CN114471179B - A kind of main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane and its preparation method - Google Patents
A kind of main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane and its preparation method Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 121
- 238000002360 preparation method Methods 0.000 title claims abstract description 40
- 239000003513 alkali Substances 0.000 title claims abstract description 37
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 31
- -1 polychlorotrifluoroethylene Polymers 0.000 claims description 64
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 47
- 238000005341 cation exchange Methods 0.000 claims description 46
- 238000006243 chemical reaction Methods 0.000 claims description 45
- 229920001577 copolymer Polymers 0.000 claims description 38
- 229910052757 nitrogen Inorganic materials 0.000 claims description 32
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N EtOH Substances CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 29
- 238000000502 dialysis Methods 0.000 claims description 27
- 239000003011 anion exchange membrane Substances 0.000 claims description 26
- UUAGAQFQZIEFAH-UHFFFAOYSA-N chlorotrifluoroethylene Chemical group FC(F)=C(F)Cl UUAGAQFQZIEFAH-UHFFFAOYSA-N 0.000 claims description 23
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 22
- 239000002243 precursor Substances 0.000 claims description 21
- 229920002493 poly(chlorotrifluoroethylene) Polymers 0.000 claims description 20
- 239000005023 polychlorotrifluoroethylene (PCTFE) polymer Substances 0.000 claims description 20
- ROFVEXUMMXZLPA-UHFFFAOYSA-N Bipyridyl Chemical compound N1=CC=CC=C1C1=CC=CC=N1 ROFVEXUMMXZLPA-UHFFFAOYSA-N 0.000 claims description 18
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 18
- 239000003054 catalyst Substances 0.000 claims description 18
- 238000010494 dissociation reaction Methods 0.000 claims description 18
- 230000005593 dissociations Effects 0.000 claims description 18
- 239000000178 monomer Substances 0.000 claims description 16
- 229920000642 polymer Polymers 0.000 claims description 16
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 14
- 239000007788 liquid Substances 0.000 claims description 14
- 239000001301 oxygen Substances 0.000 claims description 14
- 229910052760 oxygen Inorganic materials 0.000 claims description 14
- 229910021589 Copper(I) bromide Inorganic materials 0.000 claims description 13
- 239000012153 distilled water Substances 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 12
- 239000003960 organic solvent Substances 0.000 claims description 12
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical compound N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 claims description 12
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 9
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 9
- 239000006087 Silane Coupling Agent Substances 0.000 claims description 9
- 238000006116 polymerization reaction Methods 0.000 claims description 9
- XJGIDGNLXAJIOA-UHFFFAOYSA-N 2,11,20,29,37,38,39,40-octazanonacyclo[28.6.1.13,10.112,19.121,28.04,9.013,18.022,27.031,36]tetraconta-1(36),2,4,6,8,10(40),11,13,15,17,19,21(38),22,24,26,28,30,32,34-nonadecaen-37-amine Chemical compound Nn1c2nc3nc(nc4[nH]c(nc5nc(nc1c1ccccc21)c1ccccc51)c1ccccc41)c1ccccc31 XJGIDGNLXAJIOA-UHFFFAOYSA-N 0.000 claims description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 7
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 7
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 7
- 125000000524 functional group Chemical group 0.000 claims description 7
- 239000011521 glass Substances 0.000 claims description 7
- MNCGMVDMOKPCSQ-UHFFFAOYSA-M sodium;2-phenylethenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C=CC1=CC=CC=C1 MNCGMVDMOKPCSQ-UHFFFAOYSA-M 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 7
- 238000006277 sulfonation reaction Methods 0.000 claims description 7
- 125000002883 imidazolyl group Chemical group 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 6
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 6
- 229920000131 polyvinylidene Polymers 0.000 claims description 6
- 238000010926 purge Methods 0.000 claims description 6
- 229910052723 transition metal Inorganic materials 0.000 claims description 6
- 150000003624 transition metals Chemical class 0.000 claims description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 5
- 239000002585 base Substances 0.000 claims description 4
- 125000002091 cationic group Chemical group 0.000 claims description 4
- 229910052802 copper Inorganic materials 0.000 claims description 4
- 238000007590 electrostatic spraying Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- LMPKBYXVPCYJBP-UHFFFAOYSA-N 1-ethenyl-2,4,5-trimethylimidazole Chemical compound CC=1N=C(C)N(C=C)C=1C LMPKBYXVPCYJBP-UHFFFAOYSA-N 0.000 claims description 3
- ZIMGAUCXTGSYIY-UHFFFAOYSA-N 1-ethenyl-2,4-dimethylimidazole Chemical compound CC1=CN(C=C)C(C)=N1 ZIMGAUCXTGSYIY-UHFFFAOYSA-N 0.000 claims description 3
- BDHGFCVQWMDIQX-UHFFFAOYSA-N 1-ethenyl-2-methylimidazole Chemical compound CC1=NC=CN1C=C BDHGFCVQWMDIQX-UHFFFAOYSA-N 0.000 claims description 3
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 3
- 239000000443 aerosol Substances 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 235000019253 formic acid Nutrition 0.000 claims description 3
- 229910052748 manganese Inorganic materials 0.000 claims description 3
- 229910052759 nickel Inorganic materials 0.000 claims description 3
- 238000004528 spin coating Methods 0.000 claims description 3
- 238000005507 spraying Methods 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- 229910052720 vanadium Inorganic materials 0.000 claims description 3
- 229910052725 zinc Inorganic materials 0.000 claims description 3
- COVXBJIKNGVTNV-UHFFFAOYSA-N 1-chloro-1,2,2-trifluoroethene;1,1-difluoroethene Chemical group FC(F)=C.FC(F)=C(F)Cl COVXBJIKNGVTNV-UHFFFAOYSA-N 0.000 claims description 2
- 230000002378 acidificating effect Effects 0.000 claims description 2
- 238000007598 dipping method Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 229910052706 scandium Inorganic materials 0.000 claims description 2
- 229960001760 dimethyl sulfoxide Drugs 0.000 claims 2
- OSSNTDFYBPYIEC-UHFFFAOYSA-N 1-ethenylimidazole Chemical compound C=CN1C=CN=C1 OSSNTDFYBPYIEC-UHFFFAOYSA-N 0.000 claims 1
- 239000005977 Ethylene Substances 0.000 claims 1
- JACPFCQFVIAGDN-UHFFFAOYSA-M sipc iv Chemical class [OH-].[Si+4].CN(C)CCC[Si](C)(C)[O-].C=1C=CC=C(C(N=C2[N-]C(C3=CC=CC=C32)=N2)=N3)C=1C3=CC([C]1C=CC=CC1=1)=NC=1N=C1[C]3C=CC=CC3=C2[N-]1 JACPFCQFVIAGDN-UHFFFAOYSA-M 0.000 claims 1
- 238000000034 method Methods 0.000 description 11
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 10
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 10
- 229910001431 copper ion Inorganic materials 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 9
- MPMSMUBQXQALQI-UHFFFAOYSA-N cobalt phthalocyanine Chemical compound [Co+2].C12=CC=CC=C2C(N=C2[N-]C(C3=CC=CC=C32)=N2)=NC1=NC([C]1C=CC=CC1=1)=NC=1N=C1[C]3C=CC=CC3=C2[N-]1 MPMSMUBQXQALQI-UHFFFAOYSA-N 0.000 description 8
- 239000012141 concentrate Substances 0.000 description 8
- KMHSUNDEGHRBNV-UHFFFAOYSA-N 2,4-dichloropyrimidine-5-carbonitrile Chemical class ClC1=NC=C(C#N)C(Cl)=N1 KMHSUNDEGHRBNV-UHFFFAOYSA-N 0.000 description 5
- RBTKNAXYKSUFRK-UHFFFAOYSA-N heliogen blue Chemical compound [Cu].[N-]1C2=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=NC([N-]1)=C(C=CC=C3)C3=C1N=C([N-]1)C3=CC=CC=C3C1=N2 RBTKNAXYKSUFRK-UHFFFAOYSA-N 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 229910017052 cobalt Inorganic materials 0.000 description 4
- 239000010941 cobalt Substances 0.000 description 4
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 4
- 239000010949 copper Substances 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000006467 substitution reaction Methods 0.000 description 3
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 description 3
- SBKRCLAGDGVUMO-UHFFFAOYSA-N 1-ethenyl-4,5-diethyl-2-methylimidazole Chemical compound CCC=1N=C(C)N(C=C)C=1CC SBKRCLAGDGVUMO-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 206010040844 Skin exfoliation Diseases 0.000 description 2
- 238000005349 anion exchange Methods 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 2
- 229920000578 graft copolymer Polymers 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 description 2
- 150000003242 quaternary ammonium salts Chemical group 0.000 description 2
- MLMGJTAJUDSUKA-UHFFFAOYSA-N 2-ethenyl-1h-imidazole Chemical group C=CC1=NC=CN1 MLMGJTAJUDSUKA-UHFFFAOYSA-N 0.000 description 1
- AGBXYHCHUYARJY-UHFFFAOYSA-N 2-phenylethenesulfonic acid Chemical compound OS(=O)(=O)C=CC1=CC=CC=C1 AGBXYHCHUYARJY-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012046 mixed solvent Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920006260 polyaryletherketone Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/42—Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
- B01D61/44—Ion-selective electrodialysis
- B01D61/445—Ion-selective electrodialysis with bipolar membranes; Water splitting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
- B01D69/125—In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F259/00—Macromolecular compounds obtained by polymerising monomers on to polymers of halogen containing monomers as defined in group C08F14/00
- C08F259/08—Macromolecular compounds obtained by polymerising monomers on to polymers of halogen containing monomers as defined in group C08F14/00 on to polymers containing fluorine
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/30—Chemical resistance
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/42—Ion-exchange membranes
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Water Supply & Treatment (AREA)
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- Urology & Nephrology (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
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Abstract
Description
技术领域Technical field
本发明涉及一种主链碳氟-酞菁催化层酸碱双极膜及其制备方法,属于电驱动膜技术领域。The invention relates to a main chain fluorocarbon-phthalocyanine catalytic layer acid-base bipolar membrane and a preparation method thereof, and belongs to the technical field of electric drive membranes.
背景技术Background technique
双极膜是由阴离子交换膜层、阳离子交换膜层以及中间界面层(中间层) 复合而成的复合膜材料。在电场作用下,双极膜中间层的水分子发生水解离,生成氢离子和氢氧根,从而实现产酸碱的目的。双极膜水解离产酸碱理论电位为0.828V,电解水产酸碱理论电压为2.057V。此外,双极膜中间层水解离速度比一般情况下的水解离速度快约5000万倍。因此,双极膜技术具有低能耗、高效率、产物无污染等特点,已被广泛应用于酸碱生产及回收、海洋化工、污染治理和有机合成等各个领域。Bipolar membrane is a composite membrane material composed of an anion exchange membrane layer, a cation exchange membrane layer and an intermediate interface layer (intermediate layer). Under the action of an electric field, water molecules in the middle layer of the bipolar membrane undergo water dissociation to generate hydrogen ions and hydroxyl radicals, thereby achieving the purpose of generating acid and alkali. The theoretical potential of bipolar membrane water dissociation to produce acid and alkali is 0.828V, and the theoretical potential of electrolysis of water to produce acid and alkali is 2.057V. In addition, the water dissociation speed in the middle layer of the bipolar membrane is about 50 million times faster than the normal water dissociation speed. Therefore, bipolar membrane technology has the characteristics of low energy consumption, high efficiency, and pollution-free products, and has been widely used in various fields such as acid and alkali production and recycling, marine chemical industry, pollution control, and organic synthesis.
聚芳醚酮等芳香族碳骨架是目前常用的双极膜基膜材料,季铵官能团是双极膜阴离子交换膜层的常见官能团。然而,芳香族碳骨架中的碳氧键容易被氢氧根攻击而降解。此外,因为氢氧根的攻击,季铵官能团由于发生霍夫曼反应、亲和取代反应等被破坏,从而导致双极膜耐碱浓度普遍偏低。另一方面,现有的双极膜由于是阴离子交换膜层、阳离子交换膜层以及中间层复合而成,由于不同层之间理化性质的差异,使其在使用过程中容易发生剥离,进而降低了双极膜的使用寿命。Aromatic carbon skeletons such as polyaryl ether ketone are currently commonly used bipolar membrane base membrane materials, and quaternary ammonium functional groups are common functional groups in the anion exchange membrane layer of bipolar membranes. However, the carbon-oxygen bonds in the aromatic carbon skeleton are easily attacked and degraded by hydroxyl radicals. In addition, due to the attack of hydroxyl radicals, the quaternary ammonium functional group is destroyed due to the occurrence of Hoffman reaction, affinity substitution reaction, etc., resulting in a generally low alkali resistance concentration of the bipolar membrane. On the other hand, the existing bipolar membrane is composed of an anion exchange membrane layer, a cation exchange membrane layer and an intermediate layer. Due to the differences in physical and chemical properties between different layers, it is easy to peel off during use, thereby reducing the risk of improves the service life of the bipolar membrane.
发明内容Contents of the invention
为了解决现有技术所存在的上述问题,本发明提供一种主链碳氟-酞菁催化层耐碱双极膜及其制备方法,双极膜中的阴离子交换膜层和阳离子交换膜层都以全氟碳为主链,克服了常见主链中碳氧键容易受氢氧根攻击而降解的缺陷,且阴阳离子交换膜层具有相近的理化性质,从而降低了其在使用过程中剥离的可能性,延长了其使用寿命。In order to solve the above-mentioned problems existing in the prior art, the present invention provides a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane and a preparation method thereof. The anion exchange membrane layer and the cation exchange membrane layer in the bipolar membrane are both Using perfluorocarbon as the main chain overcomes the common shortcomings of carbon-oxygen bonds in the main chain being easily attacked and degraded by hydroxyl radicals, and the anion and cation exchange membrane layers have similar physical and chemical properties, thus reducing the risk of peeling off during use. possibility, extending its service life.
本发明的技术方案如下:The technical solution of the present invention is as follows:
本发明的目的之一在于提供一种主链碳氟-酞菁催化层耐碱双极膜,包括阳离子交换膜层和阴离子交换膜层,阳离子交换膜层和阴离子交换膜层都以全氟碳为主链,氮杂环作为阴离子交换膜层上的阳离子官能团;其中,阳离子交换膜层的化学结构式为:One of the objects of the present invention is to provide a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, which includes a cation exchange membrane layer and an anion exchange membrane layer. Both the cation exchange membrane layer and the anion exchange membrane layer are made of perfluorocarbon. As the main chain, the nitrogen heterocycle serves as the cationic functional group on the anion exchange membrane layer; among them, the chemical structural formula of the cation exchange membrane layer is:
阴离子交换膜层的化学结构式为:The chemical structural formula of the anion exchange membrane layer is:
其中,x为含三氟氯乙烯结构单元聚合物主链的聚合度,n为含磺酸集团取代基侧链的聚合度,m为含咪唑取代基侧链的聚合度,n、m是不为零的整数。Among them, x is the degree of polymerization of the main chain of the polymer containing chlorotrifluoroethylene structural units, n is the degree of polymerization of the side chain containing the sulfonic acid group substituent, m is the degree of polymerization of the side chain containing the imidazole substituent, n and m are not an integer that is zero.
本发明的目的还在于提供一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,具体包括以下步骤:The object of the present invention is also to provide a method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, which specifically includes the following steps:
S1、阳离子交换膜液的制备:将含三氟氯乙烯结构单元的聚合物溶于有机溶剂Ⅰ中,通氮气除氧,升温后按照摩尔比为1:(20~100):1:2将含三氟氯乙烯结构单元的聚合物、苯乙烯磺酸钠、CuBr和联吡啶加入反应体系中,在氮气保护下,在90~130℃条件下进行恒温磺化反应16~48h,将反应液装入透析袋中,在水透析24h;烘干透析袋中溶液,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);S1. Preparation of cation exchange membrane liquid: Dissolve the polymer containing chlorotrifluoroethylene structural units in organic solvent I, pass nitrogen to remove oxygen, and after heating, dissolve the polymer in a molar ratio of 1:(20~100):1:2. Polymers containing chlorotrifluoroethylene structural units, sodium styrene sulfonate, CuBr and bipyridine are added to the reaction system, and under nitrogen protection, a constant temperature sulfonation reaction is carried out at 90 to 130°C for 16 to 48 hours, and the reaction solution is Put it into a dialysis bag and dialyze in water for 24 hours; dry the solution in the dialysis bag to prepare polychlorotrifluoroethylene grafted sodium styrene sulfonate side chain copolymer (PCTEF-g-PSSNa);
S2、阴离子交换膜液的制备:将含三氟氯乙烯结构单元的聚合物溶于有机溶剂Ⅱ中,通氮气除氧,升温后按照含三氟氯乙烯结构单元的聚合物、含咪唑基单体、uBr和联吡啶的摩尔比1:(20~100):1:2混合,在氮气保护下,恒温反应 16~48h,将反应液装入透析袋中,在水透析24h;烘干透析袋中溶液,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);S2. Preparation of anion exchange membrane liquid: Dissolve the polymer containing chlorotrifluoroethylene structural units in organic solvent II, purge nitrogen to remove oxygen, and after heating, follow the steps of polymer containing chlorotrifluoroethylene structural units, imidazole-containing monomers Mix the monomer, uBr and bipyridine at a molar ratio of 1:(20~100):1:2, react under nitrogen protection at a constant temperature for 16~48 hours, put the reaction solution into a dialysis bag, and dialyze in water for 24 hours; dry for dialysis The solution in the bag is used to prepare polychlorotrifluoroethylene-grafted vinylimidazole side chain copolymer (PCTEF-g-PVIm);
S3、酞菁前驱体的制备:KH-560与氨基酞菁以摩尔比为1:1投料加入反应瓶中,加入有机溶剂Ⅲ搅拌均匀,室温反应1~3h,得到酞菁-KH560前驱体;S3. Preparation of phthalocyanine precursor: KH-560 and aminophthalocyanine are added into the reaction bottle at a molar ratio of 1:1, add organic solvent III, stir evenly, and react at room temperature for 1 to 3 hours to obtain the phthalocyanine-KH560 precursor;
S4、双极膜中间层水解离催化剂的制备:将经过步骤S3获得的酞菁-KH560 前驱体与硅烷偶联剂一起加入反应器中,同时加入酸性催化剂和蒸馏水,调节反应体系pH为2.5~3.5,在50~60℃条件下反应1~8h,得到KH-560改性酞菁硅溶胶作为双极膜中间层水解离催化剂;S4. Preparation of the water dissociation catalyst for the intermediate layer of the bipolar membrane: Add the phthalocyanine-KH560 precursor obtained through step S3 and the silane coupling agent into the reactor. At the same time, add the acidic catalyst and distilled water to adjust the pH of the reaction system to 2.5~ 3.5, react at 50-60°C for 1-8 hours to obtain KH-560 modified phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst;
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上喷涂KH-560改性酞菁硅溶胶,晾干后将经过步骤S2获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified phthalocyanine silica sol on the cation exchange membrane layer. After drying, cast the polychlorotrifluoroethylene-grafted vinylimidazole side chain copolymer obtained in step S2 on the cation exchange membrane layer and dry it. Finally, a chain fluorocarbon-phthalocyanine catalytic layer is obtained as an alkali-resistant bipolar membrane.
进一步的,所述步骤S1和S2中含三氟氯乙烯结构单元的聚合物为聚(偏氟乙烯-三氟氯乙烯)、聚(偏氟乙烯-三氟氯乙烯-四氟乙烯)、聚(四氟乙烯- 三氟氯乙烯)或聚三氟氯乙烯中的任意一种。Further, the polymers containing chlorotrifluoroethylene structural units in steps S1 and S2 are poly(vinylidene fluoride-chlorotrifluoroethylene), poly(vinylidene fluoride-chlorotrifluoroethylene-tetrafluoroethylene), poly(vinylidene fluoride-chlorotrifluoroethylene-tetrafluoroethylene), (tetrafluoroethylene-chlorotrifluoroethylene) or polychlorotrifluoroethylene.
进一步的,所述步骤S1中有机溶剂Ⅰ为N,N-二甲基乙酰胺、二甲亚砜、 N-甲基吡咯烷酮、N,N-二甲基甲酰胺中的任意一种或两种任意比例的组合。Further, the organic solvent I in step S1 is any one or two of N,N-dimethylacetamide, dimethyl sulfoxide, N-methylpyrrolidone, and N,N-dimethylformamide. Combinations in any proportion.
进一步的,所述步骤S2中含咪唑基单体为2-甲基-1-乙烯基咪唑、2,4-二甲基-1-乙烯基咪唑、2,4,5-三甲基-1-乙烯基咪唑、5-乙基-2,4-二甲基-1-乙烯基咪唑、 2-乙基-4,5-二甲基-1-乙烯基咪唑、4-乙基-2,5-二甲基-1-乙烯基咪唑、2-丙基-4,5- 二甲基-1-乙烯基咪唑、4-丙基-2,5-二甲基-1-乙烯基咪唑、2-丁基-4,5-二甲基-1- 乙烯基咪唑、4-丁基-2,5-二甲基-1-乙烯基咪唑、2,4-二乙基-5-甲基-1-乙烯基咪唑、 4,5-二乙基-2-甲基-1-乙烯基咪唑、2,4-二丁基-5-甲基-1-乙烯基咪唑、4,5-二丁基 -2-甲基-1-乙烯基咪唑中的任意一种。Further, the imidazole group-containing monomer in step S2 is 2-methyl-1-vinylimidazole, 2,4-dimethyl-1-vinylimidazole, and 2,4,5-trimethyl-1 -Vinylimidazole, 5-ethyl-2,4-dimethyl-1-vinylimidazole, 2-ethyl-4,5-dimethyl-1-vinylimidazole, 4-ethyl-2, 5-Dimethyl-1-vinylimidazole, 2-propyl-4,5-dimethyl-1-vinylimidazole, 4-propyl-2,5-dimethyl-1-vinylimidazole, 2-Butyl-4,5-dimethyl-1-vinylimidazole, 4-butyl-2,5-dimethyl-1-vinylimidazole, 2,4-diethyl-5-methyl -1-vinylimidazole, 4,5-diethyl-2-methyl-1-vinylimidazole, 2,4-dibutyl-5-methyl-1-vinylimidazole, 4,5-bis Any one of butyl-2-methyl-1-vinylimidazole.
进一步的,所述步骤S2中有机溶剂Ⅱ为四氢呋喃、N,N-二甲基乙酰胺、二甲亚砜、N-甲基吡咯烷酮、N,N-二甲基甲酰胺中的任意一种或两种任意比例的组合。Further, the organic solvent II in step S2 is any one of tetrahydrofuran, N,N-dimethylacetamide, dimethyl sulfoxide, N-methylpyrrolidone, N,N-dimethylformamide or A combination of two types in any proportion.
进一步的,所述步骤S3中有机溶剂Ⅲ为无水甲醇、无水乙醇、异丙醇、四氢呋喃、丙酮中的任意一种或两种任意比例的组合。Further, the organic solvent III in step S3 is any one of anhydrous methanol, anhydrous ethanol, isopropyl alcohol, tetrahydrofuran, and acetone or a combination of two in any proportion.
进一步的,所述步骤S3中氨基酞菁为含过渡金属氨基酞菁,过渡金属为Fe、 Mg、Ba、Sc、Ti、V、Cr、Mn、Co、Ni、Cu或Zn中的任意一种。Further, in step S3, the amino phthalocyanine is a transition metal-containing amino phthalocyanine, and the transition metal is any one of Fe, Mg, Ba, Sc, Ti, V, Cr, Mn, Co, Ni, Cu or Zn .
进一步的,所述步骤S4中硅烷偶联剂为KH540、KH550、KH602或KH792 中的任意一种;催化剂为盐酸、甲酸或乙酸中的任意一种。Further, in step S4, the silane coupling agent is any one of KH540, KH550, KH602 or KH792; the catalyst is any one of hydrochloric acid, formic acid or acetic acid.
进一步的,所述步骤S5中在阳离子交换膜层上喷涂KH-560改性酞菁硅溶胶采用气溶胶喷涂法、静电喷射、浸渍-提拉法或旋涂法中的任意一种。Further, in step S5, any one of the aerosol spraying method, electrostatic spraying, dipping-pulling method or spin coating method is used to spray KH-560 modified phthalocyanine silica sol on the cation exchange membrane layer.
相较于现有技术,本发明的有益效果在于:Compared with the existing technology, the beneficial effects of the present invention are:
(1)本发明提供的主链碳氟-酞菁催化层耐碱双极膜,其中,阳离子交换膜层和阴离子交换膜层都是以氟碳为主链,能够克服现有技术中芳香族碳骨架中的碳氧键容易被氢氧根攻击而降解的缺陷,同时利用氮杂环作为阴离子交换膜层的阳离子官能团,替代季铵盐官能团,一方面能够避免由于发生霍夫曼反应、亲和取代反应而破坏季铵盐官能团,另一方面,氮杂环官能团的电子分布更均匀,具有更强的耐碱性,能够提高双极膜的耐碱性,从而使电渗析时所产生的酸碱浓度得以提高。(1) The main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane provided by the present invention, in which the cation exchange membrane layer and the anion exchange membrane layer both use fluorocarbon as the main chain, can overcome the aromatic problems in the prior art. The carbon-oxygen bond in the carbon skeleton is easily attacked and degraded by hydroxyl radicals. At the same time, the nitrogen heterocycle is used as the cationic functional group of the anion exchange membrane layer to replace the quaternary ammonium salt functional group. On the one hand, it can avoid the occurrence of Hoffmann reaction and affinity. and substitution reaction to destroy the quaternary ammonium salt functional group. On the other hand, the electron distribution of the nitrogen heterocyclic functional group is more uniform and has stronger alkali resistance, which can improve the alkali resistance of the bipolar membrane, thereby reducing the electrodialysis generated during electrodialysis. The acid-base concentration is increased.
(2)本发明提供的主链碳氟-酞菁催化层耐碱双极膜中阴离子交换膜层和阳离子交换膜层都以氟碳链为主链,阴、阳离子交换膜层具有相近的理化性质,避免了不同层之间的理化性质差异,从而降低了其在使用过程中发生剥离的可能性,延长其使用寿命。(2) In the main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane provided by the present invention, both the anion exchange membrane layer and the cation exchange membrane layer have fluorocarbon chains as the main chain, and the anion and cation exchange membrane layers have similar physical and chemical properties. properties, avoiding differences in physical and chemical properties between different layers, thereby reducing the possibility of peeling during use and extending its service life.
具体实施方式Detailed ways
下面结合较佳实施例对本发明做进一步的说明,在本发明中所披露的范围的端点和任何值都不限于该精确的范围或值,这些范围或值应当理解为包含接近这些范围或值的值;对于数值范围来说,各个范围的端点值之间、各个范围的端点值和单独的点值之间,以及单独的点值之间可以彼此组合而得到一个或多个新的数值范围,这些数值范围应被视为在本文中具体公开。The present invention will be further described below in conjunction with preferred embodiments. The endpoints and any values of the ranges disclosed in the present invention are not limited to the precise ranges or values. These ranges or values should be understood to include those close to these ranges or values. Value; for numerical ranges, the endpoint values of each range, the endpoint values of each range and individual point values, and the individual point values can be combined with each other to obtain one or more new numerical ranges. These numerical ranges should be deemed to be specifically disclosed herein.
下述实施例中所用的材料、试剂等,如无特殊说明,均可从商业途径得到;The materials, reagents, etc. used in the following examples can all be obtained from commercial sources unless otherwise specified;
下述实施例中的实验方法,如无特殊说明,均为常规方法。The experimental methods in the following examples are all conventional methods unless otherwise specified.
实施例1Example 1
一种主链碳氟-酞菁催化层耐碱双极膜,包括阳离子交换膜层和阴离子交换膜层,阳离子交换膜层和阴离子交换膜层都以全氟碳为主链,氮杂环作为阴离子交换膜层上的阳离子官能团;其中,阳离子交换膜层的化学结构式为:An alkali-resistant bipolar membrane with a main chain fluorocarbon-phthalocyanine catalytic layer, including a cation exchange membrane layer and an anion exchange membrane layer. Both the cation exchange membrane layer and the anion exchange membrane layer have perfluorocarbon as the main chain, and nitrogen heterocycles as Cationic functional groups on the anion exchange membrane layer; among them, the chemical structural formula of the cation exchange membrane layer is:
阴离子交换膜层的化学结构式为:The chemical structural formula of the anion exchange membrane layer is:
其中,x为含三氟氯乙烯结构单元聚合物主链的聚合度,n为含磺酸集团取代基侧链的聚合度,m为含咪唑取代基侧链的聚合度,n、m是不为零的整数。Among them, x is the degree of polymerization of the main chain of the polymer containing chlorotrifluoroethylene structural units, n is the degree of polymerization of the side chain containing the sulfonic acid group substituent, m is the degree of polymerization of the side chain containing the imidazole substituent, n and m are not an integer that is zero.
实施例2Example 2
一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,括以下步骤:A method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, including the following steps:
S1、阳离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯(共聚物含25%三氟氯乙烯)溶于120mL N-甲基吡咯烷酮中,通氮气除氧,升温至120℃后加入126.3g苯乙烯磺酸钠、4.36g CuBr和4.76g联吡啶,在氮气保护下,在 120℃条件下进行恒温磺化反应24h,将反应液倒入醇/水混合溶剂(V/V=1:1) 中,沉淀得接枝聚合物,再装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);其中,接枝反应如下:S1. Preparation of cation exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene (the copolymer contains 25% chlorotrifluoroethylene)) and dissolve it in 120 mL of N-methylpyrrolidone, pass nitrogen to remove oxygen, and heat to After reaching 120°C, add 126.3g sodium styrene sulfonate, 4.36g CuBr and 4.76g bipyridine. Under nitrogen protection, perform a constant temperature sulfonation reaction at 120°C for 24 hours. Pour the reaction solution into an alcohol/water mixed solvent (V /V=1:1), precipitate the graft polymer, put it into a dialysis bag, and dialyze in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, Concentrate and dry to prepare polychlorotrifluoroethylene grafted sodium styrene sulfonate side chain copolymer (PCTEF-g-PSSNa); wherein, the grafting reaction is as follows:
S2、阴离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯)(共聚物含25%三氟氯乙烯)溶于120mL N,N-二甲基甲酰胺中,通氮气除氧,升温至80℃后加入74.44g 2-甲基-1-乙烯基咪唑、4.36gCuBr和10.56g五甲基二乙基三胺,在氮气保护下,恒温反应48h,将反应液装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);其中,接枝反应如下所示:S2. Preparation of anion exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of N,N-dimethylformamide, and purge with nitrogen. Remove oxygen, raise the temperature to 80°C, add 74.44g 2-methyl-1-vinylimidazole, 4.36g CuBr and 10.56g pentamethyldiethyltriamine, react at a constant temperature for 48 hours under nitrogen protection, and put the reaction solution into In the dialysis bag, dialyze in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate, and dry to prepare polychlorotrifluoroethylene-grafted vinylimidazole side chains. Copolymer (PCTEF-g-PVIm); wherein, the grafting reaction is as follows:
S3、酞菁前驱体的制备:称取2.36g KH-560与5.77g酞菁铜加入反应瓶中,加入35mL无水乙醇搅拌均匀,室温反应3h,蒸馏除去溶剂得到酞菁铁-KH560 前驱体;S3. Preparation of phthalocyanine precursor: Weigh 2.36g KH-560 and 5.77g copper phthalocyanine into the reaction bottle, add 35 mL of absolute ethanol, stir evenly, react at room temperature for 3 hours, and distill away the solvent to obtain iron phthalocyanine-KH560 precursor. ;
S4、双极膜中间层水解离催化剂的制备:称取经过步骤S3获得的酞菁铁 -KH560前驱体8.06g与1.11g硅烷偶联剂KH792一起加入反应器中,同时加入 18mL乙醇、7.5mL蒸馏水和0.6mL 1.0%的盐酸,调节反应体系pH为3.5,在 50℃条件下反应1h,得到KH-560改性酞菁铁硅溶胶作为双极膜中间层水解离催化剂;其中,反应如下所示:S4. Preparation of bipolar membrane intermediate layer water dissociation catalyst: Weigh 8.06g of the iron phthalocyanine-KH560 precursor obtained in step S3 and add 1.11g of silane coupling agent KH792 into the reactor. At the same time, add 18mL of ethanol and 7.5mL of ethanol. Distilled water and 0.6 mL of 1.0% hydrochloric acid were used to adjust the pH of the reaction system to 3.5. The reaction was carried out at 50°C for 1 hour to obtain KH-560 modified iron phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst. The reaction was as follows: Show:
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上采用静电喷射法喷涂KH-560改性酞菁铁硅溶胶,晾干后将经过步骤 S2获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后阴面浸泡在碘甲烷四氢呋喃溶液中5h后取出,用蒸馏水洗净膜表面杂质,得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified iron phthalocyanine silica sol on the cation exchange membrane layer using electrostatic spraying. After drying, the polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer obtained in step S2 is cast on the cation exchange membrane. After drying, the negative side was soaked in methyl iodide and tetrahydrofuran solution for 5 hours, then taken out, and the impurities on the membrane surface were washed with distilled water to obtain a chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane.
实施例3Example 3
一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,括以下步骤:A method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, including the following steps:
S1、阳离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯-四氟乙烯) (共聚物含25%三氟氯乙烯)溶于120mL二甲亚砜中,通氮气除氧,升温至80℃后加入151.6g苯乙烯磺酸钠、4.36g CuBr和10.56g五甲基二乙基三胺,在氮气保护下,在80℃条件下进行恒温磺化反应48h,将反应液倒入乙醇中,沉淀得接枝聚合物,再装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);其中,接枝反应如实施例1所示:S1. Preparation of cation exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene-tetrafluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of dimethyl sulfoxide. Oxygen, after raising the temperature to 80°C, add 151.6g sodium styrene sulfonate, 4.36g CuBr and 10.56g pentamethyldiethyltriamine, and perform a constant temperature sulfonation reaction at 80°C for 48 hours under nitrogen protection. The solution is poured into ethanol, and the graft polymer is precipitated, which is then put into a dialysis bag and dialyzed in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; the solution in the dialysis bag is collected, concentrated, and dried. Dry to prepare polychlorotrifluoroethylene grafted sodium styrene sulfonate side chain copolymer (PCTEF-g-PSSNa); wherein, the grafting reaction is as shown in Example 1:
S2、阴离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯-四氟乙烯) (共聚物含25%三氟氯乙烯)溶于120mL四氢呋喃中,通氮气除氧,升温至80℃后加入74.4g 5-乙基-2,4-二甲基-1-乙烯基咪唑、4.36gCuBr和4.76g联吡啶,在氮气保护下,恒温反应16h,将反应液装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);其中,接枝反应如下所示:S2. Preparation of anion exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene-tetrafluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of tetrahydrofuran, pass nitrogen to remove oxygen, and raise the temperature. After reaching 80°C, add 74.4g 5-ethyl-2,4-dimethyl-1-vinylimidazole, 4.36g CuBr and 4.76g bipyridine, react at a constant temperature for 16 hours under nitrogen protection, and put the reaction solution into a dialysis bag. In, dialyze in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate, and dry to prepare polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer. (PCTEF-g-PVIm); where, the grafting reaction is as follows:
S3、酞菁前驱体的制备:称取2.36g KH-560与5.70g酞菁铜加入反应瓶中,加入30mL丙酮搅拌均匀,室温反应1h,蒸馏除去溶剂得到酞菁铜-KH560前驱体;S3. Preparation of phthalocyanine precursor: Weigh 2.36g KH-560 and 5.70g copper phthalocyanine into the reaction bottle, add 30 mL acetone and stir evenly, react at room temperature for 1 hour, distill the solvent away to obtain the copper phthalocyanine-KH560 precursor;
S4、双极膜中间层水解离催化剂的制备:称取经过步骤S3获得的酞菁铜 -KH560前驱体8.13g与1.11g硅烷偶联剂KH602一起加入反应器中,同时加入 18mL乙醇、7.5mL蒸馏水和0.6mL甲酸,调节反应体系pH为2.5,在50℃条件下反应2h,得到KH-560改性酞菁铜硅溶胶作为双极膜中间层水解离催化剂;其中,反应如下所示:S4. Preparation of bipolar membrane intermediate layer water dissociation catalyst: Weigh 8.13g of copper phthalocyanine-KH560 precursor obtained in step S3 and add 1.11g of silane coupling agent KH602 into the reactor. At the same time, add 18mL of ethanol and 7.5mL of ethanol. Distilled water and 0.6 mL formic acid, adjust the pH of the reaction system to 2.5, react at 50°C for 2 hours, and obtain KH-560 modified copper phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst; the reaction is as follows:
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上采用旋涂法喷涂KH-560改性酞菁铜硅溶胶,晾干后将经过步骤S2 获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后阴面浸泡在碘甲烷四氢呋喃溶液中5h后取出,用蒸馏水洗净膜表面杂质,得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified copper phthalocyanine silica sol on the cation exchange membrane layer by spin coating. After drying, the polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer obtained in step S2 is cast on the cation exchange membrane. After drying, the negative side was soaked in methyl iodide and tetrahydrofuran solution for 5 hours, then taken out, and the impurities on the membrane surface were washed with distilled water to obtain a chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane.
实施例4Example 4
一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,括以下步骤:A method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, including the following steps:
S1、阳离子交换膜液的制备:称取10g聚(四氟乙烯-三氟氯乙烯)(共聚物含25%三氟氯乙烯)溶于120mL N,N-二甲基乙酰胺中,通氮气除氧,升温至 130℃后加入126.3苯乙烯磺酸钠、4.36g CuBr和10.56g五甲基二乙基三胺,在氮气保护下,在80℃条件下进行恒温磺化反应16h,将反应液透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);其中,接枝反应如实施例1所示:S1. Preparation of cation exchange membrane liquid: Weigh 10g of poly(tetrafluoroethylene-chlorotrifluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene), dissolve it in 120 mL of N,N-dimethylacetamide, and ventilate with nitrogen. Remove oxygen, raise the temperature to 130°C, add 126.3 sodium styrene sulfonate, 4.36g CuBr and 10.56g pentamethyldiethyltriamine, and perform a constant temperature sulfonation reaction at 80°C for 16 hours under nitrogen protection. In the dialysis bag, dialyze in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate, and dry to prepare polychlorotrifluoroethylene grafted styrene sulfonic acid. Sodium side chain copolymer (PCTEF-g-PSSNa); wherein, the grafting reaction is as shown in Example 1:
S2、阴离子交换膜液的制备:称取10g聚(四氟乙烯-三氟氯乙烯)(共聚物含25%三氟氯乙烯)溶于120mL N-甲基吡咯烷酮中,通氮气除氧,升温至85℃后加入70.4g 2,4-二甲基-1-乙烯基咪唑、4.36gCuBr和4.76g联吡啶,在氮气保护下,恒温反应18h,将反应液装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);其中,接枝反应如下所示:S2. Preparation of anion exchange membrane liquid: Weigh 10g of poly(tetrafluoroethylene-chlorotrifluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of N-methylpyrrolidone, purge nitrogen to remove oxygen, and raise the temperature. After reaching 85°C, add 70.4g 2,4-dimethyl-1-vinylimidazole, 4.36g CuBr and 4.76g bipyridine, react at a constant temperature for 18 hours under nitrogen protection, put the reaction solution into a dialysis bag, and dialyze in water 24h, remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate and dry to prepare polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer (PCTEF-g- PVIm); where, the grafting reaction is as follows:
S3、酞菁前驱体的制备:称取2.36g KH-560与5.73g酞菁钴加入反应瓶中,加入35mL四氢呋喃搅拌均匀,室温反应2h,蒸馏除去溶剂得到酞菁钴-KH560 前驱体;S3. Preparation of phthalocyanine precursor: Weigh 2.36g KH-560 and 5.73g cobalt phthalocyanine into the reaction bottle, add 35 mL tetrahydrofuran and stir evenly, react at room temperature for 2 hours, distill the solvent away to obtain the cobalt phthalocyanine-KH560 precursor;
S4、双极膜中间层水解离催化剂的制备:称取经过步骤S3获得的酞菁钴 -KH560前驱体8.09g与1.11g硅烷偶联剂KH540一起加入反应器中,同时加入 18mL乙醇、7.5mL蒸馏水和0.6mL乙酸,调节反应体系pH为3.0,在50℃条件下反应3h,得到KH-560改性酞菁钴硅溶胶作为双极膜中间层水解离催化剂;其中,反应如下所示:S4. Preparation of bipolar membrane intermediate layer water dissociation catalyst: Weigh 8.09g of cobalt phthalocyanine-KH560 precursor obtained in step S3 and add 1.11g of silane coupling agent KH540 into the reactor. At the same time, add 18mL of ethanol and 7.5mL of ethanol. Distilled water and 0.6 mL acetic acid, adjust the pH of the reaction system to 3.0, react at 50°C for 3 hours, and obtain KH-560 modified cobalt phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst; the reaction is as follows:
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上采用浸渍-提拉法喷涂KH-560改性酞菁钴硅溶胶,晾干后将经过步骤S2获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后阴面浸泡在碘甲烷四氢呋喃溶液中5h后取出,用蒸馏水洗净膜表面杂质,得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified cobalt phthalocyanine silica sol on the cation exchange membrane layer using the dipping and pulling method. After drying, cast the polychlorotrifluoroethylene-grafted vinylimidazole side chain copolymer obtained in step S2 onto the cation exchange membrane layer. On the exchange membrane layer, after drying, the negative side was soaked in methyl iodide and tetrahydrofuran solution for 5 hours, then taken out, and the impurities on the membrane surface were washed with distilled water to obtain a chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane.
实施例5Example 5
一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,括以下步骤:A method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, including the following steps:
S1、阳离子交换膜液的制备:称取10g聚三氟氯乙烯(共聚物含25%三氟氯乙烯)溶于120mL N,N-二甲基甲酰胺中,通氮气除氧,升温至110℃后加入 140.0苯乙烯磺酸钠、4.36g CuBr和10.76g五甲基二乙基三胺,在氮气保护下,在110℃条件下进行恒温磺化反应40h,将反应液透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);其中,接枝反应如实施例1所示:S1. Preparation of cation exchange membrane liquid: Weigh 10g of polychlorotrifluoroethylene (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of N,N-dimethylformamide, pass nitrogen to remove oxygen, and raise the temperature to 110 After adding 140.0 sodium styrene sulfonate, 4.36g CuBr and 10.76g pentamethyldiethyltriamine, perform a constant temperature sulfonation reaction at 110°C for 40 hours under nitrogen protection, put the reaction solution into a dialysis bag, and Dialyze against water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate, and dry to prepare polychlorotrifluoroethylene grafted sodium styrene sulfonate side chain copolymer ( PCTEF-g-PSSNa); wherein, the grafting reaction is as shown in Example 1:
S2、阴离子交换膜液的制备:称取10g聚三氟氯乙烯(共聚物含25%三氟氯乙烯)溶于120mL N,N-二甲基乙酰胺中,通氮气除氧,升温至80℃后加入 89.68g 2-乙基-4,5-二甲基-1-乙烯基咪唑、4.36gCuBr和10.56g五甲基二乙基三胺,在氮气保护下,恒温反应24h,将反应液装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);其中,接枝反应如下所示:S2. Preparation of anion exchange membrane liquid: Weigh 10g polychlorotrifluoroethylene (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL N,N-dimethylacetamide, purge nitrogen to remove oxygen, and raise the temperature to 80 89.68g 2-ethyl-4,5-dimethyl-1-vinylimidazole, 4.36g CuBr and 10.56g pentamethyldiethyltriamine were added at ℃, and the reaction was carried out at a constant temperature for 24 hours under nitrogen protection. Put it into a dialysis bag and dialyze it in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate and dry it to prepare polychlorotrifluoroethylene grafted vinyl imidazole Side chain copolymer (PCTEF-g-PVIm); where the grafting reaction is as follows:
S3、酞菁前驱体的制备:称取2.36g KH-560与5.70g酞菁钴加入反应瓶中,加入35mL异丙醇搅拌均匀,室温反应3h,蒸馏除去溶剂得到酞菁钴-KH560前驱体;S3. Preparation of phthalocyanine precursor: Weigh 2.36g KH-560 and 5.70g cobalt phthalocyanine into the reaction bottle, add 35 mL isopropyl alcohol, stir evenly, react at room temperature for 3 hours, and distill away the solvent to obtain cobalt phthalocyanine-KH560 precursor. ;
S4、双极膜中间层水解离催化剂的制备:称取经过步骤S3获得的酞菁钴 -KH560前驱体8.09g与1.11g硅烷偶联剂KH550一起加入反应器中,同时加入 18mL乙醇、7.5mL蒸馏水和0.6mL1.0%盐酸,调节反应体系pH为3.0,在50℃条件下反应1h,得到KH-560改性酞菁钴硅溶胶作为双极膜中间层水解离催化剂;其中,反应如下所示:S4. Preparation of bipolar membrane intermediate layer water dissociation catalyst: Weigh 8.09g of cobalt phthalocyanine-KH560 precursor obtained in step S3 and add 1.11g of silane coupling agent KH550 into the reactor. At the same time, add 18mL of ethanol and 7.5mL of ethanol. Distilled water and 0.6 mL 1.0% hydrochloric acid, adjust the pH of the reaction system to 3.0, react at 50°C for 1 hour, and obtain KH-560 modified cobalt phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst; where, the reaction is as follows Show:
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上采用气溶胶喷涂法喷涂KH-560改性酞菁钴硅溶胶,晾干后将经过步骤S2获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后阴面浸泡在碘甲烷四氢呋喃溶液中5h后取出,用蒸馏水洗净膜表面杂质,得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified cobalt phthalocyanine silica sol on the cation exchange membrane layer using the aerosol spraying method. After drying, the polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer obtained in step S2 is cast on the cation exchange membrane layer. On the membrane layer, after drying, the negative side was soaked in methyl iodide and tetrahydrofuran solution for 5 hours, then taken out, and the impurities on the membrane surface were washed with distilled water to obtain a chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane.
实施例6Example 6
一种主链碳氟-酞菁催化层耐碱双极膜的制备方法,括以下步骤:A method for preparing a main chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane, including the following steps:
S1、阳离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯)(共聚物含25%三氟氯乙烯)溶于120mL N-甲基吡咯烷酮中,通氮气除氧,升温至130℃后加入126.3苯乙烯磺酸钠、4.36g CuBr和4.76g联吡啶,在氮气保护下,在130℃条件下进行恒温磺化反应20h,将反应液倾入乙醇中,沉淀得接枝聚合物,沉淀物放入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物(PCTEF-g-PSSNa);其中,接枝反应如实施例1所示:S1. Preparation of cation exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of N-methylpyrrolidone, purge nitrogen to remove oxygen, and raise the temperature. After reaching 130°C, add 126.3 sodium styrene sulfonate, 4.36g CuBr and 4.76g bipyridine. Under nitrogen protection, perform a constant temperature sulfonation reaction at 130°C for 20 hours. Pour the reaction solution into ethanol and precipitate to obtain graft. Put the polymer and precipitate into a dialysis bag and dialyze in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; collect the solution in the dialysis bag, concentrate, and dry to prepare polychlorotrifluoroethylene. Grafting sodium styrene sulfonate side chain copolymer (PCTEF-g-PSSNa); wherein, the grafting reaction is as shown in Example 1:
S2、阴离子交换膜液的制备:称取10g聚(偏氟乙烯-三氟氯乙烯)(共聚物含25%三氟氯乙烯)溶于120mL二甲亚砜中,通氮气除氧,升温至80℃后加入89.68g 5-乙基-2,4-二甲基-1-乙烯基咪唑、4.36gCuBr和10.56g五甲基二乙基三胺,在氮气保护下,恒温反应18h,将反应液装入透析袋中,在水透析24h,除去铜离子、溴离子和联吡啶和未反应的单体;收集透析袋中溶液、浓缩、烘干,制得聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物(PCTEF-g-PVIm);其中,接枝反应如下所示:S2. Preparation of anion exchange membrane liquid: Weigh 10g of poly(vinylidene fluoride-chlorotrifluoroethylene) (the copolymer contains 25% chlorotrifluoroethylene) and dissolve it in 120 mL of dimethyl sulfoxide, pass nitrogen to remove oxygen, and heat to After 80°C, add 89.68g 5-ethyl-2,4-dimethyl-1-vinylimidazole, 4.36g CuBr and 10.56g pentamethyldiethyltriamine, and react at a constant temperature for 18 hours under nitrogen protection. The solution is put into a dialysis bag and dialyzed in water for 24 hours to remove copper ions, bromide ions, bipyridyl and unreacted monomers; the solution in the dialysis bag is collected, concentrated and dried to prepare polychlorotrifluoroethylene grafted vinyl. Imidazole side chain copolymer (PCTEF-g-PVIm); where, the grafting reaction is as follows:
S3、酞菁前驱体的制备:称取2.36g KH-560与5.70g酞菁铁加入反应瓶中,加入30mL无水甲醇搅拌均匀,室温反应2h,蒸馏除去溶剂得到酞菁铁-KH560 前驱体;S3. Preparation of phthalocyanine precursor: Weigh 2.36g KH-560 and 5.70g iron phthalocyanine into the reaction bottle, add 30 mL anhydrous methanol, stir evenly, react at room temperature for 2 hours, and distill away the solvent to obtain iron phthalocyanine-KH560 precursor. ;
S4、双极膜中间层水解离催化剂的制备:称取经过步骤S3获得的酞菁铁 -KH560前驱体8.06g与0.90g硅烷偶联剂KH540一起加入反应器中,同时加入 18mL乙醇、7.5mL蒸馏水和0.6mL1.0%盐酸,调节反应体系pH为3.5,在50℃条件下反应1h,得到KH-560改性酞菁铁硅溶胶作为双极膜中间层水解离催化剂;其中,反应如下所示:S4. Preparation of bipolar membrane intermediate layer water dissociation catalyst: Weigh 8.06g of the iron phthalocyanine-KH560 precursor obtained in step S3 and add 0.90g of silane coupling agent KH540 into the reactor. At the same time, add 18mL of ethanol and 7.5mL of ethanol. Distilled water and 0.6 mL 1.0% hydrochloric acid, adjust the pH of the reaction system to 3.5, react at 50°C for 1 hour, and obtain KH-560 modified iron phthalocyanine silica sol as a bipolar membrane intermediate layer water dissociation catalyst; where, the reaction is as follows Show:
S5、双极膜的制备:将经过步骤S1制得的聚三氟氯乙烯接枝苯乙烯磺酸钠侧链共聚物溶液流延在结净的玻璃板上,烘干制备阳离子交换膜层,在阳离子交换膜层上采用静电喷射法喷涂KH-560改性酞菁钴硅溶胶,晾干后将经过步骤 S2获得的聚三氟氯乙烯接枝乙烯基咪唑侧链共聚物流延于阳离子交换膜层上,烘干后阴面浸泡在碘甲烷四氢呋喃溶液中5h后取出,用蒸馏水洗净膜表面杂质,得到链碳氟-酞菁催化层耐碱双极膜。S5. Preparation of bipolar membrane: Cast the polychlorotrifluoroethylene-grafted sodium styrene sulfonate side chain copolymer solution prepared in step S1 on a clean glass plate, and dry it to prepare a cation exchange membrane layer. Spray KH-560 modified cobalt phthalocyanine silica sol on the cation exchange membrane layer using electrostatic spraying. After drying, the polychlorotrifluoroethylene grafted vinyl imidazole side chain copolymer obtained in step S2 is cast on the cation exchange membrane. After drying, the negative side was soaked in methyl iodide and tetrahydrofuran solution for 5 hours, then taken out, and the impurities on the membrane surface were washed with distilled water to obtain a chain fluorocarbon-phthalocyanine catalytic layer alkali-resistant bipolar membrane.
实施例7Example 7
与上述实施例不同之处在于:The difference from the above embodiment is:
所述步骤S2中含咪唑基单体还可以为2,4,5-三甲基-1-乙烯基咪唑、4-乙基 -2,5-二甲基-1-乙烯基咪唑、2-丙基-4,5-二甲基-1-乙烯基咪唑、4-丙基-2,5-二甲基 -1-乙烯基咪唑、2-丁基-4,5-二甲基-1-乙烯基咪唑、4-丁基-2,5-二甲基-1-乙烯基咪唑、2,4-二乙基-5-甲基-1-乙烯基咪唑、4,5-二乙基-2-甲基-1-乙烯基咪唑、2,4- 二丁基-5-甲基-1-乙烯基咪唑、4,5-二丁基-2-甲基-1-乙烯基咪唑中的任意一种。The imidazole group-containing monomer in step S2 can also be 2,4,5-trimethyl-1-vinylimidazole, 4-ethyl-2,5-dimethyl-1-vinylimidazole, 2- Propyl-4,5-dimethyl-1-vinylimidazole, 4-propyl-2,5-dimethyl-1-vinylimidazole, 2-butyl-4,5-dimethyl-1 -Vinylimidazole, 4-butyl-2,5-dimethyl-1-vinylimidazole, 2,4-diethyl-5-methyl-1-vinylimidazole, 4,5-diethyl -2-Methyl-1-vinylimidazole, 2,4-dibutyl-5-methyl-1-vinylimidazole, 4,5-dibutyl-2-methyl-1-vinylimidazole any kind.
所述步骤S3中氨基酞菁为含过渡金属氨基酞菁,除了酞菁铁、酞菁钴和酞菁铜,还可选择Mg、Ba、Sc、Ti、V、Cr、Mn、Ni或Zn中的任意一种。The amino phthalocyanine in step S3 is a transition metal-containing amino phthalocyanine. In addition to iron phthalocyanine, cobalt phthalocyanine and copper phthalocyanine, Mg, Ba, Sc, Ti, V, Cr, Mn, Ni or Zn can also be selected. any kind.
以上所述实施例均为本发明较佳的实施方式,但本发明的实施方式并不受上述实施例的限制,其它的任何未背离本专利的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本专利的保护范围之内。The above-mentioned embodiments are all preferred embodiments of the present invention, but the embodiments of the present invention are not limited by the above-mentioned embodiments. Any other changes, modifications, and substitutions may be made without departing from the spirit and principles of this patent. , combination, simplification, should all be equivalent replacement methods, and are all included in the protection scope of this patent.
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