Water treatment method and water treatment apparatus
US-2024383788-A1 · Nov 21, 2024 · US
US10005688B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10005688-B2 |
| Application number | US-201214232955-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 16, 2012 |
| Priority date | Aug 26, 2011 |
| Publication date | Jun 26, 2018 |
| Grant date | Jun 26, 2018 |
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This desalinization system, which obtains industrial-use water and drinking water from seawater and wastewater, is provided with: a purification device that purifies wastewater by removing activated sludge therefrom; a first RO membrane that removes salt from the output of the purification device by transferring said salt to first concentrated water, thereby producing industrial-use water; a UF membrane that seawater passes through and that removes particulates from said seawater; a second RO membrane that removes salt from the treated output of the UF membrane by transferring said salt to second concentrated water, producing drinking water; an agitation device to which the second concentrated water from the second RO membrane and the first concentrated water from the first RO membrane are sent to be agitated; and a third RO membrane removing salt from the liquid mixture agitated by the agitation device by transferring said salt to third concentrated water, producing industrial-use water.
Opening claim text (preview).
The invention claimed is: 1. A sea-water desalination system for acquiring industrial water and drinking water from sea-water and sewage water, comprising: a purification apparatus for purifying sewage water; a first RO membrane for generating industrial water and a first concentrated-water from the sewage water that has been purified by the purification apparatus; a UF membrane for removing particles in sea-water by permeating the sea-water; a second RO membrane for generating a second concentrated-water and drinking water from permeated water that has been filtered by the UF membrane; a stirring apparatus for stirring the second concentrated-water generated by the second RO membrane and the first concentrated-water generated by the first RO membrane being sent thereto; and a third RO membrane for generating a third concentrated-water and the industrial water from mixture fluid stirred by the stirring apparatus. 2. A sea-water desalination system according to claim 1 , comprising at least either of a first energy recovery device for recovering pressure energy of the second concentrated-water or a second energy recovery device for recovering pressure energy of the third concentrated-water. 3. A sea-water desalination system according to claim 1 , wherein the first RO membrane is configured to operate at a permeation pressure of approximately 1 to 2 MPa; the second RO membrane is configured to operate at a permeation pressure of approximately 6 to 8 MPa; and the third RO membrane is configured to operate at a permeation pressure of approximately 6 to 8 MPa.
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