Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US9550153B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9550153-B2 |
| Application number | US-201314758414-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 11, 2013 |
| Priority date | Jan 24, 2013 |
| Publication date | Jan 24, 2017 |
| Grant date | Jan 24, 2017 |
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The present invention provides a porous polymer flat-sheet membrane for MBR wherein surface of the porous polymer membrane is kept hydrophilic for a long period and high water permeability and anti-fouling properties are kept. A porous polymer flat-sheet membrane for MBR comprising a hydrophobic porous polymer membrane forming a network structure and a sheet substrate supporting it, characterized in that at least surface of the porous polymer membrane is coated and fixed with an insolubilized hydroxypropyl cellulose, that a ratio of the hydroxypropyl cellulose to the porous polymer membrane is 0.4 to 1.0% by weight and that, when NMR spectrum of the hydroxypropyl cellulose coated on and fixed to the membrane is measured using a nuclear magnetic resonance apparatus (proton NMR), an intensity ratio (B/A) of a spectral peak (B) appearing at 4.12 ppm to a spectral peak (A) appearing at 3.75 ppm is 12 to 30%.
Opening claim text (preview).
The invention claimed is: 1. A porous polymer flat-sheet membrane for MBR comprising; a hydrophobic porous polymer membrane forming a network structure, and a sheet substrate supporting it, wherein at least a surface of the hydrophobic porous polymer membrane are coated and fixed with an insolubilized hydroxypropyl cellulose, such that a content ratio of the hydroxypropyl cellulose in the porous polymer flat-sheet membrane is 0.4 to 1.0% by weight and that, when NMR spectrum of the hydroxypropyl cellulose coated on and fixed to the hydrophobic porous polymer membrane is measured using a nuclear magnetic resonance apparatus (proton NMR), an intensity ratio (B/A) of a spectral peak (B) appearing at 4.12 ppm to a spectral peak (A) appearing at 3.75 ppm is 12 to 30%. 2. The flat-sheet membrane according to claim 1 , wherein a filter flow in a dry state is 30 to 60 L/min when a pressure is 150 kPa. 3. The flat-sheet membrane according to claim 1 , wherein average pore size of the flat-sheet membrane when measured by a perm porometer is 0.2 to 0.5 μm. 4. The flat-sheet membrane according to claim 1 , wherein pure water flux is 15 to 50 mL/cm 2 /min/bar and bubble point is 0.08 to 0.3 MPa. 5. A method for producing the flat-sheet membrane according to claim 1 , wherein a sheet substrate is impregnated with a membrane-preparation solution containing hydrophobic polymer, solvent and non-solvent followed by drying to form a sheet, wherein a porous polymer membrane is formed on and in the sheet substrate, then the resulting sheet is successively put into a tank containing hydroxypropyl cellulose in an impregnating step, a water washing step in a water washing tank and a fixing step in a hot water tank of 50 to 72° C. followed by a drying step and a time for putting into the hot water tank of 50 to 72° C. is 50 to 75 minutes.
Specific non-solvents or non-solvent system · CPC title
details of construction, e.g. specially adapted seals, modules, connections · CPC title
characterised by their properties · CPC title
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Degradation or stability over time · CPC title
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