Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US2017296984A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017296984-A1 |
| Application number | US-201515515761-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 30, 2015 |
| Priority date | Sep 30, 2014 |
| Publication date | Oct 19, 2017 |
| Grant date | — |
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The present invention provides a separation membrane having excellent separation performance and permeation performance, having high membrane strength, and mainly including a cellulose-based resin. The present invention relates to a separation membrane containing a cellulose ester and having a tensile elasticity of 1,500 to 6,500 MPa.
Opening claim text (preview).
1 . A separation membrane containing a cellulose ester and having a tensile elasticity of 1,500 to 6,500 MPa and a salt rejection of 90.0% or more. 2 . The separation membrane according to claim 1 , having a shape of a hollow fiber and having a tensile elasticity in a lengthwise direction of 1,500 to 6,500 MPa. 3 . The separation membrane according to claim 2 , wherein the hollow fiber has an outer diameter of 20 to 200 μm. 4 . The separation membrane according to claim 1 , having a degree of orientation of 1.05 to 2.50 in a lengthwise direction of the separation membrane. 5 . The separation membrane according to claim 1 , having a crystal melting heat amount (ΔHm) of 4 to 20 J/g in a temperature rise measurement with a differential scanning calorimeter (DSC). 6 . The separation membrane according to claim 1 , having a positron annihilation life of 2.2 to 3.0 ns. 7 . The separation membrane according to claim 1 , wherein the cellulose ester is at least one of cellulose acetate propionate and cellulose acetate butyrate. 8 . The separation membrane according to claim 1 , containing a polyalkylene glycol having a number average molecular weight (Mn) of 2,000 to 1,000,000. 9 . The separation membrane according to claim 1 , which is any one selected from a nanofiltration membrane, a reverse osmosis membrane and a forward osmosis membrane. 10 . A method for producing a hollow fiber, the method comprising: discharging from a spinneret a polymer obtained by kneading at least 50% to 95% by weight of a cellulose ester and 5% to 50% by weight of a polyalkylene glycol, followed by winding at a draft ratio of 200 or more while cooling with cooling air. 11 . A method for producing a hollow fiber membrane, the method comprising: eluting a polyalkylene glycol from a hollow fiber containing a cellulose ester at a ratio of 50% to 95% by weight and the polyalkylene glycol at a ratio of 5% to 50% by weight. 12 . A hollow fiber membrane module comprising: a case; and the separation membrane according to claim 2 , which is filled in the case. 13 . A water production method comprising: a step of feeding mixed liquid containing water to the separation membrane according to claim 1 at a pressure of 0.3 to 6.0 MPa.
by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title
Hollow fibre membranes (manufacture of hollow fibres D01D5/24, D01F1/08) · CPC title
Mixed esters, e.g. cellulose acetate-butyrate · CPC title
Seawater, e.g. for desalination · CPC title
Mechanical properties, e.g. strength · CPC title
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