Method for separation of magnesium and calcium ions from saline water, for improving the quality of soft and desalinated waters

Patent metadata

Field	Value
Publication number	US-11279643-B2
Application number	US-201716089014-A
Country	US
Kind code	B2
Filing date	Mar 30, 2017
Priority date	Mar 31, 2016
Publication date	Mar 22, 2022
Grant date	Mar 22, 2022

Abstract

Provided is a novel Nanofiltration-DiaNanofiltration (NF-DiaNF) system and method for extracting divalent ions from saline water (e.g., seawater) to produce solutions rich in divalent ions (in particular Mg2+, Ca2+ and SO42−), while minimizing the concentrations of undesirable species (e.g., Cl−, Br−, B and Na+). The solutions may be added to water (e.g., desalinated, soft, drinking or irrigation water) to enrich the water with divalent ions, thereby improving its quality.

First claim

What is claimed is:

1. A process for treating saline water to obtain product water comprising a higher concentration of divalent ions selected from Mg 2+ , Ca 2+ and SO 4 2− as compared with said saline water, the process comprising the steps of:
a. passing a sample of saline water through a first nanofiltration (NF) membrane to obtain an NF permeate and an NF retentate (NF brine);
b. performing a first diaNanofiltration (DiaNF) cycle comprising: passing the NF brine obtained in step (a) through a second NF membrane in the presence of a diluting solution to obtain a DiaNF permeate and a DiaNF retentate (DiaNF brine), wherein the volume of the diluting solution is equal to the NF brine obtained from step (a) and is added at a flow rate substantially equal to that of the DiaNF permeate; and
c. isolating the DiaNF brine from step (b) as product water having a higher concentration of said divalent ions, and a lower concentration of species selected from Na + , Br − , Cl − and B as compared with said saline water,
wherein the process further comprises the step of lowering the Mg 2+ +Ca 2+ :SO 4 2− concentration ratio in the product water as compared with the saline water.

2. The process according to claim 1 , further comprising the step of passing the product water through at least one ultrafiltration (UF) membrane.

3. The process according to claim 1 , further comprising the step of de-carbonating the saline water prior to the NF of step (a).

4. The process according to claim 1 , wherein:
a. the saline water is selected from the group consisting of sea water, brackish water and seawater reverse osmosis (SWRO) brine; or
b. wherein the diluting solution is selected from the group consisting of low total dissolved solids (TDS) water, soft water, distilled water, tap water, NF permeate, SWRO permeate, and brine obtained after multiple SWRO stages.

5. The process according to claim 1 , wherein the recovery ratio (RR) of the NF in step (a) is between 40 and 85%.

6. The process according to claim 1 , wherein an anti-scalant is added to the saline water.

7. The process according to claim 1 , comprising between 1 and 6 DiaNF cycles, wherein the permeate of the last DiaNF cycle(s) for a given batch of saline water is recycled and used as the diluting solution of the first DiaNF cycle(s) of the next batch of saline water.

8. The process according to claim 1 , comprising between 1 and 6 DiaNF cycles, wherein
a. the diluting solution of the last DiaNF cycle(s) is seawater reverse osmosis (SWRO) permeate, distilled water or fresh water; or
b. the diluting solution of the first DiaNF cycle(s) is brine obtained after multiple SWRO stages.

9. The process according to claim 1 , wherein the first nanofiltration (NF) membrane and the second NF membrane are the same or different.

10. The process according to claim 1 , wherein the first and/or second NF membranes preferentially reject Ca 2+ and/or Mg 2+ ions over Na + , Br − , Cl − and B species.

11. The process according to claim 1 , wherein the permeates from the NF of step (a) and one or more DiaNF cycles are combined and recycled back to a desalination plant.

12. The process according to claim 1 , further comprising the step of performing at least one additional NF step prior to the DiaNF in step (b).

13. The process according to claim 1 , wherein the Mg 2+ +Ca 2+ :SO 4 2− concentration ratio is lowered by:
a. reducing the Mg 2+ and Ca 2+ concentrations in the product water by performing a cation exchange step on the saline water prior to the NF in step (a), between two NF cycles in step (a), or between the NF of step (a) and the first DiaNF cycle; or
b. increasing the SO 4 2− concentration in the product water; wherein the SO 4 2− concentration is increased by:
i. employing a membrane which preferentially rejects SO 4 2− over Mg 2+ and Ca 2+ , prior to NF of step (a), or as part of the NF in step (a);
ii. adding a SO 4 2− source to a feed of the DiaNF of step (b); or
iii. performing an anion exchange step.

14. The process according to claim 1 , wherein the Mg 2+ +Ca 2+ :SO 4 2− ratio in the saline water is about 2:1, and is lowered to between about 1.25:1 and about 1:1 in the product water.

15. The process according to claim 1 , which results in the reduction or elimination of Cl − ions in the product water.

16. The process according to claim 1 , wherein:
a. the Cl − to Mg 2+ concentration ratio is at least about 10:1 (w/w) in the saline water, and lower than about 5:1 (w/w) in the product water; or
b. the Na + to Mg 2+ concentration ratio is at least about 5:1 (w/w) in the saline water, and about 1:1 (w/w) or lower in the product water.

17. The process according to claim 1 , wherein the NF of step (a) is preceded by one or more DiaNF dilution cycles.

18. The process according to claim 1 , further comprising the step of adding the thus obtained product water to a water sample so as to supplement said water sample with Mg 2+ , Ca 2+ , and/or SO 4 2− .

19. A process for treating saline water to obtain product water comprising a higher concentration of divalent ions selected from Mg 2+ , Ca 2+ and SO 4 2− as compared with said saline water, the process comprising the steps of:
a. passing a sample of saline water through a first nanofiltration (NF) membrane to obtain an NF permeate and an NF retentate (NF brine);
b. performing a first diaNanofiltration (DiaNF) cycle comprising: passing the NF brine obtained in step (a) through a second NF membrane in the presence of a diluting solution to obtain a DiaNF permeate and a DiaNF retentate (DiaNF brine), wherein the volume of the diluting solution is equal to the NF brine obtained from step (a) and is added at a flow rate substantially equal to that of the DiaNF permeate;
c. subjecting the DiaNF brine obtained in step (b) to one or more additional DiaNF cycles in the presence of a diluting solution; and
d. isolating the DiaNF brine from step (c) as product water having a higher concentration of said divalent ions, and a lower concentration of species selected from Na + , Br − , Cl − and B as compared with said saline water,
wherein the process further comprises the step of lowering the Mg 2+ +Ca 2+ :SO 4 2− concentration ratio in the product water as compared with the saline water.

Assignees

• Technion Res & Dev Foundation

Inventors

• Lahav Ori
• Birnhack Liat
• Nativ Paz
• Nir Oded

Classifications

• B01D61/0271

  comprising multiple nanofiltration steps · CPC title

• B01D2311/2523

  to feed side · CPC title

• B01D2311/2623

  Ion-Exchange · CPC title

• B01D2311/06

  Specific process operations in the permeate stream · CPC title

• C02F2103/08

  Seawater, e.g. for desalination · CPC title