WO1998040474A2 - Aktivierter vitamin k-abhängiger blutfaktor und verfahren zu dessen herstellung - Google Patents
Aktivierter vitamin k-abhängiger blutfaktor und verfahren zu dessen herstellung Download PDFInfo
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- WO1998040474A2 WO1998040474A2 PCT/EP1998/001364 EP9801364W WO9840474A2 WO 1998040474 A2 WO1998040474 A2 WO 1998040474A2 EP 9801364 W EP9801364 W EP 9801364W WO 9840474 A2 WO9840474 A2 WO 9840474A2
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- Prior art keywords
- protease
- factor
- activation
- blood factor
- protein
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/48—Hydrolases (3) acting on peptide bonds (3.4)
- C12N9/50—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
- C12N9/64—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/48—Hydrolases (3) acting on peptide bonds (3.4)
- C12N9/50—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
- C12N9/64—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue
- C12N9/6421—Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue from mammals
- C12N9/6424—Serine endopeptidases (3.4.21)
- C12N9/647—Blood coagulation factors not provided for in a preceding group or according to more than one of the proceeding groups
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K38/00—Medicinal preparations containing peptides
Definitions
- the present invention relates to an activated vitamin K-dependent blood factor and a method for its production.
- proteases occur in the human organism itself, especially in the blood plasma.
- factor X is activated, it is a special feature that the Venom from Vipera Russelli (Russell's Viper Venom, RW) is a selective factor X activator that is also used technically to obtain factor Xa can. Since knowledge of the transmission of animal viruses to little-related animal species (prion problem), however, the use of xenogenic animal proteins as auxiliaries for the manufacture of medicines has been rejected. However, since suitable human proteases are not available in a technically sufficient amount Are available, the use of RW for preparative factor X activation is still the standard method.
- Vipera Russelli Russell's Viper Venom, RW
- proteolytic enzymes derived from prokaryotes from low eurkaryotes, e.g. Mushrooms, or from higher eukaryotes, e.g. Plants that can be isolated are known to have low substrate specificity. For this reason, they are mainly used for the total degradation of proteins in raw cell extracts, in order in this way to obtain other cell components, e.g. Carbohydrates or nucleic acids to separate or isolate. In addition, these proteases are also used for the sequencing and characterization of proteins by degradation to small peptides. Until now, the use of bacterial or vegetable proteases or of proteases from fungi as activators of plasma proteins or plasma protein cofactors or inhibitors from the group of prothrombin complex proteins was not known.
- the object of the present invention is to provide a method for activating profactors in the field of blood coagulation with the aid of highly specific proteases that are not of animal origin.
- the method according to the invention is particularly suitable for activating vitamin K-dependent blood factors. Activation of human blood factors from the groups of factor II, VII, IX, X and protein C is particularly suitable. The examples below show the advantages obtained in the activation of factor X to factor Xa- ⁇ .
- the method according to the invention is equally suitable for obtaining naturally occurring, genetically engineered, as well as chemically or genetically modified blood factors.
- protease used according to the invention a proteolytic enzyme from prokaryotes can be assumed.
- the bacterial proteases should be mentioned here in particular, e.g. Thermolysin, clostripain proteases IX and X from Bacillus polymyxa and protease IX from Bacillu ⁇ thermoproteolyticus.
- proteases from low eukaryotes e.g. Use fungi, in particular protease XXIII from the Aspergillus oricae mold, in the process according to the invention.
- proteolytic enzymes from higher eukaryotes such as e.g. Plants.
- proteolytic enzymes belonging to the group of cysteine proteases are suitable. Examples include: Bromelain (e.g. from pineapple comosus), Papain (e.g. from the milk juice of Carica papaya) or Ficin (e.g. from Ficus carica).
- the proteolytic enzymes from prokaryotes, molds and plants mentioned have a low substrate specificity. It was therefore surprising to find that the use of these enzymes enables highly specific factors in blood coagulation to be activated.
- These enzymes are either selected native enzymes, but also modified enzymes or enzyme derivatives, in particular also enzymes produced by recombinant DNA technology.
- cysteine proteases that they can fully develop their broad protease activity under reductive conditions or in the presence of activators containing sulfhydrile groups. For this reason, SH donors are often added to the incubation buffer as effectors when incubating with these enzymes.
- the A broad spectrum of activity of these proteases can, however, be shifted by moving from the optimal incubation conditions to suboptimal conditions, ie conditions outside the pH or temperature optimum or in the event of partial or complete absence of necessary cofactors or effectors, or in the presence of special effectors, in such a way that special substrates, such as, for example Plasma proteins, are no longer completely degraded and therefore do not lose their activity, provided that it concerns profactors to be activated. Rather, the activation is stopped at the target substrate level and the activation products are obtained as such. This is also demonstrated below for the first time using the example of the activation of factor X to factor Xa, in particular ⁇ factor Xa.
- cysteine proteases can also be achieved by subjecting the crude enzyme preparations purified from plants to further purification measures, for example chromatography, in order to isolate those protein fractions whose protease activity shows a restricted substrate spectrum. While this measure alone may not yet be suitable for achieving the desired highly specific activators, it is suitable in conjunction with a further measure for increasing the specificity of proteases, namely by oxidation thereof, the proteases due to the contact with atmospheric oxygen be reduced in their activity and activity spectrum. It follows from this that particularly oxidized cysteine proteases are suitable for the process according to the invention, this preferably being the case with chromatographically enriched or purified cysteine proteases. It is particularly preferred that the protease has an at least two-fold increased specific blood factor activation activity compared to the crude extract from plants or cell cultures or compared to the non-specific proteolytic activity or towards the non-specific proteolytic activity.
- the substrate spectrum can be narrowed down by adding defects to the incubation buffer of the enzymes with the substrates to be activated.
- Heavy metal ions or alkaline earth metal ions are to be mentioned in particular as defectors.
- the addition of calcium ions is particularly preferred here. For example, shown in the following examples that when factor X is activated with the addition of calcium ions, the activation product ⁇ -factor Xa is obtained, with other cleavage products only being produced in negligible amounts.
- the activation reaction can proceed more intensely without the addition of calcium ions and can also be modulated with regard to the activated factor obtained.
- ⁇ factor Xa and / or ⁇ factor Xa can also be produced according to the invention.
- the enzymes in question here can be used in immobilized form. This will make it easy to separate the protease from the substrate, e.g. by filtration. Furthermore, the use of immobilized, i.e. enzymes bound to a solid phase the repeated use of the same. In the case of the secondary modified proteins, e.g. by oxidation, by immobilization, i.e. irreversibly fixed by a covalent binding of the enzyme to a carrier material in its conformation as it is after the conversion into a highly specific activator.
- the method according to the invention is suitable for activating natural as well as recombinantly produced blood factors.
- the proteolytic interface can be modified by an amino acid sequence which is then specifically recognized and cleaved by a defined protease, so that activation is only possible more or also with a protease which does not correspond to the physiological activation mechanism.
- This specially constructed analog is, for example, an analog of a vitamin K-dependent blood factor such as factor X.
- the region around the Arg52-Ile53 position which is the interface for factor IXa, could be replaced by another amino acid sequence.
- the amino acids Arg52, Ile53 could be replaced by the sequence Glu-Gly, which then rules out cleavage by FIXa and activation by factor IXa, but enables proteolytic digestion with endoproteinase Glu C from Staphylococcus auraeus V8.
- a bacterial enzyme which can be prepared in a highly pure form and does not pose a risk of contamination with an animal or human protein, can thus be used for the activation of factor X.
- Gly-Ser can also be introduced as the cleavage sequence, which then cleaves with plant proteases, e.g. with Ficin.
- the blood factor activated according to the invention is subjected to further purification measures in order to remove proteolytic degradation products that may have arisen in this way. Chromatographic purification processes or purification by gel filtration are particularly preferred here.
- the invention also encompasses a pharmaceutical preparation containing a blood factor and a protease derived from plants or prokaryotes with a specificity for the blood factor.
- the protease can also be a mammalian, in particular a human-derived protease. According to the invention, however, no coagulation factor is used as the protease.
- plasma proteins for example also vitamin K-dependent proteins, are contained as blood factors in this pharmaceutical preparation.
- the pharmaceutical preparation comprises an activated vitamin K-dependent blood factor and the protease.
- This blood factor is preferably human and native.
- the protease in particular a purified protease, is also to be used as such, in which case the vitamin K-dependent blood factor comes from a bleeding wound.
- the factor X activator in a pharmaceutical carrier material, for example in a dressing or in a powder or as an ointment, the effect of the coagulation activator which triggers blood coagulation can be used here.
- Another pharmaceutical preparation also includes a blood factor which is present as a pro-protein and which contains a pro-protein-cleaving protease isolated from plants, fungi or prokaryotes or genetically engineered in cells of this species.
- Proteases of this type with a specificity for pro-proteins are, for example, as furin (Van de Ven, WJ et al, Enzyme 45: 257-270, 1991) or Paired Basic Amino Acid Residue Cleaving Enzyme, PACE, (Rehemtulla, A et al, Biochemistry 32: 11586-11590, 1993). If the mature protein resulting from the pro-protein is particularly unstable in a pharmaceutical preparation, the mature protein can be prepared in situ by simultaneous administration of the pro-protein processing enzyme and is then available therapeutically. Furthermore, further activation with an activator protease is possible, provided the mature protein has to be converted into an active form by further proteolytic digestion.
- a therapeutic set consisting of the stable pro-protein and the processing or activating proteolytic enzyme, therefore enables the administration of unstable proteins as active substances for the first time.
- the invention further comprises an activated vitamin K-dependent blood factor, as is obtained by the method according to the invention.
- the human, activated blood factor obtained according to the invention is characterized in that it is not contaminated by an animal protease.
- the factor X was purified from a prothrombin complex factor preparation, which contained the factors FII, FIX, FX, Protein C and Protein S, and which according to the method of Brummelhui ⁇ , (Brummelhuis HGJ, Preparation of the Prothrombin Complex. In: Methods of Plasma Protein Fractionation , edited by Curling, JM, New York: Academic Press, 1980, p. 117-128). was prepared and heat-treated for virus inactivation according to EP 0 159 311. A lyophilizate containing the prothrombin complex factors was dissolved in distilled water corresponding to an activity of 50,000 U FX / 1 and adjusted to pH 7.0.
- Calcium phosphate of a buffer 20 mmol / 1 Tris-HCl, pH 7.0, containing 10% ammonium sulfate washed by resuspending and centrifuged again each time.
- the pellet was stirred for 1 hour at room temperature with 1 mmol / 1 sodium phosphate buffer, pH 7.0 (25 ml elution solution / g calcium phosphate used).
- the chromatography material was loaded with 10 U FX / ml gel. Previously, the FX-containing solution was buffered by gel filtration against a buffer, 25 mmol / 1 trisodium citrate dihydrate, 100 mmol / 1 NaCl, pH 6.0. This factor X solution was
- Fractions were collected during the elution, which were based on the content of the prothrombin complex proteins factor X, protein C, Factors IX and II were examined using standard coagulation tests.
- the fractions containing factor X, which were poor in other prothrombin complex proteins, were combined and then immobilized via a monoclonal antibody, purified from ascites, which was directed against factor X and which was immobilized on Actigel ALD (sterogens, bioseparations, Arcadia, CA) , further cleaned.
- the protein solution containing FX was adsorbed onto the gel with a loading of 10 U FX / ml gel.
- This factor X preparation was freed from traces of contaminating protein, in particular monoclonal antibody bleeding from the immunoaffinity chromatography column, by adsorption on phenylsepharose high performance, Pharmacia-Biotech.
- the FX-containing solution was adjusted to 1.8 mmol / 1 NaCl and a pH of 7.4 after the diafiltration.
- the hydrophobic interaction chromatography gel was equilibrated in a chromatography column with 20 mmol / 1 Tris-HCl, 2 mol / 1 NaCl, 7.4 and the factor X solution set was loaded onto the column with a load of 30 U FX / ml gel.
- the FX-containing flow from the column was collected and subsequently concentrated by ultrafiltration over a membrane with an exclusion limit of 10,000 Daltons to 1/20 of the starting volume and then against a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, pH 7.4, diafiltered.
- the highly purified factor X solution obtained in this way had a specific activity of approximately 100 U / mg protein.
- the chromogenic peptide substrate CH 3 OCO-D-CHA-Gly-Arg-pNA is hydrolyzed by factor Xa, whereby CH 3 OCO-D-CHA-Gly-Arg-OH and paranitroaniline are formed.
- the kinetics of the increase in paranitroaniline is measured spectrophotometrically at 405 nm.
- the increase in optical density (OD) is proportional to the content of factor Xa in the sample to be quantified.
- ⁇ l of a sample containing factor Xa are mixed with 50 ⁇ l of dilution buffer and incubated at 37 ° C. for 90 seconds. Then 100 ⁇ l of the substrate solution are added and the increase in OD per minute at 37 ° C. at 405 nm is determined. The increase in OD must remain constant linear over the measurement period.
- Activation of purified factor X from example 1 was carried out with the enzymes, clostripain (Calbiochem, La Jolla, CA) 10 U / ml, thermolysin (Calbiochem, La Jolla, CA) 200 U / ml, papain (Boehringer Mannheim, FRG) 400 ⁇ g / ml and ficin (Sigma Chemicals Co., St. Louis, MO) 20 ⁇ g / ml, in a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, 5 mmol / 1 CaCl 2 , pH 7, 4, performed at 37 ° C and incubation for several hours.
- the concentration of factor X was 3.2 U / ml.
- samples were taken from the respective incubation mixtures and examined for factor Xa activity, as described in Example 2.
- the results are shown in Figure 1. It was shown that an activation of factor X 12. was possible with all the enzymes used and led to the highest yield of factor Xa for thermolysin after 2 hours.
- the activation phase which reached a maximum of between 30 minutes and 2 hours depending on the enzyme, was followed by inactivation of the resulting factor Xa. When activating ficin, a constant activation with stable factor Xa activity was demonstrated even after 19 hours.
- Factor X activator from Vipera russellii (RW, Pentapharm AG, Basel, CH) is known from the literature as a non-plasmatic factor X activator with a high selectivity, which is commonly used for in vitro activations of factor X.
- the activation of highly purified factor X from example 1 with RW was compared to the activation with the plant factor X activator, ficin.
- the highly purified factor X was used in a concentration of 4 U / ml in a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, 5 mmol / 1 CaCl 2 , pH 7.4, and with either Incubate 2.7 ⁇ g / ml RW (Pentapharm AG, Basel, CH) or 20 ⁇ g / ml Ficin (Sigma Chemicals Co., St. Louis, MO) at 37 ° C.
- the factor X before activation the factor X after activation with RW and after activation with ficin, and subsequent blot on nitrocellulose membranes and detection with an anti-factor X-polyclonal antibody and immunostaining were analyzed by standard methods.
- the result is shown in Figure 3. It was shown that the homogeneous factor X was split into several factor X-specific protein fragments of smaller molecular mass than the non-activated factor X before activation by both the activator RW and the activator ficin, after activation with RW a mixture of alpha- and beta factor Xa was formed, these two activation products of factor X being contained in approximately the same amount, and at least three further activation products could be identified.
- beta factor Xa was obtained as the main product (see arrow), whereby, as in the case of activation with RW, three further activation products could also be detected, although in contrast ; for activation with RW had a larger molar mass difference to the main product beta factor Xa, so that these could be separated off by simple further methods, for example gel filtration.
- factor X was used in a concentration of 4 U / ml in a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, pH 7.4, with 2 ⁇ g ficin / ml analogously to Example 4 at 37 ° C incubated for 24 hours, using the buffer medium (1) 2 mmol / 1 CaCl 2 , (2) 1 mmol / 1 cysteine, (3) 1 mmol / 1 cysteine and 2 mmol / 1 EDTA and (4) 1 mmol / 1 cysteine and 2 mmol / 1 CaCl 2 was added. After 24 hours of incubation, the factor Xa activity was determined according to Example 2. The results are shown in Table 1.
- the beta factor Xa obtained in this way can now easily be freed from residues of ficin still present in the mixture by conventional chromatographic purification methods. These include simple gel filtration, ion exchange chromatography or substrate affinity chromatography, for example on immobilized benzamidine, which is able to selectively bind factor Xa.
- the free cysteine is removed by gel filtration over Sephadex G50 and with the same phosphate buffer 1 + 3 '7 further diluted. The total amount was then applied to a Mono S HR 5/5 cation exchange chromatography column, from Pharmacia, at a flow rate of 1 ml / min. It was then washed with 45 column volumes of the same phosphate buffer and then a gradient elution was carried out, the phosphate concentration being increased continuously to 185 mmol / l in the same buffer composition over 55 column volumes. The result is shown in Figure 5. The protein mixture was separated into several individual proteins by the elution. As can be seen in the elution profile from the absorption at 280 nm (protein).
- the individual fractions were then examined for FX-activating enzyme activity using the factor Xa assay described in Example 2 and it was found that a protein peak eluting at 49 ml elution volume and a protein peak eluting between 68 and 69 ml elution volume had the highest factor X activator activity (- -x- -).
- the fractions were examined for protease activity using an unspecific protease substrate.
- the chromogenic protease substrate benzoyl-DL-arginine-p-nitroanilide hydrochloride, which under the conditions and according to the method of Eglund et al.
- the fraction containing the highest factor X activator activity in relation to the protein content was then incubated for 15 hours at 4 ° C. under the influence of atmospheric oxygen. This enabled the factor X activator activity to be increased further in relation to the non-specific protease activity.
- Crystallized ficin (Sigma) in crystal suspension was diluted to a concentration of 2.5 mg / ml and against a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, pH 7.4, by gel filtration over Sephadex G50 (Pharmacia) buffered.
- a pre-activated gel Actigel ALD Superflow (Sterogenic Bioseparations, Arcadia, CA) was washed with a buffer containing 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, pH 7.4, and then in a ratio of 1 + 1 with the offset to be immobilized ficin-containing solution and 1/15 of the volume of the coupling solution (Sterogene Bioseparations, Arcadia, CA) incubated for 3 hours at room temperature.
- the immobilizate was then separated off on a sintered suction filter and alternately washed excessively with a 20 mmol / 1 Tris-HCl, 150 mmol / 1 NaCl, pH 7.4, buffer and a 20 mmol / 1 Tris-HCl, 2 mmol / 1 NaCl , pH 7.4, buffer from the unbound ficin and the Coupling reagents exempt.
- the ficin immobilizate was subsequently used to activate factor X as follows.
- the activation was carried out in incubation mixtures containing 4 units / ml of factor X and 3 ⁇ g / ml of the activated ficin preparation in a buffer system of 20 mmol / 1 Tris-HCl, 150 mmol / 1 sodium chloride, pH 7.4 in and 10
- Presence of calcium and manganese ions carried out.
- the batches contained either 2 mmol / 1 calcium ions, 1 mmol / 1 manganese (II) ions or a combination of the two metal ions.
- the batches were examined for the composition of the activation products by means of SDS polyacrylamide gel electrophoresis. The result of the electrophoretic separation was visualized using the silver staining method and the intensity of the separated bands was evaluated densitometrically. The result of this evaluation is shown in the table below.
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Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU68295/98A AU740727B2 (en) | 1997-03-12 | 1998-03-10 | Activated vitamin K-dependent blood factor and method for the production thereof |
HU0001505A HUP0001505A3 (en) | 1997-03-12 | 1998-03-10 | Activated vitamin k-dependent blood factor and method for the production thereof |
EP98913692A EP0968280A1 (de) | 1997-03-12 | 1998-03-10 | Aktivierter vitamin k-abhängiger blutfaktor und verfahren zu dessen herstellung |
CA002284122A CA2284122A1 (en) | 1997-03-12 | 1998-03-10 | Activated vitamin k-dependent blood factor and method for the production thereof |
SK1246-99A SK124699A3 (en) | 1997-03-12 | 1998-03-10 | Activated vitamin k-dependent blood factor and method for the production thereof |
JP53920998A JP2001514516A (ja) | 1997-03-12 | 1998-03-10 | 活性化ビタミンk依存性血液因子およびその製造方法 |
NO994394A NO994394L (no) | 1997-03-12 | 1999-09-10 | Aktivert vitamin K-avhengig blodfaktor og fremgangsmÕte for fremstilling av denne |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE19710190.9 | 1997-03-12 | ||
DE19710190A DE19710190A1 (de) | 1997-03-12 | 1997-03-12 | Aktivierter Vitamin K-abhängiger Blutfaktor und Verfahren zu dessen Herstellung |
Publications (2)
Publication Number | Publication Date |
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WO1998040474A2 true WO1998040474A2 (de) | 1998-09-17 |
WO1998040474A3 WO1998040474A3 (de) | 1999-02-11 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/EP1998/001364 WO1998040474A2 (de) | 1997-03-12 | 1998-03-10 | Aktivierter vitamin k-abhängiger blutfaktor und verfahren zu dessen herstellung |
Country Status (9)
Country | Link |
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EP (1) | EP0968280A1 (de) |
JP (1) | JP2001514516A (de) |
AU (1) | AU740727B2 (de) |
CA (1) | CA2284122A1 (de) |
DE (1) | DE19710190A1 (de) |
HU (1) | HUP0001505A3 (de) |
NO (1) | NO994394L (de) |
SK (1) | SK124699A3 (de) |
WO (1) | WO1998040474A2 (de) |
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EP0068047A2 (de) * | 1981-06-25 | 1983-01-05 | Serapharm GmbH & Co. KG | Angereichertes Plasmaderivat zur Unterstützung von Wundverschluss und Wundheilung |
WO1991002065A1 (en) * | 1989-08-11 | 1991-02-21 | Zymogenetics, Inc. | Cell culture methods for producing activated protein c |
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WO1993006855A1 (en) * | 1991-10-11 | 1993-04-15 | Novo Nordisk A/S | Hemostatic composition for local hemostasis |
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WO1993013208A1 (en) * | 1991-12-31 | 1993-07-08 | Zymogenetics, Inc. | Methods for producing thrombin |
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WO1994021284A1 (en) * | 1993-03-15 | 1994-09-29 | Pharma Pacific Pty. Ltd. | Therapeutic formulation and method |
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DE4430205A1 (de) * | 1994-08-26 | 1996-02-29 | Behringwerke Ag | Zusammensetzungen, die als Gegenmittel für Blut-Antikoagulanzien geeignet sind und deren Verwendung |
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WO1996023487A1 (de) * | 1995-02-02 | 1996-08-08 | Knoll Ag | Arzneiform zur abgabe von kollagenase an wunden und verfahren zu ihrer herstellung |
US5589571A (en) * | 1994-10-28 | 1996-12-31 | Cor Therapeutics, Inc. | Process for production of inhibited forms of activated blood factors |
-
1997
- 1997-03-12 DE DE19710190A patent/DE19710190A1/de not_active Withdrawn
-
1998
- 1998-03-10 SK SK1246-99A patent/SK124699A3/sk unknown
- 1998-03-10 AU AU68295/98A patent/AU740727B2/en not_active Ceased
- 1998-03-10 WO PCT/EP1998/001364 patent/WO1998040474A2/de active IP Right Grant
- 1998-03-10 EP EP98913692A patent/EP0968280A1/de not_active Withdrawn
- 1998-03-10 CA CA002284122A patent/CA2284122A1/en not_active Abandoned
- 1998-03-10 JP JP53920998A patent/JP2001514516A/ja active Pending
- 1998-03-10 HU HU0001505A patent/HUP0001505A3/hu unknown
-
1999
- 1999-09-10 NO NO994394A patent/NO994394L/no not_active Application Discontinuation
Patent Citations (13)
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EP0068047A2 (de) * | 1981-06-25 | 1983-01-05 | Serapharm GmbH & Co. KG | Angereichertes Plasmaderivat zur Unterstützung von Wundverschluss und Wundheilung |
WO1991002065A1 (en) * | 1989-08-11 | 1991-02-21 | Zymogenetics, Inc. | Cell culture methods for producing activated protein c |
EP0443724A1 (de) * | 1990-02-20 | 1991-08-28 | Baxter International Inc. | Gereinigtes, virusfreies menschliches Thrombin |
WO1993006855A1 (en) * | 1991-10-11 | 1993-04-15 | Novo Nordisk A/S | Hemostatic composition for local hemostasis |
WO1993009807A1 (en) * | 1991-11-18 | 1993-05-27 | The Scripps Research Institute | Methods of inhibiting thrombosis via elevation of circulating endogenous activated protein c levels |
WO1993013208A1 (en) * | 1991-12-31 | 1993-07-08 | Zymogenetics, Inc. | Methods for producing thrombin |
US5432062A (en) * | 1992-04-06 | 1995-07-11 | Immuno Aktiengesellschaft | Method of proteolytically cleaving prothrombin to produce thrombin |
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Also Published As
Publication number | Publication date |
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DE19710190A1 (de) | 1998-09-17 |
JP2001514516A (ja) | 2001-09-11 |
WO1998040474A3 (de) | 1999-02-11 |
SK124699A3 (en) | 2000-06-12 |
NO994394D0 (no) | 1999-09-10 |
EP0968280A1 (de) | 2000-01-05 |
AU6829598A (en) | 1998-09-29 |
CA2284122A1 (en) | 1998-09-17 |
HUP0001505A3 (en) | 2002-01-28 |
AU740727B2 (en) | 2001-11-15 |
HUP0001505A1 (hu) | 2000-09-28 |
NO994394L (no) | 1999-11-11 |
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