Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US10561990B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10561990-B2 |
| Application number | US-201515503298-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 12, 2015 |
| Priority date | Aug 13, 2014 |
| Publication date | Feb 18, 2020 |
| Grant date | Feb 18, 2020 |
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The invention relates to a combined method for gentle molecular surface functionalisation of the very thin, selectively-acting separating layer which preferably consists of aromatic polyamides, polyurethanes and/or polyureas, of thin-film composite membranes for reverse osmosis (hyperfiltration) and for nanofiltration, subsequently collectively termed water-filtration membranes, in order to achieve a passive antifouling effect without impairing the selectivity of the water-selective separating layer made of polyamides and the water-permeability of the membrane.
Opening claim text (preview).
The invention claimed is: 1. A method for the production of antifouling coatings of thin-film composite membranes for reverse osmosis, nanofiltration, or ultrafiltration by modifying a membrane surface, in which in a first step, a primary molecular functionalisation of the membrane in the gas phase is implemented by plasma-chemical activation of at least one halogen-organic compound which is convertible into gas phase and covalent binding of the plasma-chemical activated at least one halogen-organic compound to the membrane surface; wherein the plasma-chemical activation is effected with an electron cyclotron resonance plasma (ECR); and in a second step, a wet-chemical modification of the functionalised membrane is effected by radical graft polymerisation. 2. The method according to claim 1 , the at least one halogen-organic compound is selected from the group consisting of allyl halides, C1 to C8-alkylene halides, C1 to C8 alkyl halides, and mixtures thereof. 3. The method according to claim 1 , wherein the covalent binding is effected via alkylene bridges and derivatives thereof. 4. The method according to claim 2 , wherein the primary molecular functionalisation is effected in the gas phase at atmospheric pressure, a pressure range of 100 to 1,000 mbar, or in a vacuum in a pressure range of 0.01 to 100 mbar and at temperatures in the range of 20 to 150° C. but at most however up to the decomposition temperature of the polymer membrane layer. 5. The method according to claim 2 , wherein the halogen atoms of the halogen-organic compounds are split photochemically or by catalytic effect. 6. The method according to claim 5 , wherein starting from the covalently bonded halogen atoms, immobilised radicals are produced, based on which a radical graft polymerisation is started with alkenes. 7. The method according to claim 6 , wherein oligomeric or polymeric substances grow, by radical graft polymerisation, beginning on functional groups bonded on the membrane surface and orientated away from the membrane surface. 8. The method according to claim 2 , wherein the membrane surface to be modified consists of a material selected from the group consisting of polyamide, polyurethane, and a polyurea, or a composite thereof.
Graft polymerization · CPC title
by deposition from the gaseous phase, e.g. CVD, PVD · CPC title
Ultrafiltration · CPC title
Prevention of membrane fouling or of concentration polarisation · CPC title
Antimicrobial properties · CPC title
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