Production of injection water by coupling direct-osmosis methods with other methods of filtration
US-2016040522-A1 · Feb 11, 2016 · US
US9969638B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9969638-B2 |
| Application number | US-201414452387-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 5, 2014 |
| Priority date | Aug 5, 2013 |
| Publication date | May 15, 2018 |
| Grant date | May 15, 2018 |
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Water treatment systems and associated methods are generally described. Certain of the water treatment systems and methods described herein can be used to pre-treat an aqueous stream that is subsequently transported to a desalination apparatus and/or post-treat an aqueous stream that has been produced by a desalination apparatus.
Opening claim text (preview).
What is claimed is: 1. A water treatment system, comprising: an ion-removal apparatus configured to remove at least a portion of at least one scale-forming ion from an input stream received by the ion-removal apparatus to produce an ion-diminished stream containing less of the scale-forming ion relative to the input stream received by the ion-removal apparatus; a humidification-dehumidification desalination apparatus fluidically connected to the ion-removal apparatus and configured to remove water from an aqueous stream received by the desalination apparatus to produce a concentrated saline stream enriched in a dissolved monovalent salt relative to the aqueous stream received by the desalination apparatus; a precipitation apparatus fluidically connected to the humidification-dehumidification desalination apparatus, the precipitation apparatus configured to receive at least a portion of the concentrated saline stream output by the humidification-dehumidification desalination apparatus and to precipitate at least a portion of the dissolved monovalent salt from the concentrated saline stream to produce a product stream containing less of the dissolved monovalent salt relative to the concentrated saline stream and to produce precipitated monovalent salt comprising retained water from the concentrated saline stream; and a solids-handling apparatus fluidically connected to the precipitation apparatus, the solids-handling apparatus configured to remove at least a portion of the water retained by precipitated monovalent salt from the precipitation apparatus. 2. The system of claim 1 , wherein the ion-removal apparatus comprises a chemical ion-removal apparatus. 3. The system of claim 1 , wherein wherein the ion-removal apparatus comprises an electrocoagulation apparatus. 4. The system of claim 1 , wherein the ion-removal apparatus comprises a resin bed. 5. They system of claim 1 , wherein the humidification-dehumidification desalination apparatus is operated at a pressure below 1 atmostphere. 6. The system of claim 1 , wherein the humidification-dehumidification desalination apparatus comprises a dehumidifier comprising a bubble column condenser. 7. The system of claim 1 , wherein the humidification-dehumidification desalination apparatus comprises a bubble column humidifier. 8. The system of claim 1 , wherein the concentrated saline stream is present within an outlet of the humidification-dehumidification desalination apparatus, and the concentrated saline stream has a density of from about 9 pounds per gallon and about 11 pounds per gallon. 9. They system of claim 1 , wherein the precipitation apparatus comprises a low shear mixer. 10. The system of claim 1 , wherein the precipitation apparatus comprises a vessel comprising a volume within which the concentrated saline stream is substantially quiescent. 11. The system of claim 10 , wherein the substantially quiescent volume within the vessel occupies at least about 1% of the volume of the vessel. 12. The system of claim 10 , wherein the substantially quiescent volume within the vessel occupies at least about 10% of the volume of the vessel . 13. The system of claim 10 , wherein the vessel is a first vessel, and the precipitation apparatus further comprises a second vessel in which the solids precipitated in the first vessel are allowed to settle. 14. The system of claim 1 , wherein the solids-handling apparatus is configured to produce a cake comprising at least a portion of the precipitated monovalent salt from the precipitation apparatus. 15. The system of claim 1 , further comprising a transport device configured to transport precipitated monovalent salt away from the precipitation apparatus. 16. The system of claim 15 , wherein the transport device comprises a pump. 17. The system of claim 15 , wherein the transport device comprises a conveyor. 18. The system of claim 15 , wherein the transport device is configured to transport the precipitated monovalent salt from the precipitation apparatus to the solids-handling apparatus.
by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title
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
by centrifugal separation · CPC title
Feed pretreatment · CPC title
Prevention of membrane fouling or of concentration polarisation · CPC title
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