Separation membrane and method for producing same
US-2017157572-A1 · Jun 8, 2017 · US
US2016310907A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016310907-A1 |
| Application number | US-201415103591-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 27, 2014 |
| Priority date | Dec 13, 2013 |
| Publication date | Oct 27, 2016 |
| Grant date | — |
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An object of the present invention is to provide a multilayer separation membrane having excellent performance on both removal of suspended solids in water and adsorptive removal of metal ions in water. A multilayer separation membrane of the present invention includes: a porous adsorption layer including substantially a polymer having chelating functional groups; and a porous clarification layer and the porous clarification layer is disposed neater to a raw water-side than the porous adsorption layer.
Opening claim text (preview).
1 . A multilayer separation membrane comprising: a porous adsorption layer comprising substantially a polymer having chelating functional groups; and a porous clarification layer disposed nearer to a raw water-side than the porous adsorption layer. 2 . The multilayer separation membrane according to claim 1 , wherein an average pore diameter A of pores in the porous adsorption layer and an average pore diameter B at a surface of the porous clarification layer satisfy a relation A>B. 3 . The multilayer separation membrane according to claim 1 , wherein the porous adsorption layer has a thickness of 10 μm to 500 μm. 4 . The multilayer separation membrane according to claim 1 , wherein the porous adsorption layer is a layer throughout which the polymer having the chelating functional groups is distributed uniformly, and when elemental analysis on cross sections of the porous adsorption layer is performed by an energy-dispersive X-ray analysis, an average value X of atom counts (%) of atoms derived from the chelating functional groups and a standard deviation Y thereof satisfy a relation X≧3Y. 5 . The multilayer separation membrane according to claim 4 , wherein the atoms derived from the chelating functional groups are at least one selected from the group consisting of N, O, P, S, Na and K. 6 . The multilayer separation membrane according to claim 1 , further comprising a supporting layer. 7 . The multilayer separation membrane according to claim 1 , which has a pure-water permeability of 0.10 m 3 /m 2 /hr to 10 m 3 /m 2 /hr under 50 kPa at 25° C., a rupture strength of 6 MPa or higher, and a rupture elongation of 10% or higher. 8 . The multilayer separation membrane according to claim 1 , wherein the porous adsorption layer is a layer obtained in accordance with a thermally-induced phase separation method and/or a nonsolvent-induced phase separation method. 9 . The multilayer separation membrane according to claim 1 , wherein the porous clarification layer is a layer obtained in accordance with a thermally-induced phase separation method and/or a nonsolvent-induced phase separation method.
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