Multilayer coatings and methods of making and using thereof
US-2017056834-A1 · Mar 2, 2017 · US
US10525419B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10525419-B2 |
| Application number | US-201715794034-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 26, 2017 |
| Priority date | Oct 26, 2017 |
| Publication date | Jan 7, 2020 |
| Grant date | Jan 7, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
An oil-water separation membrane is described. The oil-water separation membrane comprises a porous metal sheet with a photocatalyst layer on one side and a layer of nanoparticles and a surfactant on the other side. The layer of nanoparticles and surfactant create a superoleophobic and superhydrophilic coating that allows passage of an aqueous phase and rejection of an oil phase. The photocatalyst layer, combined with UV irradiation, enables degradation of organic contaminants in the aqueous phase. The oil-water separation membrane may be used as part of an oil-water separation system, and a filtered water product may be recycled through the membrane to increase the removal of organic contaminants.
Opening claim text (preview).
The invention claimed is: 1. An oil-water separation membrane, comprising: a porous metal sheet with a first side and a second side, a feed side coating deposited on the first side of the porous metal sheet, the feed side coating comprising: a first layer in direct contact with the first side of the porous metal sheet, wherein the first layer comprises nanoparticles and an adhesive, and a surfactant deposited on the first layer, and a permeate side coating deposited on the second side of the porous metal sheet, the permeate side coating comprising a layer of photocatalyst nanoparticles. 2. The oil-water separation membrane of claim 1 , wherein the porous metal sheet has a thickness of 40-100 μm and a pore size of 0.5-4 μm. 3. The oil-water separation membrane of claim 1 , wherein the porous metal sheet comprises steel. 4. The oil-water separation membrane of claim 1 , wherein the nanoparticles are silica nanoparticles with a diameter of 5-100 nm. 5. The oil-water separation membrane of claim 1 , wherein the adhesive comprises a cyanoacrylate in reacted form. 6. The oil-water separation membrane of claim 1 , wherein the surfactant is an amphoteric fluorosurfactant. 7. The oil-water separation membrane of claim 1 , wherein the photocatalyst nanoparticles have a diameter of 25-100 nm. 8. The oil-water separation membrane of claim 1 , wherein the photocatalyst nanoparticles comprise at least one metal oxide selected from the group consisting of TiO 2 , WO 3 , ZnO, NiO, CuO, SnO 2 , CeO 2 , SiO 2 , ZrO 2 , Al 2 O 3 , and Fe 2 O 3 . 9. The oil-water separation membrane of claim 1 , which is both hydrophilic with a water contact angle in air of 0°-5°, and oleophobic with an oil contact angle in air of 145°-165°. 10. The oil-water separation membrane of claim 1 , wherein the feed side coating has a thickness of 10-50 μm, and wherein the permeate side coating has a thickness of 200 nm-5 μm. 11. The oil-water separation membrane of claim 1 , wherein the feed side coating, the permeate side coating, or both further comprise activated carbon or a zeolite. 12. An oil-water separation system, comprising: a vessel with an internal cavity; the oil-water separation membrane of claim 1 , which divides the internal cavity into a feed zone and a permeate zone; and a UV light source configured to irradiate a UV light to the permeate side coating of the oil-water separation membrane, wherein the feed zone has a feed inlet to deliver an oil-water mixture to the feed zone, and wherein the permeate zone has a water outlet to reject water from the permeate zone. 13. The oil-water separation system of claim 12 , wherein the separation membrane is tilted at an angle of 15°-30° above a horizontal plane. 14. A method of producing a purified water product from a contaminated water mixture comprising an oil phase and an aqueous phase having an organic aqueous pollutant with the oil-water separation system of claim 12 , the method comprising: contacting the contaminated water mixture with the feed side coating of the oil-water separation membrane, wherein the aqueous phase permeates through to the permeate side coating, leaving a retained oil phase in the feed zone; and irradiating the permeate side coating with UV light to photo-catalytically degrade a portion of the organic aqueous pollutant present in the aqueous phase that permeates through the oil-water separation membrane to produce a purified water product. 15. The method of claim 14 , wherein the UV light has an intensity of 450-1550 mW/cm 2 . 16. The method of claim 15 , wherein a pressure difference across the membrane is 0-5 kPa. 17. The method of claim 16 , wherein the pressure difference is 0-1 kPa, and wherein the aqueous phase permeates through the membrane at a flow speed of 0.5-5.0 mm/s. 18. The method of claim 14 , further comprising: draining the retained oil phase from the feed zone; and reapplying the purified water product to the feed side coating. 19. The method of claim 18 , wherein the reapplying is done at least 9 times to produce a purified water product having at least a 99% reduction in a concentration of the organic contaminant compared to a concentration of the organic contaminant in the aqueous phase before the contacting. 20. The method of claim 18 , wherein the reapplying is done at least 9 times and wherein at least 99 wt % of the oil phase relative to a total weight of the oil phase in the contaminated water mixture is retained as the retained oil phase.
Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion (devices for separating or removing fatty or oily substances or similar floating material from water, waste water, or sewage C02F1/40; cleaning or keeping clear the surface of open water from oil or like materials E02B15/04; arrangements for separating lubricants from refrigerants F25B43/02) · CPC title
Irradiation devices or lamp constructions · CPC title
Organic/inorganic mixed matrix membranes · CPC title
Characteristic thickness · CPC title
Silicium oxide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.