CN103261289B - Acid blocks anionic membrane - Google Patents

Acid blocks anionic membrane Download PDF

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CN103261289B
CN103261289B CN201180061830.XA CN201180061830A CN103261289B CN 103261289 B CN103261289 B CN 103261289B CN 201180061830 A CN201180061830 A CN 201180061830A CN 103261289 B CN103261289 B CN 103261289B
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iii
cloth
amine
film
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CN103261289A (en
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郑永昌
J.巴伯
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General Electric Co
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General Electric Co
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Abstract

Provide the acid blocking-up anion selectivity polymeric membrane with weaving or non-weaving cloth enhancing structure type.The polymer of film is prepared by procedure below, and described process includes making component I, II and III copolymerization, and wherein I is ethylenically unsaturated aliphatic or aromatic uncle amine or quaternary amine monomer.II is cross-linking monomer, and III is vinyl chloride.Reaction is carried out in the presence of radical polymerization initiator.Furthermore disclosed the anion exchange membrane for electrodialysis plant type, and comprise the weaving with the copolymer dipping of the product comprising component I, II and III or non-weaving cloth.

Description

Acid blocks anionic membrane
Invention field
The present invention relates to electrodialysis anion-selective membrane and the method producing such film.
Background of invention
Bipolar electrodialysis (BPED) is that membrane separating process, wherein high purity acid and aqueous slkali can be divided by electrodialytic water Process (water splitting proces) is produced by saline solution.Generally, the equipment of design implementation such ED function is by position The composition of the stacking containing multiple cation-selective membranes, bipolar membrane and anion-selective membrane between pair of electrodes.Heap The folded assembly that can comprise cell compartment (unit cells) itself, the most each cell compartment includes above film, described film with The mode of multiple flow path or passage is provided to arrange between adjacent film.
When DC current is applied to bipolar membrane, water splitting becomes OH-Ion and H+Ion, they migrate to respectively Anode and negative electrode.Cation selective film easily makes cation (positively charged ion, such as Na+、H+) pass through, block simultaneously Anion is passed through.On the contrary, anion-selective membrane easily allows anion (electronegative ion, such as Cl-、OH-) pass through, Block cation transport simultaneously.If guiding saline solution (such as NaCl) by cation selective and anion-selective membrane Between passage, the concentration of this saline solution by the adjacent passage containing bronsted lowry acids and bases bronsted lowry formed HCl and NaOH exhaust.
Be combined with some prior art ED devices, cross the H of anion selective membrane+Migration is proved problematic.By the moon This proton seepage of ion selective membrane is it is well known that and referred to as Ge Luotusi mechanism (Grotthuss Mechanism), the hydrogen bond network of hydrone is diffused through by this mechanism proton.Prove H+Essentially by or migrate the moon from Sub-selective membrane is harmful for electrodialytic process, cause difference anion transfer current efficiency, the low concentration of bronsted lowry acids and bases bronsted lowry with And high equipment and cost of energy.
Summary of the invention
In an exemplary embodiment, it is provided that a kind of have weaving for preparation or non-weaving cloth strengthens structure The method that the acid of type blocks anion selectivity polymeric membrane.The polymer of film is prepared by procedure below, and described process includes Make (I) ethylenically unsaturated aliphatic or aromatic uncle amine or quaternary amine monomer, (II) cross-linking monomer and (III) vinyl chloride Component is copolymerization in the presence of radical polymerization initiator.In an exemplary embodiment, component (I): (II): (III's) Mol ratio is about 20-60:30-70:1-19.In another exemplary embodiment, the mol ratio of component I:II:III is about 35-45:45-55:10-15.Preceding percentage sums to 100 moles of %.
In another aspect of this invention, copolymerization is carried out under there is not non-polymerisable solvent.
In another exemplary embodiment, the feature of film is that water content percentage ratio is about 12-20 weight %, and electricity Stream efficiency is greater than about 93%.
In another aspect of this invention, it is provided that a kind of anion exchange membrane for electrodialysis plant type.Described film Including weaving or non-weaving cloth, described cloth is immersed in the copolymer of the product comprising component I, II and III, and wherein I is Ethylenically unsaturated aliphatic or aromatic uncle amine or quaternary amine monomer, II is cross-linking monomer, and III is vinyl chloride.
Detailed Description Of The Invention
In one aspect of the invention, acid blocks anion-selective membrane by by (I) ethylenically unsaturated aliphatic or aromatics uncle Amine or quaternary amine monomer and (II) cross-linking monomer in the presence of (III) vinyl chloride (VBC) copolymerization and prepare.There is also certainly By base polymerization initiator (IV).The most do not use solvent." acid blocks " used herein means the retardance H with enhancing+Migrate The anion-selective membrane of the ability passed through.Generally, by reducing the water content of film and/or improving the crosslinking of polymer, it is achieved This point.
Component I, II, III and initiator IV are mixed, to form homogeneous solution.Obtained solution is for dipping one piece Cloth, such as polypropylene, polyester, acrylic acid or modacrylic type cloth.The cloth so impregnated is placed between glass plate, And it is subsequently heated this glass sandwich structure, to cause polymerization.After completion of the polymerization reaction, glass sheet is removed, stays poly- The cloth of compound dipping.
By being immersed in aqueous acidic bath (such as 2N HCl solution), make polymer impregnated cloth swelling subsequently.Polymerization The cloth of thing dipping or sheet material can be used as acid in electrodialysis and other application subsequently and block anion-selective membrane.
About component I, exemplary aliphatic tertiary amine can include formula A.
Formula A-aliphatic tertiary amine
Wherein R1 is H or CH3, X is O or NH, and R2 is rudimentary (C1-C6) alkylidene, R3 and R4 is independently selected from rudimentary (C1- C6) alkyl.
Exemplary compositions I aliphatic quaternary amine monomers can include formula B.
Formula B-aliphatic series quaternary amine
Wherein R1, R2, R3 and R4 such as formula A is defined;R5 is selected from rudimentary (C1-C6) alkyl;It is selected from halo, nitrous acid with A Root.Sulfate radical and other inorganic or anion of organic anion.
Exemplary compositions I aromatic uncle amine monomer can include formula C.
Formula C-aromatic uncle amine
Wherein R6 is vinyl.
Exemplary compositions I aromatic quaternary ammonium monomer can include formula D.
Formula D
Wherein R6 is identical with formula C, and R2 is identical with formula A when it is present;R3, R4 are identical with formula B with R5, and A-With in formula B Definition identical.
The concrete member of (I) ethylenically unsaturated aliphatic that can be mentioned that or aromatic uncle amine or quaternary amine monomer includes
I) trimethylaminoethyl group methacrylate chloride (TMAEMC)
Formula B-R1=CH3, R2=Et, R3, R4 and R5 are CH3, and A=Cl-
Ii) vinylbenzyltrimethyl ammonium chloride (VBTMAC)
Formula D-R2=-CH2-, R3, R4 and R5=CH3, R6=vinyl, A=Cl-
Iii) vinylpyridine
Formula C-R6=vinyl;
Iv) dimethyl amino ethyl methacrylate (DMAEMA)
Formula A-R1=CH3, X=O, R2=Et, R3 and R4=CH3
V) dimethylaminopropyl Methacrylamide (DMAPMA)
Formula A-R1=CH3, X=NH, R2=propyl group, R3 and R4=CH3
Cross-linking monomer II may be generally described as containing respect to olefinically unsaturated functional group and the known friendship of optional classification of comforting oneself Connection agent, such as divinylbenzene (DVB), ethylene glycol dimethacrylate (EGDM), glycol diacrylate, 1,10-last of the ten Heavenly stems Omega-diol diacrylate or dimethylacrylate, methylene-bisacrylamide or double Methacrylamide, ten dimethylenes pair Acrylamide or double Methacrylamide, diglycol diacrylate or dimethylacrylate, 1,4-butanediol two Vinyl ethers, triethylene-glycol divinyl ether, divinyl succinate, suberate (subernate) or decanedioic acid Ester etc..
About spendable polymerization initiator, these include azo initiator, such as 2,2-azo double (2-methyl propionitrile), Double (2-methyl-malonamic (the propionamidine)) dihydrochloride of 2,2'-azo;1,1'-azo is double (cyclohexanenitrile);4,4'- Double (4-cyanopentanoic acid) purum of azo etc., peroxide initiator, such as benzoyl peroxide and t-butyl peroxy-2- Double (t-amyl peroxy) hexamethylene of ethylhexoate, 1,1-;Double (the t-butyl peroxy)-3,3,5-trimethyl-cyclohexane of 1,1-;1, Double (t-butyl peroxy) hexamethylene of 1-;2,4-pentanedione peroxide;Double (the t-butyl peroxy)-2,5-dimethylhexane of 2,5-; 2-butanone peroxide;Two t-amyl peroxy compounds;Dicumyl peroxide;Lauroyl peroxide, t-butyl peroxy-2- Ethylhexyl carbonate, t-butyl peracetate ester, tert-butyl peroxide and t-butyl peroxybenzoate etc..
In one embodiment, the addition scope of component (I), (II) and (III) is as follows: component I:II:III-(37- 40%): (48-50%): 12-13% mol ratio.
Embodiment
Embodiment 1 (A-1)
ABA-091509-vinylpyridine/DVB/VBC/PP 470
To 12 g (0.108 mol) 4-vinylpridine, 6 g (0.039 mol) vinyl chloride (VBC) and 24 The mixture of g (0.147 mol) 80% divinylbenzene (DVB) adds 0.8 g (1.9 weight %) t-butyl peroxy-2-second Base alkyl caproate.Obtained solution is the solution of clarification, does not add any non-polymerisable solvent.Solution is poured into a size of 6.5 " in Mylar dish × 6.5 ", under Mylar dish, there is one block of glass, one block of mylar is placed in the solution, subsequently at cloth On put one block of Mylar sheet material.Alternately cloth and Mylar sheet material, to form 3 layers of packaging, and places one piece of glass at the top of assembly Glass.Keep mobile for packaging 2 hours to the baking oven of 90 DEG C of temperature subsequently.Packaging is taken apart, obtains 3 pieces of film sheet strengthened. Film sheet is placed in 2 N hydrochloric acid solutions subsequently, makes it swelling, until balance.Final film is acid efficiency anionic membrane, its Can be used for bipolar electrodialysis, for reclaiming mineral acid from salt.
Embodiment 2 (A-2)
ABA-092409 – DMAEMA/DVB/VBC/PP 447
To 10 g (.0604 mol) dimethyl amino ethyl methacrylate (DMAEMA), 3 g (.0189 mol) The mixture of vinyl chloride (VBC) and 12 g (0.0735 mol) divinylbenzene (DVB) adds 0.5 g (2.0 weights Amount %) t-butyl peroxy-2-ethylhexanoate.Obtained solution is the solution of clarification, does not add any non-polymerisable molten Agent.Solution is poured into a size of 6.5 " × 6.5 " Mylar dish in, under Mylar dish, have one block of glass, by one piece of polypropylene (# 477) cloth is placed in the solution.Subsequently, one block Mylar sheet material is placed above at cloth.An another piece of cloth and Mylar sheet material are placed on In solution.Cloth and Mylar sheet material alternate intervals, to form 3 layers of packaging, and place one block of glass at the top of assembly.Subsequently Packaging is moved to baking oven and keeps 2 hours at a temperature of 90 DEG C.Packaging is taken apart, obtains 3 pieces of film sheet strengthened.Subsequently will Film sheet is placed in 2N HCl solution, makes it swelling, until balance.Final film is acid efficiency anionic membrane, and it can be used for Bipolar electrodialysis, for reclaiming mineral acid from salt.
Embodiment 3 (A-3)
ABA-100609 – DMAEMA/DVB/VBC/PE
To 60 g (0.363 mol) dimethyl amino ethyl methacrylate (DMAEMA), 18 g (0.114 mol) The mixture of vinyl chloride (VBC) and 72 g (0.442 mol) 80% divinylbenzene (DVB) adds 3 g (2 weights Amount %) t-butyl peroxy-2-ethylhexanoate.Obtained solution is the solution of clarification, does not add any non-polymerisable molten Agent.Solution is poured into a size of 10 " x11 " Mylar dish in, under Mylar dish, have one block of glass;One block of mylar is placed In the solution, on cloth, one block of Mylar sheet material is put subsequently.Alternately place cloth and Mylar sheet material, to form 3 layers of packaging, and One block of glass is placed at the top of assembly.Move to packaging subsequently the baking oven of 90 DEG C of temperature keeps 2 hours.Packaging is taken apart, To 3 pieces of film sheet strengthened.Film sheet is placed in 2 N hydrochloric acid solutions subsequently, makes it swelling, until balance.Final film For acid efficiency anionic membrane, it can be used for bipolar electrodialysis, for reclaiming mineral acid from salt.
Embodiment 4
Above film and other commercially available films some is used to carry out film compartment test (Membrane cell testing).Method described in embodiment 2 by United States Patent (USP) 4,822,471 measures membrane current efficiency.Current efficiency hundred Proportion by subtraction refers to that the electric current transmission anion using given percentage passes through anionic membrane.The electric current of residue percentage ratio represents that hydrogen oozes Anionic membrane is passed through in leakage.Mark " by force " alkali refers to quarternary amine functional group, and " weak " alkali represents tertiary amine functional group.By by film at 2N NaCl solution is soaked, first film is converted into Cl-(chloride) form, be washed out going on a tour from Cl-Ion, measures in film Quaternary amine.Subsequently, another kind of salt (such as sodium nitrate solution) is used for Cl-Ion exchanges from film, and titrates Cl-.Cause This can calculate the electric capacity of the quaternary amine in film, in terms of meq/ every g dried resin.In order to measure the tertiary amine in film, measure total amine and (include season Amine and tertiary amine).Subsequently the amount of quaternary amine is deducted from the total amine amount existed.In order to determine that the total amine being present in film (includes season Amine and tertiary amine), first tertiary amine is converted into salt by adding HCl.(quaternary amine also can be converted into Cl by this-Form).Subsequently, use 100% ethanol solution washes out the HCl of excess.Sodium nitrate solution is used to be swapped out Cl subsequently-Ion, and titrate Cl-Ion.Subsequently The total amount of amine can be calculated.Obtain following result and be shown in Table I.
Table I
The C-3-poly-(vinylpyridine) radioactivity grafting in fluorinated copolymer;It is available from Solvay-Solvay ARA
* Journal of Membrane Science, the data of 326 (2009) 650-658 are derived from.
The C-4-poly-(vinylpyridine) radioactivity grafting in fluorinated copolymer;It is available from Solvay-Solvay AW
* derives from Journal of Membrane Science, the data of 110 (1996) 181-190.
C-5-vinylpyridine/DVD/ polychloroethylene film;It is available from Asahi Glass.
Embodiment 5
(092509-470)
To 46 g (0.257 mol) dimethylaminopropyl Methacrylamide (DMAPMA), 12.8 g (0.084 Mol) mixture of vinyl chloride (VBC) and 48 g (0.295 mol) 80% divinylbenzene (DVB) adds 2.1 g (2 weight %) t-butyl peroxy-2-ethylhexanoate.Obtained solution is the solution of clarification, does not add any non-polymerizable Solvent.Solution is poured into a size of 10 " × 11 " Mylar dish in, under Mylar dish, have one block of glass, by one block of polypropylene Cloth is placed in the solution, puts one block of Mylar sheet material subsequently on cloth.Alternately place cloth and Mylar sheet material, to form 3 layers of packaging, And one block of glass is placed at the top of assembly.Move to packaging subsequently the baking oven of 90 DEG C of temperature keeps 2 hours.Packaging is torn open Open, obtain 3 pieces of film sheet strengthened.Film sheet is placed in 2 N hydrochloric acid solutions subsequently, makes it swelling, until balance.Finally Film be acid efficiency anionic membrane, it can be used for bipolar electrodialysis, for reclaiming mineral acid from salt.
Comparative example: (C-6) (ABA-#082809 VP/DVB/PP 470)
To 15 g (0.136 mol) 4-vinylpridine and 30 g (0.184 mol) 80% divinylbenzene (DVB) Mixture in add 0.8 g (1.9 weight %) t-butyl peroxy-2-ethylhexanoate.Vinyl chloride (VBC) is not added Enter in solution.Obtained solution is the solution of clarification, does not add any non-polymerisable solvent.Pour solution into size Be 6.5 " × 6.5 " Mylar dish in, one piece of polypropylene cloth is placed in the solution, on cloth, puts one block of Mylar sheet material subsequently. Alternately place cloth and Mylar sheet material, to form 3 layers of packaging, and place one block of glass at the top of assembly.Subsequently packaging is moved Keep 2 hours to the baking oven of 90 DEG C of temperature.Packaging is taken apart, obtains 3 pieces of film sheet strengthened.Subsequently film sheet is placed on In 2 N hydrochloric acid solutions, make it swelling, until it reaches balance.Final film is acid efficiency anionic membrane.The character of film is set forth in down Table II:
Table II
* resistance is under 1000 Hz, measures in 0.01N NaCl solution.
Film A-1 contains quaternary amine (highly basic) tertiary amine (weak base), and the height owing to VBC and tertiary amine (vinylpyridine) react But crosslinking, causes having compared with low water content, higher current efficiency low-resistance film.It is (weak that comparative film (C-6) contains only tertiary amine Alkali), cause low water content and high current efficiency but the film of much higher resistance.
Embodiment 6 (program similar with the embodiment 2 of United States Patent (USP) 4,822,471)
Use three compartment electrodialysis test compartments to measure the current efficiency (C.E.) of the film of the present invention, be used for as with working as The contrast of those prior aries of acid solution.Compartment comprises negative electrode and the anode electrode of the platinum being coated with titanium, and they are positioned at the end of compartment End, between be located two films, and the spacer being disposed and used liner each other disposes with electrode, with formed containing liquid every Room.Therefore, arrangement is as follows: anion exchange membrane to be tested, intermediate compartment, commercially available types of cationic exchange membrane (GE CR61CMP), anodal compartment, be finally anode electrode.
The film being arranged in test compartment has 25 cm2Active membrane, and the liquid volume of each compartment respectively be about 40 Ml, and cross section active area is 25 cm2.Solution in compartment comprises 1 N HCl in cathodic compartment, and 0.5 N HCl exists In central compartment, and 0.5N H2SO4In the anode compartment.By using magnetic stirrer solution and being maintained at the temperature of 25 DEG C Under degree.Each test is at 20 mA/cm220 minute stage of lower operation, now by the acid concentration in titration determination compartment.Result It is shown in lower Table III:
Table III
Obviously, by adding VBC in the mixture of vinylpyridine/DVB or DMAEMA/DVB or DMAPMA/DVB, mixed Compound is homogenizing.It is therefore not necessary to solvent is used for being polymerized.Upon polymerization, VBC also with a part of reactive tertiary amine, cause that there is season The film of both amine and tertiary amine, with high crosslinking degree.The A-3 film tested as shown in Table III presents the highest (93%) and higher Acid current efficiency.
By adding VBC with anti-with a part of tertiary amine in monomer (such as vinylpyridine, DMAEMA, DMAPMA etc.) Should, we can be controlled in quaternary amine and the ratio of tertiary amine in obtained film, the most also can improve film crosslinking.Due to obtained film High crosslinking degree and low water content, high current efficiency can be obtained by aliphatic monomers (such as DMAEMA, DMAPMA etc.).Due to Introducing quaternary amine in film, resistance also reduces.
At a preferred aspect of the present invention, it is I that anion blocks anion-selective membrane) DMAEMC, II (DVB) Polymeric reaction product with III (VBC).The mol ratio of I:II:III can be about 20-60:30-70:1-19, more preferably 37- 45:45-55:10-15.Preferably initiator is t-butyl peroxy-2-ethylhexanoate.More particularly, this reaction is shown in formula E The following reaction process of display, obtained polymer is shown in formula F.
Formula E-reaction process
Polymer obtained by formula F-
The acid of the present invention blocks the water content that is further characterized by of anionic membrane and is about 12-20%, preferably from about 13-18%. Additionally, they present current efficiency is about 93% and bigger, and the about 20-70% that quarternary amine functional group be total amine based on existence, The most specifically in the range of about 30-40%, as proved by specific embodiments illustrated herein.
It should be understood that the embodiments described herein is exemplary only, and without departing from claims Under the spirit and scope of the present invention limited, those skilled in the art can carry out many and change and modifications.

Claims (20)

1. for preparation, there is weaving or non-weaving cloth strengthens the method that the acid of structure blocks anion selectivity polymeric membrane, described The polymer of film is prepared by procedure below, in the presence of described process is included in radical polymerization initiator, makes component (I) olefinic Unsaturated aliphatic or aromatic uncle amine monomer, (II) cross-linking monomer and (III) vinyl chloride copolymerization, described polymer have with The tertiary amine of meq/ every g dried resin meter 1.27: 0.9~1.52: 0.53 scope and the ratio of quaternary amine, and described film have 93% and Above current efficiency.
2. the method for claim 1, wherein component I: the mol ratio of II: III is 20-60: 30-70: 1-19, Qi Zhongsuo State I, II and III and sum to 100 moles of %.
3. method as claimed in claim 2, wherein component I: the mol ratio of II: III is 35-45: 45-55: 10-15.
4. the method for claim 1, described copolymerization is carried out under there is not non-polymerisable solvent.
5. the method for claim 1, wherein said component (I) includes ethylenically unsaturated aliphatic tertiary amine.
6. the method for claim 1, wherein said component (I) includes olefinic unsaturation aromatic uncle amine.
7. method as claimed in claim 5, wherein said component I includes the member selected from DMAEMA and DMAPMA.
8. method as claimed in claim 6, wherein said component I is vinylpyridine.
9. method as claimed in claim 7, wherein said radical polymerization initiator includes peroxide initiator.
10. method as claimed in claim 7, wherein said cross-linking monomer includes the member selected from DVB and EGDM.
11. methods as claimed in claim 10, wherein said cloth includes selected from polypropylene woven cloths, Polyester woven cloth and poly-third The member of olefin(e) acid woven cloths, the water content % of described film is 12-20 weight %, and 1, under 000Hz, molten at 0.01N NaCl The resistance Rohm-cm measured in liquid2For 50-100.
12. methods as claimed in claim 10, wherein said cloth includes selected from polypropylene woven cloths, Polyester woven cloth, polyester Woven cloths, polyacrylic acid woven cloths and the member of modacrylic woven cloths.
13. 1 kinds of anion exchange membrane for electrodialysis plant type, described film comprises weaving or non-weaving cloth, and described cloth is used Comprising the copolymer dipping of the product of component (I), (II) and (III), wherein (I) is ethylenically unsaturated aliphatic or aromatics uncle Amine monomers, (II) is cross-linking monomer, and (III) is vinyl chloride, and described polymer has in terms of meq/ every g dried resin The tertiary amine of 1.27: 0.9~1.52: 0.53 scopes and the ratio of quaternary amine, and described film has 93% and above current efficiency.
14. anion exchange membrane as claimed in claim 13, wherein said component (I) is selected from formula A and C, wherein
Formula A-aliphatic tertiary amine
Wherein R1 is H or CH3, X is O or NH2, R2 is low alkyl group (C1-C6) alkylidene, and R3 and R4 is independently selected from rudimentary (C1-C6) alkyl;
Formula C-aromatic uncle amine
Wherein R6 is vinyl.
15. anion exchange membrane as claimed in claim 14, wherein component I: the mol ratio of II: III is 20-60: 30-70: 1-19%, wherein preceding percentage is added and reaches 100%.
16. anion exchange membrane as claimed in claim 15, wherein component I: the mol ratio of II: III is 35-45: 45-55% : 10-15%.
17. anion exchange membrane as claimed in claim 15, wherein component I: the mol ratio of II: III is 37-40%: 48- 50%: 12-13%.
18. anion exchange membrane as claimed in claim 16, wherein said component (I) includes selected from DMAEMA's and DMAPMA Member, the feature of described film is that current efficiency is more than 93%.
19. anion exchange membrane as claimed in claim 18, wherein crosslinking monomer component (II) is becoming selected from DVB with EGDM Member.
The anion exchange membrane of 20. 1 kinds of fabrics comprising enhancing by polymer, described polymer has a structure that
Wherein in terms of meq/ every g dried resin (m-1): the ratio of 1 is in 1.27: 0.9~1.52: 0.53 scopes.
CN201180061830.XA 2010-12-23 2011-12-16 Acid blocks anionic membrane Active CN103261289B (en)

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US12/977923 2010-12-23
US12/977,923 US8470896B2 (en) 2010-12-23 2010-12-23 Acid block anion membrane
US12/977,923 2010-12-23
PCT/US2011/065312 WO2012087770A1 (en) 2010-12-23 2011-12-16 Acid block anion membrane

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CN103261289B true CN103261289B (en) 2016-11-30

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101896271A (en) * 2007-12-18 2010-11-24 通用电气公司 Anion exchange polymers, methods for making and materials prepared therefrom

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101896271A (en) * 2007-12-18 2010-11-24 通用电气公司 Anion exchange polymers, methods for making and materials prepared therefrom

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