Treatment of saline water for agricultural and potable use and for generation of disinfectant solution
US-2019263697-A1 · Aug 29, 2019 · US
US12227441B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12227441-B2 |
| Application number | US-202117301617-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 9, 2021 |
| Priority date | Apr 9, 2020 |
| Publication date | Feb 18, 2025 |
| Grant date | Feb 18, 2025 |
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A novel process for treatment of low quality or brackish water that allows increased recovery of high quality water, recovers commodity minerals and reduces the volume of water and mass of solids that are disposed from the process.
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What is claimed is: 1. A process for treating brackish or saline water comprising, performing, in sequence, the unit operations of low pH degasification; high pH precipitation; ion exchange, nanofiltration, and desalination to produce high quality desalinated water; wherein commodity materials are selectively obtained from at least one of the high pH precipitation, ion exchange, and nanofiltration unit operations; wherein the commodity material comprises sodium chloride salt brine and using the sodium chloride salt brine to regenerate an ion exchange column in the ion exchange unit operation; and low pH de gasification occurs at a pH of less than 5; high pH precipitation occurs at a pH greater than 10.5; and high quality desalinated water is water with total dissolved solids (TDS) concentration of less than 500 mg/L. 2. The process of claim 1 wherein the brackish or saline water has a total dissolved solids (TDS) concentration of between 1,000 mg/L to 20,000. 3. The process of claim 1 wherein the brackish or saline water is flue gas desulfurization (FGD) wastewater. 4. The process of claim 1 wherein the commodity materials comprise magnesium hydroxide obtained from a selective precipitation unit operation at high pH. 5. The process of claim 1 wherein byproducts from the ion exchange and nanofiltration unit operations are combined and precipitated to obtain a commodifiable product. 6. The process of claim 1 wherein the brackish or saline water comprises concentrations of suspended solids, one or more multivalent ions or dissolved silica that cause scale formation on surf aces of thermal or membrane desalination equipment. 7. The process of claim 6 wherein the multivalent ions are selected from the group consisting of calcium, magnesium, iron, aluminum, bicarbonate/carbonate, sulfate, and dissolved silica. 8. The process of claim 5 wherein the commodifiable product is gypsum. 9. The process of claim 1 wherein the step of low pH degasification comprises lowering the pH of the water to less than pH 6. 10. The process of claim 1 wherein the step of low pH degasification comprises removing dissolved carbon dioxide from the low pH solution by air stripping. 11. The process of claim 1 wherein the pH of the feed water solution after degasification is raised to greater than pH 10.5 by addition of a strong base to achieve selective removal of high purity commodifiable magnesium hydroxide. 12. The process of claim 11 wherein selective removal of high purity commodifiable magnesium hydroxide comprises removing suspended solids from solution. 13. The process of claim 12 wherein the pH of the water is adjusted to approximately pH 7.0 after high pH selective magnesium hydroxide precipitation during or prior to the ion exchange unit operation. 14. The process of claim 1 wherein the desalination step produces a concentrate stream containing sodium chloride salt as a concentrate that is at greater than 1% concentration. 15. The process of claim 1 wherein magnesium is selectively obtained via high pH precipitation of magnesium hydroxide, calcium is selectively removed by cation exchange and sulfate is selectively removed by nanofiltration.
by ion-exchange (ion-exchange in general B01J) · CPC title
Sulfur compounds · CPC title
Halogens or halogen-containing compounds · CPC title
Regeneration of sorbents, filters · CPC title
Seawater, e.g. for desalination · CPC title
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