CN106750441A - A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof - Google Patents
A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof Download PDFInfo
- Publication number
- CN106750441A CN106750441A CN201611116453.6A CN201611116453A CN106750441A CN 106750441 A CN106750441 A CN 106750441A CN 201611116453 A CN201611116453 A CN 201611116453A CN 106750441 A CN106750441 A CN 106750441A
- Authority
- CN
- China
- Prior art keywords
- ionic liquid
- high temperature
- proton exchange
- triazole
- polybenzimidazoles
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/20—Manufacture of shaped structures of ion-exchange resins
- C08J5/22—Films, membranes or diaphragms
- C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
- C08J5/2218—Synthetic macromolecular compounds
- C08J5/2231—Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions involving unsaturated carbon-to-carbon bonds
-
- 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
- C08F126/00—Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen
- C08F126/06—Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen by a heterocyclic ring containing nitrogen
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/20—Manufacture of shaped structures of ion-exchange resins
- C08J5/22—Films, membranes or diaphragms
- C08J5/2206—Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
- C08J5/2218—Synthetic macromolecular compounds
- C08J5/2256—Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/20—Manufacture of shaped structures of ion-exchange resins
- C08J5/22—Films, membranes or diaphragms
- C08J5/2287—After-treatment
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L39/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen; Compositions of derivatives of such polymers
- C08L39/04—Homopolymers or copolymers of monomers containing heterocyclic rings having nitrogen as ring member
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L79/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen or carbon only, not provided for in groups C08L61/00 - C08L77/00
- C08L79/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
-
- 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
- H01M8/1041—Polymer electrolyte composites, mixtures or blends
- H01M8/1046—Mixtures of at least one polymer and at least one additive
- H01M8/1048—Ion-conducting additives, e.g. ion-conducting particles, heteropolyacids, metal phosphate or polybenzimidazole with phosphoric acid
-
- 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
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2339/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen; Derivatives of such polymers
- C08J2339/04—Homopolymers or copolymers of monomers containing heterocyclic rings having nitrogen as ring member
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2379/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2361/00 - C08J2377/00
- C08J2379/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2439/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen; Derivatives of such polymers
- C08J2439/04—Homopolymers or copolymers of monomers containing heterocyclic rings having nitrogen as ring member
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2479/00—Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2461/00 - C08J2477/00
- C08J2479/04—Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/16—Applications used for films
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2203/00—Applications
- C08L2203/20—Applications use in electrical or conductive gadgets
-
- 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
Abstract
The invention discloses the poly- triazole ionic liquid of a kind of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof, described cross linking membrane is with polybenzimidazoles as polymer backbone, with triazole ionic liquid base polyethylene as crosslinking agent, cross-linking type high temperature proton exchange film is formed by self-crosslinking.The poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film proposed by the present invention has preferable Proton conducting ability and excellent dimensional stability under not humidification conditions, be prevented effectively from polybenzimidazoles/phosphoric acid type high temp film phosphoric acid be lost in the electrical conductivity that causes it is unstable the shortcomings of, there is electrical conductivity and low-permeable higher.The poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film proposed by the present invention can be applied in high temperature proton exchange film fuel cell, direct alcohol fuel cell, electrochemical sensor or other electrochemical appliances.
Description
Technical field
The invention belongs to fuel cell material technical field, and in particular to a kind of poly- triazole ionic liquid of cross-linking type/poly-
Benzimidazole high temperature proton exchange film and preparation method thereof.
Background technology
Proton Exchange Membrane Fuel Cells(PEMFC)It is a kind of efficient, cleaning, environment-friendly TRT, is electronic vapour
The ideal power source of car, can act also as the Military Powers or compact power etc. such as dispersion power station, submarine and spacecraft, with very
Wide application prospect.But now widely used is perfluor type sulfonic acid membrane cell with Nafion as representative, but
The proton conducting ability of this kind of PEM is influenceed greatly by water content in film and temperature, and alcohol-rejecting ability is poor, the work of PEMFC
Make temperature no more than 80 DEG C.Because PEMFC is limited by operating temperature so that it faces CO tolerances in practical application
The problems such as difference, hydro-thermal difficult management of system.Therefore PEMFC running temperatures are brought up to more than 100 DEG C, just can be efficiently against
The above mentioned problem of traditional Nafion bases PEMFC, the fuel cell of this type(FC)Normally referred to as high temperature proton exchange film combustion
Material battery(HT-PEMFC), it is an important developing direction of PEMFC technologies.
HT-PEMFC systems have the following advantages:1)Electrochemical reaction speed is improved, and effectively reduces electrochemical cathode polarization
Overpotential, it is allowed to reduce catalyst load amount, it is allowed to use non-platinum catalyst;2)Humidification requirements reduction to reacting gas;3)Electricity
Pool inner water is managed with gas phase in the presence of hydro-thermal is simplified;Additionally, HT-PEMFC simplifies FC cooling systems to a certain extent.In view of
HT-PEMFC tempting development prospect, has carried out the development of HT-PEMFC critical materials extensively both at home and abroad, including high temperature proton is handed over
Change film, catalyst and carrier etc., and achieve preferable PRELIMINARY RESULTS, wherein high temperature proton exchange film be research focus it
One.
At present polybenzimidazoles is concentrated mainly on for the research of HT-PEMFC PEMs(PBI)On, it is in 1959
Year is reported first in United States Patent (USP), and Hoechst Celanese companies of the U.S. introduce PBI film products to the market within 1988.Such as
The present, PBI as polymer-based material the most outstanding in engineering thermoplasties, in the high temperature proton exchange as HT-PEMFC
Film aspect shows huge validity and feasibility.But PBI types membrane material is in hot operation(T≥150℃), meeting can not
Degrade with avoiding.Furthermore, phosphoric acid losing issue is also one of bottleneck of influence PBI type high temp film commercial applications, therefore,
The conduction of phosphoric acid can be replaced by the ionic liquid of other conducting hydrogen ions, so as to solve the problems, such as that phosphoric acid is lost in.
In sum, obtain at present such PEM polymeric substrates easily by free radical attack and degrade, phosphoric acid
It is lost in the problem such as serious and restricts its commercialized application, by will be built in film using ionic liquid conducting hydrogen ions, in film
Cross-linked structure, can effectively avoid the losing issue of phosphoric acid, lift the service life of film, and improve the dimensional stability of film.
The content of the invention
In view of the shortcomings of the prior art, it is an object of the invention to provide the poly- triazole ionic liquid/polyphenyl of cross-linking type simultaneously
Imidazoles high temperature proton exchange film and preparation method thereof, by with triazole ionic liquid base polyethylene as crosslinking agent, by certainly
Cross-linking type high temperature proton exchange film is cross-linked to form, so that the dimensional stability of polybenzimidazoles high temperature proton exchange film is improved, and
It is prevented effectively from phosphoric acid and is lost in the electrical conductivity loss for bringing.
To achieve these goals, the technical solution adopted by the present invention is:
A kind of preparation method of the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film, including following step
Suddenly:
(1)0.2 ~ 1 g polybenzimidazoles is dissolved in 10 ~ 20 mL high boiling solvents, after stirring and dissolving, triazole is added
Ionic liquid base polyethylene, stirring are until dissolving;Wherein, the addition of triazole ionic liquid base polyethylene be polyphenyl simultaneously
The 50% ~ 150% of imidazoles quality;
(2)Solution is put into oil bath again, is stirred at 50 ~ 100 DEG C, react 12 ~ 48 h;
(3)Solution is poured into casting film plate, solvent is evaporated at 60 ~ 80 DEG C, the high temperature proton exchange film that will be obtained carefully is taken off
Under, immersion is dried after washing in ethanol, obtains the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange
Film.
Preferably, step(1)Described in triazole ionic liquid base polyethylene intermediate ion liquid selected by sun from
Son be 1H-1,2,4- triazole cations, structure is C2H4N3 +;Anion is CH3SO3 -、CF3SO3 -、H2PO4 -In one kind or
Various mixtures.
Preferably, step(1)Described in triazole ionic liquid base polyethylene preparation method, including following step
Suddenly:
(1)1- vinyl -1 of 0.5 ~ 2 mol/L is prepared, 2,4- triazole chloroformic solutions are poured into there-necked flask, in 50 ~ 80
Stirring is extremely dissolved at DEG C;
(2)Pyrovinic acid, trifluoromethane sulfonic acid, one or more of phosphoric acid of mixture are added dropwise over, 1- vinyl -1 is added,
2,4- triazoles are 1 with the mol ratio of acid:1.5~1:3;
(3)Solution is put in heating stirring in oil bath, reaction temperature is 50 ~ 80 DEG C, after 2 ~ 4 h of reaction, by solution pour into from
In sub- water, washing, suction filtration removes many spent acid and solvent, is washed with ethanol for several times and dried, and obtains white flock powder;
(4)The white powder that will be obtained weighs 0.2 ~ 1.2 g, adds 5 ~ 15 mL high boiling solvents, stirring and dissolving;
(5)Chain initiator azodiisobutyronitrile will be added in solution, the wherein mass content of chain initiator is high boiling solvent
20~50%;
(6)After by solution stirring and dissolving, it is put into oil bath, reacts 30 ~ 60 h, reaction temperature is 50 ~ 80 DEG C;
(7)After reaction terminates, solution is poured into ethanol, obtain White Flocculus, dried after being washed with ethanol, obtain triazole
Class ionic liquid base polyethylene.
Preferably, the high boiling solvent is DMA or 1-METHYLPYRROLIDONE.
The poly- triazole ionic liquid of the cross-linking type/polybenzimidazoles high temperature proton exchange obtained using above-mentioned preparation method
Film.
The poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and its preparation side that the present invention is provided
Method, has the advantages that compared with prior art:
1. the present invention is respectively adopted polybenzimidazoles for polymer backbone, is crosslinking with triazole ionic liquid base polyethylene
Agent, uniform by structure of composite membrane obtained in self-crosslinking, it is adaptable to anhydrous system, the high temperature proton of 120 ~ 200 DEG C of operating temperature
Exchange film fuel battery.
2. the present invention uses polybenzimidazoles/polyethylene triazole cross-linked structure, after can effectively reducing film immersion phosphoric acid
It is swelling, the conduction of phosphoric acid is replaced using ionic liquid conducting hydrogen ions, be prevented effectively from the loss of phosphoric acid, improve high temperature proton and hand over
Change the stable conductivity of film.
3. the triazol radical ionic liquid in crosslinking agent of the present invention, can efficiently proton conducting so that hand over
Connection film has electrical conductivity higher.
Brief description of the drawings
Fig. 1 is the poly- triazole ionic liquid of cross-linking type obtained in embodiment 1/polybenzimidazoles high temperature proton exchange film
Electrical conductivity variation with temperature figure;
Fig. 2 is the battery of the poly- triazole ionic liquid of cross-linking type obtained in embodiment 2/polybenzimidazoles high temperature proton exchange film
Polarization curve.
Specific embodiment
Polybenzimidazoles used in example below(PBI, CAS 25928-81-8)Purchased from FuMA-Tech companies;Diformazan
Yl acetamide(DMAC, CAS: 127-19-5), 1-METHYLPYRROLIDONE(NMP, CAS: 872-50-4)Purchased from Tianjin great Mao
Chemical reagents corporation;1- vinyl -1,2,4- triazoles(CAS: 2764-83-2)Purchased from Shanghai Yuan Ye bio tech ltd;
Azodiisobutyronitrile(AIBN, CAS: 78-67-1)Purchased from Tianjin great Mao chemical reagents corporations;Phosphoric acid is purchased from Shanghai Aladdin
Biochemical technology limited company;Pyrovinic acid(CAS: 75-75-2), trifluoromethane sulfonic acid(CAS: 1493-13-61)It is purchased from
Tianjin great Mao chemical reagents corporations.
Embodiment 1
A kind of preparation method of the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film, by following step
It is rapid to prepare:
(1)1- vinyl -1 of 0.5 mol/L is prepared, 2,4- triazole chloroformic solutions are poured into there-necked flask, at 50 DEG C
Stirring is extremely dissolved;
(2)Phosphoric acid is added dropwise over, 1- vinyl -1,2,4- triazoles are 1 with the mol ratio of phosphoric acid:1.5;
(3)Solution is put in heating stirring in oil bath, reaction temperature is 50 DEG C, after 4 h of reaction, solution is poured into deionized water
In, washing, suction filtration removes many spent acid and solvent, is washed with ethanol for several times and dried, and obtains white flock powder;
(4)The white powder that will be obtained weighs 0.2 g, adds 10 mL dimethylacetylamides, stirring and dissolving;
(5)Chain initiator azodiisobutyronitrile will be added in solution, the wherein mass content of chain initiator is dimethylacetylamide
50%;
(6)After by solution stirring and dissolving, it is put into oil bath, reacts 40 h, reaction temperature is 50 DEG C;
(7)After reaction terminates, solution is poured into ethanol, obtain White Flocculus, dried after being washed with ethanol, obtain C2H4N3 +- H2PO4Ionic liquid base polyethylene;
(8)Then, 1 g polybenzimidazoles is dissolved in 20 mL 1-METHYLPYRROLIDONEs, after stirring and dissolving, adds C2H4N3 +- H2PO4Ionic liquid base polyethylene, stirring are until dissolving;Wherein, C2H4N3 +- H2PO4The addition of ionic liquid base polyethylene
Measure is the 50% of polybenzimidazoles quality;
(9)Solution is put into oil bath again, is stirred at 80 DEG C, react 12 h;
(10)Solution is poured into casting film plate, solvent is evaporated at 80 DEG C, the high temperature proton exchange film that will be obtained carefully is taken off,
Immersion in ethanol, is dried after washing, obtains the poly- triazole ionic liquid of type/polybenzimidazoles high temperature proton exchange film.
The poly- triazole ionic liquid of cross-linking type obtained in embodiment 1/polybenzimidazoles high temperature proton exchange film, tests conductance
Rate variation with temperature figure.By the poly- triazole ionic liquid of cross-linking type obtained in embodiment 1/polybenzimidazoles high temperature proton exchange
Film and its preparation be cut into size be 40 mm × 10 mm rectangular sheet, then by the poly- triazole of cross-linking type obtained in embodiment 1 from
Sub- liquid/polybenzimidazoles high temperature proton exchange film and its preparation are placed in electrical conductivity fixture, and fixture is put in into vacuum drying chamber
In, 3 h are kept at 90 DEG C, then temperature rises to 170 DEG C from 90 DEG C, the electrical conductivity of lower film is tested every 10 DEG C, as a result
As shown in Figure 1.
It will be seen from figure 1 that the poly- triazole ionic liquid of cross-linking type obtained in embodiment 1/polybenzimidazoles high temperature proton
At 150 DEG C, anhydrous condition is issued to 32 mS/cm, and electrical conductivity meets high temperature proton exchange for exchange membrane and its preparation electrical conductivity
The need for membrane cell, illustrate that prepared cross linking membrane has electrical conductivity higher.
Embodiment 2
A kind of preparation method of the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film, by following step
It is rapid to prepare:
(1)1- vinyl -1 of 2mol/L is prepared, 2,4- triazole chloroformic solutions are poured into there-necked flask, in stirring at 80 DEG C
To dissolving;
(2)Trifluoromethane sulfonic acid is added dropwise over, 1- vinyl -1 is added, 2,4- triazoles are with the mol ratio of trifluoromethane sulfonic acid
1:1.3;
(3)Solution is put in heating stirring in oil bath, reaction temperature is 80 DEG C, after 2 h of reaction, solution is poured into deionized water
In, washing, suction filtration removes many spent acid and solvent, is washed for several times with ethanol, and dries, and obtains white flock powder;
(4)The white powder that will be obtained weighs 1 g, adds 15 mLN- methyl pyrrolidones, stirring and dissolving;
(5)Chain initiator azodiisobutyronitrile will be added in solution, the wherein mass content of chain initiator is N- crassitudes
The 48% of ketone;
(6)After by solution stirring and dissolving, it is put into oil bath, reacts 60 h, reaction temperature is 80 DEG C;
(7)After reaction terminates, solution is poured into ethanol, obtain White Flocculus, dried after being washed with ethanol, obtain C2H4N3 +- CF3SO3 -Ionic liquid base polyethylene;
(8)Then, 0.5 g polybenzimidazoles is dissolved in 10 mLN- methyl pyrrolidones, after stirring and dissolving, adds C2H4N3 +- CF3SO3 -Ionic liquid base polyethylene, stirring are until dissolving;Wherein, C2H4N3 +- CF3SO3 -Ionic liquid base polyethylene
Addition is the 120% of polybenzimidazoles quality;
(9)Solution is put into oil bath again, is stirred at 70 DEG C, react 48 h;
(10)Solution is poured into casting film plate, solvent is evaporated at 60 DEG C, the high temperature proton exchange film that will be obtained carefully is taken off,
Immersion in ethanol, is dried after washing, obtains the poly- triazole ionic liquid of type/polybenzimidazoles high temperature proton exchange film.
The poly- triazole ionic liquid of cross-linking type obtained in embodiment 2/polybenzimidazoles high temperature proton exchange film, in monocell
The battery performance tested on evaluating apparatus under its different temperatures.Wherein, GND uses carbon(C)Carry nickel(Ni)Catalyst with
It is applied to after PBI solution is well mixed on carbon paper and is obtained(Using the preparation method disclosed in patent CN02127802.4), Ni accounts for
The mass percent of C/Ni catalyst is that the mass ratio of 40%, C/Ni and PBI is 1:1;Anode uses carbon(C)Carry platinum(Pt)
Catalyst is applied on carbon paper after being well mixed with PBI solution and is obtained(Using the preparation side disclosed in patent CN02127802.4
Method), the mass percent that Pt accounts for C/ Pt catalyst is 70%, and Pt carrying capacity is 0.5 mg/cm in positive pole2;Battery operating environment point
It is not set as:Battery temperature is 150 DEG C;Hydrogen and oxygen gas flow rate are respectively 50 mL/min, 100 mL/min, and gas is without increasing
Wet, pressure is 0.05 MPa, and test result is as shown in Figure 2.
Figure it is seen that the poly- triazole ionic liquid of cross-linking type obtained in embodiment 2/polybenzimidazoles high temperature proton
The high-temperature fuel cell of exchange membrane assembling, battery has excellent discharge performance, and maximum power density is up to 600 mW/cm2。
Embodiment 3
A kind of preparation method of the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film, by following step
It is rapid to prepare:
(1)1- vinyl -1 of 1.5 mol/L is prepared, 2,4- triazole chloroformic solutions are poured into there-necked flask, at 80 DEG C
Stirring is extremely dissolved;
(2)Pyrovinic acid is added dropwise over, vinyl -1 is added, 2,4- triazoles are 1 with the mol ratio of pyrovinic acid:1.4;
(3)Solution is put in heating stirring in oil bath, reaction temperature is 80 DEG C, after 2 h of reaction, solution is poured into deionized water
In, washing, suction filtration removes many spent acid and solvent, is washed with ethanol for several times and dried, and obtains white flock powder;
(4)The white powder that will be obtained weighs 0.8 g, adds 15 mL dimethylacetylamides, stirring and dissolving;
(5)Chain initiator azodiisobutyronitrile will be added in solution, the wherein mass content of chain initiator is dimethylacetylamide
48%;
(6)After by solution stirring and dissolving, it is put into oil bath, reacts 60 h, reaction temperature is 80 DEG C;
(7)After reaction terminates, solution is poured into ethanol, obtain White Flocculus, dried after being washed with ethanol, obtain C2H4N3 +- CH3SO3 -Ionic liquid base polyethylene;
(8)Then, 0.2 g polybenzimidazoles is dissolved in 10 mLN- methyl pyrrolidones, after stirring and dissolving, adds C2H4N3 +- CH3SO3 -Ionic liquid base polyethylene, stirring are until dissolving;Wherein, C2H4N3 +- CH3SO3 -Ionic liquid base polyethylene
Addition is the 80% of polybenzimidazoles quality;
(9)Solution is put into oil bath again, is stirred at 70 DEG C, react 48 h;
(10)Solution is poured into casting film plate, solvent is evaporated at 60 DEG C, the high temperature proton exchange film that will be obtained carefully is taken off,
Immersion in ethanol, is dried after washing, obtains the poly- triazole ionic liquid of type/polybenzimidazoles high temperature proton exchange film.
The above, specific embodiment only of the invention, but protection scope of the present invention is not limited thereto, ability
Other modifications or equivalent that domain those of ordinary skill is made to technical scheme, without departing from skill of the present invention
The spirit and scope of art scheme, all should cover in the middle of scope of the presently claimed invention.
Claims (5)
1. a kind of preparation method of the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film, its feature exists
In comprising the following steps:
(1)0.2 ~ 1 g polybenzimidazoles is dissolved in 10 ~ 20 mL high boiling solvents, after stirring and dissolving, triazole is added
Ionic liquid base polyethylene, stirring are until dissolving;Wherein, the addition of triazole ionic liquid base polyethylene be polyphenyl simultaneously
The 50% ~ 150% of imidazoles quality;
(2)Solution is put into oil bath again, is stirred at 50 ~ 100 DEG C, react 12 ~ 48 h;
(3)Solution is poured into casting film plate, solvent is evaporated at 60 ~ 80 DEG C, the high temperature proton exchange film that will be obtained carefully is taken off
Under, immersion is dried after washing in ethanol;Obtain the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange
Film.
2. the system of the poly- triazole ionic liquid of cross-linking type according to claim 1/polybenzimidazoles high temperature proton exchange film
Preparation Method, it is characterised in that:Step(1)Described in triazole ionic liquid base polyethylene intermediate ion liquid selected by sun
Ion is 1H-1,2,4- triazole cations, and structure is C2H4N3 +;Anion is CH3SO3 -、CF3SO3 -、H2PO4 -In one kind
Or various mixtures.
3. the system of the poly- triazole ionic liquid of cross-linking type according to claim 1/polybenzimidazoles high temperature proton exchange film
Preparation Method, it is characterised in that:Step(1)Described in triazole ionic liquid base polyethylene preparation method, it is including following
Step:
(1)Vinyl -1 of 0.5 ~ 2 mol/L is prepared, 2,4- triazole chloroformic solutions are poured into there-necked flask, in 50 ~ 80 DEG C
Lower stirring is extremely dissolved;
(2)Pyrovinic acid, trifluoromethane sulfonic acid, one or more of phosphoric acid of mixture are added dropwise over, additional proportion is:Ethene
Base -1,2,4- triazoles are 1 with the mol ratio of acid:1.5~1:3;
(3)Solution is put in heating stirring in oil bath, reaction temperature is 50 ~ 80 DEG C, after 2 ~ 4 h of reaction, by solution pour into from
In sub- water, washing, suction filtration removes many spent acid and solvent, is washed with ethanol for several times and dried, and obtains white flock powder;
(4)The white powder that will be obtained weighs 0.2 ~ 1.2 g, adds 5 ~ 15 mL high boiling solvents, stirring and dissolving;
(5)Chain initiator azodiisobutyronitrile will be added in solution, the wherein mass content of chain initiator is high boiling solvent
20~50%;
(6)After by solution stirring and dissolving, it is put into oil bath, reacts 30 ~ 60 h, reaction temperature is 50 ~ 80 DEG C;
(7)After reaction terminates, solution is poured into ethanol, obtain White Flocculus, after being washed with ethanol, dried, obtain three nitrogen
Azole ionic liquid base polyethylene.
4. the poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film according to claim 1 and 3
Preparation method, it is characterised in that:The high boiling solvent is DMAC N,N' dimethyl acetamide or 1-METHYLPYRROLIDONE.
5. the poly- triazole ionic liquid of a kind of cross-linking type/polybenzimidazoles high temperature proton exchange film, it is characterised in that:The crosslinking
The poly- triazole ionic liquid of type/polybenzimidazoles high temperature proton exchange film is by any one of Claims 1-4 claim institute
What the method stated was prepared.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611116453.6A CN106750441B (en) | 2016-12-07 | 2016-12-07 | A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611116453.6A CN106750441B (en) | 2016-12-07 | 2016-12-07 | A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106750441A true CN106750441A (en) | 2017-05-31 |
CN106750441B CN106750441B (en) | 2019-06-21 |
Family
ID=58882247
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201611116453.6A Active CN106750441B (en) | 2016-12-07 | 2016-12-07 | A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106750441B (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106549171A (en) * | 2016-12-07 | 2017-03-29 | 黄河科技学院 | A kind of cross-linking type polybenzimidazoles high temperature proton exchange film with high antioxygenic property high conductivity and preparation method thereof |
CN111303437A (en) * | 2020-03-06 | 2020-06-19 | 珠海冠宇电池有限公司 | Phosphonated (polyolefin-g-hyperbranched polybenzimidazole) graft copolymer and preparation method and application thereof |
CN113299959A (en) * | 2021-06-04 | 2021-08-24 | 中国科学院化学研究所 | Composite proton exchange membrane and preparation method and application thereof |
CN113527684A (en) * | 2020-04-21 | 2021-10-22 | 武汉理工大学 | Oxygen reduction catalyst layer based on grafted polybenzimidazole as proton conductor and preparation method thereof |
US11180621B2 (en) | 2018-09-14 | 2021-11-23 | University Of South Carolina | Method for producing PBI films without organic solvents |
CN113735786A (en) * | 2021-09-03 | 2021-12-03 | 中国科学院过程工程研究所 | Multi-site triazole ionic liquid capable of efficiently and reversibly absorbing ammonia gas |
US11302948B2 (en) | 2018-09-14 | 2022-04-12 | University Of South Carolina | Polybenzimidazole (PBI) membranes for redox flow batteries |
US11482721B2 (en) | 2018-09-14 | 2022-10-25 | University Of South Carolina | Low permeability polybenzimidazole (PBI) gel membranes for redox flow batteries |
CN115513505A (en) * | 2022-09-14 | 2022-12-23 | 华中科技大学 | Ionic liquid/polymer composite membrane and preparation method and application thereof |
US11777124B2 (en) | 2020-03-06 | 2023-10-03 | University Of South Carolina | Proton-conducting PBI membrane processing with enhanced performance and durability |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040228823A1 (en) * | 2003-05-16 | 2004-11-18 | University Of Nebraska Board Of Regents | Cross-linked ionic core micelles |
CN103050719A (en) * | 2012-12-12 | 2013-04-17 | 常州大学 | Proton type ionic liquid based proton exchange membrane and preparation method thereof |
US20130309190A1 (en) * | 2012-05-15 | 2013-11-21 | L'oreal S.A. | Hair cosmetic and styling compositions based on maleic acid copolymers and polyamines |
CN104124463A (en) * | 2013-04-26 | 2014-10-29 | 中国科学院大连化学物理研究所 | Ionic liquid-polymer composite membrane for hydrogen chloride fuel cell and preparation and application thereof |
-
2016
- 2016-12-07 CN CN201611116453.6A patent/CN106750441B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040228823A1 (en) * | 2003-05-16 | 2004-11-18 | University Of Nebraska Board Of Regents | Cross-linked ionic core micelles |
US20130309190A1 (en) * | 2012-05-15 | 2013-11-21 | L'oreal S.A. | Hair cosmetic and styling compositions based on maleic acid copolymers and polyamines |
CN103050719A (en) * | 2012-12-12 | 2013-04-17 | 常州大学 | Proton type ionic liquid based proton exchange membrane and preparation method thereof |
CN104124463A (en) * | 2013-04-26 | 2014-10-29 | 中国科学院大连化学物理研究所 | Ionic liquid-polymer composite membrane for hydrogen chloride fuel cell and preparation and application thereof |
Non-Patent Citations (2)
Title |
---|
MOUSUMI HAZARIKA 等: ""Proton Exchange Membrane Developed from Novel Blends of Polybenzimidazole and Poly(vinyl-1,2,4-triazole)"", 《ACS APPLIED MATERIALS & INTERFACES》 * |
李莉 等: ""聚苯并咪唑在离子液体中流变行为的研究"", 《合成技术及应用》 * |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106549171B (en) * | 2016-12-07 | 2019-03-22 | 黄河科技学院 | A kind of cross-linking type polybenzimidazoles high temperature proton exchange film and preparation method thereof with the high conductivity of high antioxygenic property |
CN106549171A (en) * | 2016-12-07 | 2017-03-29 | 黄河科技学院 | A kind of cross-linking type polybenzimidazoles high temperature proton exchange film with high antioxygenic property high conductivity and preparation method thereof |
US11482721B2 (en) | 2018-09-14 | 2022-10-25 | University Of South Carolina | Low permeability polybenzimidazole (PBI) gel membranes for redox flow batteries |
US11884787B2 (en) | 2018-09-14 | 2024-01-30 | University Of South Carolina | PBI films formed without use of organic solvents |
US11180621B2 (en) | 2018-09-14 | 2021-11-23 | University Of South Carolina | Method for producing PBI films without organic solvents |
US11799112B2 (en) | 2018-09-14 | 2023-10-24 | University Of South Carolina | Polybenzimidazole (PBI) membranes for redox flow batteries |
US11302948B2 (en) | 2018-09-14 | 2022-04-12 | University Of South Carolina | Polybenzimidazole (PBI) membranes for redox flow batteries |
CN111303437A (en) * | 2020-03-06 | 2020-06-19 | 珠海冠宇电池有限公司 | Phosphonated (polyolefin-g-hyperbranched polybenzimidazole) graft copolymer and preparation method and application thereof |
CN111303437B (en) * | 2020-03-06 | 2022-03-18 | 珠海冠宇电池股份有限公司 | Phosphonated (polyolefin-g-hyperbranched polybenzimidazole) graft copolymer and preparation method and application thereof |
US11777124B2 (en) | 2020-03-06 | 2023-10-03 | University Of South Carolina | Proton-conducting PBI membrane processing with enhanced performance and durability |
CN113527684A (en) * | 2020-04-21 | 2021-10-22 | 武汉理工大学 | Oxygen reduction catalyst layer based on grafted polybenzimidazole as proton conductor and preparation method thereof |
CN113527684B (en) * | 2020-04-21 | 2023-11-03 | 武汉理工大学 | Oxygen reduction catalytic layer based on grafted polybenzimidazole as proton conductor and preparation method thereof |
CN113299959B (en) * | 2021-06-04 | 2022-07-08 | 中国科学院化学研究所 | Composite proton exchange membrane and preparation method and application thereof |
CN113299959A (en) * | 2021-06-04 | 2021-08-24 | 中国科学院化学研究所 | Composite proton exchange membrane and preparation method and application thereof |
CN113735786A (en) * | 2021-09-03 | 2021-12-03 | 中国科学院过程工程研究所 | Multi-site triazole ionic liquid capable of efficiently and reversibly absorbing ammonia gas |
CN115513505A (en) * | 2022-09-14 | 2022-12-23 | 华中科技大学 | Ionic liquid/polymer composite membrane and preparation method and application thereof |
CN115513505B (en) * | 2022-09-14 | 2023-09-29 | 华中科技大学 | Ionic liquid/polymer composite membrane and preparation method and application thereof |
WO2024056017A1 (en) * | 2022-09-14 | 2024-03-21 | 华中科技大学 | Ionic liquid/polymer composite film, and preparation method therefor and use thereof |
Also Published As
Publication number | Publication date |
---|---|
CN106750441B (en) | 2019-06-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106750441B (en) | A kind of poly- triazole ionic liquid of cross-linking type/polybenzimidazoles high temperature proton exchange film and preparation method thereof | |
Lin et al. | Bis-imidazolium based poly (phenylene oxide) anion exchange membranes for fuel cells: the effect of cross-linking | |
Winardi et al. | Sulfonated poly (ether ether ketone)-based proton exchange membranes for vanadium redox battery applications | |
EP1648047B1 (en) | Polymer electrolyte for a direct oxidation fuel cell, method of preparing the same, and direct oxidation fuell cell comprising the same | |
CN109524699B (en) | Cross-linked high-temperature proton exchange membrane with high conductivity and preparation method thereof | |
Sun et al. | A comparative study of Nafion and sulfonated poly (ether ether ketone) membrane performance for iron-chromium redox flow battery | |
CN1764001B (en) | Polymer electrolyte for a direct oxidation fuel cell, method of preparing the same, and direct oxidation fuel cell comprising the same | |
Liao et al. | Fluoro-methyl sulfonated poly (arylene ether ketone-co-benzimidazole) amphoteric ion-exchange membranes for vanadiumáredox flow battery | |
CN106750442A (en) | A kind of cross-linking type polybenzimidazoles with high conductivity/polyethylene triazole high temperature proton exchange film and preparation method thereof | |
CN100473693C (en) | Polymer electrolyte and fuel cell using the same | |
Gan et al. | Facile fabrication of amphoteric semi-interpenetrating network membranes for vanadium flow battery applications | |
CN102838863B (en) | Novel polymer proton exchange membrane and preparation method thereof | |
CN100572428C (en) | Polymeric film that fuel cell is used and preparation method thereof and fuel cell system | |
Meenakshi et al. | Chitosan‐polyvinyl alcohol‐sulfonated polyethersulfone mixed‐matrix membranes as methanol‐barrier electrolytes for DMFCs | |
CN106549171B (en) | A kind of cross-linking type polybenzimidazoles high temperature proton exchange film and preparation method thereof with the high conductivity of high antioxygenic property | |
CN106558719A (en) | A kind of polybenzimidazoles with high antioxygenic property/polyvinylbenzylchloride cross-linking type high temperature proton exchange film and preparation method thereof | |
CN105601968B (en) | A kind of preparation method of polybenzimidazoles multilayer complex films used for high-temperature fuel cell | |
Roh et al. | Investigation on physico-chemical and electrochemical performance of poly (phenylene oxide)-based anion exchange membrane for vanadium redox flow battery systems | |
Mu et al. | Novel ether-free membranes based on poly (p-terphenylene methylimidazole) for vanadium redox flow battery applications | |
Higa et al. | Characteristics and direct methanol fuel cell performance of polymer electrolyte membranes prepared from poly (vinyl alcohol-b-styrene sulfonic acid) | |
CN111276724A (en) | Half-interpenetrating network anion exchange membrane based on polyphenyl ether/polyvinyl alcohol and preparation method thereof | |
CN106450395A (en) | Polybenzimidazole-high-conductivity graphene layered composite high-temperature proton exchange membrane with high conductivity and stability and preparation method of polybenzimidazole-high-conductivity graphene layered composite high-temperature proton exchange membrane | |
CN112259769A (en) | Polybenzimidazole proton exchange membrane with micropores, preparation method and application thereof | |
Che et al. | The effect of grafted alkyl side chains on the properties of poly (terphenyl piperidinium) based high temperature proton exchange membranes | |
KR100534658B1 (en) | Composition of Polymer Electrolyte for Direct Methanol Fuel Cell with the Suppressed Methanol Crossover |
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 | ||
TA01 | Transfer of patent application right | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20190527 Address after: Room 207, Building A, Emerging Industry Development Center, Zhangjiagang Free Trade Zone, Suzhou City, Jiangsu Province Applicant after: Zhangjiagang Institute of industrial technology, Dalian Institute of Chemical Physics, China Academy of Sciences Address before: 450063 No. 123 Lianyun Road, Erqi District, Zhengzhou City, Henan Province Applicant before: Huanghe S & T College |
|
GR01 | Patent grant | ||
GR01 | Patent grant |