acid (≈5 mM) in 200 mM sodium acetate, pH 5.0. After 15 minutes of incubation at 37° C., the reaction was stopped by addition of an equal volume of 15% trichloroacetic acid. The liberated phosphate was quantified by mixing 100 &mgr;l of the assay mixture with 900 &mgr;l H2O and 1 ml of 0.6 M H2SO4, 2% ascorbic acid and 0.5% ammonium molybdate. Standard solutions of potassium phosphate were used as reference. One unit of enzyme activity was defined as the amount of enzyme that releases 1 &mgr;mol phosphate per minute at 37° C. The protein concentration was determined using the enzyme extinction coefficient at 280 nm calculated according to Pace et al. (1995): consensus phytase-1.101; consensus phytase-7, 1.068; consensus phytase-1 10, 1.039.

[0183] In case of pH-optimum curves, purified enzymes were diluted in 10 mM sodium acetate, pH 5.0. Incubations were started by mixing aliquots of the diluted protein with an equal volume of 1% phytic acid (≈10 mM) in a series of different buffers: 0.4 M glycine/HCl, pH 2.5; 0.4 M acetate/NaOH, pH 3.0, 3.5, 4.0, 4.5, 5.0, 5.5; 0.4 M imidazole/HCl, pH 6.0, 6.5; 0.4 M Tris/HCl pH 7.0, 7.5, 8.0, 8.5, 9.0. Control experiments showed that the pH was only slightly affected by the mixing step. Incubations were performed for 15 minutes at 37° C. as described above.

[0184] For determining the substrate specificities of the phytases, phytic acid in the assay mixture was replaced by 5 mM concentrations of the respective phosphate compounds. The activity tests were performed as described above.

[0185] For determination of the temperature optimum, enzyme (100 &mgr;l) and substrate solution (100 &mgr;l) were pre-incubated for 5 minutes at the given temperature. The reaction was started by addition of the substrate solution to the enzyme. After 15 minutes of incubation, the reaction was stopped with trichloroacetic acid and the amount of phosphate released was determined.

[0186] The pH-optimum of the original consensus phytase was about pH 6.0-6.5 (80 U/mg). By introduction of the QSOT mutation, the pH-optimum shifted to pH 6.0 (130 U/mg). After introduction of K91A, the pH optimum shifted one pH-unit into the acidic pH-range showing a higher specific activity between pH 2.5 and pH 6.0. That was shown for the stabilized mutants and for consensus phytase-10, too (FIGS. 15 and 16).

[0187] Consensus phytase-7, which was constructed to transfer the catalytic characteristics of the A. niger NRRL 3135 phytase into consensus phytase-1, had a pH-profile very similar to that of A. niger NRRL 3135 phytase (see FIG. 19). The substrate specificity of consensus phytase-7 also resembled A. niger NRRL 3135 phytase more than it resembled consensus phytase-1.

[0188] The temperature optimum of consensus phytase-1 (71° C.) was 16-26° C. higher than the temperature optimum of the wild-type phytases (45-55° C., Table 7) which were used to calculate the consensus sequence. The improved consensus phytase-10 showed a further increase of its temperature optimum to 80° C. (FIG. 12). The temperature optimum of the consensus phytase-1-thermo[8] phytase was found in the same range (78° C.) when using the supernatant of an overproducing S. cerevisiae strain. The highest temperature optimum reached of 82° C. was determined for consensus phytase-10-thermo[3]-Q50T-K91A. 25 TABLE 7 Temperature optimum and Tm-value of consensus phytase and of the phytases from A. fumigatus, A. niger, E. nidulans, and M. thermophila. The determination of the temperature optimum was performed as described in Example 14. The Tm-values were determined by differential scanning calorimetry as described in Example 15 Temperature Tm Phytase optimum [° C.] [° C.] Consensus phytase-10-thermo[3]-Q50T-K91A 82 89.3 Consensus phytase-10-thermo[3]-Q50T 82 88.6 Consensus phytase-10 80 85.4 Consensus phytase-1-thermo[8]-Q50T 78 84.7 Consensus phytase-1-thermo[8]-Q50T-K91A 78 85.7 Consensus phytase-1 71 78.1 A. niger NRRL3135 55 63.3 A. fumigatus 13073 55 62.5 A. fumigatus 13073 60 67.0 &agr;-mutant A. fumigatus 13073 63 — &agr;-mutant (optimized) A. terreus 9A-1 49 57.5 A. terreus cbs.116.46 45 58.5 E. nidulans 45 55.7 M. thermophila 55 n.d. T. thermophilus 45 n.d.

Example 15

Determination of the Melting Point by Differential Scanning Calorimetry (DSC)

[0189] To determine the unfolding temperature of the phytases, differential scanning calorimetry was applied as previously published by Lehmann et al. (2000). Solutions of 50-60 mg/ml homogeneous phytase were used for the tests. A constant heating rate of 10° C./min was applied up to 90-95° C.

[0190] The determined melting points reflect the results obtained for the temperature optima (Table 7). The most stable consensus phytase designed is consensus phytase-10-thermo[3]-Q50T-K91A showing a melting temperature under the chosen conditions of 89.3° C. This is 26 to 33.6° C. higher than the melting points of the wild-type phytases used.

Example 16

Transfer of Basidiomycete Phytase Active Site into Consensus Phytase-10-Thermo[3]-Q50T-K91A

[0191] As described previously (Example 8), mutations derived from the basidiomycete phytase active site were introduced into the consensus phytase-10. The following five constructs a) to e) were prepared:

[0192] (a) This construct is called consensus phytase-12, and it contains a selected number of active site residues of the basidio consensus sequence. Its amino acid sequence (consphy 12) is shown in FIG. 22 (the first 26 amino acids form the signal peptide, amended positions are underlined);

[0193] (b) a cluster of mutations (Cluster II) was transferred to the consensus phytase-10 sequence, viz.: S80Q, Y86F, S90G, K91A, S92A, K93T, A94R, Y951;

[0194] (c) another cluster of mutations (Cluster III) was transferred to the consensus phytase-10 sequence, viz.: T129V, E133A, Q143N, M136S, V137S, N138Q, S139A;

[0195] (d) a further cluster of mutations (Cluster IV) was transferred to the consensus phytase-10 sequence, viz.: A168D, E171T, K172N, F173W;

[0196] (e) and finally, a further cluster of mutations (Cluster V) was transferred to the consensus phytase-10 sequence, viz.: Q297G, S298D, G300D, Y305T.

[0197] These constructs were expressed as described in Examples 11-13.

[0198] The following references are incorporated herein by reference as if recited in full herein:

[0199] Akanuma, S., Yamagishi, A., Tanaka, N. & Oshima, T. (1998). Serial increase in the thermal stability of 3-isopropylmalate dehydrogenase from Bacillus subtilis by experimental evolution. Prot. Sci. 7, 698-705.

[0200] Arase, A., Yomo, T., Urabe, I., Hata, Y., Katsube, Y. & Okada, H. (1993). Stabilization of xylanase by random mutagenesis. FEBS Lett. 316, 123-127.

[0201] Berka, R. M., Rey, M. W., Brown, K. M., Byun, T. & Klotz, A. V. (1998). Molecular characterization and expression of a phytase gene from the thermophilic fungus Thermomyces lanuginosus. Appl. Environ. Microbiol. 64, 4423-4427.

[0202] Blaber, M., Lindstrom, J. D., Gassner, N., Xu, J., Heinz, D. W. & Matthews, B. W. (1993). Energetic cost and structural consequences of burying a hydroxyl group within the core of a protein determined from Ala‘Ser and Val‘Thr substitutions in T4 lysozyme. Biochemistry 32, 113,63-11373.

[0203] Cosgrove, D. J. (1980) Inositol phosphates—their chemistry, biochemistry and physiology: studies in organic chemistry, chapter 4. Elsevier Scientific Publishing-Company, Amsterdam, Oxford, New York.

[0204] Devereux, J., Haeberli, P.& Smithies, O. (1984) A comprehensive set of sequence analysis programs for the VAX. Nucleic Acids Res. 12, 387-395.

[0205] Gellissen, G., Hollenberg, C. P., Janowicz, Z. A. (1994) Gene expression in methylotrophic yeasts. In: Smith, A. (ed.) Gene expression in recombinant microorganisms. Dekker, New York, 395-439.

[0206] Gellissen; G., Piontek, M., Dahlems, U., Jenzelewski, V., Gavagan, J. E., DiCosimo, R., Anton, D. I. & Janowicz, Z. A. (1996) Recombinant Hansenula polymorpha as a biocatalyst: coexpression of the spinach glycolate oxidase (GO) and the S. cerevisiae catalase T (CITI) gene. Appl. Microbiol. Biotechnol. 46, 46-54.

[0207] Gerber, P. and Muiller, K. (1995) Moloc molecular modeling software. J. Comput. Aided Mol. Des. 9, 251-268

[0208] Hinnen, A., Hicks, J. B. & Fink, G, R. (1978) Transformation of yeast. Proc. Natl. Acad. Sci. USA 75, 1929-1933.

[0209] Imanaka, T., Shibazaki, M. & Takagi, M. (1986). A new way of enhancing the thermostability of proteases. Nature 324, 695-697.

[0210] Janes, M., Meyhack, B., Zimmermann, W. & Hinnen, A. (1990) The influence of GAP promoter variants on hirudine production, average plasmid copy number and cell growth in Saccharomyces cerevisiae. Curr. Genet. 18, 97-103.

[0211] Karpusas, M., Baase, W. A., Matsumura, M. & Matthews, B. W. (1989). Hydrophobic packing in T4 lysozyme probed by cavity-filling mutants. Proc. Natl. Acad. Sci. (USA) 86, 8237-8241.

[0212] Lehmann, L., Kostrewa, D., Wyss, M., Brugger, R., D'Arcy, A., Pasamontes, L., van Loon, A. (2000), From DNA sequence to improved functionality: using protein sequence comparisons to rapidly design a thermostable consensus phytase, Protein Engineering 13, 49-57.

[0213] Margarit, I., Campagnoli, S., Frigerio, F., Grandi, G., Fillipis, V. D. & Fontana, A. (1992). Cumulative stabilizing effects of glycine to alanine substitutions in Bacillus subtilis neutral protease. Prot. Eng. 5, 543-550.

[0214] Matthews, B. W. (1987a). Genetic and structural analysis of the protein stability problem. Biochemistry 26, 6885-6888.

[0215] Matthews, B. W. (1993). Structural and genetic analysis of protein stability. Annu. Rev. Biochem. 62, 139-160.

[0216] Matthews, B. W., Nicholson, H. & Becktel, W. (1987). Enhanced protein thermostability from site-directed mutations that decrease the entropy of unfolding. Proc. Natl. Acad. Sci. (USA) 84, 6663-6667.

[0217] Mitchell, D. B., Vogel, K., Weimann, B. J., Pasamontes, L. & van Loon, A. P. G. M. (1997) The phytase subfamily of histidine acid phosphatases: isolation of genes for two novel phytases from the fungi Aspergillus terreus and Myceliophthora thermophila, Microbiology 143, 245-252.

[0218] Mullaney, E. J., Hamer, J. E., Roberti, K. A., Yelton, M. M. & Timberlake, W. E. (1985) Primary structure of the trpC gene from Aspergillus nidulans. Mol. Gen. Genet. 199, 37-46.

[0219] Munoz, V. & Serrano, L. (1995). Helix design, prediction and stability. Curr. Opin. Biotechnol. 6, 382-386.

[0220] Pace, N. C., Vajdos, F., Fee, L., Grimsley, G. & Gray, T. (1995). How to measure and predict the molar absorption coefficient of a protein. Prot. Sci. 4, 2411-2423.

[0221] Pantoliano, M. W., Landner, R. C., Brian, P. N., Rollence, M. L., Wood, J. F. & Poulos, T. L. (1987). Protein engineering of subtilisin BPN′: enhanced stabilization through the introduction of two cysteines to form a disulfide bond. Biochemistry 26, 2077-2082.

[0222] Pasamontes, L., Haiker, M., Henriquez-Huecas, M., Mitchell, D. B. & van Loon, A. P. G. M. (1997a). Cloning of the phytases from Emericella nidulans and the thermophilic fungus Talaromyces thermophilus. Biochim. Biophys. Acta 1353, 217-223.

[0223] Pasamontes, L., Haiker, M., Wyss, M., Tessier, M. & van Loon, A. P. G. M. (1997) Cloning, purification and characterization of a heat stable phytase from the fungus Aspergillus fumigatus, Appl. Environ. Microbiol. 63, 1696-1700.

[0224] Piddington, C. S., Houston, C. S., Paloheimo, M., Cantrell, M., Miettinen-Oinonen, A. Nevalainen, H., & Rambosek, J. (1993) The cloning and sequencing of the genes encoding phytase (phy) and pH 2.5-optimum acid phosphatase (aph) from Aspergillus niger var. awamori. Gene 133, 55-62.

[0225] Purvis, I. J., Bettany, A. J. E., Santiago, T. C., Coggins, J. R., Duncan, K., Eason, R. & Brown, A. J. P. (1987). The efficiency of folding of some proteins is increased by controlled rates of translation in vivo. J. Mol. Biol. 193, 413-417.

[0226] Risse, B., Stempfer, G., Rudolph, R., Schumacher, G. & Jaenicke, R. (1992). Characterization of the stability effect of point mutations of pyruvate oxidase from Lactobacillus plantarum: protection of the native state by modulating coenzyme binding and subunit interaction. Prot. Sci. 1, 1710-1718.

[0227] Sambrook, J., Fritsch, E. F. & Maniatis, T. (1989) Molecular Cloning: A Laboratory Manual, 2nd Ed., Cold Spring Harbor Laboratory, Cold Spring Harbor, N.Y.

[0228] Sauer, R., Hehir, K., Stearman, R., Weiss, M., Jeitler-Nilsson, A., Suchanek, E. & Pabo, C. (1986). An engineered, intersubunit disulfide enhances the stability and DNA binding of the N-terminal domain of 1-repressor. Biochemistry 25, 5992-5999.

[0229] Serrano, L., Day, A. G. & Fersht, A. R. (1993). Step-wise mutation of bamase to binase. A procedure for engineering increased stability of proteins and an experimental analysis of the evolution of protein stability. J. Mol. Biol. 233, 305-312.

[0230] Sheman, J. P., Finck, G. R. & Hicks, J. B. (1986) Laboratory course manual for methods in yeast genetics. Cold Spring Harbor University.

[0231] Steipe, B., Schiller, B., Plueckthun, A. & Steinbach, S. (1994). Sequence statistics reliably predict stabilizing mutations in a protein domain. J. Mol. Biol. 240, 188-192.

[0232] van den Burg, B., Vriend, G., Veltman, O. R., Venema & G., Eijsink, V. G. H. (1998). Engineering an enzyme to resist boiling. Proc. Natl. Acad. Sci. (USA) 95, 2056-2060.

[0233] Van Etten, R. L. (1982) Human prostatic acid phosphatase: a histidine phosphatase. Ann. NY Acad. Sci. 390, 27-50.

[0234] van Hartingsveldt, W., van Zeijl, C. M. F., Harteveld, G. M., Gouka, R. J., Suykerbuyk, M. E. G., Luiten, R. G. M., van Paridon, P. A., Selten, G. C. M., Veenstra, A. E., van Gorcom, R. F. M., & van den Hondel, C. A. M. J. J. (1993) Cloning, characterization and overexpression of the phytase-encoding gene (phyA) of Aspergillus niger. Gene 127, 87-94.

[0235] The invention being thus described, it will be obvious that the same may be varied in many ways. Such variations are not to be regarded as a departure from the spirit and scope of the invention and all such modifications are intended to be included within the scope of the following claims.

Claims

1. A fermentation assembly comprising

(a) a vessel for culturing living cells;

(b) at least two storage flasks in fluid communication with the vessel for supply of liquids and a first transport means for transferring the liquids from the storage flasks to the vessel;

(c) individual appliances operably connected to the transport means for monitoring the supply of the contents of the storage flasks to the vessel;

(d) a harvest flask in fluid communication with the vessel and a second transport means for transferring the fermentation broth from the vessel to the harvest flask; and

(e) a device operably connected to the first transport means for controlling and maintaining a constant dilution rate in the vessel with varying rates of individual supply of liquid from the storage flasks to the vessel.

2. A fermentation assembly according to claim 1 wherein the at least two storage flasks comprise individual storage flasks for solutions of carbon, nitrogen, and mineral sources.

3. A fermentation assembly according to claim 1 wherein at least one of the at least two storage flasks contains a controlling agent.

4. A fermentation assembly according to claim 1 further comprising an additional storage flask containing water.

5. A fermentation assembly according to claim 1 wherein the vessel contains a bed of immobilized living cells.

6. A fermentation assembly according to, claim 5 wherein the bed of immobilized cells is selected from the group consisting of a fixed bed, an expanded bed, a moving bed, and combinations thereof.

7. An assembly according to claim 5 wherein the living cells are immobilized on a porous carrier.

8. A process for the manufacture of a protein comprising:

(a) providing a continuous culture of living cells in a fermentation reactor; and

(b) individually feeding nutrients and other agents required for the growth of the cells into the reactor at a constant dilution rate to achieve optimal production of the protein.

9. A process according to claim 8 wherein the protein is selected from the group consisting of catalase, lactase, phenoloxidase, oxidase, oxidoreductase, glucanase, cellulase, xylanase and other polysaccharides peroxidase, lipase, hydrolase, esterase, cutinase, protease and other proteolytic enzymes, aminopeptidase, carboxypeptidase, phytase, lyase, pectinase, pectinolytic enzymes, amylase, glucosidase, mannosidase, isomerase, invertase, transferase, ribonuclease, chitinase, and desoxyribonuclease.

10. A process according to claim 8 wherein the protein is a therapeutic protein.

11. A process according to claim 10 wherein the therapeutic protein is selected from the group consisting of antibodies, vaccines, and antigens.

12. A process according to claim 8 wherein the protein is an antibacterial and/or health-beneficial protein.

13. A process according to claim 12 wherein the antibacterial and/or health-beneficial protein is selected from the group consisting of lactoternin, lactoperoxidase and lysozyme.

14. A process according to claim 8 wherein the cells are immobilized.

15. A process according to claim 8 wherein the cell is a phytase-producing microorganism.

16. A process according to claim 15 wherein the phytase-producing microorganism is Hansenula polymorpha.

17. A process according to claim 16 wherein the phytase-producing microorganism is Hansenula polymorpha transformed by a DNA encoding a phytase of fungal or consensus origin.

18. A process according to claim 8 wherein the fermentation reactor contains a bed of immobilized cells on a porous carrier.

19. A process according to claim 18 wherein the bed is selected from the group consisting of a fixed bed, an expanded bed, a moving bed, and combinations thereof.

20. A process according to claim 8 wherein the nutrients comprises a carbon source.

21. A process according to claim 20 wherein the carbon source is glycerol or sugar.

22. A process according to claim 21 wherein the sugar is selected from the group consisting of mono-, di-, and polysaccharides.

23. A process according to claim 20 wherein t he carbon source is glucose.

24. A process according to claim 20 wherein the carbon source is methanol.

25. A process according to claim 20 wherein the carbon source is glucose and methanol.

26. A process according to claim 25 wherein the total amount of methanol and glucose is from about 10 g/l to about 500 g/l each.

27. A fermentation assembly comprising:

(a) a fermentor 1 equipped with inlet tubes 2a in fluid communication with a storage flask 2 for supply of liquids to the fermentor;

(b) a pump 3 operably connected to the inlet tubes for transporting liquids from the storage flask 2 to the fermentor 1;

(c) a scale 4 in contact with each storage flask for monitoring the amount of liquid supplied to and discharged from the fermentor;

(d) a gas inlet 9 and out let tubes 10 in communication with the fermentor for introducing and removing gas therefrom;

(e) a pump 6 operably connected to an outlet tube 5a which is in fluid connection with the fermentor, wherein the pump discharges fermentation broth from the fermentor to a harvest flask 5;

(f) a main controlling unit 7 operably connected to the fermentation assembly for overall process monitoring and steering;

(g) a controlling unit 11 operably connected to individual control systems 17 for monitoring and steering temperature, pH, gas pressure, fermentor content, and antifoam agents;

(h) a circuit 12 for monitoring gas supply and taking samples including an outlet tube from the fermentor, which circuit is operably connected to the outlet to be pump 13; and

(i) gas inlet and outlet flow control devices 14 and 15 operably connected to the gas inlet and outlet tubes 9, 10.

29. A fermentation assembly according to claim 28 further comprising sterile filters 16 and thermostating unit 8.