Application of rejection enhancing agents (REAs) that do not have cloud point limitations on desalination membranes
US-9216385-B2 · Dec 22, 2015 · US
US9527040B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9527040-B2 |
| Application number | US-201214352001-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 18, 2012 |
| Priority date | Oct 20, 2011 |
| Publication date | Dec 27, 2016 |
| Grant date | Dec 27, 2016 |
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Continuous processes for depleting residuals in hollow fiber membranes comprising polysulfone or polyethersulfone and polyvinylpyrrolidone by rinsing the membranes while compressing them in a pinching device comprising grooved rollers.
Opening claim text (preview).
The invention claimed is: 1. A process for removing residuals from hollow fiber membranes by enforced convective transport of a washing fluid through a membrane wall, said process comprising the step of bringing the hollow fiber membranes to a bath of the washing fluid prior to mechanically compressing the hollow fiber membranes, wherein the hollow fiber membranes are rinsed with the washing fluid during mechanical compression, and wherein the hollow fiber membranes are guided through a pinching device comprising a roller bearing a groove having a width smaller than the outer diameter of the membranes, and guiding the hollow fiber membranes over the roller bearing the groove having a width smaller than the outer diameter of the membranes, the hollow fiber membranes being passed through the groove. 2. A process according to claim 1 , wherein the groove width of the roller is in the range of from 50 to 200 μm. 3. A process according to claim 2 wherein a vacuum is applied to the hollow fiber membranes to suck the washing fluid through the wall of the membranes. 4. A process according to claim 3 wherein the hollow fiber membranes are guided over a roller comprising radial slots, the slots being smaller in width than the outer diameter of the hollow fiber membranes, the roller further comprising a center chamber having an access to the slots, wherein by applying vacuum to the center chamber and to the slots, the hollow fiber membrane is sucked into the slots, and wherein by simultaneously pouring a washing fluid over the hollow fibers, the washing fluid is sucked from the outside through the membranes into the center chamber. 5. The process of claim 2 wherein the washing fluid is water. 6. A process according to claim 1 wherein a vacuum is applied to the hollow fiber membranes to suck the washing fluid through the wall of the membranes. 7. A process according to claim 6 , wherein the hollow fiber membranes are guided over a roller comprising radial slots, the slots being smaller in width than the outer diameter of the hollow fiber membranes, the roller further comprising a center chamber having an access to the slots, wherein by applying vacuum to the center chamber and to the slots, the hollow fiber membrane is sucked into the slots, and wherein by simultaneously pouring a washing fluid over the hollow fibers, the washing fluid is sucked from the outside through the membranes into the center chamber. 8. The process of claim 7 wherein the washing fluid is water. 9. The process of claim 7 wherein the slots comprise at their narrowest point a depth and a width in the range of 0.2 mm to 1 mm. 10. The process of claim 7 wherein the slots comprise at their narrowest point a depth and a width in the range of 0.3 mm to 0.5 mm. 11. The process of claim 6 wherein the vacuum applied corresponds to a pressure in the range of from 0.2 to 1 bar. 12. The process of a claim 11 , wherein the vacuum applied corresponds to a pressure in the range of from 0.4 to 0.8 bar. 13. The process of claim 6 wherein the washing fluid is water. 14. The process of claim 1 wherein the washing fluid is water. 15. The process of claim 14 wherein the water is present at a temperature in the range of 15° C. to 100° C. 16. The process of claim 14 wherein the water is present at a temperature in the range of 40° C. to 90° C. 17. The process of claim 1 wherein the hollow fiber membranes comprise one or more of polysulfone, polyethersulfone, and polyvinylpyrrolidone. 18. The process of claim 1 wherein the washing fluid is present at a temperature in the range of 15° C. to 100° C. 19. The process of claim 1 wherein the washing fluid is present at a temperature in the range of 40° C. to 90° C.
Details of membrane preparation apparatus · CPC title
By suction · CPC title
Ultrasonic treatment · CPC title
Pulsated flow · CPC title
Physical treatment with compounds, e.g. swelling, coating or impregnation · CPC title
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