CN110690486A - Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure - Google Patents
Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure Download PDFInfo
- Publication number
- CN110690486A CN110690486A CN201911079021.6A CN201911079021A CN110690486A CN 110690486 A CN110690486 A CN 110690486A CN 201911079021 A CN201911079021 A CN 201911079021A CN 110690486 A CN110690486 A CN 110690486A
- Authority
- CN
- China
- Prior art keywords
- hours
- polymer
- membrane
- cross
- flexible long
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G61/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G61/02—Macromolecular compounds containing only carbon atoms in the main chain of the macromolecule, e.g. polyxylylenes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/103—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
- H01M8/1072—Polymeric electrolyte materials characterised by the manufacturing processes by chemical reactions, e.g. insitu polymerisation or insitu crosslinking
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
- H01M8/1018—Polymeric electrolyte materials
- H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
- H01M8/1086—After-treatment of the membrane other than by polymerisation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/10—Definition of the polymer structure
- C08G2261/12—Copolymers
- C08G2261/122—Copolymers statistical
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/10—Definition of the polymer structure
- C08G2261/14—Side-groups
- C08G2261/146—Side-chains containing halogens
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2261/00—Macromolecular compounds obtained by reactions forming a carbon-to-carbon link in the main chain of the macromolecule
- C08G2261/30—Monomer units or repeat units incorporating structural elements in the main chain
- C08G2261/31—Monomer units or repeat units incorporating structural elements in the main chain incorporating aromatic structural elements in the main chain
- C08G2261/312—Non-condensed aromatic systems, e.g. benzene
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M2008/1095—Fuel cells with polymeric electrolytes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Abstract
The invention provides a preparation method of a cross-linking type alkaline anion membrane based on a flexible long side chain multi-cation structure, belonging to the field of fuel cell anion exchange membrane materials. The alkaline anion-exchange membrane is prepared by reacting a halogenated polycation cross-linking agent with a biphenyl polymer through a Moxiujin reaction, and comprises four steps of polymer main chain synthesis, polymer membrane main chain ionization, membrane casting and alkali treatment. The method is simple, the formation of a hydrophilic and hydrophobic micro-phase separation structure is promoted by a multi-cation structure, the water absorption swelling of the membrane is inhibited by the flexible long-side chain crosslinking structure, the mechanical performance of the membrane is improved on the basis of ensuring the conductivity, so that the contradiction between the conductivity and the mechanical strength is relieved, and the alkali stability of the ion exchange membrane can be improved.
Description
Technical Field
The invention belongs to the field of fuel cell anion exchange membrane materials, and relates to a preparation method of a cross-linking type alkaline anion membrane based on a flexible long side chain multi-cation structure.
Background
At present, energy shortage and environmental pollution have become the two most important problems facing the present society, and fuel cells are receiving wide attention from all countries as a new clean energy source. Alkaline polymer fuel cells have been rapidly developed by virtue of their fast reaction kinetics, the ability to use non-noble metal catalysts, no carbonate crystallization, low fuel permeation rates, and the like.
However, the commercialization of alkaline polymer fuel cells is still faced with many challenges, and the alkaline anion-exchange membrane as a key material has two major problems of low conductivity and poor chemical stability in alkaline environment. Therefore, how to improve the chemical stability and conductivity of the anionic membrane becomes a problem to be solved urgently.
As a traditional ion exchange group, the SN generated by quaternary ammonium salt under the condition of high temperature and alkali2In recent years, electrolyte membranes containing novel ionic groups such as imidazole, morpholine, guanidino, pyrrolidine and the like have attracted interest.
In contrast, in recent years, Kreuer et al found that 6-membered aliphatic heterocyclyl cationic piperidines exhibit high resistance to nucleophilic substitution and elimination under basic conditions and high temperatures. The authors attribute this to a high transition state energy and low ring strain of the piperidine structure in the degradation reaction, and thus are more stable in alkaline environments.
Disclosure of Invention
Aiming at the two problems of the anion membrane, the invention provides a novel anion exchange membrane for an alkaline fuel cell and a preparation method thereof, wherein a piperidine ring and quaternary ammonium salt cations with excellent alkali stability are used as ionizing reagents, a polymer without heteroatoms in a framework is used as an ion exchange membrane main chain, and an ion exchange membrane with a multi-cation structure is prepared.
In order to achieve the purpose, the invention adopts the technical scheme that:
a preparation method of a cross-linking type basic anion membrane based on a flexible long side chain polycation structure comprises the steps of firstly reacting an anaerobic structure containing biphenyl and the like with N-methyl piperidone and 1,1, 1-trifluoroacetone to obtain a first-step product, then reacting with excessive large-volume halide to obtain an ionized polymer, and preparing the anion exchange membrane by a casting method. The preparation process comprises the steps of synthesizing a polymer main chain, ionizing the polymer film main chain, casting a film and treating alkali. The method comprises the following specific steps:
(1) copolymerization synthesis of copolymerized biphenyl class oxygen-free main chain
Dissolving biphenyl substances into a solvent A, and adding a mixed reagent under the protection of nitrogen atmosphere. And then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, and reacting for 2-5 h under ice bath. The reaction mixture was poured into a precipitant to precipitate, and dried in vacuo to give a polymer: copolymerized biphenyls oxygen-free backbones. The molar ratio of the biphenyl substances, the solvent A and the catalyst is 1: 200-240: 9 to 10. The mixed reagent consists of N-methyl piperidone and 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone, wherein the molar ratio of the N-methyl piperidone to the 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone is 1: 0 to 1; the degree of functionalization of the polymer is controlled by controlling the addition amount of 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone, and the degree of substitution of the polymer is in the range of 0.3-1 mmol-g-1。
The molar ratio of trifluoroacetic acid to trifluoromethanesulfonic acid in the catalyst of step (1) is 1: 6-8.
The biphenyl substances in the step (1) comprise biphenyl and m-terphenyl.
The solvent A in the step (1) can be dichloromethane. The precipitant is ethyl acetate and petroleum ether.
The temperature of the vacuum drying in the step (1) is 40-100 ℃, and the time is 12-48 hours;
(2) preparation of ionizing Agents
Firstly, adding diamine substances into solvent ethanol, and preparing a co-solution with the volume fraction of 2-6%. Secondly, adding a dibromo substance into the co-solution dropwise, stirring the obtained solution at 0-4 ℃ for 8-12 hours, and keeping the solution at 50 ℃ for 3-8 hours, wherein 22mL of the dibromo substance is added to every 2mL of diamine substance. And thirdly, pouring the reacted solution into a precipitator, cooling to 0-4 ℃, and placing in a refrigerator for 12 hours to precipitate the product. Finally, the crude product was collected by vacuum absorption and washed with a precipitant to remove unreacted monomers, and after vacuum drying at 30 ℃ for 12 hours, a crosslinking agent for ionization reaction was obtained. The diamine substance in the step (2) comprises butanediamine and pentanediamine.
The dibromo-class substance in the step (2) comprises 1, 4-dibromobutane and 1, 5-dibromopentane.
The precipitant in the step (2) comprises petroleum ether and ethyl acetate.
(3) And (2) ionizing the main chain of the polymer film, dissolving the copolymerized biphenyl oxygen-free main chain obtained in the step (1) in an organic solvent, adding an ionizing reagent obtained in the step (2) as a cross-linking agent, and performing an ionizing reaction for 3-24 hours at the temperature of 40-80 ℃. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.5 to 2.
The organic solvent in the step (3) can be N, N-dimethylformamide and N-methylpyrrolidone.
(4) Cast film
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 12-36 hours at the temperature of 60-80 ℃.
(5) Alkali treatment to obtain anion exchange membrane
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The cross-linking type alkaline anion-exchange membrane based on the flexible long-side-chain polycation structure is applied to the field of fuel cells, and is prepared by reacting a halogenated polycation cross-linking agent with a biphenyl polymer through a Moxiujin reaction.
The biphenyl polymer is a biphenyl anaerobic main chain and a m-terphenyl anaerobic main chain, and the substitution degree range of the polymer is 0.3-1 mmol/g-1. It is composed ofThe structural formula is as follows:
the invention has the beneficial effects that:
(1) the piperidine structure enhances the alkali resistance of the anionic membrane due to the high transition state energy and low ring strain of its degradation reaction; the oxygen-free main chain does not contain electron-withdrawing groups such as ether bond and the like, so that OH is reduced-The attack of the ion exchange membrane improves the alkali stability of the ion exchange membrane;
(2) the formation of a hydrophilic and hydrophobic micro-phase separation structure is promoted by the multi-cation structure, the flexible long-side chain crosslinking structure inhibits the water absorption swelling of the membrane, the anion exchange membrane with high substitution degree is prepared, the mechanical property of the membrane is improved on the basis of ensuring the conductivity, and thus the contradiction between the conductivity and the mechanical strength is relieved.
Drawings
FIG. 1 shows FT-IR spectrum and chemical structure of the ion exchange membrane after ionization in example 1. In the spectrogram: the abscissa is the wavenumber and the ordinate is the intensity.
FIG. 2 is a graph of H for the first step product copolymerization of oxygen free backbone polymers1NMR spectrum with chemical shift value ppm on the abscissa.
FIG. 3 shows H of an ionic liquid1NMR spectrum with chemical shift value ppm on the abscissa.
Detailed Description
The method for producing a crosslinked anionic membrane according to the present invention will be described in further detail below with reference to examples.
Example 1
(1) Copolymerized synthetic polymer backbone
2.5g of biphenyl was dissolved in 6mL of dichloromethane, and the mixture was added under nitrogen atmosphere in a molar ratio of 1: 0N-methyl piperidone and 1,1, 1-trifluoroacetone, wherein the volume of N-methyl piperidone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 6, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 2h in ice bath. Mixing the reactionThe product is poured into 1M NaOH precipitant for precipitation, washed to be neutral by deionized water, and dried in vacuum at 40 ℃ for 48 hours to obtain a polymer: copolymerization of bigeminal oxygen-free backbone with a degree of functionalization of 1mmol g-1。
(2) Preparation of ionizing Agents
2mL of butanediamine was added to ethanol to form a 2% dropwise co-solution, followed by dropwise addition of 22mL of 1, 4-dibromobutane. The solution obtained above was stirred at 0 ℃ for 12 hours and kept at 50 ℃ for 3 hours. The resulting solution was poured into petroleum ether (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with petroleum ether to remove unreacted monomers. Vacuum drying at 30 deg.C for 12 hr to obtain the crosslinking reagent 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecylbromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N, N-dimethylformamide, adding 2.1g of 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecyl bromide ionizing reagent obtained in the step (2) as a crosslinking agent, and carrying out an ionization reaction at 40 ℃ for 24 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.5, wherein the amount of the polymer was 0.2 g.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 41.6 percent, the swelling rate is 19.7 percent, and the hydroxyl conductivity at 30 ℃ is 55.6 mS/cm.
Example 2
(1) Copolymerized synthetic polymer backbone
2.5g of biphenylene were dissolved in 6mL of dichloromethane under nitrogenAdding the mixture according to a molar ratio of 1: 1 and 1,1, 1-trifluoroacetone, wherein the volume of the N-methylpiperidinone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 7, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 3.5h in ice bath. The reaction mixture was poured into 1M NaOH solution for precipitation, washed to neutrality with deionized water, and vacuum dried at 70 ℃ for 30 hours to give polymer: copolymerized biphenyl oxygen-free main chain with the degree of functionalization of 0.5 mmol/g-1。
(2) Preparation of ionizing Agents
2mL of butanediamine was added to ethanol to form a 4% dropwise co-solution, and 22mL of a 1, 4-dibromobutane substance was added dropwise. The solution obtained above was stirred at 0 ℃ for 10 hours and kept at 50 ℃ for 5.5 hours. The resulting solution was poured into petroleum ether (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with petroleum ether to remove unreacted monomers. Vacuum drying at 30 deg.C for 12 hr to obtain the crosslinking reagent 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecylbromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N, N-dimethylformamide, adding 2.1g of 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecyl bromide ionizing reagent obtained in the step (2) as a crosslinking agent, and carrying out an ionization reaction at 60 ℃ for 13.5 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.75, wherein the polymer is 0.2 g.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 40.8 percent, the swelling rate is 18.6 percent, and the hydroxyl conductivity at 30 ℃ is 55.3 mS/cm.
Example 3
(1) Copolymerized synthetic polymer backbone
2.5g of biphenyl was dissolved in 6mL of dichloromethane, and the mixture was added under nitrogen atmosphere in a molar ratio of 1: 3 and 1,1, 1-trifluoroacetone, wherein the volume of the N-methylpiperidinone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 8, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 5h in ice bath. The reaction mixture was poured into 1M NaOH precipitant for precipitation, washed to neutrality with deionized water, and vacuum dried at 100 ℃ for 12 hours to give a polymer: copolymerized biphenyl oxygen-free main chain with the functionalization degree of 0.3 mmol/g-1。
(2) Preparation of ionizing Agents
2mL of butanediamine was added to ethanol to form a co-solution with a drop volume fraction of 6%, and 22mL of a 1, 4-dibromobutane substance was added dropwise. The solution obtained above was stirred at 0 ℃ for 8 hours and kept at 50 ℃ for another 8 hours. The resulting solution was poured into petroleum ether (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with petroleum ether to remove unreacted monomers. Vacuum drying at 30 deg.C for 12 hr to obtain the crosslinking reagent 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecylbromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N, N-dimethylformamide, adding 2.1g of 1, 14-dibromo-5, 10- (N, N-dimethylammonium) tetradecyl bromide ionizing reagent obtained in the step (2) as a crosslinking agent, and carrying out an ionization reaction at 80 ℃ for 3 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 2. of these, 0.2g of a polymer was used.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 51.6 percent, the swelling rate is 26.7 percent, and the hydroxyl conductivity at 30 ℃ is 65.6 mS/cm.
Example 4
(1) Copolymerized synthetic polymer backbone
3.8g of m-terphenyl is dissolved in 6mL of dichloromethane, and a mixture of m-terphenyl and dichloromethane is added under the protection of nitrogen in a molar ratio of 1: 0N-methyl piperidone and 1,1, 1-trifluoroacetone, wherein the volume of N-methyl piperidone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 6, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 2h in ice bath. The reaction mixture was poured into 1M NaOH precipitant for precipitation, washed to neutrality with deionized water, and vacuum dried at 40 ℃ for 48 hours to give a polymer: copolymerized meta-terphenyls have oxygen-free backbones. The degree of functionalization is 1mmol g-1。
(2) Preparation of ionizing Agents
2mL of pentanediamine was added to ethanol to form a co-solution with a drop volume fraction of 6%, and 22mL of 1, 5-dibromopentane was added dropwise. The solution obtained above was stirred at 4 ℃ for 8 hours and kept at 50 ℃ for another 8 hours. The resulting solution was poured into ethyl acetate (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with ethyl acetate to remove unreacted monomers. Vacuum drying at 30 deg.c for 12 hr to obtain the cross-linking reagent 1, 17-dibromo-6, 12- (N, N-dimethylammonium) heptadecane bromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N-methylpyrrolidone, adding 2.2g of 1, 17-dibromo-6, 12- (N, N-dimethylammonium) heptadecane bromide ionizing reagent obtained in the step (2) as a cross-linking agent, and carrying out an ionization reaction at 40 ℃ for 24 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.5. of these, 0.2g of a polymer was used.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 88.7 percent, the swelling rate is 40.1 percent, and the hydroxyl conductivity at 30 ℃ is 70.8 mS/cm.
Example 5
(1) Copolymerized synthetic polymer backbone
3.8g of m-terphenyl is dissolved in 6mL of dichloromethane, and a mixture of m-terphenyl and dichloromethane is added under the protection of nitrogen in a molar ratio of 1: 1 and 1,1, 1-trifluoroacetone, wherein the volume of the N-methylpiperidinone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 8, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 3.5h in ice bath. The reaction mixture was poured into 1M NaOH precipitant for precipitation, washed to neutrality with deionized water, and vacuum dried at 70 ℃ for 30 hours to give a polymer: copolymerized meta-terphenyls have oxygen-free backbones. The degree of functionalization is 0.5 mmol/g-1。
(2) Preparation of ionizing Agents
2mL of pentanediamine was added to ethanol to form a 4% dropwise co-solution, followed by dropwise addition of 22mL of the 1, 4-dibromobutane material. The solution obtained above was stirred at 0 ℃ for 10 hours and kept at 50 ℃ for 5.5 hours. The resulting solution was poured into ethyl acetate (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with ethyl acetate to remove unreacted monomers. Vacuum drying at 30 deg.c for 12 hr to obtain the crosslinking reagent 1, 15-dibromo-6, 12- (N, N-dimethylammonium) pentadecane bromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N-methylpyrrolidone, adding 1.9g of 1, 15-dibromo-6, 12- (N, N-dimethylammonium) pentadecane bromide ionizing reagent obtained in the step (2) as a cross-linking agent, and carrying out an ionization reaction at 60 ℃ for 13.5 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.75. of these, 0.2g of a polymer was used.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 54.2 percent, the swelling rate is 24.1 percent, and the hydroxyl conductivity at 30 ℃ is 65.6 mS/cm.
Example 6
(1) Copolymerized synthetic polymer backbone
3.8g of m-terphenyl is dissolved in 6mL of dichloromethane, and a mixture of m-terphenyl and dichloromethane is added under the protection of nitrogen in a molar ratio of 1: 3 and 1,1, 1-trifluoroacetone, wherein the volume of the N-methylpiperidinone is 1.2 mL. Then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, wherein the molar ratio of the trifluoroacetic acid to the trifluoromethanesulfonic acid is 1: 8, wherein, the trifluoroacetic acid is 1.8 mL. The reaction was carried out for 5h in ice bath. The reaction mixture was poured into 1M NaOH precipitant for precipitation, washed to neutrality with deionized water, and vacuum dried at 100 ℃ for 12 hours to give a polymer: copolymerized meta-terphenyls have oxygen-free backbones. The degree of functionalization is 0.3 mmol/g-1。
(2) Preparation of ionizing Agents
2mL of pentanediamine was added to ethanol to form a co-solution with a drop volume fraction of 6%, and 22mL of 1, 5-dibromopentane was added dropwise. The solution obtained above was stirred at 0 ℃ for 8 hours and kept at 50 ℃ for another 8 hours. The resulting solution was poured into ethyl acetate (500mL) and cooled to 0 ℃ and left in a refrigerator for 12 hours to precipitate the product. Then, the crude product was collected by vacuum absorption and washed three times with ethyl acetate to remove unreacted monomers. Vacuum drying at 30 deg.c for 12 hr to obtain the cross-linking reagent 1, 17-dibromo-6, 12- (N, N-dimethylammonium) heptadecane bromide for ionization reaction.
(3) Ionization of polymer membrane backbone
Dissolving 2g of biphenyl oxygen-free main chain obtained in the step (1) in N-methylpyrrolidone, adding 2.2g of 1, 17-dibromo-6, 12- (N, N-dimethylammonium) heptadecane bromide ionizing reagent obtained in the step (2) as a cross-linking agent, and carrying out an ionization reaction at 80 ℃ for 3 hours. The molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 2. of these, 0.2g of a polymer was used.
(4) Casting membrane, alkali treatment to obtain anion exchange membrane
And (4) placing the reaction mixture prepared in the step (3) on a glass plate to be cast into a film or cast into a film, and standing for 36 hours at the temperature of 60 ℃.
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
The water absorption rate of the prepared anion exchange membrane at room temperature is 88.6 percent, the swelling rate is 37.4 percent, and the hydroxyl conductivity at 30 ℃ is 76.8 mS/cm.
The above-mentioned embodiments only express the embodiments of the present invention, but not should be understood as the limitation of the scope of the invention patent, it should be noted that, for those skilled in the art, many variations and modifications can be made without departing from the concept of the present invention, and these all fall into the protection scope of the present invention.
Claims (8)
1. A preparation method of a cross-linking type basic anionic membrane based on a flexible long side chain polycation structure is characterized by comprising the following steps:
(1) copolymerization synthesis of copolymerized biphenyl class oxygen-free main chain
Dissolving biphenyl substances in a solvent A, and adding a mixed reagent under the protection of nitrogen atmosphere; then adding trifluoroacetic acid and trifluoromethanesulfonic acid as catalysts, and reacting for 2-5 h under ice bath; the reaction mixture was poured into a precipitant to precipitate, and dried in vacuo to give a polymer: a copolymerized biphenyl oxygen-free backbone; the molar ratio of the biphenyl substances, the solvent A and the catalyst is 1: 200-240: 9-10; the mixed reagent consists of N-methyl piperidone and 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone, wherein the molar ratio of the N-methyl piperidone to the 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone is 1: 0 to 1; the degree of polymer functionalization is controlled by controlling the addition amount of 1,1, 1-trifluoroacetone or 1,1, 1-trifluoroacetophenone;
(2) preparation of ionizing Agents
Firstly, adding butanediamine or pentanediamine into ethanol serving as a solvent, and preparing a co-solution with the volume fraction of 2-6%; secondly, dropwise adding 1, 4-dibromobutane or 1, 5-dibromopentane into the co-solution, stirring the obtained solution at 0-4 ℃ for 8-12 hours, and keeping the solution at 50 ℃ for 3-8 hours; thirdly, pouring the reacted solution into a precipitator, cooling to 0-4 ℃, standing in a refrigerator and precipitating a product; finally, collecting the crude product through vacuum absorption, washing the crude product with a precipitator to remove unreacted monomers, and drying the crude product in vacuum to obtain a crosslinking reagent for an ionization reaction;
(3) ionizing the main chain of the polymer film, dissolving the copolymerized biphenyl oxygen-free main chain obtained in the step (1) in an organic solvent, adding the ionizing reagent obtained in the step (2) as a cross-linking agent, and performing an ionizing reaction for 3-24 hours at 40-80 ℃; the molar ratio of the polymer to the organic solvent to the ionizing agent is 1: 10: 1.5-2;
(4) cast film
Placing the reaction mixture prepared in the step (3) on a glass plate to form a film by casting or tape casting;
(5) alkali treatment to obtain anion exchange membrane
And stripping the obtained anion exchange membrane from the surface of the glass plate, soaking in 1.0M alkali solution for 24 hours, and washing off free ions on the surface of the membrane to obtain the anion exchange membrane.
2. The method for preparing the cross-linked basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the molar ratio of trifluoroacetic acid to trifluoromethanesulfonic acid in the catalyst in step (1) is 1: 6-8.
3. The method for preparing the cross-linked basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the biphenyl substances in the step (1) comprise biphenyl and m-terphenyl.
4. The method for preparing the cross-linked basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the solvent A in the step (1) can be dichloromethane.
5. The method for preparing the cross-linking type basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the temperature of the vacuum drying in the step (1) is 40-100 ℃, and the time is 12-48 hours.
6. The method for preparing the cross-linking type basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein in the step (2), 22mL of dibromo-class substance is added for every 2mL of diamine-type substance.
7. The method for preparing the cross-linking type basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the temperature of the vacuum drying in the step (2) is 30 ℃ and the time is 12 hours.
8. The method for preparing the cross-linking type basic anionic membrane based on the flexible long-side chain polycation structure according to claim 1, wherein the precipitating agent in the step (2) and the step (1) comprises petroleum ether and ethyl acetate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911079021.6A CN110690486A (en) | 2019-11-07 | 2019-11-07 | Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911079021.6A CN110690486A (en) | 2019-11-07 | 2019-11-07 | Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure |
Publications (1)
Publication Number | Publication Date |
---|---|
CN110690486A true CN110690486A (en) | 2020-01-14 |
Family
ID=69115560
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201911079021.6A Withdrawn CN110690486A (en) | 2019-11-07 | 2019-11-07 | Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110690486A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111921566A (en) * | 2020-09-08 | 2020-11-13 | 长春工业大学 | Polyarylpiperidine type anion exchange membrane and preparation method and application thereof |
CN112778558A (en) * | 2021-02-05 | 2021-05-11 | 长春工业大学 | Polyether bond-free anion exchange membrane of polyarylpiperidine for fuel cell and preparation method thereof |
CN112980187A (en) * | 2021-04-09 | 2021-06-18 | 陕西国防工业职业技术学院 | Long-side-chain cross-linked polysulfone anion-exchange membrane and preparation method thereof |
CN113372596A (en) * | 2021-05-28 | 2021-09-10 | 西安交通大学 | Alkaline anion exchange membrane based on chemical crosslinking and preparation method thereof |
CN113471498A (en) * | 2021-07-07 | 2021-10-01 | 长春工业大学 | Multi-quaternary ammonium side long-chain type polysulfone anion-exchange membrane and preparation method thereof |
CN113871671A (en) * | 2021-09-24 | 2021-12-31 | 长春工业大学 | Preparation method of multi-cation cross-linked anion exchange membrane |
CN113956445A (en) * | 2021-11-26 | 2022-01-21 | 合肥工业大学 | Cationic polymer containing branched structure and preparation method and application thereof |
CN114634650A (en) * | 2020-12-15 | 2022-06-17 | 中国科学院大连化学物理研究所 | Alkaline polymer electrolyte membrane and preparation and application thereof |
WO2024055284A1 (en) * | 2022-09-16 | 2024-03-21 | 深圳华大生命科学研究院 | Ion cross-linked biomimetic membrane, preparation method therefor, and use thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019068051A2 (en) * | 2017-09-28 | 2019-04-04 | Yushan Yan | Poly(aryl piperidinium) polymers including those with stable cationic pendant groups for use as anion exchange membranes and ionomers |
CN109687003A (en) * | 2018-11-29 | 2019-04-26 | 大连理工大学 | A kind of cross-linking type alkaline anionic membrane and preparation method thereof based on piperidines |
CN110041519A (en) * | 2019-05-05 | 2019-07-23 | 大连理工大学 | A kind of long-chain branch poly (arylene ether nitrile) anion-exchange membrane and preparation method thereof |
-
2019
- 2019-11-07 CN CN201911079021.6A patent/CN110690486A/en not_active Withdrawn
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019068051A2 (en) * | 2017-09-28 | 2019-04-04 | Yushan Yan | Poly(aryl piperidinium) polymers including those with stable cationic pendant groups for use as anion exchange membranes and ionomers |
CN109687003A (en) * | 2018-11-29 | 2019-04-26 | 大连理工大学 | A kind of cross-linking type alkaline anionic membrane and preparation method thereof based on piperidines |
CN110041519A (en) * | 2019-05-05 | 2019-07-23 | 大连理工大学 | A kind of long-chain branch poly (arylene ether nitrile) anion-exchange membrane and preparation method thereof |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111921566A (en) * | 2020-09-08 | 2020-11-13 | 长春工业大学 | Polyarylpiperidine type anion exchange membrane and preparation method and application thereof |
CN111921566B (en) * | 2020-09-08 | 2022-11-01 | 长春工业大学 | Polyarylpiperidine type anion exchange membrane and preparation method and application thereof |
CN114634650A (en) * | 2020-12-15 | 2022-06-17 | 中国科学院大连化学物理研究所 | Alkaline polymer electrolyte membrane and preparation and application thereof |
CN112778558A (en) * | 2021-02-05 | 2021-05-11 | 长春工业大学 | Polyether bond-free anion exchange membrane of polyarylpiperidine for fuel cell and preparation method thereof |
CN112980187A (en) * | 2021-04-09 | 2021-06-18 | 陕西国防工业职业技术学院 | Long-side-chain cross-linked polysulfone anion-exchange membrane and preparation method thereof |
CN112980187B (en) * | 2021-04-09 | 2023-03-14 | 陕西国防工业职业技术学院 | Long side chain cross-linked polysulfone anion-exchange membrane and preparation method thereof |
CN113372596A (en) * | 2021-05-28 | 2021-09-10 | 西安交通大学 | Alkaline anion exchange membrane based on chemical crosslinking and preparation method thereof |
CN113372596B (en) * | 2021-05-28 | 2023-12-15 | 西安交通大学 | Alkaline anion exchange membrane based on chemical crosslinking and preparation method thereof |
CN113471498A (en) * | 2021-07-07 | 2021-10-01 | 长春工业大学 | Multi-quaternary ammonium side long-chain type polysulfone anion-exchange membrane and preparation method thereof |
CN113871671A (en) * | 2021-09-24 | 2021-12-31 | 长春工业大学 | Preparation method of multi-cation cross-linked anion exchange membrane |
CN113956445A (en) * | 2021-11-26 | 2022-01-21 | 合肥工业大学 | Cationic polymer containing branched structure and preparation method and application thereof |
CN113956445B (en) * | 2021-11-26 | 2024-04-19 | 合肥工业大学 | Cationic polymer containing branched structure and preparation method and application thereof |
WO2024055284A1 (en) * | 2022-09-16 | 2024-03-21 | 深圳华大生命科学研究院 | Ion cross-linked biomimetic membrane, preparation method therefor, and use thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110690486A (en) | Preparation method of crosslinking type alkaline anionic membrane based on flexible long-side-chain multi-cation structure | |
CN110862516B (en) | Cardo structure-containing isatin aromatic hydrocarbon copolymer, and preparation method and application thereof | |
CN110690487B (en) | Preparation method of basic anion membrane based on branched anaerobic main chain | |
CN113956445B (en) | Cationic polymer containing branched structure and preparation method and application thereof | |
CN108530660B (en) | A kind of quaternized polyfluorene ether ketone compound of local dense and preparation method thereof | |
CN112851932B (en) | Multi-cation side chain type anion exchange membrane prepared based on soft template method and preparation method thereof | |
CN109096473B (en) | Aromatic piperidine amphoteric ion exchange membrane without aryl ether bond and preparation method thereof | |
CN109306151B (en) | Ether-oxygen-bond-free polymer anion exchange membrane and preparation method thereof | |
CN105906812A (en) | Novel block anion exchange membrane and preparation method thereof | |
CN113621131A (en) | Polyelectrolyte material, preparation method thereof and polyelectrolyte membrane | |
CN107573501A (en) | A kind of cross-linking fluorine-containing sulfonated polyether compound and preparation method thereof | |
CN114133555A (en) | Preparation method of cross-linked fluorine-containing polyfluorene ether anion exchange membrane | |
WO2016029735A1 (en) | Amphoteric ion exchange membrane and preparation method therefor | |
CN111732717A (en) | Polymer containing polyaryl piperidyl side chain, preparation method thereof, anion exchange membrane and preparation method thereof | |
CN114230831A (en) | Preparation method of cross-linked anion exchange membrane with high oxidation stability and high ionic conductivity | |
KR102022676B1 (en) | Anion Exchange Membrane with Large Size Ionic Channel for Non-aqueous Vanadium Redox Flow Battery and preparation method thereof | |
CN117304536A (en) | Polyarylacridine anion exchange membrane with high ion conductivity and high dimensional stability, and preparation method and application thereof | |
CN114835935B (en) | Oximino-assisted ether-oxygen-bond-free polymer anion exchange membrane and preparation method thereof | |
CN113307966B (en) | Copolymer containing tetramethyl piperidine oxide quaternary ammonium salt, and preparation method and application thereof | |
CN114560964B (en) | Synthesis method and application of carboxyl functionalized polyionic liquid | |
CN109687004A (en) | A kind of multipole ion cross-linking type anion-exchange membrane and preparation method thereof | |
KR20190026133A (en) | Anion-exchange membrane based on aminated poly(tyrene-ethylene-butylene-styrene) copolymer and manufacturing method thereof | |
CN113871671A (en) | Preparation method of multi-cation cross-linked anion exchange membrane | |
CN109280199B (en) | Crystalline anion exchange membrane with microphase separation structure and preparation method thereof | |
CN108409927B (en) | Imidazole functionalized polymer and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20200114 |
|
WW01 | Invention patent application withdrawn after publication |