SINGLE UNIT ANTIBODY PURIFICATION

• US 20130131318A1
• Filed: 02/10/2011
• Published: 05/23/2013
• Est. Priority Date: 02/12/2010
• Status: Abandoned Application

• Current Assignee: DPx Holdings BV (Netherlands) (Thermo Fisher Scientific Incorporated)
• Original Assignee: DPx Holdings BV (Netherlands) (Thermo Fisher Scientific Incorporated)
• Inventors: Kremer, Diderik Reinder, Maarleveld, Randal William
• Application Number:
  US13/578,679
• Publication Number:
  US 20130131318A1
• Time in Patent Office: Days
• US Class Current: 530/387.1
• CPC Class Codes: B01D 15/32 Bonded phase chromatography
• CPC Class Codes: B01D 15/327 with hydrophobic interaction
• CPC Class Codes: B01D 15/363 Anion-exchange
• CPC Class Codes: C07K 1/36 by a combination of two or more processes of different types
• CPC Class Codes: C07K 16/00 Immunoglobulins [IGs], e.g. monoclonal or polyclonal antibodies antibodies with enzymatic activity, e.g. abzymes C12N9/0002

Abstract

The present invention relates to a method for the purification of antibodies from a protein mixture produced in a bioreactor, at least comprising the steps of intermediate purification and polishing, wherein the intermediate purification and polishing step comprises in-line anion exchange chromatography (AEX) treatment and hydrophobic interaction chromatography (HIC) treatment in flow through mode. The present invention further relates to a single operational unit comprising both an anion exchange chromatography part and a hydrophobic interaction chromatography part, which are serially connected, wherein the unit comprises an inlet at the upstream end of the anion exchange chromatography part and an outlet at the downstream end of the hydrophobic interaction chromatography part and wherein the unit also comprises an inlet between the anion exchange chromatography part and the hydrophobic interaction chromatography part.

Claims

1. Method for the purification of antibodies from a protein mixture produced in a bioreactor, at least comprising the steps of intermediate purification and polishing, wherein the intermediate purification and polishing steps comprise serial in-line anion exchange chromatography (AEX), yielding as a flow-through fraction a separation mixture, followed by hydrophobic interaction chromatography (HIC) yielding as a flow through fraction a purified antibody preparation, and wherein the purified antibody preparation is subjected to at least one further purification step.

2. Method according to claim 1 wherein anion exchange chromatography and hydrophobic interaction chromatography take place in two separate devices which are serially connected.

3. Method according to claim 1 wherein the serial in-line AEX and HIC are performed as a single unit operation.

4. Method according to claim 1 wherein the separation mixture prior to HIC is supplemented with an adequate amount of lyotropic salt.

5. Method according to claim 1 wherein the separation mixture prior to HIC is supplemented with an adequate amount of ammonium sulfate, sodium sulfate, potassium sulfate, ammonium phosphate, sodium phosphate, potassium phosphate, potassium chloride and sodium chloride.

6. A single operational unit which can be used in a method according to claim 1 comprising both an anion exchange chromatography part and a hydrophobic interaction chromatography part, which are serially connected, wherein the outlet of the anion exchange chromatography part is connected to the inlet of the hydrophobic interaction chromatography part, wherein the unit comprises an inlet at the upstream end of the anion exchange chromatography part and an outlet at the downstream end of the hydrophobic interaction chromatography part and wherein the unit also comprises an inlet between the anion exchange chromatography part and the hydrophobic interaction chromatography part.