Cross-linked polyzwitterion/anion for the removal of strontium from aqueous solutions
US-8937104-B2 · Jan 20, 2015 · US
US9480979B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-9480979-B1 |
| Application number | US-201514918722-A |
| Country | US |
| Kind code | B1 |
| Filing date | Oct 21, 2015 |
| Priority date | Oct 21, 2015 |
| Publication date | Nov 1, 2016 |
| Grant date | Nov 1, 2016 |
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Cross-linked cyclocopolymers made up of one or more quaternary ammonium salts and sulfur dioxide as monomers. One of the quaternary ammonium salts is also an aspartic acid derivative. The cross-linked copolymers include a repeating unit with multiple chelating centers that different metal ions can bind to. The cross-linked copolymers are zwitterionic or anionic, and can be in either an acidic form or a basic form. A method for removing metal ions from an aqueous sample with these cross-linked copolymers is also described.
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The invention claimed is: 1. A copolymer, comprising: an aspartic acid derivative; a quaternary ammonium salt; and sulfur dioxide; wherein: the aspartic acid derivative, the quaternary ammonium salt and the sulfur dioxide are cyclopolymerized to form the copolymer; and in the copolymer, a sulfur dioxide molecule connects every two molecules of the aspartic acid derivative, the quaternary ammonium salt, or both. 2. The copolymer of claim 1 , wherein the quaternary ammonium salt cross-links one polymer chain of the copolymer to another polymer chain of the copolymer. 3. The copolymer of claim 1 , wherein the aspartic acid derivative comprises a quaternary nitrogen atom. 4. The copolymer of claim 3 , wherein the aspartic acid derivative is represented by Formula A: wherein: R 1 is a hydrogen, a halide or an optionally substituted C 1 -C 6 alkyl group; X − is F − , Cl − , Br − , I − , NO 3 − or other suitable monoanion other than OH − . 5. The copolymer of claim 4 , wherein R 1 is a hydrogen and X − is Cl − . 6. The copolymer of claim 1 , wherein the quaternary ammonium salt is represented by Formula B: wherein: R 2 -R 5 are each independently a hydrogen, a halide or an optionally substituted C 1 -C 6 alkyl group; and Y − and Z − are each F − , Cl − , Br − , I − , NO 3 − or other suitable monoanion other than OH. 7. The copolymer of claim 1 , wherein R 2 -R 5 are each a hydrogen and Y − and Z − are each Cl − . 8. The copolymer of claim 1 , being in a basic and anionic form. 9. The copolymer of claim 1 , having a repeating unit represented by Formula 1 or Formula 2: wherein: R 1 -R 5 are each independently a hydrogen, a halide, an optionally substituted methyl group, or an optionally substituted ethyl group; in Formula 1, each W − is F − , Cl − , Br − , I − , NO 3 − or other suitable monoanion other than OH − ; in Formula 2, each M + is Li + , Na + , K + or other suitable monocation other than H + ; and n=9-19. 10. The copolymer of claim 9 , having the repeating unit represented by Formula 1, wherein: R 1 -R 5 are each a hydrogen; and W − is Cl − . 11. The copolymer of claim 9 , having the repeating unit represented by Formula 2, wherein: R 1 -R 5 are each a hydrogen; and M + is Na + . 12. The copolymer of claim 1 , having a Pb 2+ adsorption capacity of 50-100 mg g −1 based on a total weight of the copolymer. 13. A method for making the copolymer of claim 1 , comprising: cyclopolymerizing the aspartic acid derivative, the quaternary ammonium salt and the sulfur dioxide in the presence of an initiator and a non-aqueous solvent to form a cross-linked polyzwitterionic acid polymer; and optionally treating the polyzwitterionic acid polymer with a base to form a cross-linked anionic polyelectrolyte polymer. 14. The method of claim 13 , wherein the initiator is azoisobutyronitrile and the non-aqueous solvent is dimethylsulfoxide. 15. A method for removing Pb 2+ from an aqueous sample, comprising: contacting the aqueous sample with the copolymer of claim 1 to adsorb Pb 2+ from the aqueous sample onto the copolymer. 16. The method of claim 15 , wherein the copolymer has a concentration of 0.02-5.0 g L −1 in the aqueous sample. 17. The method of claim 15 , wherein the contacting is carried out at a temperature of 10-100° C. 18. The method of claim 15 , wherein the contacting is carried out at an aqueous sample pH range of 3 to 9. 19. The method of claim 15 , wherein the contacting is carried out for 5-180 min. 20. The method of claim 15 , wherein the contacting removes more than 90% of the Pb 2+ present in the aqueous sample.
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