Anion exchange membranes and process for making
View Patent ↗Embodiments of the present invention provide for anion exchange membranes and processes for their manufacture. The anion exchange membranes described herein are made the polymerization product of at least one functional monomer comprising a tertiary amine which is reacted with a quaternizing agent in the polymerization process.
1. An anion exchange membrane, comprising:
a microporous membrane support having a porous first side, a porous second side, and a continuous porous structure comprising pores having a size of about 0.05 microns to about 10 microns extending from said first side to said second side; and
a crosslinked ion transferring polymer filling said continuous porous structure, said polymer formed in the porous structure.
2. The anion exchange membrane of claim 1 , wherein the polymer comprises a polymerization product of at least one functional monomer comprising a tertiary amine, at least one crosslinking monomer, at least one quaternizing agent, and at least one polymerization initiator.
3. The anion exchange membrane of claim 2 , wherein the at least one functional monomer is selected from the group consisting of vinylimidazole and vinylcarbazole.
4. The anion exchange membrane of claim 2 , wherein the at least one crosslinking monomer is selected from the group consisting of: divinylbenzene, ethylene glycol dimethacrylate, vinylbenzyl chloride, dichloroethane, propylene glycol dimethacrylate, isobutylene glycol dimethacrylate, C 16 H 24 O 12 Si 8 , C 32 H 72 O 20 Si 16 , (CH 2 CH) n (SiO 1.5 ) n wherein n=8, 10, or 12, C 14 H 38 O 12 Si 7 , C 28 H 66 O 12 Si 7 , C 56 H 122 O 12 Si 7 , C 16 H 56 O 20 Si 16 , H 8 O 12 Si 8 , (C 8 H 13 O) n (SiO 1.5 ) n wherein n=8, 10, 12, (C 6 H 11 O 2 ) n (SiO 1.5 ) n wherein n=8, 10, or 12, (C 7 H 11 O 2 ) n (SiO 1.5 ) n wherein n=8, 10, or 12, and (C 6 H 9 O 2 ) n wherein n=8, 10, or 12.
5. The anion exchange membrane of claim 2 , wherein the at least one quaternizing agent is selected from the group consisting of benzyl chloride, benzyl bromide, vinyl benzyl chloride, dichloroethane, or methyl iodide.
6. The anion exchange membrane of claim 2 , wherein the at least one polymerization initiator is selected from the group consisting of organic peroxides, 2,2′ azobis[2,[2-imidazolin-2-yl]-propane] dihydrochloride, a,a′-azoisobutyronitrile, 2,2′-azobis[2-methylpropioaminidine]dihydrochloride, 2,2′ azobis[2, [2-imidazolin-2-yl]propane], or dimethyl2,2′azobis[2-methylpropionate.
7. The anion exchange membrane of claim 6 , wherein the organic peroxide is benzoyl peroxide.
8. The anion exchange membrane of claim 2 , wherein the monomeric solution further comprises at least one polymerization inhibitor.
9. The anion exchange membrane of claim 8 , wherein the at least one polymerization inhibitor is selected from the group consisting of 4-methoxyphenol and 4-tert-butyl catechol.
10. The anion exchange membrane of claim 1 , wherein the microporous support comprises polypropylene, high molecular weight polyethylene, ultrahigh molecular weight polyethylene or polyvinylidene fluoride.
11. The anion exchange membrane of claim 1 , wherein the thickness of the microporous porous support is greater than about 55 microns and less than about 155 microns.
12. The anion exchange membrane of claim 1 , wherein the thickness of the microporous porous support is greater than about approximately 20 microns and less than about 55 microns.
13. The anion exchange membrane of claim 1 , wherein the microporous membrane support has a pore size of from about 0.1 microns to about 1.0 microns.
14. The anion exchange membrane of claim 13 , wherein the microporous membrane support has a pore size of from about 0.1 microns to about 0.2 microns.
15. A process for producing an ion exchange membrane, comprising:
choosing a porous substrate having a porous first side, a porous second side, and a continuous porous structure extending from the first side to the second side, the continuous porous structure comprising pores having a size of about 0.05 microns to about 10 microns;
saturating the porous regions of the substrate with a monomeric solution;
removing excess solution from the substrate while leaving the continuous porous structure filled with solution; and
initiating polymerization to form a crosslinked anion exchange polymer in the continuous porous structure of the substrate.
16. The process of claim 15 , wherein the monomeric solution comprises a polymerization product of at least one functional monomer comprising a tertiary amine, at least one crosslinking monomer, at least one quaternizing agent, and at least one polymerization initiator.
17. The process of claim 16 , wherein the at least one functional monomer is selected from the group consisting of vinylimidazole and vinylcarbazole.
18. The process of claim 16 , wherein the at least one crosslinking monomer is selected from the group consisting of: divinylbenzene, vinylbenzyl chloride, dichloroethane, an octaglycidyl-polyhedral oligomeric silsequioxane or ethylene glycol dimethacrylate.
19. The process of claim 16 , wherein the at least one quaternizing agent is selected from the group consisting of benzyl chloride, vinyl benzyl chloride, dichloroethane, or methyl iodide.
20. The process of claim 16 , wherein the at least one polymerization initiator is selected from the group consisting of organic peroxides, 2,2′-azobis[2,(2-imidazolin-2-yl)-propane] dihydrochloride, a,a′azoisobutyronitrile, 2,2′-azobis(2-methylpropioaminidine) dihydrochloride, 2,2′-azobis[2,(2-imidazolin-2-yl)-propane], and dimethyl 2,2′-azo bis (2-methyl propionate).
21. The process of claim 20 , wherein the organic peroxide is benzoyl peroxide.
22. The process of claim 16 , wherein the monomeric solution further comprises at least one polymerization inhibitor.
23. The process of claim 16 , wherein the at least one polymerization inhibitor is selected from the group consisting of 4-methoxyphenol and 4-tert-butyl catechol.
24. The process of claim 15 , wherein the microporous support comprises polypropylene, high molecular weight polyethylene, ultrahigh molecular weight polyethylene or polyvinylidene fluoride.
25. The process of claim 15 , wherein the thickness of the microporous porous support is greater than about 55 microns and less than about 155 microns.
26. The process of claim 15 , wherein the thickness of the microporous porous support is greater than about 20 microns and less than about 55 microns.
27. The process of claim 15 , wherein the microporous membrane support has a pore size of from about 0.1 microns to about 1.0 microns.
28. The process of claim 27 , wherein the microporous membrane support has a pore size of from about 0.1 microns to about 0.2 microns.