IP Library Granted Patent US 7,413,660
Granted Patent B2
US 7,413,660 · App. 11/241,524 · Granted Aug 19, 2008

Single pass method and apparatus for separating a target molecule from a liquid mixture

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Quick Facts
Patent No.
US 7,413,660
App. No.
11/241,524
Granted
Aug 19, 2008
Kind
B2
Abstract

A single pass simulated moving bed apparatus and methods are described for continuously separating a target molecule from a liquid mixture, using a simulated moving bed system. The simulated moving bed system includes a plurality of filter cartridge modules in serial fluid communication. Each filter cartridge module includes a volume of stationary phase particulates adjacent a porous substrate layer. The volume of stationary phase particulates has a bed height of less than 1 centimeter.

Claims (19)

1. A single pass method of continuously separating a target molecule from a solution mixture comprising steps of:

providing a simulated moving bed apparatus comprising a plurality of filter cartridge modules, each filter cartridge module comprising a volume of stationary phase particulates adjacent a porous substrate layer and the volume of stationary phase particulates having a bed height of less than 1 centimeter, each filter cartridge module having a filter cartridge module inlet and a filter cartridge module outlet, the plurality of filter cartridge modules being in serial fluid connection;

flowing a solution mixture comprising a target molecule continuously through the plurality of filter cartridge modules;

binding the target molecule to the volume of stationary phase particulates to form a target molecule:stationary phase particulate product;

removing a loaded filter cartridge module containing the target molecule:stationary phase particulate product from the solution mixture flow;

separating the target molecule from the target molecule:stationary phase particulate product from the loaded filter cartridge to form an isolated target molecule product and a regenerated filter cartridge; and

adding the regenerated filter cartridge module to the solution mixture flow.

2. A method according to claim 1 , wherein the providing step comprises providing a simulated moving bed apparatus comprising a plurality of filter cartridge modules, each filter cartridge module comprising a volume of stationary phase particulates adjacent a porous substrate layer and the volume of stationary phase particulates having a bed height in a range from 0.04 to 0.10 centimeters.

3. A method according to claim 1 , wherein the providing step comprises providing a simulated moving bed apparatus comprising a plurality of filter cartridge modules, each filter cartridge module comprising a volume of stationary phase particulates adjacent a porous substrate layer and the volume of stationary phase particulates having a mean diameter in a range from 5 to 30 micrometers.

4. A method according to claim 3 , wherein the flowing step comprises flowing a solution mixture comprising a target molecule continuously through the plurality of filter cartridge modules, wherein the solution mixture flows through each filter cartridge at a rate of at least 5 liters/minute per liter of stationary phase particulates in each filter cartridge module and each filter cartridge has a pressure drop from the filter cartridge module inlet to the filter cartridge module outlet of 69 kPa (10 psi) or less.

5. A method according to claim 3 , wherein the flowing step comprises flowing a solution mixture comprising a target molecule continuously through the plurality of filter cartridge modules, wherein the solution mixture flows through each filter cartridge at a rate of at least 3 liters/minute per liter of stationary phase particulates in each filter cartridge module and each filter cartridge has a pressure drop from the filter cartridge module inlet to the filter cartridge module outlet of 34 kPa (5 psi) or less.

6. A method according to claim 1 , wherein the flowing step comprises flowing a solution mixture comprising a target molecule wherein the target molecule comprises a biomacromolecule.

7. A method according to claim 1 , wherein the flowing step comprises flowing a solution mixture comprising a target molecule wherein the target molecule comprises a protein.

8. A method according to claim 1 , wherein the removing step and the adding step occur at the same time.

9. A method according to claim 1 , wherein the removing step, the flowing step and the adding step occur at the same time.

10. A method according to claim 1 , wherein the separating step, and the binding step occur at the same time.

11. A method according to claim 1 , wherein the removing step, the separating step, the flowing step, the binding step, and the adding step occur at the same time.

12. A method according to claim 1 , wherein the removing step comprises removing a loaded filter cartridge module containing a first concentration of target molecule per milliliter of stationary phase particulate and wherein the adding step comprises adding the regenerated filter cartridge module containing a second concentration of target molecule per milliliter of stationary phase particulate, and the first concentration of target molecule per milliliter of stationary phase particulate being greater than the second concentration of target molecule per milliliter of stationary phase particulate.

13. A method according to claim 1 , wherein the flowing step comprises flowing a solution mixture comprising a target molecule continuously through the plurality of filter cartridge modules and a feed flow rate and a filter cartridge module flow rate is substantially identical.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 1, 2024
From: 3M INNOVATIVE PROPERTIES COMPANY
To: SOLVENTUM INTELLECTUAL PROPERTIES COMPANY
Reel/Frame 066444/0535 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 30, 2005
From: GIBBENS, KELLY J.; NAKAMURA, MASAYUKI; SESHADRI, KANNAN; RABINS, ANDREW W.; CARSON, LARRY J.; FITZSIMONS, ROBERT T., JR.
To: 3M INNOVATIVE PROPERTIES COMPANY
Reel/Frame 017051/0719 →