초록 ▼

A deep gradient-density filter device capable of effectively filtering a fluid containing a distribution of particles in the range of approximately 25 microns to approximately 0.2 micron at a fluid velocity of at least approximately 100 cm/hr and an initial hydraulic permeability of greater than app

A deep gradient-density filter device capable of effectively filtering a fluid containing a distribution of particles in the range of approximately 25 microns to approximately 0.2 micron at a fluid velocity of at least approximately 100 cm/hr and an initial hydraulic permeability of greater than approximately 10 cm/hr/psi. The deep gradient-density filter device includes several layers of filtration material, each having specific predetermined particle retention properties. In one product embodiment, the deep gradient-density filter device uses "loose" fibrillated cellulose fiber material as a primary filter element. In a method aspect, the deep gradient-density filter device is used for either the secondary clarification of industrial-scale volumes of cultured or fermented protein-containing biopharmaceutical fluids or the primary clarification of pilot-scale volumes.

대표청구항 ▼

The invention claimed is: 1. A deep gradient-density filter device having a depth of at least approximately 0.5 inch (1.27 cm.) and capable of filtering a fluid containing a distribution of particles in the range of approximately 25 microns to approximately 0.2 micron, the deep gradient-density fi

The invention claimed is: 1. A deep gradient-density filter device having a depth of at least approximately 0.5 inch (1.27 cm.) and capable of filtering a fluid containing a distribution of particles in the range of approximately 25 microns to approximately 0.2 micron, the deep gradient-density filter device comprising in order: (a) a pre-filtration zone comprising layers of filtration material, said pre-filtration zone capable of retaining particles in the range of approximately 25 microns to approximately 1 micron, (b) a primary filtration zone comprising filtration material, said primary filtration zone capable retaining particles in the range of approximately 1 micron to approximately 0.3 micron, and (c) a polishing zone comprising layers of filtration material, said polishing zone capable of retaining particles in the range of approximately 0.3 micron to approximately 0.2 micron; and wherein the retention capabilities of the pre-filtration zone, the primary filtration zone, and the polishing zone, as recited in (a), (b), and (c) respectively, are established at a fluid velocity of at least approximately 100 cm/hr and an initial hydraulic permeability of greater than approximately 10 cm/hr/psi. 2. The deep gradient-density filter device of claim 1, wherein said primary filtration zone comprises at least one layer of fibrillated fiber containing material. 3. The deep gradient-density filter device of claim 1, wherein said pre-filtration zone comprises: (i) a layer of non-woven fiber material having an approximately 25 micron nominal pore rating; and (ii) a layer of non-woven fiber material having an approximately 1 micron nominal pore rating. 4. The deep gradient-density filter device of claim 3, wherein said layers (i) and (ii) of said primary filtration zone are both substantially made of propylene fiber material, and both have a thickness within the range of approximately 0.10 inch (0.254 cm.) to approximately 0.15 inch (0.381 cm). 5. The deep gradient-density filter device of claim 3, wherein said primary filtration zone comprises at least one layer of fibrillated fiber containing material. 6. The deep gradient-density filter device of claim 5, wherein said polishing zone comprises: (i) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 140 to approximately 260 LMH/psi; (ii) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 68 to approximately 120 LMH/psi; (iii) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 300 to approximately 560 LMH/psi; (iv) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 140 to approximately 260 LMH/psi; and (v) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 70 to approximately 120 LMH/psi. 7. The deep gradient-density filter device of claim 6, wherein said layers (i), (ii), (iii), (iv), and (v) of said polishing zone each have a thickness within the range of approximately 0.10 inch (0. 254 cm.) to approximately 0.15 inch (0.381 cm). 8. A biopharmaceutical fluid processing methodology comprising the steps of: providing a manufactured protein-containing solution comprising a synthetically-enriched concentration of a predetermined target protein and a distribution of solid particles of differing sizes; providing a deep gradient-density filter device comprising abutting layers of filtration materials that collectively have a depth of at least approximately a half-inch; and passing said manufactured protein-containing solution through said deep gradient-density filter device at a velocity of at least approximately 100 cm/hr. 9. The biopharmaceutical fluid processing methodology of claim 8, wherein said abutting layers of filtration material of said deep gradient-density filter device define a pre-filtration zone, and primary filtration zone, and a polishing zone; wherein said pre-filtration zone is capable of retaining particles in the range of approximately 25 microns to approximately 1 micron, said primary filtration zone is capable retaining particles in the range of approximately 1 micron to approximately 0.3 micron, and said polishing zone is capable of retaining particles in the range of approximately 0.3 micron to approximately 0.2 micron; and wherein the retention capabilities of the pre-filtration zone, the primary filtration zone, and the polishing zone are established at a fluid velocity of at least approximately 100 cm/hr and an initial hydraulic permeability of greater than approximately 10 cm/hr/psi. 10. The biopharmaceutical fluid processing methodology of claim 8, wherein said abutting layers of filtration material of said deep gradient-density filter device define a pre-filtration zone, and primary filtration zone, and a polishing zone; and wherein said pre-filtration zone is capable of retaining particles within a first size distribution range; said primary filtration zone comprises at least one layer of fibrillated fiber containing material and is capable of retaining particles within a second size distribution range smaller than said first size distribution range, and said polishing zone is capable of retaining particles within a third size distribution range smaller than said second size distribution range. 11. A deep gradient-density filter device comprising in order: a pre-filtration zone comprising layers of filtration material, said pre-filtration zone capable of retaining particles within a first size distribution range; a primary filtration zone comprising at least one layer of fibrillated fiber containing material, said primary filtration zone capable of retaining particles within a second size distribution range, said second size distribution range being smaller than said first size distribution range; and a polishing zone comprising layers of filtration material, said polishing zone capable of retaining particles within a third size distribution range, said third size distribution range being smaller than said second size distribution range. 12. The deep gradient-density filter device of claim 11, wherein the device is capable of filtering a fluid containing a distribution of particles in the range of approximately 25 microns to approximately 0.2 micron; and wherein said first size distribution range is approximately 25 microns to approximately 1 micron, said second size distribution range is approximately 1 micron to approximately 0.3 micron, and said third size distribution range is approximately 0.3 micron to approximately 0.2 micron; and wherein the retention capabilities of the pre-filtration zone, the primary filtration zone, and the polishing zone are established at a fluid velocity of at least approximately 100 cm/hr and an initial hydraulic permeability of greater than approximately 10 cm/hr/psi. 13. The deep gradient-density filter device of claim 11, wherein said pre-filtration zone comprises: (i) a layer of non-woven fiber material having an approximately 25 micron nominal pore rating; and (ii) a layer of non-woven fiber material having an approximately 1 micron nominal pore rating. 14. The deep gradient-density filter device of claim 13, wherein said layers (i) and (ii) of said primary filtration zone are both substantially made of propylene fiber material. 15. The deep gradient-density filter device of claim 13, wherein said polishing zone comprises: (i) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 140 to approximately 260 LMH/psi; (ii) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 68 to approximately 120 LMH/psi; (iii) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 300 to approximately 560 LMH/psi; (iv) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 140 to approximately 260 LMH/psi; and (v) a wet-laid layer of cellulose and diatomaceous earth having a permeability of approximately 70 to approximately 120 LMH/psi.