Process and system for obtaining botulinum neurotoxin
US-9206409-B2 · Dec 8, 2015 · US
US9469849B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9469849-B2 |
| Application number | US-201514796235-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 10, 2015 |
| Priority date | Oct 21, 2009 |
| Publication date | Oct 18, 2016 |
| Grant date | Oct 18, 2016 |
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Methods and systems for chromatographically purifying a botulinum neurotoxin are provided. These methods and systems allow for efficient purification of a non-complexed form of the botulinum neurotoxin in high purity and yield that can be used as an active ingredient in pharmaceutical preparations.
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What is claimed is: 1. A method for purifying a non-complexed botulinum toxin type A ( botulinum toxin A), the method comprising: (a) providing a mixture comprising a crude non-complexed botulinum toxin A, in which said crude non-complexed botulinum toxin A is dissociated from native non-toxin proteins; wherein said mixture is obtained by: (i) subjecting a fermentation culture comprising botulinum toxin A to acid precipitation to produce an insoluble acid precipitate; (ii) concentrating the acid precipitate from step (i) to produce a concentrated sample; (iii) subjecting the sample to nuclease digestion under conditions which reduce host cell nucleic acid content and which maintain a complex of botulinum toxin A and non-toxin proteins; (iv) removing cell debris from the sample of step (iii) to produce a clarified sample; (v) loading a hydrophobic interaction column with the clarified sample from step (iv) under conditions to permit capture of the botulinum toxin A complex by the hydrophobic interaction column and impurities to flow through the column; (vi) eluting the botulinum toxin A complex from the hydrophobic interaction column of step (vi); and (vii) dissociating the botulinum toxin A complex obtained from step (vi) under conditions which disrupt the complex and produce a mixture comprising crude non-complexed botulinum toxin A dissociated from the native non-toxin proteins; (b) loading the mixture containing the crude non-complexed botulinum toxin A dissociated from native non-toxin proteins from step (a) on an anion exchange column under conditions permitting capture of the non-complexed botulinum toxin A by the anion exchange column; (c) eluting the non-complexed botulinum toxin A from the anion exchange column of step (b) to give an eluent comprising the non-complexed botulinum toxin A; (d) loading a cation exchange column with the eluent from the anion exchange column of step (c) under conditions permitting capture of the non-complexed botulinum toxin A by the cation exchange column; and (e) eluting purified non-complexed botulinum toxin A from the cation exchange column of step (d). 2. The method according to claim 1 , wherein, in step (i), the fermentation culture comprising botulinum toxin A is acid precipitated with sulfuric acid. 3. The method according to claim 2 , wherein the concentrated sample of step (ii) is obtained by performing tangential flow filtration on the acid precipitate to concentrate the precipitate. 4. The method according to claim 1 , wherein the sample of step (iii) is subjected to nuclease digestion at a pH of 5 to 7. 5. The method according to claim 4 , wherein the nuclease is derived from a non-animal source. 6. The method according to claim 5 , wherein, in step (iv), the cell debris is removed by centrifugation and/or filtration to produce the clarified sample. 7. The method according to claim 6 , wherein the clarified sample of step (iv) is combined with a buffer comprising ammonium sulfate prior to loading the hydrophobic interaction column in step (v). 8. The method according to claim 7 , wherein the clarified sample of step (iv) is combined with a buffer comprising ammonium sulfate and phosphate at pH 6 prior to loading the hydrophobic interaction column in step (v). 9. The method according to claim 8 , wherein, in step (vii), the botulinum toxin A complex is dissociated in a buffer having a pH of 7.0 to 8.4 to obtain the mixture comprising the crude non-complexed botulinum toxin A dissociated from the native non-toxin proteins. 10. The method according to claim 9 , wherein the botulinum toxin A complex is dissociated in Tris buffer at pH 7.8. 11. The method according to claim 10 , wherein the method is substantially animal product free. 12. The method according to claim 11 , wherein the hydrophobic interaction column comprises a chromatography gel matrix comprising beaded agarose, having attached thereto chemical groups selected from butyl, octyl, or phenyl groups. 13. The method according to claim 12 , wherein a loading or equilibration buffer for the hydrophobic interaction column is selected from acetate, citrate, 2-(N-morpholino)ethanesulfonic acid (MES), histidine, piperazine and malonate. 14. The method according to claim 13 , wherein the pH of the hydrophobic interaction column buffer is in the range of pH 4.0 to 7.0. 15. The method according to claim 14 , wherein the pH of the hydrophobic interaction column buffer is in the range of pH 4.5 to 6.5. 16. The method according to claim 15 , wherein the pH of the hydrophobic interaction column buffer is pH 6. 17. The method according to claim 12 , wherein the bound botulinum toxin A complex is eluted from the hydrophobic interaction column in a descending gradient of an elution buffer selected from the group consisting of ammonium sulfate, sodium sulfate, sodium chloride, potassium chloride and ammonium acetate. 18. The method according to claim 17 , wherein the elution buffer is ammonium sulfate. 19. The method according to claim 17 , wherein the concentration range of the descending gradient elution buffer is from 0.6 M to 0.0 M. 20. The method according to claim 17 , wherein the concentration range of the descending gradient elution buffer is from 0.5 M to 0.0 M. 21. The method according to claim 17 , wherein the concentration range of the descending gradient elution buffer is from 0.4 M to 0.0 M. 22. The method according to claim 17 , wherein the concentration range of the descending gradient elution buffer is from 0.25 M to 0.0 M. 23. The method according to claim 12 , wherein the bound botulinum toxin A complex is eluted from the hydrophobic interaction column in a descending gradient of ammonium sulfate elution buffer in a concentration range of 0.4 M to 0.0 M at pH 6. 24. The method according to claim 17 , wherein the anion exchange column comprises a chromatography gel matrix comprising beaded agarose having a net negative charge, and wherein the cation exchange column comprises a chromatography gel matrix comprising beaded agarose having a net positive charge; wherein said anion and cation exchange columns provide separation of proteins based on electrostatic charge. 25. The method according to claim 24 , wherein the non-complexed botulinum toxin A is loaded onto the anion exchange column in a buffer selected from the group consisting of Tris, bis-Tris, triethanolamine, and N-methyl diethanolamine. 26. The method according to claim 25 , wherein the buffer is used at a pH from 7.2 to 8.6. 27. The method according to claim 25 , wherein the buffer is used at a pH from 7.4 to 8.2. 28. The method according to claim 24 , wherein the non-complexed botulinum toxin A is loaded onto the cation exchange column in a buffer selected from the group consisting of sodium phosphate, 2-(N-morpholino)ethanesulfonic acid (MES) and HEPES. 29. The method according to claim 28 , wherein the buffer is used at a pH of from 6.0 to 7.0. 30. The method according to claim 24 , wherein the pH of the anion exchange column is from 7.4 to 8.2. 31. The method according to claim 30 , wherein the buffer is used at a pH of from 6.8 to 7.0. 32. The method according to claim 24 , wherein a concentration gradient of an elution buffer for eluting the non-comp
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