Claims
- 1. A method of producing a coisolated and copurified mixture of proteins of respiratory syncytial virus (RSV), which comprises: growing RSV on cells in a culture medium; separating the grown virus from the culture medium; solubilizing at least the fusion (F) protein, attachment (G) protein and the matrix (M) protein from the separated virus; and coisolating and copurifying the solubilized RSV proteins.
- 2. The method of claim 1 wherein said coisolation and copurification are effected by: loading the solubilized proteins onto an ion-exchange matrix; and selectively coeluting the F, G and M proteins from the ion-exchange matrix.
- 3. The method of claim 2 wherein said ion-exchange matrix is a hydroxyapatite matrix.
- 4. The method of claim 1 wherein said grown virus is washed with urea to remove contaminants without substantial removal of F, G and M proteins prior to solubilization step.
- 5. The method of claim 2 including contacting said eluted F, G and M proteins with an anion exchange matrix to remove any residual nucleic acid.
- 6. A method of producing a co-isolated and co-purified mixture of proteins of respiratory syncytial virus (RSV) which comprises the steps of:
i. Growing suitable cells in a culture medium in microcarriers; ii. Infecting said cells with RSV virus; iii. Growing said infected cells; iv. Solubalizing said infected cells to produce an extract; v. Clarifying said extract; vi. Co-isolating and co-purifying antigens from said extract; vii. Removing residual nucleic acids from said co-purified antigen extract; viii. Concentrating and formulating said extract.
- 7. The method of claim 6 wherein co isolation and co purification step are effected by loading said solubalized extract onto ion exchange matrix and selectively coeluting F, G, and M proteins from the ion-exchange matrix.
- 8. The method of claim 7 wherein the ion exchange matrix is ceramic hydroxyapetite II matrix.
- 9. The method of claim 8 wherein the removal of residual nucleic acid is effected by anion exchange adsorption column chromatography.
- 10. The method if claim 9 wherein the anion exchange adsorption column is sartobind Q.
- 11. The method of claim 10 where the ecoisolated and copurified F, G, and M proteins have a composition of
F—40 to 55% wt/wt G—6.4 to 10% wt/wt M—25 to 40% wt/wt Impurities 5 to 20% as determined by HPLC chromatography analysis.
REFERENCE TO RELATED APPLICATIONS
[0001] This application is a continuation-in-part of copending U.S. patent application Ser. No. 09/214,605 filed Jul. 11, 1997 which itself is a United States National Phase filing under 35 USC 371 of PCT/CA97/00497 filed Jul. 11, 1997 and a continuation-in-part of U.S. patent application Ser. No. 08/679,060 filed Jul. 12, 1996 (now U.S. Pat. No. 6,020,182).
Continuation in Parts (2)
|
Number |
Date |
Country |
Parent |
09214605 |
May 1999 |
US |
Child |
10901147 |
Jul 2004 |
US |
Parent |
08679060 |
Jul 1996 |
US |
Child |
10901147 |
Jul 2004 |
US |