Porous membranes for high pressure filtration
US-12064731-B2 · Aug 20, 2024 · US
US10744467B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10744467-B2 |
| Application number | US-201515128385-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 26, 2015 |
| Priority date | Mar 26, 2014 |
| Publication date | Aug 18, 2020 |
| Grant date | Aug 18, 2020 |
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One aspect of the present invention concerns a porous hollow fiber membrane containing a vinylidene fluoride-based resin. The hollow fiber membrane has a gradient structure in which a pore diameter of pores in the hollow fiber membrane gradually becomes smaller at least toward one of inner and outer peripheral surface sides and is hydrophilized by containing a crosslinked body of a polyvinylpyrrolidone-based resin.
Opening claim text (preview).
The invention claimed is: 1. A porous hollow fiber membrane, comprising a vinylidene fluoride-based resin, wherein the hollow fiber membrane has a gradient structure in which a pore diameter of pores in the hollow fiber membrane gradually becomes smaller at least toward one of inner and outer peripheral surface sides; the hollow fiber membrane is hydrophilized by containing from 0.1 to 15 mass % of a crosslinked body of a polyvinylpyrrolidone-based resin; and a ratio (FD10/FW) of a water permeation speed (FD10) at an inter-membrane differential pressure of 0.1 MPa in the dry state after wet and dry states are alternately repeated ten times to a water permeation speed (FW) at an inter-membrane differential pressure of 0.1 MPa in the wet state is 40% or higher; wherein a K-value of the polyvinylpyrrolidone-based resin is from 60 to 120. 2. The hollow fiber membrane according to claim 1 , wherein: a water permeation amount at an inter-membrane differential pressure of 0.1 MPa is 1000 to 40000 L/m 2 /hr; and a fractionation particle diameter is 0.001 to 0.5 μm. 3. The hollow fiber membrane according to claim 1 , wherein the hollow fiber membrane comprises a single layer. 4. The hollow fiber membrane according to claim 1 , wherein the crosslinked body is obtained by crosslinking the polyvinylpyrrolidone-based resin contained in the hollow fiber membrane before crosslinking in forming the hollow fiber membrane before crosslinking. 5. A method for producing the hollow fiber membrane according to claim 1 , the method comprising: extruding a membrane forming solution comprising the vinylidene fluoride-based resin, the polyvinyl-pyrrolidone-based resin, and a solvent into a hollow fiber; solidifying the membrane forming solution extruded into the hollow fiber and forming a hollow fiber membrane before crosslinking; washing the hollow fiber membrane before crosslinking; and crosslinking the polyvinylpyrrolidone-based resin in the hollow fiber membrane before crosslinking, wherein a mass ratio of the vinylidene fluoride-based resin to the polyvinylpyrrolidone-based resin is from 1.54 to 4.38. 6. The method according to claim 5 , wherein said crosslinking comprises immersing the hollow fiber membrane before crosslinking in an aqueous solution comprising a radical initiator. 7. The hollow fiber membrane according to claim 1 , wherein a pure water permeability coefficient is from 0.4×10 −11 ×L (m 2 ) to 6×10 −11 ×L (m 2 ) when a thickness of the hollow fiber membrane is L (m).
Chemical modification · CPC title
Dense layers being placed on the outer side of the cross-section · CPC title
Hollow fibre modules · CPC title
Coagulation · CPC title
Casting solutions therefor · CPC title
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