IL53503A

Pure gamma globulin fraction,its preparation and pharmaceutical compositions containing it

Abstract

This record has no abstract on file.

Term

No projected expiry on record.

  1. Priority
  2. Filed
  3. Published
  4. Today

32 claims: 18 independent, 14 dependent

  1. 1
    A gamma globulin fraction suitable for intravenous administration and having an anticomplementary activity of less than 0.01 units per mg, and preferably of from 0.0005 to 0.0025 units per mg, which is substantially free of aggregates and decomposition products F (ab)^, F. (ab) 2 and Fc, has a sedimentation coefficient of about 7S, is clearly soluble in water and has an antibody spectrum and subclass distribution substantially the same as Cohn Fraction II or a mixture of Cohn Fractions II and III of the plasma from which said fraction is obtained.
  2. 2
    A fraction as claimed in Claim 1 in lyophilized form.
  3. 3
    a fraction as claimed in Claim 2 having a stability of at least 2 years.
  4. 4
    a gamma globulin fraction as claimed in Claim 1 substantially as herein described in any of Examples 1 to 4.
  5. 5
    a process for the preparation of a gamma globulin fraction according to Claim 1 substantially free of anticomplementary activity and suitable for intravenous administration which comprises:a) extracting a paste or powder of Fraction II or II + III plasma protein or of a placental extract containing said fraction with pyrogen-free water at־ a pH of from 4.9 to 6;b) separating the extract thus obtained from solid material and treating said extract with polyethylene glycol in an amount of about 4% weight/volume;c) separating the glycol-treated extract from solid material thus precipitated and subsequently treating with ethanol in an X amount of from 4 to 12% weight/volume at' temperatures of fro® -6 to 10°C;d) separating solid material from,the ethanol-treated extract thus obtained to yield a further extract;and by precipitation e) isolating the gamma globulin fraction/from said further extract at temperatures of from -6 to 20°C and at a pH of from 7 to 8.2 by means of the addition of either polyethylene glycol in an amount of up to 12% weight/volume or of ethanol in an amount of up to 30% volume/volume, said gamma globulin fraction being substantially free of anticomplementary activity» 6־ A process as claimed in claim 5 wherein the Fraction has a protein content of from 20 to 30%.
  6. 7
    8. A process as claimed in any of the preceding claims 5-7, wherein the extraction with pyrogen.-free water is effected at temperatures of from 0 to 5 0 C.
  7. 8
    9. A process as claimed in any of the preceding claims 5-8, wherein *the conductivity of the suspension of the paste or powder in the pyrogen-free water is about 300 x 10 6 κ - 1 cm .ohm .
  8. 9
    10. A process as claimed in any O f the preceding claims ־ _ζ ׳ ״herein the treatment 1״th p״ly־th yl ene glycol in step (b) IS effected at temperatures of from 0 to 5°C.
  9. 10
    11. A process as claimed in any of the preceding claims 5-10 ״herein the treatment «1th ethanol in step (c) is effected at temperatures of from -6.to 0״C.
  10. 11
    12. A process as claimed in claim ״״herein the treatment ״!th ethanol in step (c) is effected at a temperature of about -2°C.
  11. 12
    13. A process as claimed in any of the preceding claims 5-12, ״herein, in the treatment ״Ith ethanol in step (c)״ the ethanol is present in an amount of about 65״ ׳eight/uolume.
  12. 13
    14. A process as claimed in any of the preceding claims 5-,״ ״herein the treatment with ethylene glycol in step (b) and/or the treatment with ethanol in step (c) is effected at a pH of about 5.,1.
  13. 14
    15. A process as claimed in any of the preceding claims״-־, wherein the further extr«rt 4 e . י cner extract is adjusted to a pH of about 8 before isolation of the gamma globulin fraction. 15. A process as claimed in any of the preceding claims 5-15, ״herein sodium chloride is added to the further extract in a concentration of about 0.01 M before isolation of the gamma globulin fraction. 1/. A process as claimed in any of the preceding claims 5-16, ״herein the isolation of the ga»a globulin fraction is effected at temperatures of from -6 to 0°C. 53503/2
  14. 15
    18. A process as claimed in any of the preceding claims 5-17, wherein isolation of the gamma globulin fraction is effected by means of the addition of polyethylene glycol in an amount of from 10 to 12% weight/volume.
  15. 16
    19. A process as claimed in any of claims 5 to 17 ,wherein isolation of the gamma globulin fraction is effected by means of the addition of ethanol in an amount of from 20 to 30% volume/volume*
  16. 17
    20. A process as claimed in claim .19,wherein isolation of » » the gamma globulin fraction is effected by means of the addition of ethanol in an amount of about 25% volume/volume. ,5-20 . י * 1״
  17. 18
    21. A process as claimed m any of the preceding claims/Wherein the polyethylene glycol used has a molecular weight of from 4000 to 6000.
  18. 19
    22. A process as claimed in any of the preceding claims 5-21, wherein the pyrogen-free water additionally contains about 2% polyethylene glycol and about 0.2% albumin.
  19. 20
    23. A process as claimed in any of the preceding claims 5-22, wherein the isolated gamma globulin fraction is subsequently dissolved in a carrier or adjuvant.
  20. 21
    24. A process as claimed in claim .23 wherein the carrier or adjuvant includes human albumin, sodium acetate, potassium acetate, glycine, lactose and/or mannitol. ־ f 25., A process as claimed in claim 23 or claim 24 wherein the solution of the isolated gamma globulin fraction in the carrier or adjuvant is adjusted to a pH of from 5.0 to 5,5. 26., A process as claimed in claim 25 wherein the solution is subsequently adjusted to a pH of 6.4 to 6.6. 27., A process as claimed in claim 19 wherein the solution is lyophilized. 5-27, 28 . A process as claimed in any of the preceding claims/wherein the fraction has a protein content of from 20 to 30%, the conductivity of the suspension of the paste or powder in the pyrogen-free water is about 300 x 10”θ cm ohm * and isolation of the gamma globulin fraction is effected by means of the addition of either polyethylene glycol in an amount of from 10 to 12% weight/volume or ethanol in an amount of from 20 to 30% volume/volume.
  21. 22
    29. A process as claimed in any of claims 5;. to 28 wherein the extraction with pyrogen-free water is effected in the presence of a salt.
  22. 24
    31. A process according to any of the preceding claims 5-30 for the preparation of a gamma globulin fraction according to Claim 1, substantially free of anticomplementary activity, substantially as herein described in any of Examples 1 to 4. 27 53503/2 f-
  23. 25
    32. A gamma globulin fraction according to Claim 1, substantially free of anticomplementary activity whenever prepared by a process as claimed in any of Claims 5 to 31.
  24. 30
    37. Compositions as claimed in any of claims 33 to :36 containing a surfactant.
  25. 32
    40. Compositions as claimed in Claim 33, substantially as herein described.
Independent claims25