IP Library Granted Patent US 10,183,108
Granted Patent B2
US 10,183,108 · App. 15/015,350 · Granted Jan 22, 2019

Inline diafiltration with multi-channel pump

Inventors: Engin Ayturk (Shrewsbury, MA); Catherine Casey (Framingham, MA)
Assignee: Pall Corporation
A61M1/3413B01D61/14B01D61/145B01D61/18B01D61/22B01D63/08B01D63/085C07K1/34C07K16/00B01D2311/16B01D2311/165B01D2313/18B01D2313/243B01D2313/54B01D2315/10B01D2315/16B01D2319/04
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Quick Facts
Patent No.
US 10,183,108
App. No.
15/015,350
Granted
Jan 22, 2019
Kind
B2
Abstract

A diafiltration system comprises a fluid treatment assembly comprising two or more fluid treatment modules, the fluid treatment assembly comprising a feed inlet, a permeate outlet, and a retentate outlet; each module comprising a cross flow treatment assembly including an ultrafiltration membrane and having a feed side and a permeate side, and a diafiltration fluid distribution plate comprising a diafiltration fluid feed inlet and a common feed permeate/diafiltration fluid permeate outlet port; two or more diafiltration fluid conduits, each conduit in fluid communication with a respective single diafiltration fluid feed inlet; and, a diafiltration fluid pump comprising at least a first multiple channel pump head having at least two channels including separate channels for separate conduits in fluid communication with respective single diafiltration fluid feed inlets, wherein the pump provides simultaneously controlled diafiltration fluid flow rates through each of the conduits to the respective diafiltration fluid feed inlets.

Claims (19)

1. A diafiltration system comprising

(a) a fluid treatment assembly comprising two or more fluid treatment modules, the fluid treatment assembly comprising a feed inlet, a permeate outlet, and a retentate outlet;

(i) each fluid treatment module comprising a cross flow treatment assembly including at least one ultrafiltration membrane, the cross flow treatment assembly having at least one feed side and at least one opposite permeate side, and a diafiltration fluid distribution plate comprising a diafiltration fluid feed inlet and a common feed permeate/diafiltration fluid permeate outlet port;

(b) two or more separate diafiltration fluid conduits, each separate diafiltration fluid conduit in fluid communication with a respective single diafiltration fluid feed inlet;

(c 1 ) a feed fluid pump and a feed fluid conduit, wherein the feed fluid conduit is in fluid communication with the fluid treatment assembly feed inlet, wherein the feed fluid pump provides a controlled feed fluid flow rate through the feed fluid conduit to the fluid treatment assembly feed inlet

and,

(c 2 ) a diafiltration fluid pump, the diafiltration fluid pump comprising at least a first multiple channel pump head having at least two channels including separate channels for separate diafiltration fluid conduits in fluid communication with respective single diafiltration fluid feed inlets, wherein the diafiltration pump provides simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits to the respective single diafiltration fluid feed inlets,

wherein the system is arranged to pass feed fluid through the feed inlet at a controlled flow rate that is at least about 10% less than the simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits.

2. The diafiltration system of claim 1 , including at least one additional channel pump head having including a separate channel for a separate diafiltration fluid conduit in fluid communication with a single diafiltration fluid feed inlet, wherein the pump, via the first multiple channel pump head and the additional channel pump head, provides simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits to the respective single diafiltration fluid feed inlets.

3. The diafiltration system of claim 2 , including at least one additional multiple channel pump head having at least two channels including a separate channel for a separate diafiltration fluid conduit in fluid communication with a single diafiltration fluid feed inlet, wherein the pump, via the first multiple channel pump head and the additional multiple channel pump head, provides simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits to the respective single diafiltration fluid feed inlets.

4. The diafiltration system of claim 1 , including at least one additional multiple channel pump head having at least two channels including a separate channel for a separate diafiltration fluid conduit in fluid communication with a single diafiltration fluid feed inlet, wherein the pump, via the first multiple channel pump head and the additional multiple channel pump head, provides simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits to the respective single diafiltration fluid feed inlets.

5. The diafiltration system of claim 1 , further comprising a retentate throttling valve, arranged to allow the system to maintain a desired ratio of feed flow rate to retentate flow rate.

6. A diafiltration method, the method comprising passing a feed fluid containing undesirable material and desirable biomolecules, and a diafiltration fluid suitable for washing out undesirable material from the feed fluid, through the fluid treatment assembly in the diafiltration system of claim 1 , wherein the method includes

(a) passing the feed fluid at a controlled feed fluid flow rate through the feed inlet of the fluid treatment assembly;

(b) passing the diafiltration fluid at a controlled diafiltration fluid flow rate through each of the separate diafiltration fluid conduits in fluid communication with respective single diafiltration fluid feed inlets, such that the diafiltration fluid washes undesirable material from the feed fluid, wherein the controlled diafiltration fluid flow rate is simultaneously controlled through each of the separate diafiltration fluid conduits;

(c) passing a feed permeate/diafiltration fluid permeate fluid through each of the common feed permeate/diafiltration fluid permeate outlet ports;

(d) passing a retentate fluid from the retentate outlet of fluid treatment assembly, the retentate fluid comprising desirable biomolecules and a lower concentration of undesirable material than the concentration of undesirable material in the feed fluid; and,

(e) passing the feed permeate/diafiltration fluid permeate fluid from the permeate outlet of the fluid treatment assembly,

including passing the feed fluid through the feed inlet at a controlled flow rate that is at least about 10% less than the simultaneously controlled diafiltration fluid flow rates through each of the separate diafiltration fluid conduits.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 22, 2023
From: PALL CORPORATION
To: CYTIVA US LLC
Reel/Frame 063144/0716 →
CORRECTION BY DECLARATION OF INCORRECT NUMBER 29553358 RECORDED AT REEL/FRAME 037740/0577 Recorded Mar 21, 2017
From: PALL CORPORATION
To: PALL CORPORATION
Reel/Frame 042051/0461 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 10, 2017
From: AYTURK, ENGIN; CASEY, CATHERINE
To: PALL CORPORATION
Reel/Frame 040921/0860 →
Continuity (1)
Related Publication 20170225123A1 · Aug 10, 2017