US2021024913A1PendingUtilityA1
Animal product free system and process for purifying a botulinum toxin
Est. expiryMar 3, 2025(expired)· nominal 20-yr term from priority
Inventors:Hui Xiang
C07K 14/33C07K 1/36C07K 1/20C07K 1/18A61P 1/00C12N 9/52A61P 17/00A61P 21/02C12P 21/02C12Y 304/24069A61P 21/00C12N 1/20C12N 9/6489A61P 27/02A61P 25/06
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Claims
Abstract
Chromatographic processes and systems for purifying a botulinum toxin from an APF fermentation medium.
Claims
exact text as granted — not AI-modified1 - 14 . (canceled)
15 . A formulated botulinum toxin type A product that is free of bovine DNase, RNase, and casein, comprising:
(i) a purified, approximately 150 kDa botulinum toxin type A molecule that is essentially free of animal products; and (ii) at least one pharmaceutically acceptable excipient that is essentially free of animal products; wherein the purified, approximately 150 kDa botulinum toxin type A molecule is obtained from a process comprising the steps of:
(a) preparing a botulinum toxin fermentation culture comprising botulinum toxin type A, wherein the fermentation culture is essentially animal product free (APF);
(b) contacting a hydrophobic interaction chromatography (HIC) column resin with the botulinum toxin fermentation culture;
(c) eluting the botulinum toxin type A from the HIC column resin to provide a first eluent;
(d) conditioning the first eluent with a buffer having a pH of between about 7-8, whereby dissociated eluted botulinum toxin type A is formed comprising (1) at least one approximately 150 kDa botulinum toxin type A molecule and (2) at least one non toxin complex protein;
(e) contacting an anion exchange column resin with the first eluant;
(f) eluting the botulinum toxin type A from the anion exchange column resin to provide a second eluant;
(g) contacting a cation exchange column resin with the second eluant; and
(h) eluting the botulinum toxin type A from the cation exchange column to provide purified approximately 150 kDa botulinum toxin type A molecule.
16 . The formulated botulinum toxin type A product of claim 15 , wherein the purified approximately 150 kDa botulinum toxin type A molecule has a potency that meets or exceeds the potency of a purified botulinum toxin product obtained from a Schantz or a modified Schantz process.
17 . The formulated botulinum toxin type A product of claim 15 , wherein the purified approximately 150 kDa botulinum toxin type A molecule has a potency that exceeds the potency of a purified botulinum toxin product obtained from a Schantz or a modified Schantz process.
18 . The formulated botulinum toxin type A product of claim 15 , wherein the purified approximately 150 kDa botulinum toxin type A molecule has a specific potency of 1-2×10 8 LD 50 U/mg or greater.
19 . The formulated botulinum toxin type A product of claim 15 , wherein more than 99% of non- botulinum toxin proteins and impurities are removed.
20 . The formulated botulinum toxin type A product of claim 15 , wherein the formulated botulinum toxin type A product is essentially free of animal product (APF).
21 . The formulated botulinum toxin type A product of claim 15 , wherein the formulated botulinum toxin type A product is free of animal product (APF).
22 . The formulated botulinum toxin type A product of claim 15 , wherein there is no more than 6 ng/ml residual DNA from Clostridium botulinum bacterium.
23 . The formulated botulinum toxin type A product of claim 15 , wherein the fermentation culture is prepared with a fermentation medium comprising about 10-100 g/L hydrolyzed soy protein.
24 . The formulated botulinum toxin type A product of claim 15 , wherein the fermentation culture is prepared with a fermentation medium comprising about 6 wt % of hydrolyzed soy protein.
25 . The formulated botulinum toxin type A product of claim 15 , wherein the fermentation culture is prepared with a fermentation medium comprising about 1 wt % of yeast extract.
26 . The formulated botulinum toxin type A product of claim 15 , wherein the fermentation culture is prepared with a fermentation medium comprising about 1 wt % of glucose.
27 . The formulated botulinum toxin type A product of claim 15 , wherein the fermentation culture is prepared with a fermentation medium comprising about 6 wt % of hydrolyzed soy protein, about 1 wt % of yeast extract, and about 1 wt % of glucose.
28 . The formulated botulinum toxin type A product of claim 15 , wherein a yield of greater than about 50 mg botulinum toxin complex for each 10 liters of the botulinum toxin fermentation culture is obtained.
29 . The formulated botulinum toxin type A product of claim 15 , wherein a potency of about 38×10 5 LD 50 units/mL of botulinum toxin fermentation culture is obtained.
30 . A method for obtaining a biologically active botulinum toxin type A, comprising the steps of:
(a) providing a fermentation medium which is free of an animal product; (b) culturing a Clostridium botulinum type A bacterium in the fermentation medium under conditions which permit production of a botulinum toxin type A, and; (c) recovering a biologically active botulinum toxin type A from the fermentation medium, wherein the fermentation medium comprises a protein product obtained from yeast or from a vegetable and wherein the vegetable is selected from the group consisting of soy, malt and corn.
31 . A method for making an animal product free pharmaceutical composition in which the active ingredient is a botulinum toxin type A, the method comprising the steps of:
(a) obtaining a biologically active botulinum toxin type A by:
i. providing a fermentation medium which is free of an animal product;
ii. culturing a Clostridium botulinum type A bacterium in the fermentation medium under conditions which permit production of a botulinum toxin type A, and;
iii. recovering a biologically active botulinum toxin type A from the fermentation medium;
(b) formulating the botulinum toxin type A with a suitable excipient, thereby making an animal product free pharmaceutical composition in which the active ingredient is a botulinum toxin type A, wherein the fermentation medium comprises a protein product obtained from yeast or from a vegetable and wherein the vegetable is selected from the group consisting of soy, malt and corn.
32 . An animal protein free (“APF”) process for purifying a biologically active botulinum toxin, the process comprising the steps of:
(a) obtaining a sample of a botulinum toxin fermentation culture, wherein the botulinum toxin fermentation culture results from a substantially APF process,
(b) contacting a hydrophobic interaction chromatography column resin with the culture sample so as to permit capture of a botulinum toxin by the hydrophobic interaction chromatography column;
(c) washing impurities off the hydrophobic interaction chromatography column;
(d) eluting the botulinum toxin from the hydrophobic interaction column;
(e) loading an ion exchange column chromatography column resin with the eluent from the hydrophobic interaction chromatography column;
(f) washing impurities off the ion exchange chromatography column, and;
(g) eluting the botulinum toxin from the ion exchange column, thereby obtaining a purified biologically active botulinum toxin through a process for purifying a botulinum toxin which is a substantially APF purification process.Join the waitlist — get patent alerts
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