Process for the preparation of MOFs-porous polymeric membrane composites
US-9713796-B2 · Jul 25, 2017 · US
US10005044B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10005044-B2 |
| Application number | US-201414766844-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 24, 2014 |
| Priority date | Feb 25, 2013 |
| Publication date | Jun 26, 2018 |
| Grant date | Jun 26, 2018 |
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The invention relates to a virus filter membrane which can be used for the removal of virus particles including parvovirus. The invention further relates to a method for producing the membrane. The membrane comprises polyacrylonitrile and polyvinylpyrrolidone.
Opening claim text (preview).
The invention claimed is: 1. A porous hollow fiber membrane having a homogeneous sponge-like structure free of macrovoids having a largest dimension of more than 5 μm, the membrane comprising: 75-85 wt % of polyacrylonitrile and 15-25 wt % of polyvinylpyrrolidone, relative to the total weight of the membrane, wherein the polyvinylpyrrolidone has a weight average molecular weight in the range of from 1,000 to 2,000 kDa, wherein the membrane is prepared from a polymer solution comprising, relative to the total weight of the polymer solution, from 8 to 12 wt % of polyacrylonitrile and from 2 to less than 6 wt % of polyvinylpyrrolidone, and the membrane has a sieving coefficient for IgG, determined by dead-end filtration of a solution of 15.0 g/l IgG in PBS buffer at 25° C., of greater than 0.9, and a Gold Particle Retention (GPR) value for 20 nm gold particles, measured at 25° C., of greater than 1.7. 2. The membrane of claim 1 , having a hydraulic permeability, measured at 37° C., of from 8·10 −4 to 15·10 4 cm 3 /(cm 2 ·bar·sec). 3. The membrane of claim 1 , having a hydraulic permeability, measured at 37° C., of from 20·10 −4 to 40·10 −4 cm 3 /(cm 2 ·bar·sec). 4. The membrane of claim 1 , having an inner diameter of from 300 to 400 μm; a wall thickness from 40 to 85 μm; and a burst pressure of at least 5 bar(g). 5. A continuous solvent phase inversion spinning process for preparing a porous hollow fiber membrane, the process comprising: dissolving at least one polyacrylonitrile and at least one polyvinylpyrrolidone in N-methyl-2-pyrrolidone to form a polymer solution; extruding the polymer solution through an outer ring slit of a nozzle with two concentric openings into a precipitation bath; simultaneously extruding a center fluid through the inner opening of the nozzle; washing the membrane obtained; and subsequently drying the membrane; wherein the polymer solution comprises, relative to the total weight of the polymer solution, from 8 to 12 wt % of polyacrylonitrile and from 2 to less than 6 wt % of polyvinylpyrrolidone having a weight average molecular weight in the range of from 1,000 to 2,000 kDa. 6. The process of claim 5 , wherein the polymer solution has a viscosity, measured according to DIN EN ISO 1628-1 at 22° C., in the range of from 50,000 to 140,000 mPa·s. 7. The process of claim 5 , wherein the center fluid comprises 20 to 40 wt % of water and 60 to 80 wt % of NMP, relative to the total weight of the center fluid. 8. The process of claim 5 , wherein the precipitation bath comprises 20 to 40 wt % of water and 60 to 80 wt % of NMP, relative to the total weight of the precipitation bath. 9. The process of claim 5 , wherein the temperature of the spinneret is in the range of from 25 to 50° C. 10. The process of claim 5 , wherein the membrane is spun at a speed of from 5 to 10 m/min. 11. The process of claim 5 , wherein the membrane is sterilized with beta radiation or electron beam at from 25 to 50 kGy subsequently to drying. 12. A diffusion and/or filtration device comprising a membrane according to claim 1 , or a membrane prepared according to claim 5 . 13. A method of using a membrane according to claim 1 , or a membrane prepared according to claim 5 , the method comprising: filtration of a liquid through the membrane for removing virus particles from the liquid. 14. The method of claim 13 , wherein the filtration is tangential-flow filtration. 15. A diffusion and/or filtration device comprising a plurality of membranes according to claim 1 . 16. A diffusion and/or filtration device comprising a plurality of membranes prepared according to claim 5 .
Ultrafiltration; Microfiltration · CPC title
characterised by the fibre diameter · CPC title
Characteristic thickness · CPC title
Co-extrusion; Co-spinning · CPC title
by radiation · CPC title
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