Porous membrane and method for manufacturing the same
US-2015298067-A1 · Oct 22, 2015 · US
US9314745B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9314745-B2 |
| Application number | US-201314380551-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 28, 2013 |
| Priority date | Mar 30, 2012 |
| Publication date | Apr 19, 2016 |
| Grant date | Apr 19, 2016 |
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Disclosed are a porous membrane having improved water permeability and elongation at break as well as high mechanical strength and impurity rejection rate and a method for manufacturing the same. The porous membrane of the present invention comprises a symmetric bead structure comprising a plurality of spherical crystallites. Each of the plurality of spherical crystallites comprises a plurality of sub-spherical crystallites.
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The invention claimed is: 1. A porous membrane comprising a symmetric bead structure comprising a plurality of spherical crystallites, wherein each of the plurality of spherical crystallites comprises a plurality of sub-spherical crystallites. 2. The porous membrane of claim 1 , wherein the plurality of spherical crystallites comprise polyvinylidene difluoride. 3. The porous membrane of claim 2 , wherein the plurality of spherical crystallites further comprise zeolite. 4. The porous membrane of claim 1 , wherein water permeability of the porous membrane measured under nitrogen pressure of 1.0 to 3.0 kgf/cm 2 is 0.7 (ml/cm 2 )·(min) −1 ·(kgf/cm 2 ) −1 or more, and wherein compaction index of the porous membrane as defined by a following equation is 0.5 or less: CI=( Lp 1.0 −Lp 3.0 )/ Lp 1.0 [Equation] wherein ‘CI’ represents the compaction index, ‘Lp 1.0 ’ represents water permeability of the porous membrane measured under a nitrogen pressure of 1.0 kgf/cm 2 , and ‘Lp 3.0 ’ represents water permeability of the porous membrane measured under a nitrogen pressure of 3.0 kgf/cm 2 . 5. The porous membrane of claim 1 , wherein the porous membrane has tensile strength of 0.7 kgf/fiber or more and elongation at break of 50% or more, and wherein rejection rate of the porous membrane with respect to particles having a diameter of 0.1 μm is 90% or more. 6. A method for manufacturing a porous membrane, the method comprising: dissolving at least one polymer selected from the group consisting of polyethersulfone, polysulfone, and polyvinylidene difluoride in a poor solvent to prepare a basic solution; adding an ionic liquid to the basic solution to prepare a spinning dope; extruding the spinning dope through a spinneret; and bringing the extruded spinning dope into contact with a coagulation solution so as to form a porous structure; wherein the membrane comprises a symmetric bead structure comprising a plurality of spherical crystallites, wherein each of the plurality of spherical crystallites comprises a plurality of sub-spherical crystallites. 7. The method of claim 6 , wherein the at least one polymer is dissolved in the poor solvent at a temperature of 100° C. or more but below a boiling point of the poor solvent. 8. The method of claim 6 , wherein the poor solvent comprises at least one of cyclohexanone, isophorone, γ-butyrolactone, methyl isoamyl ketone, dimethyl phthalate, propylene glycol methyl ether, propylene carbonate, diacetone alcohol, and glycerol triacetate. 9. The method of claim 8 , wherein the poor solvent comprises γ-butyrolactone. 10. The method of claim 6 , wherein the basic solution comprises 20 to 40% by weight of the at least one polymer and 60 to 80% by weight of the poor solvent, and wherein the spinning dope is prepared by adding the ionic liquid to the basic solution in an amount of 2 to 20% by weight based on total weight of the at least one polymer. 11. The method of claim 6 , wherein the ionic liquid comprises 1-butyl-3-methylimidazolium tetrafluoroborate. 12. The method of claim 6 , further comprising adding zeolite to the basic solution. 13. The method of claim 6 , wherein the coagulation solution comprises 20 to 80% by weight of water and 20 to 80% by weight of a volatile organic solvent, and wherein the volatile organic solvent comprises at least one of methanol, ethanol, isopropyl alcohol, acetone, butanone, diacetyl, acetylacetone, hexane-2,5-dione, diethyl ether, diisopropyl ether, and polyether. 14. The method of claim 6 , wherein a temperature of the coagulation solution is maintained at 5 to 20° C.
characterised by their properties · CPC title
Molecular sieves (carbon B01D71/021) · CPC title
Coagulation · CPC title
Details relating to pores or porosity of the membranes · CPC title
Details relating to the spinning process · CPC title
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