Desalination brine concentration system and method
A system and method for producing very high concentration brine streams from which commercially efficiently obtained minerals may be obtained is produced by a dual membrane brine concentrator system (DTRI Concentrator). The system includes a nano-filtration system which removes divalent ions from the seawater, a brine concentrator such as a hollow fine fiber forward osmosis system which receives and further concentrates the brine rejected from the nano-filtration system, a SWRO system which receives the NF system permeate and removes monovalent ions, and another brine concentrator which further concentrates the brine rejected from SWRO system. Various permeate and reject brine flow may be forwarded through the Dual Membrane Brine Concentrator system, and multiple stages of the system components may be used, to enhance brine concentration and improve system efficiency.
1. A brine concentration system, comprising:
a divalent ion concentration unit;
a first reverse osmosis membrane unit;
a second reverse osmosis membrane unit;
a first brine concentrator; and
a second brine concentrator,
wherein, the divalent ion concentration unit is configured to receive a saline source stream at a retentate side of the divalent ion concentration unit, and output a retentate side stream and a permeate side stream,
the first reverse osmosis membrane unit is configured to receive at least a portion of the divalent ion concentration unit permeate side stream at a retentate side, and output a retentate side stream and a permeate side stream,
the second reverse osmosis membrane unit is configured to receive at least a portion of the first reverse osmosis unit retentate side stream at a retentate side, and output a retentate side stream and a permeate side stream,
the first brine concentrator is configured to receive at least a portion of the second reverse osmosis membrane unit retentate side stream at a retentate side, and output a retentate side stream and a permeate side stream,
the second brine concentrator is configured to receive the at least a portion of first brine concentrator retentate side stream at a retentate side, and output a retentate side stream and a permeate side stream, and
the first reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the first brine concentrator and/or at least a portion of the permeate from the second brine concentrator, and the second reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the first brine concentrator and/or at least a portion of the permeate from the second brine concentrator.
2. The brine concentration system of claim 1 , wherein the divalent ion concentration unit is a nanofiltration unit, a hollow-fine fiber forward osmosis (HFF-FO) unit, or a brackish water reverse osmosis (BWRO) unit.
3. The brine concentration system of claim 1 , further comprising a third brine concentrator system operably linked to the divalent ion concentration unit retentate side stream.
4. The brine concentration system of claim 3 , wherein the third brine concentrator system comprises at least one nano-filtration unit, a first nano-filtration unit, wherein the first nano-filtration unit is configured to receive at least a portion of the retentate side stream of the divalent ion concentration unit, and configured to deliver at least a portion of a permeate to the first reverse osmosis membrane unit.
5. The brine concentration system of claim 4 , further comprising at least a second nano-filtration unit configured to receive at least a portion of a retentate of the first nano-filtration unit, and configured to deliver at least a portion of a permeate to the first reverse osmosis membrane unit.
6. The brine concentration system of claim 1 , wherein the second reverse osmosis membrane unit has a bursting pressure of up to 120 Bars.
7. The brine concentration system of claim 1 , wherein the first brine concentrator comprises a reverse osmosis membrane.
8. The brine concentration system of claim 1 , wherein the second brine concentrator comprises a reverse osmosis membrane.
9. The brine concentration system of claim 1 , wherein the first reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the first brine concentrator without the portion of the permeate side stream from the first brine concentrator contacting another reverse osmosis membrane and/or brine concentrator membrane between the first reverse osmosis membrane and the first brine concentrator.
10. The brine concentration system of claim 1 , wherein the second reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the second brine concentrator without the portion of the permeate side stream from the second brine concentrator contacting another reverse osmosis membrane and/or brine concentrator membrane between the second reverse osmosis membrane and the second brine concentrator.
11. The brine concentration system of claim 1 , wherein the system is configured to produce the retentate from the second brine concentrator comprising a mineral concentration of 120,000 to 250,000 parts per million (ppm).
12. The brine concentration system of claim 1 , further comprising a crystallizer configured to receive at least a portion of a retentate stream from the second brine concentrator.
13. The brine concentration system of claim 12 , wherein the crystallizer is configured to crystalize sodium chloride.
14. The brine concentration system of claim 1 , further comprising one or more energy recovery devices operably connected to the divalent ion concentration unit retentate stream, first brine concentrator retentate stream, and/or second brine concentrator retentate stream.
15. The brine concentration system of claim 1 , wherein a recovery of the brine concentration system is at least 60%.
16. A brine concentration system, comprising:
a divalent ion concentration unit;
a first reverse osmosis membrane unit;
a second reverse osmosis membrane unit;
a first brine concentrator; and
a second brine concentrator,
wherein, the divalent ion concentration unit is configured to receive a saline source stream at a retentate side of the divalent ion concentration unit, and output a retentate side stream and a permeate side stream,
the first reverse osmosis membrane unit is configured to receive at least a portion of the divalent ion concentration unit permeate side stream at a retentate side, and output a retentate side stream and a permeate side stream,
the second reverse osmosis membrane unit is configured to receive at least a portion of the first reverse osmosis unit retentate side stream at a retentate side, and output a retentate side stream and a permeate side stream,
the first brine concentrator is configured to receive a first portion of the second reverse osmosis membrane unit retentate side stream at a retentate side, and a second portion of the second reverse osmosis membrane unit retentate side stream at a permeate side, and output a retentate side stream and a permeate side stream,
the second brine concentrator is configured to receive a first portion of the first brine concentrator retentate side stream at a retentate side, and a second portion of the first brine concentrator retentate side stream at a permeate side, and output a retentate side stream and a permeate side stream, and
the first reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the first brine concentrator and/or at least a portion of the permeate from the second brine concentrator, and the second reverse osmosis membrane unit is configured to receive, at a retentate side only, at least a portion of the permeate side stream from the first brine concentrator and/or at least a portion of the permeate from the second brine concentrator.