Brine mining process
US-2016272513-A1 · Sep 22, 2016 · US
US9919936B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9919936-B2 |
| Application number | US-201314081165-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 15, 2013 |
| Priority date | Nov 16, 2012 |
| Publication date | Mar 20, 2018 |
| Grant date | Mar 20, 2018 |
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A water recovery method for improving water recovery efficiency may include inflowing a low concentration solution including water into an in-series flow path. The in-series flow path may include a plurality of flow paths for a low concentration solution coupled in series. The method may additionally include inflowing a high concentration solution having the same concentration into a plurality of flow paths for a high concentration solution. Each of the plurality of flow paths for the high concentration solution may be connected to each of plurality of flow paths for the low concentration solution via a respective semipermeable membrane being interposed therebetween.
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What is claimed is: 1. A water recovery method comprising: inflowing a low concentration solution into an in-series flow path, the low concentration solution including water, the in-series flow path including a plurality of first flow paths coupled in series, and inflowing a high concentration solution into a plurality of second flow paths, the high concentration solution in each of the plurality of second flow paths having a same concentration of a draw solute, each of the plurality of second flow paths for the high concentration solution being connected to a segment of the in-series flow path for the low concentration solution with a respective semipermeable membrane that is interposed between the in-series flow path and each of the plurality of second flow paths such that a net flow of water passes through the respective semipermeable membrane of the semipermeable membranes from the low concentration solution to the high concentration solution via forward osmosis while the low concentration solution and the high concentration solution flow in opposite directions, the semipermeable membranes being configured such that each of an upstream semipermeable membrane is thicker than a downstream semipermeable membrane relative to an inlet of the in-series flow path, each of the plurality of second flow paths being in parallel and having a same inlet flow rate. 2. The water recovery method of claim 1 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes an outlet flow rate of the in-series flow path for the low concentration solution being higher than a sum of an inlet flow rate of each of the plurality of second flow paths for the high concentration solution. 3. The water recovery method of claim 1 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes an inlet flow rate of the in-series flow path for the low concentration solution being higher than a sum of an inlet flow rate of each of the plurality of second flow paths for the high concentration solution. 4. The water recovery method of claim 1 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes the plurality of second flow paths for the high concentration solution being narrower than the in-series flow path for the low concentration solution. 5. The water recovery method of claim 1 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes each of the semipermeable membranes being arranged such that a downstream semipermeable membrane has a higher permeability coefficient for the water than an upstream semipermeable membrane relative to an inlet of the in-series flow path. 6. The water recovery method of claim 1 , wherein the inflowing a low concentration solution includes the low concentration solution being sea water. 7. The water recovery method of claim 2 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes an inlet flow rate of the in-series flow path for the low concentration solution being higher than a sum of an inlet flow rate of each of the plurality of second flow paths for the high concentration solution. 8. The water recovery method of claim 2 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes the plurality of second flow paths for the high concentration solution being narrower than the in-series flow path for the low concentration solution. 9. The water recovery method of claim 3 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes the plurality of second flow paths for the high concentration solution being narrower than the in-series flow path for the low concentration solution. 10. The water recovery method of claim 2 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes each of the semipermeable membranes being arranged such that a downstream semipermeable membrane has a higher permeability coefficient for the water than an upstream semipermeable membrane relative to an inlet of the in-series flow path. 11. The water recovery method of claim 3 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes each of the semipermeable membranes being arranged such that a downstream semipermeable membrane has a higher permeability coefficient for the water than an upstream semipermeable membrane relative to an inlet of the in-series flow path. 12. The water recovery method of claim 4 , wherein the inflowing a low concentration solution and the inflowing a high concentration solution includes each of the semipermeable membranes being arranged such that a downstream semipermeable membrane has a higher permeability coefficient for the water than an upstream semipermeable membrane relative to an inlet of the in-series flow path. 13. The water recovery method of claim 2 , wherein the inflowing a low concentration solution includes the low concentration solution being sea water. 14. The water recovery method of claim 3 , wherein the inflowing a low concentration solution includes the low concentration solution being sea water. 15. The water recovery method of claim 4 , wherein the inflowing a low concentration solution includes the low concentration solution being sea water. 16. The water recovery method of claim 5 , wherein the inflowing a low concentration solution includes the low concentration solution being sea water. 17. The water recovery method of claim 1 , wherein the plurality of second flow paths for the high concentration solution have a same inlet flow rate.
Specific process operations in the concentrate stream · CPC title
Reject series · CPC title
Specific supply elements · CPC title
by forward osmosis · CPC title
Forward osmosis or direct osmosis · CPC title
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