CN115101790A - A kind of composite electrolyte membrane with high electrical conductivity and preparation method thereof - Google Patents
A kind of composite electrolyte membrane with high electrical conductivity and preparation method thereof Download PDFInfo
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- 239000012528 membrane Substances 0.000 title claims abstract description 43
- 239000002131 composite material Substances 0.000 title claims abstract description 36
- 239000003792 electrolyte Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- 239000004693 Polybenzimidazole Substances 0.000 claims abstract description 54
- 229920002480 polybenzimidazole Polymers 0.000 claims abstract description 54
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 23
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 19
- 229920000642 polymer Polymers 0.000 claims abstract description 18
- 238000010438 heat treatment Methods 0.000 claims abstract description 8
- 229920001328 Polyvinylidene chloride Polymers 0.000 claims abstract description 7
- 238000001035 drying Methods 0.000 claims abstract description 7
- 239000005033 polyvinylidene chloride Substances 0.000 claims abstract description 7
- 238000005266 casting Methods 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 5
- 150000004820 halides Chemical class 0.000 claims abstract description 3
- 239000003495 polar organic solvent Substances 0.000 claims abstract description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 18
- 239000003960 organic solvent Substances 0.000 claims description 12
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 4
- 150000008282 halocarbons Chemical class 0.000 claims description 4
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- DLFVBJFMPXGRIB-UHFFFAOYSA-N Acetamide Chemical compound CC(N)=O DLFVBJFMPXGRIB-UHFFFAOYSA-N 0.000 claims 2
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- 239000002994 raw material Substances 0.000 abstract description 2
- 238000010923 batch production Methods 0.000 abstract 1
- 238000004132 cross linking Methods 0.000 description 11
- 239000000463 material Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 4
- 239000002033 PVDF binder Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- QMKYBPDZANOJGF-UHFFFAOYSA-N benzene-1,3,5-tricarboxylic acid Chemical compound OC(=O)C1=CC(C(O)=O)=CC(C(O)=O)=C1 QMKYBPDZANOJGF-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- LUIVNNXFXHFZFD-UHFFFAOYSA-N 1,2-dibromo-3-methylbenzene Chemical compound CC1=CC=CC(Br)=C1Br LUIVNNXFXHFZFD-UHFFFAOYSA-N 0.000 description 1
- BCMCBBGGLRIHSE-UHFFFAOYSA-N 1,3-benzoxazole Chemical compound C1=CC=C2OC=NC2=C1 BCMCBBGGLRIHSE-UHFFFAOYSA-N 0.000 description 1
- HSTOKWSFWGCZMH-UHFFFAOYSA-N 3,3'-diaminobenzidine Chemical compound C1=C(N)C(N)=CC=C1C1=CC=C(N)C(N)=C1 HSTOKWSFWGCZMH-UHFFFAOYSA-N 0.000 description 1
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
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- 238000007334 copolymerization reaction Methods 0.000 description 1
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- 230000007797 corrosion Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- -1 dichloromethyl hypophosphorous acid Chemical compound 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical group [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 1
- 125000002883 imidazolyl group Chemical group 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000005549 size reduction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000009864 tensile test Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- 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
- H01M8/1065—Polymeric electrolyte materials characterised by the form, e.g. perforated or wave-shaped
-
- 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
- H01M8/1067—Polymeric electrolyte materials characterised by their physical properties, e.g. porosity, ionic conductivity or thickness
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- 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. in situ polymerisation or in situ crosslinking
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- 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
- H01M8/1081—Polymeric electrolyte materials characterised by the manufacturing processes starting from solutions, dispersions or slurries exclusively of polymers
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- 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
- H01M8/1088—Chemical modification, e.g. sulfonation
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Abstract
Description
技术领域technical field
本发明涉及一种复合电解质膜的制备领域,更具体的是涉及一种高导电能力的复合电解质膜及其制备方法。The invention relates to the field of preparation of a composite electrolyte membrane, and more particularly to a composite electrolyte membrane with high electrical conductivity and a preparation method thereof.
背景技术Background technique
现如今,化石能源日益减少且因使用化石能源所带来的环境问题也日益凸显,氢能源被认为是化石能源良好的替代品,氢能源的使用需要进行能量转化。质子交换膜燃料电池PEMFC作为能量转化装置,可用于新能源车辆等移动设备的能源装置。质子交换膜PEM也称为质子膜或氢离子交换膜,是一种离子选择性透过膜,在电池中起到为质子迁移和传输提供通道、分离气体反应物并阻隔电解液的作用。Nowadays, fossil energy is decreasing day by day and the environmental problems caused by the use of fossil energy are becoming more and more prominent. Hydrogen energy is considered to be a good substitute for fossil energy, and the use of hydrogen energy requires energy conversion. The proton exchange membrane fuel cell (PEMFC), as an energy conversion device, can be used in the energy device of mobile equipment such as new energy vehicles. Proton exchange membrane PEM, also known as proton membrane or hydrogen ion exchange membrane, is an ion-selective permeable membrane that functions in batteries to provide channels for proton migration and transport, to separate gaseous reactants, and to block electrolytes.
PEM中受到广泛研究的是聚苯并咪唑(PBI)及其衍生物。聚苯并咪唑(PBI)是重复单元中含有聚苯并咪唑基团的线性杂环聚合物,它具有良好的热稳定性和化学稳定性以及较高的机械强度,但聚苯并咪唑自身并没有质子传导能力,因此需要与磷酸进行复合以后才能获得较高的质子传导能力,通常需要较高的磷酸掺杂量才能获得较高的电池性能,但同时也会造成成膜材料的机械性能下降,同时膜材料的磷酸掺杂量过大时会产生大量极易流失的“游离酸”,磷酸的流失也会造成膜材料的性能下降、尺寸缩小和电极腐蚀等问题。One of the most widely studied in PEM is polybenzimidazole (PBI) and its derivatives. Polybenzimidazole (PBI) is a linear heterocyclic polymer containing polybenzimidazole groups in repeating units. It has good thermal and chemical stability and high mechanical strength, but polybenzimidazole itself does not. There is no proton conductivity, so it needs to be compounded with phosphoric acid to obtain higher proton conductivity. Usually, a higher doping amount of phosphoric acid is required to obtain higher battery performance, but at the same time, it will also cause the mechanical properties of the film-forming material to decline. At the same time, when the phosphoric acid doping amount of the membrane material is too large, a large amount of "free acid" that is easily lost will be generated, and the loss of phosphoric acid will also cause problems such as performance degradation, size reduction and electrode corrosion of the membrane material.
目前为应对磷酸掺杂量过大机械强度下降的问题,一般采用交联改性来进行加强联改性根据反应的不同又分为共聚交联和后共价交联两种主要的方式。共聚交联发生在合成PBI树脂的过程中,是将3,3'-二氨基联苯胺和间苯二甲酸与均苯三酸之类的多酸化合物发生反应得到交联改性的聚合物,这种聚合物具有超支化的结构。而共价交联改性是发生在PBI合成之后,将PBI树脂和合适的交联剂同时溶于有机溶剂中,使交联剂和PBI结构上咪唑环上的N-H进行取代反应。目前较为常用的交联剂有二氯甲基次磷酸、苯并恶唑、二溴甲苯和环氧树脂等,这些交联剂通常需要参与PBI树脂合成反应过程,对PBI树脂合成反应带来不利影响,而且制备得到的树脂因交联作用而不易溶于有机溶剂,给成膜带来不便。因此需要对现有的工艺进行改进。At present, in order to cope with the problem that the mechanical strength of the phosphoric acid is too large, cross-linking modification is generally used to strengthen the linking modification. Copolymerization crosslinking occurs in the process of synthesizing PBI resin, which is a crosslinking modified polymer obtained by reacting 3,3'-diaminobenzidine and isophthalic acid with polyacid compounds such as trimesic acid. This polymer has a hyperbranched structure. The covalent crosslinking modification occurs after the synthesis of PBI, and the PBI resin and a suitable crosslinking agent are dissolved in an organic solvent at the same time, so that the crosslinking agent and the N-H on the imidazole ring on the PBI structure undergo a substitution reaction. At present, the commonly used cross-linking agents include dichloromethyl hypophosphorous acid, benzoxazole, dibromotoluene and epoxy resin, etc. These cross-linking agents usually need to participate in the PBI resin synthesis reaction process, which is unfavorable to the PBI resin synthesis reaction. In addition, the prepared resin is not easily soluble in organic solvents due to cross-linking, which brings inconvenience to film formation. Therefore, there is a need to improve existing processes.
发明内容SUMMARY OF THE INVENTION
为解决现有的电解质膜因掺杂磷酸量过高而损耗机械强度的不足,现提供一种高导电能力的复合电解质膜及其制备方法。In order to solve the problem that the existing electrolyte membrane loses mechanical strength due to the excessive amount of doped phosphoric acid, a composite electrolyte membrane with high conductivity and a preparation method thereof are provided.
具体的技术方案如下:The specific technical solutions are as follows:
一种高导电能力的复合电解质膜的制备方法,其特征在于,包括以下步骤:A method for preparing a composite electrolyte membrane with high electrical conductivity, comprising the following steps:
S1:将聚苯并咪唑、聚偏氯乙烯溶于极性有机溶剂中;S1: Dissolve polybenzimidazole and polyvinylidene chloride in polar organic solvent;
S2:将交联剂加入至S1中,搅拌均匀得到聚合物溶液,所述的交联剂为二元或多元卤代烃R-X,将改性发生在PBI合成后,因此不参与PBI树脂合成反应,不会对PBI树脂合成反应带来不利影响,且不会带来复合膜成膜困难的问题;S2: Add the cross-linking agent to S1, stir evenly to obtain a polymer solution, the cross-linking agent is a binary or polyvalent halogenated hydrocarbon R-X, and the modification occurs after the PBI synthesis, so it does not participate in the PBI resin synthesis reaction , will not adversely affect the synthesis reaction of PBI resin, and will not bring about the problem of difficult film formation of composite films;
S3:将S2所述的聚合物溶液浇铸在模具中,干燥后进行热处理得到聚苯并咪唑薄膜;S3: casting the polymer solution described in S2 in a mold, and performing heat treatment after drying to obtain a polybenzimidazole film;
S4:将S3得到的聚苯并咪唑薄膜浸入磷酸后静置,静置后取出得到复合电解质膜。S4: the polybenzimidazole film obtained in S3 is immersed in phosphoric acid and then left to stand, and then taken out to obtain a composite electrolyte membrane.
聚苯并咪唑膜在磷酸掺杂处理后,因为大量的磷酸分子会进入到聚合物链之间破坏其中的氢键。并且掺入的磷酸分子的“强塑化”作用,会明显降低膜材料的机械性能,导致尺寸溶胀。交联一般是指在聚合物中形成网络结构的过程,是一种常见的聚合物改性方法,通过形成的网络结构可以在发生链段和链间运动时提供额外的作用力,从而提高膜材料的机械性能。而在发生溶胀时可以增强聚合物链间作用力,使得膜材料表现出更高的尺寸稳定性。同时,交联网络的形成可以在磷酸流失时提供更大的阻力,提高其磷酸保留能力。After the polybenzimidazole film is doped with phosphoric acid, a large number of phosphoric acid molecules will enter between the polymer chains to break the hydrogen bonds. And the "strong plasticization" effect of the incorporated phosphoric acid molecules will significantly reduce the mechanical properties of the membrane material, resulting in dimensional swelling. Crosslinking generally refers to the process of forming a network structure in a polymer, which is a common polymer modification method. Mechanical behavior. When swelling occurs, the interchain force of the polymer can be enhanced, so that the membrane material exhibits higher dimensional stability. At the same time, the formation of a cross-linked network can provide greater resistance to phosphoric acid loss and improve its phosphoric acid retention capacity.
所述S1中聚苯并咪唑、聚偏氯乙烯与有机溶剂的质量比为1:(100~400)。The mass ratio of polybenzimidazole, polyvinylidene chloride and organic solvent in the S1 is 1:(100-400).
所述S2中交联剂的质量与聚苯并咪唑和聚偏氯乙烯的质量比为1:(10~100),相比于离子交联结构,形成的共价交联结构对于膜的机械性能提高更为明显,意味着可以承受更高的磷酸掺杂水平,但同时,随着交联度的上升,将使得聚合物的链堆积的更为紧密,限制了磷酸的掺杂能力,两者相互影响相互制衡,因此需要控制优化交联剂的使用量以达到最优的效果。The mass ratio of the cross-linking agent in the S2 to the mass ratio of polybenzimidazole and polyvinylidene chloride is 1: (10-100). Compared with the ionic cross-linking structure, the formed covalent cross-linking structure is very important for the mechanical properties of the membrane. The performance improvement is more obvious, which means that it can withstand higher phosphoric acid doping levels, but at the same time, as the crosslinking degree increases, the polymer chains will be packed more tightly, which limits the doping ability of phosphoric acid. Therefore, it is necessary to control and optimize the amount of cross-linking agent to achieve the optimal effect.
所述S3中进行热处理的温度为150~200℃。The temperature at which the heat treatment is performed in the S3 is 150-200°C.
所述S3中进行干燥的温度为80~120℃。The drying temperature in S3 is 80-120°C.
所述的卤代物R-X中的X为Cl、Br或I。X in the halide R-X is Cl, Br or I.
所述S1中有机溶剂为N,N-二甲基甲酰胺、N,N-二甲基乙酰胺、二甲基亚砜和N-甲基吡咯烷酮中的以任意比例混合的混合物。The organic solvent in S1 is a mixture of N,N-dimethylformamide, N,N-dimethylacetamide, dimethyl sulfoxide and N-methylpyrrolidone in any proportion.
所述S4中静置的时间为1~12h。The standing time in S4 is 1-12 hours.
一种高导电能力的复合电解质膜是由上述制备方法制备而成。A composite electrolyte membrane with high electrical conductivity is prepared by the above preparation method.
有益效果:Beneficial effects:
(1)本发明提供的一种高导电能力的复合电解质膜及其制备方法,针对复合膜机械强度降低的问题,使用交联剂对其进行改性,本制备方法所使用的交联剂为二元或多元卤代物,且改性发生在PBI合成后,因此不参与PBI树脂合成反应,不会对PBI树脂合成反应带来不利影响,且不会带来复合膜成膜困难的问题。(1) A composite electrolyte membrane with high electrical conductivity and a preparation method thereof provided by the present invention, in view of the problem that the mechanical strength of the composite membrane is reduced, a cross-linking agent is used to modify it. The cross-linking agent used in the preparation method is: Binary or polyhalogenated compounds, and the modification occurs after PBI synthesis, so it does not participate in the PBI resin synthesis reaction, does not adversely affect the PBI resin synthesis reaction, and does not bring about the problem of difficulty in forming a composite film.
(2)通过添加交联剂使聚合物骨架具有网格状结构,同时通过优化交联剂的添加比例使复合膜具有较高的机械强度。(2) The polymer backbone has a grid-like structure by adding a cross-linking agent, and at the same time, the composite film has a higher mechanical strength by optimizing the addition ratio of the cross-linking agent.
(3)本制备方法所添加的交联剂的量为PBI/PVDF质量的1%-10%,既没有限制磷酸的掺杂能力,也使复合膜获得优异的机械性能。(3) The amount of the crosslinking agent added in this preparation method is 1%-10% of the mass of PBI/PVDF, which neither limits the doping ability of phosphoric acid, but also enables the composite membrane to obtain excellent mechanical properties.
(4)本发明的制备工艺简单、易实施,成本低、不改变PBI树脂合成过程和反应条件,对成膜设备也无改造要求,工艺非常简单,原料成本低,是易于批量化生产的工艺。(4) The preparation process of the present invention is simple, easy to implement, low in cost, does not change the PBI resin synthesis process and reaction conditions, and has no requirement for modification of film-forming equipment, the process is very simple, the cost of raw materials is low, and it is a process that is easy to mass-produce .
附图说明Description of drawings
图1是不同交联比例PVDF/聚苯并咪唑膜的拉伸曲线。Figure 1 shows the tensile curves of PVDF/polybenzimidazole films with different crosslinking ratios.
图2是不同交联比例PVDF/聚苯并咪唑/磷酸复合膜的质子电导率。Figure 2 shows the proton conductivity of PVDF/polybenzimidazole/phosphoric acid composite membranes with different crosslinking ratios.
具体实施方式Detailed ways
为了加深对本发明的理解,下面将结合实施例和附图对本发明作进一步详述,该实施例仅用于解释本发明,并不构成对本发明保护范围的限定。In order to deepen the understanding of the present invention, the present invention will be described in further detail below with reference to the embodiments and the accompanying drawings. The embodiments are only used to explain the present invention and do not constitute a limitation on the protection scope of the present invention.
实施例1Example 1
一种高导电能力的复合电解质膜的制备方法,主要包括以下步骤:A preparation method of a composite electrolyte membrane with high electrical conductivity mainly comprises the following steps:
(1)将0.6g聚苯并咪唑溶于100gN,N-二甲基甲酰胺中;(1) dissolve 0.6g of polybenzimidazole in 100g of N,N-dimethylformamide;
(2)待步骤(1)中的聚苯并咪唑完全溶解后,将聚合物溶液浇铸在平整模具中,在100℃下干燥使有机溶剂进行挥发;(2) after the polybenzimidazole in step (1) is completely dissolved, the polymer solution is cast in a flat mold, and dried at 100° C. to volatilize the organic solvent;
(3)待步骤(2)中的有机溶剂挥发彻底后,再在180℃下进行热处理形成聚苯并咪唑薄膜;(3) after the organic solvent in step (2) is completely volatilized, heat treatment at 180° C. to form a polybenzimidazole film;
(4)将聚苯并咪唑薄膜浸入130℃的浓硫酸中,静置12小时。(4) Immerse the polybenzimidazole film in concentrated sulfuric acid at 130° C. and let it stand for 12 hours.
实施例2Example 2
一种高导电能力的复合电解质膜的制备方法,主要包括以下步骤:A preparation method of a composite electrolyte membrane with high electrical conductivity mainly comprises the following steps:
(1)将0.6g聚苯并咪唑溶于100gN,N-二甲基甲酰胺中;(1) dissolve 0.6g of polybenzimidazole in 100g of N,N-dimethylformamide;
(2)待步骤(1)中的聚苯并咪唑完全溶解后,添加0.024g的卤代烃,搅拌均匀得到均一稳定的聚苯并咪唑溶液;(2) after the polybenzimidazole in step (1) is completely dissolved, add the halogenated hydrocarbon of 0.024g, and stir to obtain a uniform and stable polybenzimidazole solution;
(3)将聚合物溶液浇铸在平整模具中,在在100℃下干燥使有机溶剂进行挥发;(3) casting the polymer solution in a flat mold, drying at 100°C to volatilize the organic solvent;
(4)待步骤(3)中的有机溶剂挥发彻底后,再在180℃下进行热处理形成聚苯并咪唑薄膜;(4) after the organic solvent in step (3) is completely volatilized, heat treatment at 180° C. to form a polybenzimidazole film;
(5)将聚苯并咪唑薄膜浸入130℃的浓硫酸中,静置12小时。(5) Immerse the polybenzimidazole film in concentrated sulfuric acid at 130° C. and let it stand for 12 hours.
实施例3Example 3
一种高导电能力的复合电解质膜的制备方法,主要包括以下步骤:A preparation method of a composite electrolyte membrane with high electrical conductivity mainly comprises the following steps:
(1)将0.6g聚苯并咪唑溶于100gN,N-二甲基甲酰胺中;(1) dissolve 0.6g of polybenzimidazole in 100g of N,N-dimethylformamide;
(2)待步骤(1)中的聚苯并咪唑完全溶解后,添加0.042g的卤代烃,搅拌均匀得到均一稳定的聚苯并咪唑溶液;(2) after the polybenzimidazole in step (1) is completely dissolved, add the halogenated hydrocarbon of 0.042g, and stir to obtain a uniform and stable polybenzimidazole solution;
(3)将聚合物溶液浇铸在平整模具中,在在100℃下干燥使有机溶剂进行挥发;(3) casting the polymer solution in a flat mold, drying at 100°C to volatilize the organic solvent;
(4)待步骤(3)中的有机溶剂挥发彻底后,再在180℃下进行热处理形成聚苯并咪唑薄膜;(4) after the organic solvent in step (3) is completely volatilized, heat treatment at 180° C. to form a polybenzimidazole film;
(5)将聚苯并咪唑薄膜浸入130℃的浓硫酸中,静置12小时。(5) Immerse the polybenzimidazole film in concentrated sulfuric acid at 130° C. and let it stand for 12 hours.
对上述三组实施例制得的复合膜进行性能测试:The composite films prepared by the above-mentioned three groups of embodiments are tested for performance:
(一)机械性能测试(1) Mechanical performance test
测试方法:在测试前,将所有样品裁剪成一定规格的样片,运行过程中的复合电解质膜必须具有一定的机械性能承受两侧气体流产生的压力,因此对膜样品进行拉伸测试来评估其机械性能,图1是使用不同交联剂比例制得的复合膜的拉伸曲线,从图1中可看出,实施例1因为没有添加交联剂,因此在进行磷酸掺杂处理后,大量的磷酸分子进入到聚合物中起到“强塑化”的作用,使得复合膜表现出较低的机械强度,实施例3中当交联剂的比例为PBI质量的7%时,所具有的拉伸强度最好。Test method: Before the test, all samples are cut into samples of a certain size. The composite electrolyte membrane during operation must have certain mechanical properties to withstand the pressure generated by the gas flow on both sides. Therefore, a tensile test is performed on the membrane samples to evaluate its performance. Mechanical properties, Figure 1 is the tensile curve of the composite film prepared by using different ratios of cross-linking agents. It can be seen from Figure 1 that because no cross-linking agent is added in Example 1, after phosphoric acid doping treatment, a large amount of The phosphoric acid molecules enter the polymer to play the role of "strong plasticization", which makes the composite film show lower mechanical strength. In Example 3, when the proportion of crosslinking agent is 7% of the mass of PBI, the Tensile strength is the best.
(二)质子传导率测试(2) Proton conductivity test
将三组实施例制得的复合膜样品裁剪成同等规格,将裁减后的样品用于质子传导率测试。测试在从180℃到100℃的降温过程中进行以去除水的影响,样品的阻抗值(R)通过四电极AC阻抗法测得,通过计算得到质子传导率σ,公式为:σ=L/(A×R);其中L为两电极间的距离;A为膜样品的横截面积。图2是使用不同交联剂比例制得的复合膜的质子电导率,从图中可以看出当交联剂的比例为PBI质量的4%时电导率最好。The composite membrane samples prepared in the three groups of examples were cut into the same specifications, and the cut samples were used for proton conductivity test. The test was carried out during the cooling process from 180°C to 100°C to remove the influence of water. The impedance value (R) of the sample was measured by the four-electrode AC impedance method, and the proton conductivity σ was obtained by calculation. The formula is: σ=L/ (A×R); where L is the distance between the two electrodes; A is the cross-sectional area of the film sample. Figure 2 shows the proton conductivity of composite membranes prepared with different ratios of cross-linking agents. It can be seen from the figure that the conductivity is the best when the ratio of cross-linking agent is 4% of the mass of PBI.
作为进一步改进,以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。As a further improvement, the above are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall include within the protection scope of the present invention.
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