IP Library Patent Application 12908647
Patent Application
App. No. 12/908,647

Methods and Systems for Purifying Non-Complexed Botulinum Neurotoxin

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Patent No.
US None
App. No.
12/908,647
Abstract

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.

Claims (35)

1 . A method for purifying a non-complexed botulinum toxin, the method comprising:

(i) providing a crude non-complexed botulinum toxin;

(ii) loading the crude non-complexed botulinum toxin on an anion exchange column so as to permit capture of the non-complexed botulinum toxin by the anion exchange column;

(iii) eluting the non-complexed botulinum toxin from the anion exchange column to give an eluent comprising the non-complexed botulinum toxin;

(iv) loading a cation exchange column with the eluent from the anion exchange column so as to permit capture of the non-complexed botulinum toxin by the cation exchange column; and

(v) eluting purified non-complexed botulinum toxin from the cation exchange column.

2 . The method according to claim 1 , wherein the crude non-complexed botulinum toxin is obtained by

obtaining a sample comprising botulinum toxin complex;

loading a hydrophobic interaction column with the sample so as to permit capture of the botulinum toxin complex by the hydrophobic interaction column;

eluting the botulinum toxin complex from the hydrophobic interaction chromatography column; and

dissociating the botulinum toxin complex to obtain a mixture comprising the crude non-complexed botulinum toxin.

3 . The method according to claim 2 , wherein the sample is a supernatant or filtrate comprising the botulinum toxin complex.

4 . The method according to claim 2 , wherein the sample is obtained by:

subjecting a fermentation culture comprising the botulinum toxin to acid precipitation to obtain an acid precipitate; and

performing tangential flow filtration on the precipitate to concentrate precipitate.

5 . The method according to claim 2 , wherein the sample is obtained by subjecting an insoluble fraction of a fermentation culture to tangential flow filtration.

6 . The method according to claim 2 , wherein the sample is subjected to a nuclease digestion before loading on the hydrophobic interaction column.

7 . The method according to claim 6 , wherein the nuclease is derived from an animal product free process.

8 . The method according to claim 1 , wherein the method is substantially animal product free.

9 . The method according to claim 1 , wherein the purified non-complexed botulinum toxin comprises at least one of botulinum toxin type A, B, C 1 , D, F, F and G.

10 . The method according to claim 1 , wherein the purified non-complexed botulinum toxin comprises a botulinum toxin type A.

11 . The method according to claim 1 , wherein the purified non-complexed botulinum toxin is at least 95% pure.

12 . The method according to claim 1 , wherein the purified non-complexed botulinum toxin has an activity of at least 200 LD 50 units/ng.

13 . The method according to claim 1 , wherein the method produces a yield of at least about 2 mg/L fermentation culture.

14 . The method according to claim 1 wherein the anionic column is selected from the group consisting of a Q Sepharose HP, Q Sepharose Fast Flow, and Q XL Sepharose column, and wherein the cationic column is selected from the group consisting of a SP Sepharose, SP Sepharose HP, SP Sephrose Fast Flow, Mono S, Source-S, Source-30S, and Source-15S column.

15 . The method according to claim 1 wherein a buffer for loading the non-complexed botulinum toxin onto the anionic column is selected from the group consisting of Tris, bis-Tris, triethanolamine, and N-methyl diethanolamine.

16 . The method according to claim 15 wherein the buffer is used at a pH from 7.4 to 8.2.

17 . The method according to claim 1 wherein a buffer for loading the non-complexed botulinum toxin onto the cationic column is selected from the group consisting of sodium phosphate, MES, and HEPES.

18 . The method according to claim 17 wherein the buffer is used at a pH from 6.0 to 7.0

19 . The method according to claim 1 wherein pH of the anionic column is from 7.4 to 8.2.

20 . The method according to claim 1 wherein pH of the cationic column is from 6.0 to 7.0.

21 . The method according to claim 1 wherein a gradient for eluting the non-complexed botulinum toxin from the anionic column is selected from the group consisting of an ascending gradient of sodium chloride and an ascending gradient of potassium chloride.

22 . The method according to claim 21 wherein the gradient is used at a pH from 7.4 to 8.4.

23 . The method according to claim 1 wherein a gradient for eluting the non-complexed botulinum toxin from the cationic column is selected from the group consisting of an ascending gradient of sodium chloride and an ascending gradient of potassium chloride.

24 . The method according to claim 23 wherein the gradient is used at a pH from 6.0 to 7.0.

Assignments (3)
RELEASE OF SECURITY INTEREST Recorded Sep 27, 2019
From: HERCULES CAPITAL, INC. (F/K/A HERCULES TECHNOLOGY GROWTH CAPITAL, INC.)
To: REVANCE THERAPEUTICS, INC.
Reel/Frame 050565/0300 →
SECURITY AGREEMENT Recorded Sep 22, 2011
From: REVANCE THERAPEUTICS, INC.
To: HERCULES TECHNOLOGY GROWTH CAPITAL, INC.
Reel/Frame 026953/0726 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 29, 2010
From: RUEGG, CURTIS L.
To: REVANCE THERAPEUTICS, INC.
Reel/Frame 025553/0399 →