Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
158 words
A process for producing an AHF concentrate substantially free of denatured AHF and immunoglobulins and having a solubility in an aqueous injection medium of from 200 to 500 units AHF/ml and a specific activity of from 3.85 to 50 units AHF/mg protein which comprises subjecting a solution of a cryoprecipitate from blood plasma to the following treatment steps: (a) removal of prothrombin present, (b) a first treatment with from 2 to 6% by weight of PEG 200-20,000 thereby to precipitate a substantial amount of the fibrinogen present, (c) a second treatment of the supernatant from the first PEG precipitation with from 6 to 20% by weight of PEG 200 to 20,000 in the presence of an effective amount of a salting-in agent selected from the group consisting of amino acids, carbohydrates and sugar alcohols thereby to precipitate the AHF while essentially keeping the other proteins present in solution, (d) recovering the precipitate having a concentrated content of AHF.
Claim 2
Dependent Claim
158 words
A process for producing an AHF concentrate substantially free of denatured AHF and immunoglobulins and having a solubility in an aqueous injection medium of from 200 to 500 units AHF/ml and a specific activity of from 3.85 to 50 units AHF/mg protein which comprises subjecting a solution of a cryoprecipitate from blood plasma to the following treatment steps: (a) removal of prothrombin present, (b) a first treatment with from 2 to 6% by weight of PEG 200-20,000 thereby to precipitate a substantial amount of the fibrinogen present, (c) a second treatment of the supernatant from the first PEG precipitation with from 6 to 20% by weight of PEG 200 to 20,000 in the presence of an effective amount of a salting-in agent selected from the group consisting of amino acids, carbohydrates and sugar alcohols thereby to precipitate the AHF while essentially keeping the other proteins present in solution, (d) recovering the precipitate having a concentrated content of AHF.
Claim 3
Dependent Claim
21 words
A process according to claim 1, wherein the salting-in agent used in the second precipitation step is a basic amino acid.
Claim 4
Dependent Claim
14 words
A process according to claim 2, wherein the salting-in agent is lysine or arginine.
Claim 5
Dependent Claim
24 words
A process according to claim 1, wherein the salting-in agent used in the second precipitation step is a carbohydrate selected from mono- and disaccharides.
Claim 6
Dependent Claim
12 words
A process according to claim 4, wherein the salting-in agent is saccharose.
Claim 7
Dependent Claim
26 words
A process according to claim 4, wherein PEG is added in the first precipitation step until a concentration of about 4% by weight of the solution.
Claim 8
Dependent Claim
25 words
A process according to claim 4, wherein PEG is added in the second precipitation step corresponding to a total concentration of about 12% by weight.
Claim 9
Dependent Claim
29 words
A process according to claim 3, wherein lysine or arginine is added in the second precipitation step in an amount corresponding to a concentration of 0.1 to 0.9 mole/l.
Claim 10
Dependent Claim
28 words
A process according to claim 8, wherein the pH in the first precipitation step is 6.0 to 8.5 and in the second precipitation step is 5.0 to 8.5.
Claim 11
Dependent Claim
37 words
A process according to claim 9, wherein the recovered Factor VIII concentrate is heated to 60° C. for at least 10 hours in the presence of a suitable stabilizer so as to provide a safeguard against hepatitis.
Claim 12
Dependent Claim
14 words
A process according to claim 10, wherein the recovered Factor VIII concentrate is freeze-dried.
Claim 13
Dependent Claim
21 words
A process according to claim 8, wherein lysine or arginine is added in an amount corresponding to 0.3 to 0.8 mole/l.
Claim 14
Dependent Claim
28 words
A process according to claim 9, wherein the pH in the first precipitation step is 6.2 to 6.6 and in the second precipitation step is 6.0 to 6.6.
Claim 15
Dependent Claim
26 words
A process according to claim 13, wherein the pH in the first precipitation step is about 6.4 and in the second precipitation step is about 6.3.