Methods of treating complement mediated thrombotic microangiopathy using an anti-c5 antibody
US-2024092881-A1 · Mar 21, 2024 · US
US9920124B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9920124-B2 |
| Application number | US-201314654384-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 19, 2013 |
| Priority date | Dec 20, 2012 |
| Publication date | Mar 20, 2018 |
| Grant date | Mar 20, 2018 |
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The present invention provides methods of preparing active immunoconjugates, including anti-CD22 immunoconjugates. Suitably, the methods include a fed-batch refolding process and/or column stripping process that result in an increase in yield of the immunoconjugate over other processes that do not utilize the methods.
Opening claim text (preview).
What is claimed is: 1. A method of preparing an active immunoconjugate, wherein said immunoconjugate is composed of two polypeptide chains joined by a disulfide bond, the method comprising refolding said immunoconjugate in a fed-batch refolding process in a refold buffer having a pH of 9.5 or less, and purifying the refolded immunoconjugate using a two cycle elution on an ion exchange column, wherein the column is stripped between a first elution and a second elution with a stripping buffer comprising arginine, urea and dithiothreitol (DTT), wherein the stripping buffer comprises 0.25M to about 0.75 M arginine, 7M to about 9 M urea and 9 mM to about 11 mM DTT. 2. The method of claim 1 , wherein an amount of the immunoconjugate recovered from the method of preparation is at least three-hundred % (300%) greater than an amount of the immunoconjugate recovered utilizing a method that does not comprise a fed-batch refolding process and/or purification on an ion exchange column that has been stripped using the stripping buffer. 3. The method of claim 2 , wherein the polypeptide or immunoconjugate comprises an antibody or antigen binding fragment thereof. 4. The method of claim 3 , wherein the antibody or antigen binding fragment comprises a Fab, a Fab′, a F(ab′)2, a Fd, a single chain Fv or scFv, a disulfide linked Fv, a V-NAR domain, an IgNar, an intrabody, an IgGΔCH2, a minibody, a F(ab′)3 a tetrabody, a triabody, a diabody, a single-domain antibody, DVD-Ig, Fcab, mAb 2 , a (scFv)2, or a scFv-Fc. 5. The method of claim 2 , wherein the polypeptide or immunoconjugate comprises a toxin. 6. The method of claim 5 , wherein the toxin is a Pseudomonas exotoxin, or variant thereof. 7. The method of claim 6 , wherein said Pseudomonas exotoxin, or variant thereof has an amino acid sequence selected from the group consisting of SEQ ID NOs: 16-22. 8. The method of claim 7 , wherein said Pseudomonas exotoxin, or variant thereof has the amino acid sequence of SEQ ID NO:22. 9. The method of claim 3 , wherein said antibody or antigen binding fragment thereof comprises a VH and a VL sequence. 10. The method of claim 9 , wherein said VH sequence is selected from the group consisting of SEQ ID NOs: 6-11. 11. The method of claim 9 , wherein said VL sequence is selected from the group consisting of SEQ ID NOs: 2, and 12-15. 12. The method of claim 2 , wherein the immunoconjugate comprises an anti-CD22 antibody or antigen binding fragment thereof and a PE or variant thereof. 13. The method of claim 12 , wherein the immunoconjugate is the Moxetumomab pasudotox immunotoxin comprising the VH-PE38 subunit of SEQ ID NO: 1 and the VL subunit of SEQ ID NO:2. 14. The method of claim 2 , wherein the refold buffer has a pH of 9.4. 15. The method of claim 2 , wherein the fed batch process uses an addition rate of about 52 mL of solubilized inclusion bodies per L of refold buffer per hour to about 13 mL solubilized inclusion bodies per L refold buffer per hour. 16. The method of claim 15 , wherein the fed batch process uses an addition rate of about 35 mL of solubilized inclusion bodies per L of refold buffer per hour to about 17 mL solubilized inclusion bodies per L refold buffer per hour. 17. The method of claim 16 , wherein the fed batch process uses an addition rate of about 30 mL of solubilized inclusion bodies per L of refold buffer per hour to about 18 mL solubilized inclusion bodies per L refold buffer per hour. 18. The method of claim 17 , wherein the fed batch process uses an addition rate of about 26 mL of solubilized inclusion bodies per L of refold buffer per hour. 19. The method of claim 15 , wherein the fed batch process occurs over a period of about 2 to about 8 hours.
from Pseudomonadaceae (F) · CPC title
Specific host cells or culture conditions, e.g. components, pH or temperature · CPC title
Stabilisation, fragmentation · CPC title
against the immunoglobulin superfamily · CPC title
by reversible modification of the secondary, tertiary or quarternary structure, e.g. using denaturating or stabilising agents · CPC title
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