IP Library Granted Patent US 10,399,039
Granted Patent B2
US 10,399,039 · App. 14/750,838 · Granted Sep 3, 2019

Compact spiral-wound filter elements, modules and systems

Inventor: Jonathan Steen (Billerica, MA)
Assignee: EMD Millipore Corporation
B01D63/12B01D61/025B01D61/145B01D63/10B01D63/103C02F1/44C02F1/441C02F1/442D06C15/02B01D61/147B01D67/0086B01D71/68B01D2313/14B01D2313/143B01D2313/146B01D2313/50B01D2315/10B01D2315/16B01D2317/02C02F1/444
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Quick Facts
Patent No.
US 10,399,039
App. No.
14/750,838
Granted
Sep 3, 2019
Kind
B2
Abstract

The present invention provides compact spiral-wound filter elements having cassette-like performance. The invention further provides filtration systems (e.g., TFF systems) and processes (e.g., SPTFF processes) employing compact spiral-wound filter elements having cassette-like performance.

Claims (29)

1. A spiral-wound filter element comprising:

a) a feed channel having a height of less than about 450 μm and a length that is less than about 800 times the feed channel height, the feed channel including a mesh fiber feed screen;

b) a permeate channel having a height of less than about 300 μm, the permeate channel including a mesh fiber permeate screen; and

c) a filtration membrane having a pore size in the range of about 1 nm to about 100 nm.

2. The filter element of claim 1 , wherein the feed channel has a length of about 18 inches (45.72 cm) or less.

3. The filter element of claim 1 , comprising two or more spiral-wound filter sub-elements.

4. The filter element of claim 1 , wherein the mesh fiber permeate screen is a woven fiber screen having flattened or removed tangent points along an outer surface of the woven fiber screen.

5. The filter element of claim 1 , wherein the mesh fiber feed screen has an uncompressed height of about 600 μm or less.

6. The filter element of claim 1 , wherein the mesh fiber permeate screen is configured to compress less than about 130 μm under compression at about 50 psi at an operating temperature of about 15° C. to about 30° C.

7. The filter element of claim 1 , comprising an outermost feed channel layer that is blocked.

8. The filter element of claim 1 , wherein the mesh fiber feed screen is imprinted into the membrane, precompressed, or a combination thereof.

9. The filter element of claim 1 , wherein the mesh fiber feed screen is capable of expanding and maintaining contact with a surface of a membrane during operation.

10. The filter element of claim 1 , wherein the filter element is in a housing, sleeve, or liner.

11. A tangential flow filtration (TFF) system comprising at least one filter element claim 1 .

12. The TFF system of claim 11 , wherein the TFF system can be operated in a single-pass mode.

13. The TFF system of claim 11 , comprising at least two filter elements of claim 1 , and wherein the filter elements are fluidly connected in series, in parallel, or in a configuration having both serial and parallel connections.

14. The TFF system of claim 11 , further comprising a reservoir for diafiltration solution and a conduit for delivering diafiltration to a feed reservoir.

15. The filter element of claim 1 , wherein the mesh fiber permeate screen is compressible.

16. The filter element of claim 1 , wherein the mesh fiber permeate screen has an uncompressed height of 300 μm or less.

17. The filter element of claim 1 , wherein the mesh fiber permeate screen is woven.

18. A process for filtering a liquid, comprising:

providing at least one spiral-wound filter element comprising:

a feed channel having a height of less than about 450 μm and a length that is less than about 800 times the feed channel height, the feed channel including a mesh fiber feed screen,

a permeate channel having a height of less than about 300 μm, the permeate channel including a mesh fiber permeate screen, and

a filtration membrane having a pore size in the range of about 1 nm to about 100 nm;

passing a liquid feed through the at least one filter element;

separating the liquid feed into permeate and retentate in the filter element; and

recovering the permeate and at least a portion of the retentate from the filter element.

19. The process of claim 18 , wherein the process is a tangential flow filtration (TFF) process.

Assignments (2)
CHANGE OF ADDRESS Recorded Feb 15, 2018
From: EMD MILLIPORE CORPORATION
To: EMD MILLIPORE CORPORATION
Reel/Frame 045341/0166 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 8, 2015
From: STEEN, JONATHAN
To: EMD MILLIPORE CORPORATION
Reel/Frame 036760/0429 →
Continuity (2)
Provisional Application 62017084 · Jun 25, 2014
Related Publication 20150375173A1 · Dec 31, 2015
Cited By (6)
US 12,201,925 US 12,226,737 US 12,297,229 US 12,611,839 US 12,636,617 US 12,673,287