Claims
- 1. A process for the preparation of hydrosoluble extracts of delipidated mycobacteria, said extracts having a molecular weight in the range of about 3,500 to 20,000, said process consisting essentially of subjecting the bacterial residues of said delipidated mycobacteria to a treatment with pyridine, extracting with a solvent selected from the group consisting of alcohol and water, and isolating hydrosoluble substances from the extract by physicochemical means.
- 2. The process of claim 1, wherein the treatment with pyridine is carried out in presence of acetic anhydride.
- 3. The process of claim 1, wherein the bacterial residues of delipidated mycobacteria used as starting material are obtained from mycobacteria containing D-wax.
- 4. The process of claim 3, wherein said mycobacteria are selected from the group consisting of Mycobacterium tuberculosis, var.hominis, Peurois strain,Test-Strain, Brevannes strain or H.sub.37 R.sub.a strain,Mycobacterium kansasii, Mycobacterium tuberculosis, var.bovis, LA,BB and Behring strains.
- 5. Hydrosoluble extracts of delipidated mycobacteria obtained from mycobacteria containing "D wax", said extracts having a molecular weight in the range about of 3,500 to 30,000 and having adjuvant and nonarthrogen properties and prepared by the process of claim 1.
- 6. The hydrosoluble extract of claim 5 having the following properties:
- appearance:pulverulent yellow powder (after freeze-drying)
- composition:
- a. amino acids (molecular ratio):alanine (3) glutamic acid (2), .alpha.,.alpha.'-diaminopimelic acid (2),
- b. amino sugars (molecular ratio):N-acetylglucosamine (2),N-acetylmuramic acid (2),
- c. non-amino reducing sugars:mannose,glucose;presence of arabinose; absence of galactose,
- d. absence of lipids
- molecular weight (calculated on the basis of three alanine residues per molecule)4,000 .+-. 200
- sedimentation constant S.sub.2O = 0,7.
- 7. The hydrosoluble extract of claim 5 having the following properties:
- appearance:white powder after freeze-drying
- composition:
- a. amino acids (molecular ratio):alanine (3) glutamic acid (2),.alpha.,.alpha.'-diaminopimelic acid (2)
- b. amino sugars (molecular ratio):N-acetylglucosamine (2)N-glucolylmuramic acid (2),
- c. non amino reducing sugars:galactose, mannose, arabinose
- molecular weight (calculated on the basis of three alanine residues per molecule) 6,000 .+-. 500.
- 8. Pharmaceutical compositions which contain an effective amount of hydrosoluble extract obtained by the process of claim 1, in association with a pharmaceutically acceptable diluent or adjuvant.
- 9. A process for the preparation of acetylated hydrosoluble extracts of delipidated mycobacteria, said extracts having a molecular weight in the range of about 3,500 to 20,000, said process consisting essentially of subjecting bacterial residues of said delipidated mycobacteria to treatment with pyridine in presence of acetic anhydride, adding alcohol, separating the alcohol solution from the undissolved residue, removing the solvent from the alcohol solution to leave a dry material and extracting said dry material with water to form a solution of active acetylated material.
- 10. The process of claim 9, wherein said active acetylated material is purified by chromatography on an adsorbent of the weak anionic exchange agent type, equilibrated at pH 7.7 by eluting with a pH 7.7 buffer and by modifying the molarity of the buffer during eluting.
- 11. The process according to claim 10, wherein the eluting is carried out with a pyridine-acetic acid buffer.
- 12. The process according to claim 10, wherein the adsorbent is the product known under the trade name "DEAE Biogel A", the said adsorbent is equilibrated at pH 7.7 with a pyridine-acetic acid buffer, the eluting is effected with the same buffer having a molarity of 0.01 until a peak at 220 m.mu. is obtained by optical reading and is then effected with the same buffer having a molarity of 0.2 until a peak at 220 m.mu. is obtained, said hydrosoluble extract being recovered during the second eluting.
- 13. The process of claim 12, wherein a hydrosoluble extract highly purified is obtained, said extract essentially consisting of an acetylated tetrasaccharideheptapeptide free of non-aminated reducing sugars and having the following composition, the figures in brackets indicating the molecular ratios of the amino acids=
- Alanine (3)
- Glutamic acid (2)
- Diaminopimelic acid (2)
- N-acetylglucosamine (2)
- N-acetylmuramic acid (2).
- 14. A process for the preparation of a hydrosoluble extract having the following properties:
- appearance:pulverulent yellow powder (after freeze-drying)
- composition:
- a. amino acids (molecular ratio):alanine (3) glutamic acid (2),.alpha.,.alpha.'-diaminopimelic acid (2),
- b. amino sugars (molecular ratio); N-acetylglucosamine (2),N-acetylmuramic acid (2),
- c. non amino reducing sugars:mannose, glucose; presence of arabinose; absence of galactose,
- d. absence of lipids
- molecular weight (calculated on the basis of three alanine residues per molecule)4,000 .+-. 200
- sedimentation constant S.sub.20 = 0,7
- said process consisting of treating the delipidated bacterial residues of mycobacteria with pyridine-acetic anhydride mixture, after which ethyl alcohol is added, the alcohol-insoluble fraction is extracted with water, then the hydrosoluble extract obtained is isolated and purified by chromatography.
- 15. A process for the preparation of a hydrosoluble extract having the following properties:
- appearance: white powder after freeze-drying
- composition:
- a. amino acids (molecular ratio):alanine (3) glutamic acid (2) .alpha.,.alpha.'-diaminopimelic acid (2)
- b. amino sugars (molecular ratio):N-acetylglucosamine (2), N-glucolylmuramic acid (2)
- c. non amino reducing sugars:galactose, mannose, arabinose molecular weight (calculated on the basis of three alanine residues per molecule) 6,000 .+-. 500,
- said process consisting of treating the delipidated bacterial residues of mycobacteria with pyridine, after which ethyl alcohol is added, the alcohol-insoluble fraction is extracted by homogenization in an aqueous medium, then, after centrifugation, two salting out steps are effected on the hydrosoluble fraction by means of ammonium sulfate, each followed by centrifugation, the obtained supernatant layer is dialysed against distilled water and finally the hydrosoluble extract is separated, isolated and purified by chromatography.
Priority Claims (3)
Number |
Date |
Country |
Kind |
72.22208 |
Jun 1972 |
FR |
|
73.16130 |
May 1973 |
FR |
|
74.30107 |
Sep 1974 |
FR |
|
Parent Case Info
This application is a continuation-in-part of application Ser. No. 371,658, filed June 19, 1973, now abandoned.
Non-Patent Literature Citations (1)
Entry |
chem. Abst. 8th Collective Index, vol. 66-75 (1967-1971) p. 19857s. |
Continuation in Parts (1)
|
Number |
Date |
Country |
Parent |
371658 |
Jun 1973 |
|