Novel membranes
US-2016158707-A1 · Jun 9, 2016 · US
US10569227B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10569227-B2 |
| Application number | US-201415029568-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 13, 2014 |
| Priority date | Oct 15, 2013 |
| Publication date | Feb 25, 2020 |
| Grant date | Feb 25, 2020 |
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Polyethers (A), whose main chain essentially consists of repeating units of the formulae (1) and (2) in alternating order, are useful as an additive to a porous polymer membrane, or as the main polymer constituent of a porous polymer membrane, for stabilizing said membrane against detrimental effects of oxidizing agents and/or for improving the stability of a filtration module comprising said membrane against detrimental effects of oxidizing agents.
Opening claim text (preview).
The invention claimed is: 1. A filtration process, comprising subjecting a membrane polymer material to a chemically enhanced backwash comprising an aqueous solution comprising an oxidizing agent, wherein the oxidizing agent is hypochlorite, wherein the chemically enhanced backwash is a plurality of chemically enhanced backwashes with a period between chemically enhanced backwashes being between 3 and 24 hours, and wherein the hypochlorite is present in the chemically enhanced backwashes at a concentration of 1000 ppm or higher; wherein the membrane polymer material comprises a polyether (A), whose main chain comprises 95 to 100% by weight of repeating units of the formulae (1) and (2) in alternating order, wherein the polyether (A) has a molecular weight Mw in a range of 10 to 500 kDa, wherein the membrane polymer material is an asymmetric polymer membrane obtained from a polymer solution in a coating process or in a phase inversion process, and the polyether (A) has been added to the polymer solution, wherein the asymmetric polymer membrane has a dense layer and a supporting layer, wherein a thickness of the supporting layer is from 30 to 2000 μm, and a thickness of the dense layer is not more than 0.5 μm, wherein the polyether (A) is present in the membrane polymer material in a total amount of not less than 85% by weight, and wherein the filtration process is a water filtration process. 2. The filtration process according to claim 1 , wherein the polyether (A) containing repeating units of the formulae (1) and (2) has a formula (3) wherein n ranges from 30 to 1000. 3. The filtration process according to claim 1 , wherein the membrane polymer material comprises the polyether (A) and a further polyether (B) comprising 95 to 100% by weight of repeating units of the formula (2), in an amount of 85 to 100% of the total weight of membrane polymers. 4. The filtration process according to claim 1 , wherein the membrane polymer material is a water filtration membrane. 5. The filtration process of claim 1 , wherein the membrane polymer material is in a form of a filtration module or plant. 6. The filtration process of claim 1 , wherein the oxidizing agent is NaOCl. 7. The filtration process of claim 1 , wherein the supporting layer has a pore size of from 1 to 100 μm. 8. The filtration process of claim 1 , wherein the dense layer has a pore size of from 0.01 to 1.0 μm. 9. The filtration process of claim 1 , wherein the chemically enhanced backwash is performed with a washing time of from 10 to 60 minutes.
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
Tubular membranes · CPC title
using a bath, e.g. extruding into an open bath to coagulate or cool the material · CPC title
Use of other chemical agents · CPC title
Permeability to liquids; Adsorption · CPC title
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