High performance membranes for water reclamation using polymeric and nanomaterials
US-2016038885-A1 · Feb 11, 2016 · US
US2015321151A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2015321151-A1 |
| Application number | US-201314005902-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 7, 2013 |
| Priority date | Jun 8, 2012 |
| Publication date | Nov 12, 2015 |
| Grant date | — |
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The present invention relates to a reverse osmosis membrane including: a porous support; and a polyamide active layer formed on the porous support and including zeolite, surface-treated with a compound having at least one functional group selected from a group consisting of an amino group and a glycidyl group, and a method of manufacturing the same.
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1 . A reverse osmosis membrane comprising: a porous support; and a polyamide active layer formed on the porous support and including zeolite, surface-treated with a compound having at least one functional group selected from a group consisting of an amino group and a glycidyl group. 2 . The reverse osmosis membrane of claim 1 , wherein the compound is a silane compound having the at least one functional group selected from the group consisting of the amino group and the glycidyl group. 3 . The reverse osmosis membrane of claim 1 , wherein the surface-treated zeolite is zeolite, surface-treated with the compound having the amino group, and the amino group is chemically bonded to the polyamide active layer. 4 . The reverse osmosis membrane of claim 1 , wherein the zeolite has an MFI (Zeolite Socony Mobil-five) type structure, an LTA (Zeolite A) type structure, or a FAU(Faujasite) type structure. 5 . The reverse osmosis membrane of claim 1 , wherein a difference between a maximum particle diameter and a minimum particle diameter of the surface-treated zeolite is 10 to 200 nm. 6 . The reverse osmosis membrane of claim 1 , wherein an average particle diameter of the surface-treated zeolite is 50 to 200 nm. 7 . A method of manufacturing a reverse osmosis membrane, the method comprising: forming a porous support; and forming a polyamide active layer on the porous support by interfacially polymerizing a polyfunctional amine solution including zeolite surface-treated with a compound having at least one functional group selected from a group consisting of an amino group and a glycidyl group and a polyfunctional acid halide compound solution. 8 . The method of claim 7 , wherein the surface-treated zeolite is included in an amount of 0.001 wt % to 1 wt %, with respect to 100 wt % of the polyfunctional amine solution.
Type ZSM-5 · CPC title
Adsorbents being present on the surface of the membranes or in the pores · CPC title
Polyamides, e.g. polyester-amides · CPC title
Reverse osmosis; Hyperfiltration · CPC title
Organic/inorganic mixed matrix membranes · CPC title
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