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US4470969A
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Process for producing a concentrate of coagulation factors VII and VIIa
Assignee: Bayer Corp
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Filing: 1983-12-02
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Granted: 1984-09-11
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Expires: 2003-12-02
Abstract
Abstract There is disclosed a process for producing coagulation factors VII and VIIa in relatively high purity by contacting an aqueous preparation containing factors VII and VIIa with a protein precipitant and separating the coagulation factors and other proteins therefrom, contacting the resulting solution with a divalent metal salt adsorbent having selective affinity for calcium-binding coagulation factors and eluting the coagulation factors therefrom, and contacting the eluate with an anionic exchange resin and selectively eluting coagulation factors VII and VIIa therefrom by step or gradient elution techniques to obtain factors VII and VIIa free of other coagulation factors and other proteins.
Inventors
- 👤 Nazreen Pancham
- 👤 Timothy Zuffi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 02:20
CPC Classifications
C; C12; C12N; C12N9/00; C12N9/14; C12N9/48; C12N9/50; C12N9/64; C12N9/6421; C12N9/6424; C12N9/6437; C12Y; C12Y304/00; C12Y304/21; C12Y304/21021; A; A61; A61K; A61K38/00; Y; Y10; Y10S; Y10S530/00; Y10S530/827; Y10S530/829; Y10S530/83; Y10S530/831
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
335 words
A process for producing a concentrate consisting essentially of blood coagulation factors VII and VIIa and having a specific activity in the range of about 500 to 3000 u/A 280 consisting essentially of the steps of: (a) contacting an aqueous preparation, in the form of a solution or suspension, of plasma proteins containing factors VII and VIIa, at a temperature of about 4° to 25° C. and at a pH of about 4 to 9 and in the presence of a suitable buffer to maintain the pH at about 4 to 9, with about 1 to 10% (weight/volume, based on total weight of plasma proteins) of polyethylene glycol having a molecular weight of about 200 to 20,000 to precipitate from the preparation PEG-precipitable proteins and other insoluble matter present in the aqueous preparation to obtain an aqueous supernatant containing factors VII and VIIa separated from the PEG-precipitable proteins and insoluble matter; (b) contacting the aqueous supernatant from step (a), adjusted to a pH of about 6 to 8, with an adsorbent having selective affinity for calcium-binding proteins, including factors II, VII, IX and X, selected from the group of water-insoluble divalent metal salts, to adsorb calcium-binding proteins; (c) selectively eluting, by techniques selected from step and gradient elution techniques, factors II, VII and VIIa, IX and IXa, and X and Xa from the protein-bound adsorbent from step (b) by the addition of a buffer solution containing suitable soluble salts effective to displace the bound proteins and collecting the eluate pool; (d) contacting the eluate pool from step (c), adjusted to a pH of about 3 to 11, with an anionic exchange resin having affinity for the calcium-binding proteins, including factors II, VII and VIIa, IX and IXa, and X and Xa, and adsorbing thereon the calcium-binding proteins; and (e) selectively eluting, by techniques selected from step and gradient elution techniques, factors VII and VIIa from the protein-bound adsorbent from step (d) by the addition of a buffer solution containing suitable salts in increasing ionic strength.
Claim 2
Dependent Claim
335 words
A process for producing a concentrate consisting essentially of blood coagulation factors VII and VIIa and having a specific activity in the range of about 500 to 3000 u/A 280 consisting essentially of the steps of: (a) contacting an aqueous preparation, in the form of a solution or suspension, of plasma proteins containing factors VII and VIIa, at a temperature of about 4° to 25° C. and at a pH of about 4 to 9 and in the presence of a suitable buffer to maintain the pH at about 4 to 9, with about 1 to 10% (weight/volume, based on total weight of plasma proteins) of polyethylene glycol having a molecular weight of about 200 to 20,000 to precipitate from the preparation PEG-precipitable proteins and other insoluble matter present in the aqueous preparation to obtain an aqueous supernatant containing factors VII and VIIa separated from the PEG-precipitable proteins and insoluble matter; (b) contacting the aqueous supernatant from step (a), adjusted to a pH of about 6 to 8, with an adsorbent having selective affinity for calcium-binding proteins, including factors II, VII, IX and X, selected from the group of water-insoluble divalent metal salts, to adsorb calcium-binding proteins; (c) selectively eluting, by techniques selected from step and gradient elution techniques, factors II, VII and VIIa, IX and IXa, and X and Xa from the protein-bound adsorbent from step (b) by the addition of a buffer solution containing suitable soluble salts effective to displace the bound proteins and collecting the eluate pool; (d) contacting the eluate pool from step (c), adjusted to a pH of about 3 to 11, with an anionic exchange resin having affinity for the calcium-binding proteins, including factors II, VII and VIIa, IX and IXa, and X and Xa, and adsorbing thereon the calcium-binding proteins; and (e) selectively eluting, by techniques selected from step and gradient elution techniques, factors VII and VIIa from the protein-bound adsorbent from step (d) by the addition of a buffer solution containing suitable salts in increasing ionic strength.
Claim 3
Dependent Claim
55 words
A process according to claim 1 wherein the anionic exchange resin used in step (d) is a polysaccharide adsorbent selected from the group of polygalactose, polydextran and cellulose resins wherein the polysaccharide chains have positively charged groups selected from diethylaminoethyl groups and quaternary ethyl amino groups attached by to the glucose units in the polysaccharide.
Claim 4
Dependent Claim
37 words
A process according to claim 1 wherein the plasma protein is selected from Cohn fractions III and IV-1 and wherein the plasma protein is present in a concentration in the range of about 1 to 80% (weight/volume).
Claim 5
Dependent Claim
19 words
A process according to claim 1 wherein the volume of the eluate from step (e) is reduced by ultra-filtration.
Claim 6
Dependent Claim
28 words
A process according to claim 1 including the further step of treatment to render the eluate from step (e) non-viral infective and to reduce or eliminate infectious microorganisms.
Claim 7
Dependent Claim
28 words
A process according to claim 4 including the further step of treatment to render the eluate from step (e) non-viral infective and to reduce or eliminate infectious microorganisms.
Claim 8
Dependent Claim
310 words
A process for producing a concentrate consisting essentially of blood coagulation factors VII and VIIa and having a specific activity of about 500 to 3000 u/A 280 consisting essentially of the steps of: (a) contacting an aqueous preparation, in the form of a solution or suspension, of plasma proteins selected from Cohn fraction III and Cohn fraction IV-1, containing coagulation factors II, VII, IX and X, at a temperature of about 4° to 25° C. and at a pH of about 6 to 9 and in the presence of a suitable buffer to maintain the pH of the preparation at about 6 to 9, with 3% polyethylene glycol having a molecular weight of about 6,000 to precipitate from the preparation PEG-precipitable proteins and other insoluble matter present in the aqueous preparation to obtain an aqueous supernatant containing factors VII and VIIa separated from the PEG-precipitable proteins and insoluble matter; (b) contacting the supernatant from step (a), adjusted to a pH of about 5 to 8, with tricalcium phosphate (hydroxyapatite) to adsorb thereon the calcium-binding coagulation factors II, VII, IX and X; (c) selectively eluting, by gradient elution techniques, factors II, VII, IX and X, and of activated factors present, VIIa, IXa and Xa, from the protein-bound adsorbent from step (b) by the addition of a buffer solution containing soluble salts effective to displace the bound proteins and collecting the eluate pool; (d) contacting the eluate pool from step (c), adjusted to a pH of about 5 to 8, with an anionic exchange resin selected from the group of polygalactose, polydextran and cellulose wherein the polysaccharide chains have diethylaminoethyl groups attached to the glucose units in the polysaccharide; and (e) selectively eluting, by gradient elution techniques, factors VII and VIIa from the protein-bound adsorbent from step (d) by the addition of a buffer solution containing suitable salts in increasing ionic strength.
Claim 9
Dependent Claim
310 words
A process for producing a concentrate consisting essentially of blood coagulation factors VII and VIIa and having a specific activity of about 500 to 3000 u/A 280 consisting essentially of the steps of: (a) contacting an aqueous preparation, in the form of a solution or suspension, of plasma proteins selected from Cohn fraction III and Cohn fraction IV-1, containing coagulation factors II, VII, IX and X, at a temperature of about 4° to 25° C. and at a pH of about 6 to 9 and in the presence of a suitable buffer to maintain the pH of the preparation at about 6 to 9, with 3% polyethylene glycol having a molecular weight of about 6,000 to precipitate from the preparation PEG-precipitable proteins and other insoluble matter present in the aqueous preparation to obtain an aqueous supernatant containing factors VII and VIIa separated from the PEG-precipitable proteins and insoluble matter; (b) contacting the supernatant from step (a), adjusted to a pH of about 5 to 8, with tricalcium phosphate (hydroxyapatite) to adsorb thereon the calcium-binding coagulation factors II, VII, IX and X; (c) selectively eluting, by gradient elution techniques, factors II, VII, IX and X, and of activated factors present, VIIa, IXa and Xa, from the protein-bound adsorbent from step (b) by the addition of a buffer solution containing soluble salts effective to displace the bound proteins and collecting the eluate pool; (d) contacting the eluate pool from step (c), adjusted to a pH of about 5 to 8, with an anionic exchange resin selected from the group of polygalactose, polydextran and cellulose wherein the polysaccharide chains have diethylaminoethyl groups attached to the glucose units in the polysaccharide; and (e) selectively eluting, by gradient elution techniques, factors VII and VIIa from the protein-bound adsorbent from step (d) by the addition of a buffer solution containing suitable salts in increasing ionic strength.
Claim 10
Dependent Claim
19 words
A process according to claim 7 wherein the volume of the eluate from step (e) is reduced by ultra-filtration.
Claim 11
Dependent Claim
28 words
A process according to claim 7 including the further step of treatment to render the eluate from step (e) non-viral infective and to reduce or eliminate infectious microorganisms.
Claim 12
Dependent Claim
28 words
A process according to claim 8 including the further step of treatment to render the eluate from step (e) non-viral infective and to reduce or eliminate infectious microorganisms.
References Cited (Backward Citations)
US4357321A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-09-11 | 1988-03-12 | 1988-09-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-09-11 | 1992-03-12 | 1992-09-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-09-11 | 1996-03-12 | 1996-09-11 | $7700.00 | Window Closed / Lapsed |