Desalination systems and associated methods
Systems and methods related to the desalination of aqueous solutions containing one or more dissolved salts are generally described.
1. A method for desalinating water, comprising:
removing, within an ion-removal apparatus, at least a portion of at least one scale-forming ion from an aqueous feed stream, the aqueous feed stream comprising the at least one scale-forming ion and at least one dissolved monovalent salt comprising a monovalent cation and a monovalent anion to produce an ion-diminished stream containing less of the scale-forming ion relative to the aqueous feed stream;
removing, within a desalination apparatus, water from the ion-diminished stream to produce a concentrated saline stream enriched in the dissolved monovalent salt relative to the ion-diminished stream, wherein the removing comprises contacting a gaseous stream with the ion-diminished stream within a humidifier to evaporate water from the ion-diminished stream into the gaseous stream; and
precipitating, within a precipitation apparatus, 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
recycling at least a portion of the product stream to the desalination apparatus;
wherein:
the precipitating comprises forming crystals comprising at least a portion of the dissolved monovalent salt, and/or
the precipitating comprises adjusting the temperature of the concentrated saline stream.
2. The method of claim 1 , wherein a concentration of the dissolved monovalent salt within the concentrated saline stream differs from a concentration of the dissolved monovalent salt within the ion-diminished stream by no more than about 20%.
3. The method of claim 1 , wherein the ion-removal apparatus comprises an ion-removal medium contained within a vessel, and the ion-removal medium comprises a composition configured to induce precipitation of the at least one scale-forming ion.
4. The method of claim 1 , wherein the at least one scale-forming ion comprises Mg 2+ , Ca 2+ , Sr 2+ , and/or Ba 2+ .
5. The method of claim 1 , comprising transporting the gaseous stream to a dehumidifier and condensing at least a portion of the water within the gaseous stream.
6. The method of claim 1 , wherein the precipitating comprises reducing the flow velocity of the concentrated saline stream.
7. The method of claim 6 , wherein the reducing the flow velocity of the concentrated saline stream comprises substantially stopping the flow of the concentrated saline stream.
8. The method of claim 1 , wherein the precipitating comprises adjusting the temperature of the concentrated saline stream.
9. The method of claim 1 , wherein the bulk concentration of at least one of the dissolved monovalent salts within the concentrated saline stream exiting the desalination apparatus can be increased by at least about 1% without reaching a saturation limit.
10. The method of claim 1 , wherein, during operation, at least about 1 wt % of the concentrated saline stream that enters the precipitation apparatus is precipitated as a solid salt in the precipitation apparatus.
11. The method of claim 1 , wherein there are substantially no regions within the desalination apparatus in which the ion-diminished stream is quiescent.
12. The method of claim 1 , comprising removing at least one of the ion-removal apparatus, the desalination apparatus, and/or the precipitation apparatus while performing the method.
13. The method of claim 1 , wherein the precipitating comprises forming crystals comprising at least a portion of the dissolved monovalent salt.
14. The method of claim 1 , wherein the precipitating comprises precipitating, within the precipitation apparatus, sodium chloride.
15. The method of claim 1 , wherein the recycling comprises recycling at least the portion of the product stream from the precipitation apparatus to the desalination apparatus via a direct fluidic connection between the precipitation apparatus and the desalination apparatus.
16. A method for desalinating water, comprising:
removing, within a desalination apparatus, water from an aqueous feed stream, the aqueous feed stream comprising at least one dissolved monovalent salt comprising a monovalent cation and a monovalent anion to produce a concentrated saline stream enriched in the dissolved monovalent salt relative to the aqueous feed stream;
precipitating, within a precipitation apparatus, 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
recycling at least a portion of the product stream to the desalination apparatus;
wherein substantially no precipitation of the dissolved monovalent salt occurs within the desalination apparatus; and
wherein:
the precipitating comprises forming crystals comprising at least a portion of the dissolved monovalent salt, and/or
the precipitating comprises adjusting the temperature of the concentrated saline stream.
17. The method of claim 16 , wherein the removing comprises contacting a gaseous stream with the aqueous feed stream within a humidifier to evaporate water from the aqueous feed stream into the gaseous stream.
18. The method of claim 16 , wherein the precipitating comprises forming crystals comprising at least a portion of the dissolved monovalent salt.
19. The method of claim 16 , wherein the precipitating comprises adjusting the temperature of the concentrated saline stream.
20. The method of claim 16 , wherein the precipitating comprises precipitating, within the precipitation apparatus, sodium chloride.
21. The method of claim 16 , wherein the recycling comprises recycling at least the portion of the product stream from the precipitation apparatus to the desalination apparatus via a direct fluidic connection between the precipitation apparatus and the desalination apparatus.
22. A water desalination system, comprising:
an ion-removal apparatus configured to receive an aqueous feed stream, the aqueous feed stream comprising at least one scale-forming ion and at least one dissolved monovalent salt, and to remove at least a portion of the at least one scale-forming ion to produce an ion-diminished stream containing less of the scale-forming ion relative to the feed stream;
a desalination apparatus fluidically connected to the ion-removal apparatus and configured to remove water from the ion-diminished stream to produce a concentrated saline stream enriched in the dissolved monovalent salt relative to the ion-diminished stream;
a precipitation apparatus fluidically connected to the desalination apparatus and configured 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, wherein the precipitation apparatus comprises a crystallizer; and
a recycle stream directly fluidically connecting the precipitation apparatus to the desalination apparatus and configured to recycle at least a portion of the product stream from the precipitation apparatus to the desalination apparatus.
23. The system of claim 22 , wherein the desalination apparatus comprises:
a humidifier configured to evaporate water from the ion-diminished stream to produce a vapor-containing gaseous stream and the concentrated stream, and
a dehumidifier fluidically connected to the humidifier and configured to condense at least a portion of the water from the gaseous stream,
wherein the dehumidifier comprises a bubble column condenser.