IP Library Granted Patent US 8,403,153
Granted Patent B2
US 8,403,153 · App. 12/718,336 · Granted Mar 26, 2013

Adsorbent filter media for removal of biological contaminants in process liquids

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Quick Facts
Patent No.
US 8,403,153
App. No.
12/718,336
Granted
Mar 26, 2013
Kind
B2
Abstract

Adsorbent filter media particularly suited for removal of biological contaminants in process liquids. A porous fixed bed of adsorbent material is formed, using only a granular adsorbent and a water-insoluble thermoplastic binder. The resulting composite filter allows for a higher amount of adsorbent with smaller adsorbent particles than conventional depth filters. Elimination of cellulose fiber, as well as the elimination of the thermoset binder, results in reduced contamination of the process liquid.

Claims (18)

1. A porous composite monolith for removing biological contaminants in process liquids comprising:

a compressed heat fused composite porous monolith having an adsorbent chromatography media material, and a water-insoluble thermoplastic binder dry mixture compressed to about 50-70% of the original volume of the composite porous monolith prior to and/or during heat fusing together the adsorbent chromatography media material and the thermoplastic binder, the composite porous monolith being substantially devoid of cellulose and a thermoset binder,

wherein the thermoplastic binder includes polyolefins, polyethylene, polypropylene, ultra-high molecular weight polyethylene, or mixtures thereof, and

the ratio of thermoplastic binder to adsorbent chromatography media material ratio is about 1:1 to about 1:3 by weight.

2. The composite monolith of claim 1 , wherein the adsorbent chromatography media material includes beads, powder, or particles, and the thermoplastic binder includes fibers, microfibers, beads or powder.

3. The composite monolith of claim 1 , further comprising porous glass beads.

4. The composite monolith of claim 1 , wherein the thermoplastic binder comprises ultra-high molecular weight polyethylene.

5. The composite monolith of claim 1 , wherein the composite is formed by heating the adsorbent chromatography media material and the binder to a temperature at which the binder at least partially melts or softens to thermally bond the adsorbent chromatography media material together.

6. The composite monolith of claim 3 , wherein the adsorbent chromatography media material has a particle size range about 0.2 microns to about 25 microns, the binder comprises ultra-high molecular weight polyethylene powder having an average particle size about 25 microns, and the porous glass beads have an average bead diameter about 20 microns to 30 microns.

7. The composite monolith of claim 1 , having a thickness about 2 mm to about 4 mm.

8. The composite monolith of claim 7 , further comprising an adsorbent filter media.

9. The composite monolith of claim 7 , further comprising a pre-filter.

10. A biopharmaceutical clarification system, comprising:

a) a bioreactor;

b) a sterile filter downstream of the bioreactor; and

c) a composite filter media downstream of the bioreactor and upstream of the sterile filter, the composite filter media including a heat fused composite porous monolith having an adsorbent chromatography media material and a water-insoluble thermoplastic binder dry mixture compressed to about 50-70% of the original volume of the composite porous monolith prior to and/or during heat fusing together the adsorbent chromatography media material and the thermoplastic binder, the composite filter media being substantially devoid of cellulose and a thermoset binder, wherein the thermoplastic binder includes polyolefins, polyethylene, polypropylene, ultra-high molecular weight polyethylene, or mixtures thereof, and

the ratio of thermoplastic binder to adsorbent chromatography media material is about 1:1 to about 1:3 by weight.

11. The biopharmaceutical clarification system of claim 10 , further comprising an aqueous product stream feedstock from the bioreactor, pretreated through the composite filter media, the resulting filtrate being processed through the sterile filter.

Assignments (2)
CHANGE OF ADDRESS Recorded Feb 15, 2018
From: EMD MILLIPORE CORPORATION
To: EMD MILLIPORE CORPORATION
Reel/Frame 045341/0166 →
CHANGE OF NAME Recorded Jan 31, 2012
From: MILLIPORE CORPORATION
To: EMD MILLIPORE CORPORATION
Reel/Frame 027620/0891 →