PROCESS FOR PURIFYING FACTOR VIII

Abstract: Proteases generally tend to reduce the activity of coagulation factor VIII by degrading the molecule. The present invention relates to a process for reducing the detrimental influence of metal-dependent proteases upon recombinant factor VIII molecules, by adding an inhibitor of metal-dependent proteases to a solution after harvest. The solution is suitably the harvest solution or any aqueous solution being fed to or leaving the primary isolation, being the initial step of the purifying sequence. The inhibitor is selected from: i) complexing agents with a stronger affinity for the metal ion of the protease than for the ion or ions stabilizing the factor VIII molecule and ii) compounds structurally related to the natural substrate of the protease and containing an electronegative moiety. The presence of an inhibitor, preferably a complexing agent, after harvest allows for a prolonged harvest period and considerably higher yield with essentially retained factor VIII activity. The invention further relates to an aqueous solution containing recombinant factor VIII which has been purified according to the present process and use of such an aqueous solution, for the manufacture of a medicament for administration to a patient having the symptoms of hemophilia. Also, the invention relates to a method for treatment of hemophilia by administration of a therapeutically effective amount of recombinant factor VIII which has been purified according to the present process.

Description: PROCESS FOR PURIFYING FACTOR VIII FIELD OF THE INVENTION Proteases generally tend to reduce the activity of coagulation factor VIII by degrading the molecule. The present invention relates to a process for reducing the detrimental influence of metal-dependent proteases upon recombinant factor VLII molecules, by adding an inhibitor of metal-dependent proteases to a solution after harvest. The solution is suitably the harvest solution or any aqueous solution being fed to or leaving the primary isolation, being the initial step of the purifying sequence. The inhibitor is selected from i) complexing agents with a stronger affi¬ nity for the alkaline-earth metal ion or metal ion of the protease than for the ion or ions stabilizing the factor VIII molecule and ii) compounds structurally related to the natural substrate of the protease and containing an electronegative moiety. The presence of an inhibitor, preferably a complexing agent, after harvest allows for a prolonged harvest period and considerably higher yield with essentially retained factor VIII activity. The invention further relates to an aqueous solution containing recombinant factor VIII which has been purified according to the present process and use of such an aqueous solution, for the manufacture of a medicament for administration to a patient having the symptoms of hemophilia. Also, the invention relates to a method for treatment of hemophilia by administration of a therapeuti- cally effective amount of recombinant factor VLTI which has been purified accord¬ ing to the present process. BACKGROUND OF THE INVENTION Hemophilia is an inherited disease which has been known for centuries, but it is only within the last four decades that it has been possible to differentiate between the various forms; hemophilia A and hemophilia B. Hemophilia A is the most frequent form. It affects only males with an incidence of one or two indivi¬ duals per 10000 live-bom males. The disease is caused by strongly decreased level or absence of biologically active coagulation factor VIII (antihemophilic factor), which is a protein normally present in plasma. The clinical manifestation of hemo¬ philia A is a strong bleeding tendency and before treatment with factor VIII con¬ centrates was introduced, the mean age of the patients concerned was less than 20 years. Concentrates of factor VIII obtained from plasma have been available for about three decades. This has improved the situation for treatment of hemophilia patients considerably and offered them the possibility of living a normal life. Until recently, therapeutic factor VIII concentrates have been prepared by fractionation of plasma. However, there are since some years methods available for production of factor VLLT in cell culture using recombinant DNA techniques as reported in e.g. W. Wood et al, Nature, 312, p. 330-37 (1984) and EP-A-0 160457. It is well known that proteins are cleaved by proteases, such as serine, cys- teine, aspartic and metallo proteases. Many proteases need alkaline-earth metals or metals (in the following just denoted metals) for their activity. The metal-depen- dent proteases are either considered to be metal-activated proteases (to which metal ions must be added for activity) or metallo proteases (which contain metals as an integral part of their structure). Concerning the first group, activation and stabilization of enzymes by metals frequently occur in several ust's of rrnteases, such as serine and cysteine proteases. The importance of a metallo protease in cultured , ιT Is tor the secretion of a certain metabolite has been shown by R. Ikegaw a ft ai in Biochem. Biophys. Res. Comm. 171(2), p. 669-675 (1990). This was revealed by the suppress¬ ing effect on this secretion recognized by the addition of a metallo protease specific inhibitor. It was evident, however, that the enzyme was confined to the intracellu- lar space, since no effect of the inhibitor was obtained in a cell-free conditioned medium. The effect of proteases are though far more often mentioned in the context of the potential risk of degradation of the protein at issue. US-A-5149787 (The Blood Center Research Foundation) relates to a method for maintaining an intact, non-degraded molecular complex of factor VIII (FVIII) /- von Willebrand factor (vWf) during processing of blood, plasma and plasma frac- tions further containing cellular sources of a calcium (Ca^+) activated protease cap¬ able of cleaving the FVLTI/vVVf complex. The functional integrity of the FVIII/vWf complex can be preserved by avoiding the action of the proteases(s) specifically on the vWf portion of the complex. The action of the calcium activated protease(s) may be avoided by removing the platelet source of the protease(s) from the plasma or by inactivating the protease(s). The protease(s) may be inactivated by removing the calcium necessary for activation, e.g. by chelation, or by inhibiting the protea- se(s) by specific inhibitors directed against cysteine proteases. US-A-5149787 is thus specifically directed to a method for maintaining the von Willebrand factor portion of the FVIII /vWf complex obtained from blood or plasma. Various solutions have been suggested to reduce the degradation by protea¬ ses of plasma derived as well as recombinant factor VIII molecules. These solutions have been directed to reduce the influence of serine and cysteine proteases, consi¬ dered to be the most detrimental ones in blood plasma as well as in cell cultures. Thus, WO-A-9310143 (Johnson et al) discloses a method for recovering a purified and stabilized protein by contacting a biological sample containing factor VTII with at least one protease inhibiting or protease removing agent. The method is particu¬ larly directed to inhibit or remove thrombin, since factor Mil is said t.< verv sen¬ sitive to minute quantities of this serine protease naturally present ιr- plasma. The protease inhibitors include e.g. benzamidine, antithromrnr, 111 h-.-r rin and hirudin. The effect of the method is only shown for plasma aenveu tactor VIII. WO-A-9002175 (Novo-Nordisk) discloses a method for producing polypep- tides by culturing eukaryotic cells in the presence of protease inhibitors. Specific examples include factor Mil as the polypeptide, but the protease inhibitors are all directed to serine and cysteine proteases and the inhibitors are present in the cell culture per se. The problem encountered with metal-dependent proteases in the production of various proteins, has been much less surveyed than the role of serine and cys¬ teine proteases. More particularly, this specific problem has never been addressed previously in connection with factor MIL The aim of the present invention is there¬ fore to counteract the influence of metal-dependent proteases in production of recombinant factor Mil, in such a way that essentially all factor Mil activity obtain¬ ed after harvest is retained throughout the purification process. DESCRIPTION OF THE INMJNTION An object of the present invention is to reduce the influence of metal- dependent proteases on recombinant factor Mil, by inhibiting the action of the metal-dependent proteases per se. A further object of the of the present invention is to reduce the influence of metal-dependent proteases on recombinant factor Mil, by inhibiting the action of or removing the metal ions required for activity of these proteases. Another object of the present invention is to provide an efficient purification process, where the activity of recombinant factor Mil is essentially retained. Yet another object of the present invention is to provide an efficient process, for producing a highly concentrated and very pure solution of recombinant factor MIL The objects above are met by the present invention, which relates to a pro¬ cess for reducing the degradation of recombinant coagulation factor Mil caused by metal-dependent proteases, wherein an inhibitor of metal-dependent proteases is added to a solution after harvest, and in that the inhibitor is selected from the group consisting of i) complexing agents with a stronger affinity for the alkaline-earth metal ion or metal ion of the protease than for the ion or ions stabilizing the factor Mil molecule and ii) compounds structurally related to the natural substrate of the protease and con- taining an electronegative moiety. The inventors of the present invention have found that certain inhibitors of metal-dependent proteases have a surprisingly positive impact on the activity of recombinant factor Mil in and after the purifying sequence. The presence of these inhibitors makes it possible to efficiently inhibit the action of the metal-dependent proteases per se and /or inhibit the action of or remove the metal ions required for activity of the proteases particularly detrimental to the recombinant factor Mil molecule. In this way, the influence of these metal-dependent proteases can be reduced, giving essentially retained factor Mil activity throughout the entire puri¬ fication process. The metal-dependent proteases are either considered to be metal-activated proteases (to which metal ions must be added for activity) or metallo proteases (which contain metals as an integral part of their structure). Concerning the first group, activation and stabilization of enzymes by metals frequently occur in seve¬ ral classes of proteases, such as serine and cystein proteases. For example, in the field of blood functions, especially coagulation, fibrinolysis, and complement acti- vation, a group of vitamin K-dependent calcium-binding domains are common (see e.g. Laszlό Patthy in Methods in Enzymology, 222, p. 10-21 (1993)). Concerning the latter metallo proteases, a review of mammalian metalloendopeptidases, being an important subgroup of this protease class, can be found in Bond et al, Int. J. Bio- chem., 17, no. 5, p. 565-574 (1985). These authors conclude, that Zn^ + appears to be the essential metal for all of the characterized mammalian metallo proteases. In a more recent review ( D. A. Auld, Methods in Enzymology, 248, p. 229-242 (1995)) this ion is still considered to be the active ion of an overwhelming majority of the metallo proteases. This does not exclude a structural and functional role also of other metals, like Cu 2+ , Fe^ + , Fe^ + , Mn^+, Co^ + and Cd2+(Auld, see above). Thus, an enzyme dependent on Zn^+as well as Ca^ + , is described in Butler et al, Biochem. J., 241, p. 229-235 (1987). In the present invention, the term after harvest relates to process activities and steps after separation of cells from the conditioned medium, e.g. by centrifu- gation and /or filtration. In the present invention, the inhibitor of metal-dependent proteases can be added to any solution obtained or used after harvest. It is however preferred to add the inhibitor to a solution selected from the group consisting of the harvest solution and any aqueous solution being fed to or leaving the primary isolation. More particularly, in the present invention, the inhibitor can be present in the harvest solution, in the optionally preconcentrated aqueous solution containing factor Mil before loading, in the washing liquid, in the elution liquid, in the solu¬ tion resulting from the primary isolation, or a combination thereof. If the primary isolation is a chromatography step, the solution resulting from the primary isola¬ tion is termed eluate. If the inhibitor is added to the solution resulting from the primary isolation, the addition is made before the solution is brought to the next process step. In this way, it is possible to considerably reduce the content of deg- raded factor Mil molecules. In the present invention, factor Mil is recombinant and it can be full-length factor Mil or preferably a deletion derivative of full-length factor Mil having coa¬ gulant activity. By deletion derivative is here meant coagulation factor Mil, in which the whole or part of the B-domain is missing, while the coagulant activity is retained. The structure and biochemistry of recombinant factor VIII products in general have been described by Kaufman in Trends in Biotechnology, 9, p. 353-359 (1991) and Hematology, 63, p. 155-65 (1991). Factor Mil concentrates derived from human plasma contain several frag¬ mented fully active factor VIII forms as described by Andersson et al, Proc. Natl. Acad. Sci. USA, 83, p. 2979-83 (May 1986). The smallest active form has a molecu¬ lar mass of 170 kDa and consists of two chains of 90 kDa and 80 kDa held together by metal ion(s). Reference is here made to EP-A-0 197901 (Pharmacia AB). Pharmacia AB of Stockholm, Sweden, has developed a recombinant factor VIII product which corresponds to the 170 kDa plasma factor VIII form in thera- peutic factor Mil concentrates. The truncated recombinant factor Mil molecule is termed r-MII SQ and is produced by Chinese Hamster Ovary (CHO) cells in a cell culture process in serum-free medium. The structure and biochemistry of r-MII SQ have been described in WO-A-9109122 (Pharmacia AB). In the present invention, more preferably the deletion derivative is recombinant factor VIII SQ (r-VIII SQ). Suitably, the conditioned medium obtained after harvesting the cell culture when producing the recombinant coagulation factor VIII according to the present invention is essentially free of the von Willebrand factor (vWf), and preferably totally free thereof. It is more preferred that the cell culture used for producing the recombinant coagulation factor Mil is essentially free of the von Willebrand factor (vWf), and preferably totally free. In this way, the entire process for producing the recombinant factor Mil is free of vWf. This makes possible production of a factor Mil with a very high activity. Many proteins contain ions of alkaline earth metals or metals. This is also valid for the factor il molecule, requiring a bridge of at least one divalent ion, for reasons of structural integrity and retained activity. This ion is generally consider¬ ed to be calcium. However, in tests in-vitro various divalent ions have been used to advantage, e.g. calcium, manganese, cobalt, or a combination thereof. Reference is here made to Andersson et al (see above), Nordfang et al, J. Biol. Chem., 263, p. 1115-1118 (1988) and Fay et al in J. Biol. Chem., 267, p. 13246-13250 (1992). Recently, the content of copper in factor Mil has been revealed by N. Bihoreau et al in Eur. J. Biochemistry, 222, p. 41-48 (1994). The authors suggest that the presence of this cation is not directly related to the coagulant activity but is of structural importance for the molecule. However, Nordfang et al (see above) failed when attempting to reassociate dissociated factor Mil chains by addition of copper. The presence of a divalent ion, such as calcium, makes factor MLT a protein particularly sensitive to the presence of complexing agents which tend to trap ions of alkaline earth metals or metals. Thus, to cite Bo Ersson et al in Protein Purifica¬ tion; Principles, High Resolution Methods, and Applications, VCH Publishers, Inc., New York, p. 7-10 (1989): "Many proteins are stabilized by calcium ions. The diva- lent ions calcium and magnesium are trapped by EDTA and cannot be used in com¬ bination with this chela tor". In Andersson et al (see above), thorough tests were carried out to determine the role of metal ions in the structure of factor Mil derived from human plasma. The results showed that EDTA dissociated the 80 kDa doublet chain from each of the heavier chains having molecular sizes from 200 to 90 kDa. The presence of che- lators caused dissociation of the dimer subunits as disclosed also by Fay et al (see above). For the above reasons, it is especially surprising that complexing agents can be present in a factor Mil solution, without destabilizing the factor Mil molecules to any appreciable extent. Thus, contrary to the previous belief complexing agents can be used to advantage in a process for purifying recombinant factor MIL In the present invention, the inhibitors for metal-dependent proteases are selected from i) complexing agents with a stronger affinity for the metal ion of the protease than for the ion or ions stabilizing the factor Mil molecule and ii) com¬ pounds structurally related to the natural substrate of the protease and containing an electronegative moiety. Compounds from the latter group are suitably peptides or peptide analogues, preferably selected from the group consisting of hydro- xamates, phosphoramidates and carboxylates. The mechanism for the inhibition of metallo proteases by peptides or peptide analogues functionalized with e.g. hydro- xamates, phophoramidates or carbonyl groups is not fully clear. However, in the literature their effect is considered to be due to a chelating function (see especially p. 221-222 of Birkedal-Hansen et al, Critical Review in Oral Biology and Medicine, 4(2), p. 197-250 (1993)). Hence, the two classes of compounds which can be used as inhibitors for metal-dependent proteases according to the present invention are so closely related so as to form a single general inventive concept. Compounds from the group of structurally related compounds can be natu¬ ral, as in the case of phosphoramidon, or synthetic. The design of such synthetic inhibitors is reviewed in Bond et al (see above). One example, described by N. Nishino and J. C. Powers in Biochemistry, 17 (14), p. 2846-2850 (1978), is the syn¬ thesis of specific inhibitors for the zinc metalloendopeptidase thermolysin. In this case, the specificity of the inhibitor peptide analogue was achieved by including a hydrophobic amino acid, intended for interaction with a corresponding pocket in the active site of the enzyme, as well as a hydroxamic acid residue, for interaction with the zinc atom. An illustration of this phenomenon is given in B. Roques et al in Methods in Enzymology, 248, p. 263-283, especially p. 268-269 and 272 (1995)). Further examples of hydroxamates are disclosed in WO 90/05719. In the present invention, the inhibitor of metal-dependent proteases is suit¬ ably a complexing agent. In the following, therefore, the invention will be describ¬ ed with reference to complexing agents as inhibitors of metal-dependent proteases. The selection of complexing agent in the present invention is e.g. dependent upon the affinity for the various relevant ions, concentration required, toxicity and cost. The complexing agents of the present invention have a higher affinity for the metal ion of the protease than for the ion or ions stabilizing the factor Mil molecule. The ranking of affinity is here aimed at the actual metal chelating equilibrium situation, i.e. related to the strength of the binding between the actual ions and the chelating sites in the actual proteins. This should be compared to the strength of the binding between these ions and the added complexing agent. Furthermore, the equilibrium situation should be related to the actual ionic strength, pH and other physico- chemical factors of importance. Complexing agents suitable in the present invention include nitrogenous polycarboxylic acids, heterocyclic amines, phenanthrolines, pyridine carboxylic acids, quinolines, salicylates, N-acyl derivatives of collagen, N-aminoacyl deriva¬ tives of β-diketones, thiol compounds and di- and tricarboxylic acids. Examples of nitrogenous polycarboxylic acids are ethylenediamine tetraacetic acid (EDTA), [ethylenedioxy)diethylenedinitrilo]tetraacetic acid (EGTA) and nitriloacetic acid (NTA). Examples of heterocyclic amines are imidazole and L-histidine. Examples of phenanthrolines are 1,10-phenanthroline and methyl-derivatives of phenanthro- line. Examples of pyridine carboxylic acids and quinolines are pyridine-2,6- dicarboxylic acid (dipicolinic acid) and 8-hydroxyquinoline. Examples of di- and tricarboxylic acids are oxalic acid and citric acid. Other examples are disclosed in David Auld (see above, especially in Table I) and Vincent H.L. Lee, J. Cont. Release, 13, p. 213-223 (1990). For reasons of affinity toward the metal ion or ions of the pro¬ tease as well as toward the ion or ions stabilizing the factor Mil molecule, and for reasons of toxicity, simplicity and economy, it is preferred to use EDTA in the pre¬ sent invention. Of the various salts of EDTA it can be advantageous to use a salt containing at least one of the ions stabilizing the factor Mil molecule, e.g. the calcium and sodium salt of EDTA. Data for toxicity and other properties of the di- and trisodium salts of EDTA as well as the corresponding calcium disodium salt can be found in the Merck Index, Merck & Co., Inc., Rahway, New Jersey, USA, 11th ed., p. 550, (1989), and Martindale, The Extra Pharmacopoeia, Pharmaceutical Press, 30th ed., p. 681-682 and 693-694 (1993). The concentration of the complexing agent should be regulated such that the ion or ions stabilizing factor Mil still can be detected as free ions in the solution at issue. This makes possible retained activity of the factor Mil molecules. The total concentration of the ion or ions stabilizing factor Mil is suitably at least about 0.2 mM, preferably in the range of from 1 up to 300 mM and more preferably in the range of from 5 up to 50 mM. The concentration is independent of the point of addition, but is dependent upon the concentration of complexing agent. When the complexing agent is a nitrogenous polycarboxylic acid and added to the harvest solution, the concentration of complexing agent should be in the range of from about 0.01 up to about 10 mM, suitably from 0.1 up to 5 mM and preferably from 0.3 up to 3 mM. When the complexing agent is a nitrogenous polycarboxylic acid and added to a liquid used for washing in the primary isolation, the concentration of complex¬ ing agent should be in the range of from about 0.01 up to about 50 mM, suitably from 0.1 up to 10 mM and preferably from 0.5 up to 5 mM. When the primary isolation is a chromatography step, the concentration of a nitrogenous polycarboxylic acid as complexing agent in the liquid used for eluting the adsorbed factor Mil molecules should be in the range of from about 0.1 up to about 30 mM, suitably from 0.5 up to 15 mM and preferably from 1 up to 5 mM. When the complexing agent is a nitrogenous polycarboxylic acid and added to the solution resulting from the primary isolation, the concentration of complex- ing agent should be in the range of from about 0.1 up to about 30 mM, suitably from 0.5 up to 15 mM and preferably from 1 up to 5 mM. When the complexing agent is a compound other than a nitrogenous poly¬ carboxylic acid, it lies within the competence of the skilled person to arrive at suit¬ able concentrations for performing the present invention. For example, when using phenanthroline, the concentration required may be double that of the nitrogenous polycarboxylic acids. With the heterocyclic amines histidine and imidazole, the concentration may be even higher, especially with imidazole, being the weaker complexing agent. The primary isolation of the present invention can be any process step aimed at increasing the concentration of factor Mil in the harvest solution. Suitable and well known examples include chromatography steps, ultrafiltration, precipitation e.g. with ammonium sulfate and the like. The chromatography steps include cation exchange, anion exchange, affinity and hydrophobic interaction chromatography steps. In the present invention, it is especially advantageous to use an ion-exchange chromatography step as primary isolation. This is because ion-exchange gels are rigid allowing for treatment with strong alkaline solutions to restore the adsorbing capacity, if the gel surface is still contaminated after elution. In preferred embodi¬ ments, the primary isolation is a cation-exchange chromatography step. The use of a cation-exchange step as the primary isolation, allows for an immediate and dra¬ matic reduction in liquid volume and total protein content of the harvest solution. This is particularly true if albumin is present in the harvest solution. Thus, with a cationic gel the albumin is not adsorbed to the gel surface to any substantial degree, and can be easily removed by washing, as opposed to an anionic gel. Cation-exchange gels of various types can be used in the present invention. The ligands are suitably selected from the group consisting of sulfoethyl, sulfo- propyl, sulfobutyl, sulfonate, and carboxymethyl. Preferably, the ligand is sulfo- propyl or sulfonate since this allows for a wide pH range. Characteristics of suit¬ able cation-exchange gels can be found in Protein Purification; Principles, High Resolution Methods, and Applications, VCH Publishers, Inc., New York, p. 107-148 (1989) and E. Boschetti, J: Chromatogr., A 658, 1994, p. 207-236, which are hereby incorporated by reference. The matrix can be selected from various strongly hydro- philic matrices e.g. agarose matrices such as a wide variety of Sepharose® matrices sold by Pharmacia Biotech of Uppsala, Sweden, organic polymer matrices such as TSK-GEL:s sold by Tosoh Corp. of Tokyo, Japan, or highly porous organic polymer matrices sold by Per Septive Biosystems of Boston, USA. Membrane matrices are also suitable, e.g. Sartobind® sold by Sartorius of Germany and MemSep® sold by Millipore of USA. The matrix is preferably an agarose matrix. Suitable agarose mat¬ rices in the present invention are, apart from Sepharose®, Minileak® sold by Kem- En-Tec A/S of Copenhagen, Denmark and Bio-Gel A sold by Bio-Rad, of Brussels, Belgium. Preferably, the matrix is cross-linked allowing for a fast flow (FF) and thereby high production capacity. More preferably, chromatography of the present invention is carried out on a SP Sepharose® FF gel. In the following, the invention will be described using a cation-exchange step as primary isolation. When the primary isolation is a different step, it lies within the competence of the skilled person to arrive at suitable conditions for per¬ forming the present invention. This applies e.g. to pH and ionic strength of the various solutions as well as process temperature. The ionic strength of the solution being loaded onto the cation-exchange resin as well as the ionic strength of the eluting solution, are important for the type of purification obtained as well the efficiency of the purification. Thus, to make possible an efficient separation primarily of factor Mil and impurities, the ionic strength of the solution being loaded onto the cation-exchange resin and /or a solu¬ tion used for washing factor Mil adsorbed to the cation-exchange resin, should be in the range of from about 0.05 up to about 0.3 M, suitably from 0.1 up to 0.25 M, and preferably from 0.15 up to 0.2 M. The ionic strength of the solution used for eluting factor VIII from the cation-exchange resin should be at least about 0.3 M when the elution is commenced, suitably in the range of from 0 4 up to 2 M. and preferably from 0.5 up to 0.9 M. The ionic strength can be kert ror>:.ιr>? throughout the elution, or increased linearly or step-wise or combination-* tnere.-: The ionic strength of the solution being loaded onto trie >. ti n rv ^ nange resin as well as the solution used to eluate factor MIL are suitably obtained by the presence of an alkali metal chloride, e.g. sodium chloride or potassium chloride, or ammonium acetate, or any combination thereof. The solution being loaded onto the cation-exchange resin for adsorbing fac- tor Mil to the gel surface as well as the solution used for eluting the factor Mil molecules from the gel surface, should have a pH in the range of from about 5 up to about 8, suitably from 5.4 up to 7.0. With the present invention, the process temperature is less critical than with the prior art techniques, where a temperature well below ambient temperature was deemed necessary to avoid excessive loss in yield. With the present invention it is possible to run the primary isolation as well as the subsequent process steps at ambient temperature, without risking severe destabilization of the factor Mil mole¬ cules. Thus, adsorption as well as desorption of factor VIII in a cation-exchange step, can be carried out at a temperature of e.g. 18 up to 25°C. It is, however, suitable to adsorb as well as desorb out at a temperature below ambient, preferably at a temperature in the range of from about 2°C up to about 10°C. In the present invention, the cation-exchange chromatography step can be repeated, to give totally two, three or even more cation-exchange steps in a purifi¬ cation sequence. The use of several cation-exchange steps can reduce the content of impurities further, and at the same time increase the concentration of factor MIL These and other advantages, of course, have to be weighed against the increase in apparatus costs. If at least two cation-exchange steps are used, they can be used with or without intermediate process steps. The following examples are intended to further illustrate the present inven¬ tion, without limiting the scope of the invention. EXPERIMENTAL Preparation of recombinant factor Mil The production of recombinant factor VIII SQ (r-MII SQ) was essentially performed as described in patent WO-A-9109122, example 1-3. A DHFR deficient CHO cell-line (DG44N.Y.) was electroporated with an expression vector contain¬ ing the r-MII SQ gene and an expression vector containing the dihydrofolate- reductase gene. Following selection on selective media surviving colonies were amplified through growth in stepwise increasing amounts of methotrexate. Super¬ natant from the resulting colonies were individually screened for factor Mil acti- vity. A production clone was chosen and this was subsequently adapted to serum free suspension growth in a defined medium and finally a large scale cell cultiva¬ tion process was developed. Supernatant is collected after certain time periods and further purified as described below. Example 1 The efficiency of the present invention was established by determination of proteolytic activity modified according to Twining and disclosed in Boehringer Mannheim Biochemica. The method chosen was a protease assay with casein which was resorufin-labeled. By treatment with proteases, resorufin-labeled peptides are released from the casein. The concentration of these resorufin-labeled peptides in the supernatant is a measure of the proteolytic activity present. The test sample was incubated at 37 C for a period of time which was dependent upon the sample at issue. The absorption wave-length chosen was 574 nm throughout the tests. The conditioned medium (containing human serum albumin) was clarified and the disodium salt of EDTA was subsequently added in an amount ranging from 0.23 mM up to 23 mM. Preincubation of the conditioned medium with or without EDTA was con¬ ducted at 37 C for 2 h. After the addition of substrate, further incubation was car¬ ried out for 17 h. The pH in the incubation mixture was 7.5. Absorbance corrected, refers to the absorption after subtraction of the blank value. The results are given in the following Table. TABLE I Protease activity in a harvest solution with and without EDTA Experi¬ Protease ment EDTA Mean absorbance activity no. mM corrected (%) 1 0 (Blank) 970 0 — 2 0.23 1835 865 43 3 1.2 1141 171 8 4 2.3 1069 99 5 5 11.5 994 24 1 6 23 933 -37 -2 As is evident from the Table, the addition of a complexing agent to a har¬ vest solution dramatically reduces the protease activity. The experiments were repeated twice and the results obtained were well in agreement with the results disclosed in Table I. Example 2 Conditioned medium (containing human serum albumin) was clarified and imidazole subsequently added in an amount ranging from 3.6 mM up to 360 mM. The preincubation, incubation and the tests of relative protease activity were carried out according to Example 1. The results are given in the following Table. TABLE π Protease activity in a harvest solution with and without imidazole Experi¬ Protease ment Imidazole Mean absorbance activity no. mM corrected (%) 1 Blank 970 0 — 2 3.6 2891 1921 95 3 18 2985 2015 100 4 36 3190 2220 110 5 180 1258 288 14 6 360 1143 173 9 As is evident from the Table, the addition of a complexing agent to a harvest solution dramatically reduces the protease activity. Example 3 Conditioned medium (containing human serum albumin) was clarified and histidine subsequently added in an amount ranging from 0.14 mM to 13.6 mM. The preincubation, incubation and the tests of relative protease activity were carried out according to Example 1. The results are given in the following Table. TABLE m Protease activity in a harvest solution with and without histidine Experi- Protease ment Histidine Mean absorbance activity no. mM corrected (%) 1 Blank 970 0 — 2 0.14 2561 1591 79 3 0.7 2857 1887 94 4 1.4 3153 2183 108 5 7 1495 525 26 6 13.6 1684 714 35 As is evident from the Table, the addition of a complexing agent to a har¬ vest solution dramatically reduces the protease activity. Example 4 Conditioned mediums (containing human serum albumin) from two con¬ secutive harvests, were clarified and buffered with NHjAc. Each resulting solu- tion, with a pH of 6.8, was loaded onto a column containing SP Sepharose® FF sold by Pharmacia AB of Uppsala, Sweden. This cation-exchange chromatography step was performed at about 8°C. After washing, factor Mil was eluted with a salt buffer containing 0.8 M NaCl and 0.1 M NHjAc. The washing liquid as well as the elution liquid contained 3 mM EDTA in the tests with harvest solution no. 2. Tests without EDTA present was carried out for comparison (harvest solution no. 1). The preincubation, incubation and the tests of relative protease activity were carried out according to Example 1, except that the incubation time was 2 h. The concentration of unbound Ca2+-ions was determined by an ion-selective elec¬ trode. The results are given in the following Table. TABLE IV Protease activity after elution from a SP Sepharose® FF as primary isolation Harvest Protease Unbound solution EDTA Mean absorbance activity Ca^+ions no. mM corrected (%) (mM) - Blank 0.041 0 — 1 0 0.324 0.283 100 44 2 3 0.064 0.023 8 25 As is evident from the Table, the addition of a complexing agent to a washing and elution liquid dramatically reduces the protease activity. Example 5 Conditioned mediums (containing human serum albumin) from four har¬ vests being different from the previous Examples were clarified and buffered with NH4AC Each resulting solution, with a pH of 6.8, was loaded onto a column con¬ taining SP Sepharose® FF. This cation-exchange chromatography step was perfor- med at about 8°C. After washing, factor Mil was eluted with a salt buffer contain¬ ing 0.8 M NaCl and 0.1 M NH4AC. The washing liquid as well as the elution liquid contained 3 mM EDTA. Tests without EDTA present were carried out for compa¬ rison. The procoagulant activity of factor Mil was determined by use of a chro- mogenic substrate method, Coatest® Factor il kit (Chromogenix AB of Sweden) after storage at ambient temperature for up to 24 hours. The relative standard deviation (RSD) of the method is 7%. The results are given in the following Table. O 96/15150 l g PCΪYSE95/U1351 TABLE V Stability of factor Mil after elution from a SP Sepharose® FF as primary isolation followed by storage at ambient temperature Comparing Harvest Storage time Factor Mil activity (%)!) experiment solution for S-eluate In preparation In preparation No No (h) without EDTA with 3 mM EDTA 1 0 100 100 1 6 96 98 1 24 84 100 B 2 0 100 100 2 6 82 101 2 24 15 98 3 0 100 100 3 6 89 109 3 24 29 109 D 4 0 100 100 4 6 81 103 4 24 15 102 1) as compared to the zero-time value for each storage series As is evident from the Table, the addition of a complexing agent to a wash¬ ing and elution liquid dramatically increases the possibility to maintain the activity of factor MIL Example 6 A conditioned medium (containing human serum albumin) from a different harvest than the previous Examples, was clarified and buffered with NH4AC. The resulting solution, with a pH of 6.8, was loaded onto a column containing SP Sepharose® FF . This cation-exchange chromatography step was performed at about 8°C. After washing, factor Mil was eluted with a salt buffer containing 0.4 M NaCl and 0.1 M NH4AC. After elution, various amounts of EDTA were added to the resulting solution. Tests without EDTA present were carried out for compa- rison. The procoagulant activity of factor MTI was determined after storage at ambient temperature for up to 246 hours, in accordance to the procedure described in Example 5. The results are given in the following Table. TABLE M Activity of factor Mil in % of the initial value after addition of EDTA to an eluted solution from a SP Sepharose® FF as primary isolation EDTA Storagetime(h) (mM) 0 2.5 5 10 24 48 72 100 246 0 100 79 55 30 1.7 0.01 100 77 59 32 1.9 0.03 100 76 59 33 2.1 0.1 100 82 65 43 4.6 0.3 100 79 71 55 11 1.0 100 90 97 97 75 54 3.0 100 92 102 104 100 96 80 91 72 As is evident from the Table, the addition of a complexing agent to a solu- tion already eluted from a cation-exchange resin, dramatically increases the possibility to maintain the activity of factor Mil. Example 7 A conditioned medium (containing human serum albumin) from a different harvest than the previous Examples, was clarified and buffered with NH4AC. The resulting solution, with a pH of 6.8, was loaded onto a column containing SP Sepharose® FF. This cation-exchange chromatography step was performed at about 8°C. After washing, factor M T was eluted with a salt buffer containing 0.8 M NaCl and 0.1 M NH4AC. After elution, various amounts of EDTA were added to the resulting solution. Tests without EDTA present were carried out for compa- rison. The procoagulant activity of factor Mil was determined after storage at ambient temperature for up to 28 hours, in accordance to the procedure described in Example 5. The results are given in the following Table. TABLE MI Activity of factor Mil in % of the initial value after addition of EDTA to an eluted solution from a SP Sepharose® FF as primary isolation EDTA Storage time (h) (mM) 0 5 28 0 100 82 0 1 100 119 64 2 100 120 100 3 100 120 90 4 100 109 103 5 100 116 91 As is evident from the Table, the addition of a complexing agent to a solution already eluted from a cation-exchange resin, dramatically increases the possibility to maintain the activity of factor MIL Example 8 A conditioned medium (containing human serum albumin) from a different harvest than the previous Examples, was clarified and buffered with NH4AC The resulting solution was loaded onto a column containing SP Sepharose® FF. This cation-exchange chromatography step was performed at 10°C. After washing, fac- tor Mil was eluted with a salt buffer containing 0.8 M NaCl and 0.1 M NH4AC. After elution, EDTA or 1,10-Phenanthroline were added to the resulting solution. The procoagulant activity of factor Mil was determined after storage at ambient temperature for up to 24 hours, in accordance to the procedure described in Example 5. The results are given in the following Table. TABLE MLT Stability of factor Mil after elution from a SP Sepharose® FF as primary isolation Experi¬ Incuba¬ Phenan¬ ment tion time EDTA throline Factor Mil activity no. (h) (mM) (mM) (IU/ml) (%) 1 0 0 0 888 100 2 4.5 0 0 448 50 3 4.5 3 0 813 92 4 4.5 0 5 750 84 5 4.5 0 11 8 ^ ^s 6 7.5 0 0 264 .V> 7 7.5 3 0 862 97 8 7.5 0 5 964 109 9 7.5 0 11 996 112 10 24 0 0 8 1 11 24 3 0 763 86 12 24 0 5 933 105 13 24 0 11 916 103 As is evident from the Table, the addition of a complexing agent to a solution already eluted from a cation-exchange resin, dramatically increases the possibility to maintain the activity of factor MIL

Claims: CLAIMS 1. A process for reducing the degradation of recombinant coagulation factor Mil caused by metal-dependent proteases, characterized in that an inhibitor of metal-dependent proteases is added to a solution after harvest, and in that the inhibitor is selected from the group consisting of i) complexing agents with a stronger affinity for the alkaline-earth metal ion or metal ion of the protease than for the ion or ions stabilizing the factor Mil molecule and ii) compounds structurally related to the natural substrate of the protease and con¬ taining an electronegative moiety. 2. A process according to claim 1, characterized in that the complexing agent is selected from nitrogenous polycarboxylic acids, heterocyclic amines, phenanthrolines, pyridine carboxylic acids, quinolines, salicylates, N-acyl derivatives of collagen, N-aminoacyl derivatives of β-diketones, thiol compounds and di- and tricarboxylic acids. 3. A process according to claim 2, characterized in that the complexing agent is a nitrogenous polycarboxylic acid. 4. A process according to claim 3, characterized in that the nitrogenous polycarboxylic acid is ethylenediamine tetraacetic acid (EDTA). 5. A process according to claim 2, characterized in that the complexing agent is selected from the group consisting of 1,10-phenanthroline, imidazole and L-histidine. 6. A process according to claim 1, characterized in that the compound containing an electronegative moiety is selected from the group consisting of hydroxamates, phosphoramidates and carboxylates. 7. A process according to any previous claim, characterized in that the solu¬ tion is selected from the group consisting of the harvest solution and any aqueous solution being fed to or leaving the primary isolation. 8. A process according to claim 7, characterized in that the primary iso¬ lation is a chromatography step selected from the group consisting of cation exchange, anion exchange, affinity and hydrophobic interaction. 9. A process according claim 8, characterized in that the primary isolation is a chromatography step using a cation-exchange gel. 10. A process according to claim 9, characterized in that the ligands of the gel are sulfopropyl or sulfonate. 11. A process according to any previous claim, characterized in that the inhibitor is added to the harvest solution. 12. A process according to claim 11, characterized in that the inhibitor is a nitrogenous polycarboxylic acid in a concentration within the range of from about 0.01 up to about 10 mM. 13. A process according to any previous claim, characterized in that the inhibitor is added to a liquid used for washing the factor Mil molecules in the pri- mary isolation. 14. A process according to claim 13, characterized in that the inhibitor is a nitrogenous polycarboxylic acid in a concentration within the range of from 0.1 up to 10 mM. 15. A process according to any of claims 8-10, characterized in that the inhibitor is added to an elution liquid. 16. A process according to claim 7, characterized in that the inhibitor is added to a solution resulting from the primary isolation. 17. A process according to claims 15 or 16, characterized in that the inhibitor is a nitrogenous polycarboxylic acid in a concentration within the range of from about 0.5 up to about 15 mM. 18. A process according to claims 9 or 10, characterized in that the factor Mil molecules adsorbed to the cationic gel is eluted with a solution with an ionic strength of at least about 0.3 M. 19. A process according to any previous claim, characterized in that the cell culture used for producing the recombinant coagulation factor Mil is essentially free of the von Willebrand factor (vWf). 20. A process according to any previous claim, characterized in that the recombinant coagulation factor VIII is a deletion derivative of full-length factor Mil with retained coagulant activity. 21. A process according to claim 20, characterized in that the deletion deri¬ vative of factor VLTJ is deletion derivative recombinant factor Mil SQ (r-MII SQ). 22. A process according to any previous claim, characterized in that the metal-dependent protease is a metallo protease. • 23. A process according to claim 22, characterized in that the metallo protease is a metalloendopeptidase. 24. A process according to any previous claim, characterized in that the metal ion required for activity of the metal-dependent protease is selected from the group consisting of Zn^+, Cu^+, Fe2+, Fe^" 1 ", Mn2+, Co^+and Cd2+ 25. A process according to claim 24, characterized in that the metal ion required for activity of the metal-dependent protease is Zn^ + . 26. An aqueous solution containing recombinant factor Mil, which has been puri¬ fied in a process according to any of claims 1-25. 27. Use of an aqueous solution containing recombinant factor Mil purified accor¬ ding to any of claims 1-25, for the manufacture of a medicament for administration to a patient having the symptoms of hemophilia. 28. Method for treatment of hemophilia by administration of a therapeutically effective amount of recombinant factor Mil which has been purified according to any of claims 1-25.

Inventors: ALMSTEDT ANNELIE, OESTLIN ANNA, SANDBERG HELENA, SMEDS ANNA-LISA, WRANGEL MARIA, ALMSTEDT, ANNELIE, OESTLIN, ANNA, SANDBERG, HELENA, SMEDS, ANNA-LISA, WRANGEL, MARIA
Applicants: ALMSTEDT ANNELIE, OESTLIN ANNA, PHARMACIA AB, SANDBERG HELENA, SMEDS ANNA LISA, WRANGEL MARIA, ALMSTEDT, ANNELIE, OESTLIN, ANNA, SANDBERG, HELENA, SMEDS, ANNA-LISA, WRANGEL, MARIA
Application year: 1995
Main classification: C07K14
IPC codes: A61K35, A61K38, A61P7, C07K14