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CN1385915A - Composite type proteon exchange film for high-temp. direct methanol fue cell and preparation process thereof - Google Patents

Composite type proteon exchange film for high-temp. direct methanol fue cell and preparation process thereof Download PDF

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CN1385915A
CN1385915A CN02115184A CN02115184A CN1385915A CN 1385915 A CN1385915 A CN 1385915A CN 02115184 A CN02115184 A CN 02115184A CN 02115184 A CN02115184 A CN 02115184A CN 1385915 A CN1385915 A CN 1385915A
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proton exchange
exchange membrane
acid
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CN1202583C (en
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周震涛
何燕
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South China University of Technology SCUT
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

本发明涉及电化学的燃料电池技术,更详细地是高温直接甲醇燃料电池用质子交换膜以及该膜的制备方法。本发明的高温直接甲醇燃料电池用复合型质子交换膜是以市售的聚偏氟乙烯或聚乙烯醇为原料,并加入掺有无机多元酸的纳米陶瓷粉末,通过流延热压法、涂浆法、压延法或浸胶法制备的具有纳米微孔结构的复合型质子交换膜。本发明所制备的质子交换膜具有纳米微孔结构,80~180℃温度范围的甲醇渗透率比Nafion膜的小,阻醇性能好。本发明制备质子交换膜的制备工艺简单,膜的成本低于Nafion膜,易于产业化,可用作在高温(100℃以上)下也能正常运转的直接甲醇燃料电池的质子交换膜。The present invention relates to electrochemical fuel cell technology, in particular to a high-temperature direct methanol fuel cell proton exchange membrane and a preparation method of the membrane. The composite proton exchange membrane for high-temperature direct methanol fuel cell of the present invention uses commercially available polyvinylidene fluoride or polyvinyl alcohol as raw material, and adds nano-ceramic powder mixed with inorganic polybasic acid. Composite proton exchange membrane with nano-microporous structure prepared by slurry method, calendering method or dipping method. The proton exchange membrane prepared by the invention has a nano-microporous structure, the methanol permeability in the temperature range of 80-180 DEG C is smaller than that of the Nafion membrane, and the alcohol resistance performance is good. The preparation process of the proton exchange membrane prepared by the present invention is simple, the cost of the membrane is lower than that of the Nafion membrane, the industrialization is easy, and it can be used as the proton exchange membrane of the direct methanol fuel cell which can also operate normally at high temperature (above 100°C).

Description

高温直接甲醇燃料电池用复合型质子交换膜及其制备方法Composite proton exchange membrane for high temperature direct methanol fuel cell and preparation method thereof

技术领域technical field

本发明涉及电化学的燃料电池技术,更详细地是高温直接甲醇燃料电池用质子交换膜,本发明还涉及了该膜的制备方法。The invention relates to an electrochemical fuel cell technology, more specifically a proton exchange membrane for a high-temperature direct methanol fuel cell, and also relates to a preparation method for the membrane.

背景技术Background technique

当今世界燃油汽车尾气的排放已成为环境污染的主要来源之一,研制以电能为动力源的电动汽车则是减小燃油车辆尾气排放量,降低环境污染程度的有效手段。而具有“零排放”特征的燃料电池则是最有希望代替现有的燃油发动机作汽车动力源的新型能源。在各种不同类型的燃料电池之中,直接甲醇燃料电池(DMFC)除了具有其它燃料电池一般优点之外,还具有燃料来源丰富易得、价格便宜、易于运输和贮存、电池结构简单、体积和重量小(约为氢氧燃料电池的1/3)以及成本较低(约为氢氧燃料电池的1/2)等优点。因此,直接甲醇燃料电池(DMFC)系统是最适宜用作电动汽车或者其它便携式设备用的可移动动力电源。由于该燃料电池系统所使用的燃料甲醇在100℃以下的催化氧化反应进行相当缓慢,影响了系统的整体性能。因此,高温(100℃以上)直接甲醇燃料电池成为燃料电池发展的新的趋势。然而,现有在直接甲醇燃料电池中使用的Nafion膜不但存在价格昂贵的问题,而且还存在着高温质子传导性能差、甲醇对膜的渗透率高并且该两缺点还随着温度的升高而增大等问题,不适于用在高温直接甲醇燃料电池方面。因此,如何提高质子交换膜的高温质子传导速率,降低其高温下甲醇的渗透率,研制出高性能低成本的新型质子交换膜,是开发高温直接甲醇燃料电池的一项重大技术难题。研究人员目前纷纷将此类燃料电池的研究重点集中在质子交换膜方面。In today's world, fuel vehicle exhaust emissions have become one of the main sources of environmental pollution. The development of electric vehicles powered by electric energy is an effective means to reduce the exhaust emissions of fuel vehicles and reduce the degree of environmental pollution. The fuel cell with the characteristics of "zero emission" is the most promising new energy source to replace the existing fuel engine as the power source of automobiles. Among various types of fuel cells, in addition to other general advantages of fuel cells, direct methanol fuel cells (DMFC) also have the advantages of abundant and easy-to-obtain fuel sources, cheap prices, easy transportation and storage, simple battery structure, volume and It has the advantages of small weight (about 1/3 of hydrogen-oxygen fuel cell) and low cost (about 1/2 of hydrogen-oxygen fuel cell). Therefore, the direct methanol fuel cell (DMFC) system is the most suitable mobile power source for electric vehicles or other portable devices. Since the catalytic oxidation reaction of fuel methanol used in the fuel cell system is very slow at temperatures below 100° C., the overall performance of the system is affected. Therefore, high temperature (above 100°C) direct methanol fuel cells have become a new trend in the development of fuel cells. However, the existing Nafion membrane used in direct methanol fuel cells not only has the problem of high price, but also has poor proton conductivity at high temperature, high permeability of methanol to the membrane, and these two shortcomings also decrease with the increase of temperature. Problems such as increase, are not suitable for use in high-temperature direct methanol fuel cells. Therefore, how to improve the high-temperature proton conduction rate of the proton exchange membrane, reduce its methanol permeability at high temperature, and develop a new type of proton exchange membrane with high performance and low cost is a major technical problem in the development of high-temperature direct methanol fuel cells. Researchers are currently focusing their research on this type of fuel cell on the proton exchange membrane.

发明内容Contents of the invention

本发明的目的在于克服现有技术的不足之处,提供一种高温下的质子传导性能和阻醇性能好,且价格低于市售Nafion膜的价格,可应用在高温直接甲醇燃料电池中的复合型质子交换膜。The purpose of the present invention is to overcome the deficiencies of the prior art, to provide a high-temperature proton conductivity and good alcohol resistance, and the price is lower than the price of the commercially available Nafion membrane, which can be applied in high-temperature direct methanol fuel cells Composite proton exchange membrane.

本发明还提供了上述高温直接甲醇燃料电池用复合型质子交换膜的制备方法。The invention also provides a preparation method of the composite proton exchange membrane for the high-temperature direct methanol fuel cell.

本发明的高温直接甲醇燃料电池用复合型质子交换膜是以市售的聚偏氟乙烯或聚乙烯醇为原料,并加入掺有无机多元酸的纳米陶瓷粉末,通过流延热压法、涂浆法、压延法或浸胶法制备的具有纳米微孔结构的复合型质子交换膜;The composite proton exchange membrane for high-temperature direct methanol fuel cell of the present invention uses commercially available polyvinylidene fluoride or polyvinyl alcohol as raw material, and adds nano-ceramic powder mixed with inorganic polybasic acid. Composite proton exchange membrane with nano-microporous structure prepared by slurry method, calendering method or dipping method;

所述的无机多元酸是指通式为A3BM12O40·nH2O具有阴离子簇为[BM12O40]n结构(Keggin结构)的化合物,其中A=H,B=Si、P,M=Mo、W;无机多元酸选自硅钨酸、磷钼酸、磷钨酸或硅钼酸等;The inorganic polybasic acid refers to a compound with the general formula A 3 BM 12 O 40 ·nH 2 O having an anionic cluster of [BM 12 O 40 ] n structure (Keggin structure), wherein A=H, B=Si, P , M=Mo, W; the inorganic polybasic acid is selected from silicotungstic acid, phosphomolybdic acid, phosphotungstic acid or silicomolybdic acid, etc.;

所述的纳米陶瓷粉末是指掺有无机多元酸的陶瓷化合物,其中的纳米无机陶瓷粉末选自硅土、锆土或二氧化硅粉末,颗粒粒径≤30nm。The nano-ceramic powder refers to a ceramic compound mixed with inorganic polybasic acid, wherein the nano-inorganic ceramic powder is selected from silica, zirconia or silicon dioxide powder, and the particle size is ≤30nm.

本发明的具体制备过程如下:Concrete preparation process of the present invention is as follows:

(1)在纳米陶瓷粉末中加入相当于纳米陶瓷粉末重量5%~50%的无(1) Add 5% to 50% of the weight of the nano-ceramic powder in the nano-ceramic powder without

   机多元酸,混合均匀后待用;Organic polybasic acid, mix well and set aside;

(2)取100重量份的聚偏氟乙烯或聚乙烯醇与15~70重量份的掺有无(2) Take 100 parts by weight of polyvinylidene fluoride or polyvinyl alcohol and 15 to 70 parts by weight of

   机多元酸的纳米陶瓷粉末混合均匀备料;The nano-ceramic powder of organic polybasic acid is mixed evenly and prepared;

(3)将聚偏氟乙烯或聚乙烯醇溶解于常规溶剂配制成高分子溶液,并(3) dissolving polyvinylidene fluoride or polyvinyl alcohol in a conventional solvent to prepare a polymer solution, and

   向该高分子溶液中加入掺有无机多元酸的纳米陶瓷粉末,均匀振Add nano-ceramic powder mixed with inorganic polybasic acid to the polymer solution, vibrate evenly

   荡5~30分钟,其中的常规溶剂选自N-甲基吡咯烷酮、丙酮或者Swing for 5 to 30 minutes, the conventional solvent is selected from N-methylpyrrolidone, acetone or

   水; water;

(4)采用流延热压法,将此混合液平铺在玻璃培养皿表面,在室温~(4) Spread the mixed solution on the surface of the glass petri dish by casting hot pressing method, at room temperature ~

   90℃加热10~40分钟,然后在室温下干燥0.5~20小时,将溶剂Heating at 90°C for 10-40 minutes, then drying at room temperature for 0.5-20 hours, the solvent

   干燥后所形成的薄膜从培养皿表面撕下,在100~170℃下热压3~The film formed after drying is torn off from the surface of the petri dish, and hot-pressed at 100-170°C for 3-

   20分钟即可;或者采用涂浆法、压延法或浸胶法工艺制备成膜。It takes 20 minutes; or the film can be prepared by slurrying method, calendering method or dipping method.

本发明与现有材料和技术相比具有如下的优点:Compared with existing materials and technologies, the present invention has the following advantages:

1.利用本发明所提出的制备方法制成的具有纳米微孔结构的复合型质子交1. The compound type proton exchange compound with nano-microporous structure made by the preparation method proposed by the present invention

  换膜在高温下的质子传导性能优异,其质子传导速率大于Nafion膜的质The exchange membrane has excellent proton conduction performance at high temperature, and its proton conduction rate is greater than that of Nafion membrane.

  子传导率。sub-conductivity.

2.利用本发明所制备的质子交换膜具有纳米微孔结构,80~180℃温度范围2. The proton exchange membrane prepared by the present invention has a nano-microporous structure, and the temperature range is 80-180°C

  的甲醇渗透率比Nafion膜的小,阻醇性能好。以样品1为例,详见表1。The methanol permeability is smaller than that of Nafion membrane, and the alcohol resistance performance is good. Take sample 1 as an example, see Table 1 for details.

3.本发明制备质子交换膜的制备工艺简单,膜成本低于Nafion膜,易于产3. the present invention prepares the preparation technology of proton exchange membrane simple, and membrane cost is lower than Nafion membrane, is easy to produce

  业化,将可推动高温直接甲醇燃料电池的发展。Industrialization will promote the development of high-temperature direct methanol fuel cells.

具体实施方式Detailed ways

实施例1Example 1

在粒径为7.5nm的二氧化硅粉末中掺杂相当于二氧化硅粉末重量30%的磷钨酸,混合均匀。称取100重量份的聚偏氟乙烯和60重量份掺有磷钨酸的二氧化硅,将聚偏氟乙烯溶解在N-甲基吡咯烷酮中形成高分子溶液,向其中加入含30%磷钨酸的二氧化硅,用超声波均匀振荡20分钟;将此混合溶液平铺在培养皿表面,在80℃下加热20分钟,室温下干燥15小时成膜,最后将此薄膜于160℃下热压10分钟即可,所制得的膜为样品1。用前先将膜在80℃下浸泡于去离子水中3小时。样品1与Nafion膜的高温甲醇渗透的比较详见表1。Dope phosphotungstic acid equivalent to 30% of the weight of the silicon dioxide powder into the silicon dioxide powder with a particle size of 7.5nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 60 parts by weight of silicon dioxide doped with phosphotungstic acid, dissolve polyvinylidene fluoride in N-methylpyrrolidone to form a polymer solution, and add 30% phosphotungsten Acidic silicon dioxide, vibrate evenly with ultrasonic waves for 20 minutes; spread the mixed solution on the surface of a petri dish, heat at 80°C for 20 minutes, dry at room temperature for 15 hours to form a film, and finally press the film at 160°C Just 10 minutes, and the prepared film is sample 1. Soak the membrane in deionized water at 80°C for 3 hours before use. The comparison of high temperature methanol permeation between sample 1 and Nafion membrane is shown in Table 1.

实施例2Example 2

在粒径为7.5nm的二氧化硅粉末中掺入相当于二氧化硅粉末重量45%的硅钨酸,混合均匀。称取100重量份的聚偏氟乙烯和60重量份掺有磷钨酸的二氧化硅,将聚偏氟乙烯溶解在N-甲基吡咯烷酮中形成高分子溶液,向其中加入含45%磷钨酸的二氧化硅,用超声波振荡20分钟;将此混合溶液平铺在培养皿表面,在90℃下加热5分钟,室温干燥15小时成膜,最后将此薄膜于160℃下热压10分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add silicotungstic acid equivalent to 45% of the weight of the silicon dioxide powder into the silicon dioxide powder with a particle size of 7.5nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 60 parts by weight of silicon dioxide doped with phosphotungstic acid, dissolve polyvinylidene fluoride in N-methylpyrrolidone to form a polymer solution, add 45% tungsten phospho Acidic silicon dioxide, vibrated by ultrasonic waves for 20 minutes; spread the mixed solution on the surface of a petri dish, heat at 90°C for 5 minutes, dry at room temperature for 15 hours to form a film, and finally press the film at 160°C for 10 minutes That's it. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例3Example 3

在粒径为12nm的硅土粉末中掺入相当于硅土粉末重量30%的磷钨酸,混合均匀。称取100重量份的聚偏氟乙烯和70重量份掺有磷钨酸的硅土粉末,将聚偏氟乙烯溶解在N-甲基吡咯烷酮中形成高分子溶液,向其中加入含30%磷钨酸的硅土,用超声波均匀振荡10分钟;将此混合溶液平铺在培养皿表面,在25℃下加热40分钟,室温下干燥24小时成膜,最后将此薄膜于170℃下热压3分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add phosphotungstic acid equivalent to 30% of the weight of the silica powder into the silica powder with a particle size of 12nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 70 parts by weight of silica powder mixed with phosphotungstic acid, dissolve polyvinylidene fluoride in N-methylpyrrolidone to form a polymer solution, and add 30% phosphotungsten Acidic silica, vibrate evenly with ultrasonic wave for 10 minutes; spread the mixed solution on the surface of the petri dish, heat at 25°C for 40 minutes, dry at room temperature for 24 hours to form a film, and finally press the film at 170°C for 3 minutes. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例4Example 4

在粒径为12nm的锆土粉末中掺入相当于锆土粉末重量50%的硅钨酸,混合均匀。称取100重量份的聚偏氟乙烯和15重量份掺有硅钨酸的锆土粉末,将聚偏氟乙烯溶解在丙酮中形成高分子溶液,向其中加入含50%硅钨酸的锆土粉末,用超声波振荡30分钟;将此混合溶液平铺在培养皿表面,在90℃下加热5分钟,室温下干燥1小时成膜,最后将此薄膜于100℃下热压20分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add silicotungstic acid equivalent to 50% of the weight of the zirconia powder into the zirconia powder with a particle size of 12nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 15 parts by weight of zirconia powder mixed with silicotungstic acid, dissolve polyvinylidene fluoride in acetone to form a polymer solution, and add zirconia containing 50% silicotungstic acid to it Powder, oscillate with ultrasound for 30 minutes; spread the mixed solution on the surface of a petri dish, heat at 90°C for 5 minutes, dry at room temperature for 1 hour to form a film, and finally press the film at 100°C for 20 minutes. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例5Example 5

在粒径为12nm的硅土粉末中掺入相当于硅土粉末重量5%的磷钨酸,混合均匀。称取100重量份的聚偏氟乙烯和40重量份掺有磷钨酸的硅土粉末,将聚偏氟乙烯溶解在N-甲基吡咯烷酮中形成高分子溶液,向其中加入含1%磷钨酸的硅土粉末,用超声波振荡1分钟;将此混合溶液平铺在培养皿表面,在70℃下加热20分钟,室温下干燥0.5小时成膜,最后将此薄膜于160℃下热压10分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add phosphotungstic acid equivalent to 5% of the weight of the silica powder into the silica powder with a particle size of 12nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 40 parts by weight of silica powder mixed with phosphotungstic acid, dissolve polyvinylidene fluoride in N-methylpyrrolidone to form a polymer solution, and add 1% phosphotungsten Acidic silica powder, oscillated by ultrasound for 1 minute; spread the mixed solution on the surface of a petri dish, heat at 70°C for 20 minutes, dry at room temperature for 0.5 hour to form a film, and finally heat press the film at 160°C for 10 minutes. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例6Example 6

在粒径为7.5nm的硅土粉末中掺入相当于硅土粉末重量45%的磷钨酸,混合均匀。称取100重量份的聚偏氟乙烯和70重量份掺有磷钨酸的硅土粉末,将聚偏氟乙烯溶解在丙酮中形成高分子溶液,向其中加入含45%磷钨酸的硅土粉末,用超声波振荡30分钟;将此混合溶液平铺在培养皿表面,在60℃下加热10分钟,室温下干燥20小时成膜,最后将此薄膜于100℃下热压20分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add phosphotungstic acid equivalent to 45% of the weight of the silica powder into the silica powder with a particle size of 7.5nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 70 parts by weight of silica powder mixed with phosphotungstic acid, dissolve polyvinylidene fluoride in acetone to form a polymer solution, and add silica containing 45% phosphotungstic acid Powder, oscillate with ultrasound for 30 minutes; spread the mixed solution on the surface of a petri dish, heat at 60°C for 10 minutes, dry at room temperature for 20 hours to form a film, and finally press the film at 100°C for 20 minutes. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例7Example 7

在粒径为12nm的锆土粉末中掺入相当于锆土粉末重量30%的磷钨酸,混合均匀。称取100重量份的聚偏氟乙烯和70重量份掺有磷钨酸的锆土粉末,将聚偏氟乙烯溶解在丙酮中形成高分子溶液,向其中加入含30%磷钨酸的锆土粉末,用超声波振荡30分钟;将此混合溶液平铺在培养皿表面,在50℃下加热40分钟,室温下干燥20小时成膜,最后将此薄膜于170℃下热压5分钟即可。用前先将膜在80℃下浸泡于去离子水中3小时。Add phosphotungstic acid equivalent to 30% of the weight of the zirconia powder into the zirconia powder with a particle size of 12nm, and mix evenly. Weigh 100 parts by weight of polyvinylidene fluoride and 70 parts by weight of zirconia powder mixed with phosphotungstic acid, dissolve polyvinylidene fluoride in acetone to form a polymer solution, and add zirconia containing 30% phosphotungstic acid Powder, oscillate with ultrasound for 30 minutes; spread the mixed solution on the surface of a petri dish, heat at 50°C for 40 minutes, dry at room temperature for 20 hours to form a film, and finally heat-press the film at 170°C for 5 minutes. Soak the membrane in deionized water at 80°C for 3 hours before use.

实施例8Example 8

在粒径为12nm的锆土粉末中掺入相当于锆土粉末重量30%的磷钨酸,混合均匀。称取100重量份的聚乙烯醇和70重量份掺有磷钨酸的锆土粉末混合均匀,采用压延法,将粘合剂高压聚乙烯在压延机中加热混炼至塑化完全,随即加入增柔剂橡胶,均一混合后加入少量润滑剂和上述的混合物料,反复混炼、拉膜,在膜两边覆盖上尼龙网布,并经油压机热压,冷却后成膜。Add phosphotungstic acid equivalent to 30% of the weight of the zirconia powder into the zirconia powder with a particle size of 12nm, and mix evenly. Weigh 100 parts by weight of polyvinyl alcohol and 70 parts by weight of zirconia powder mixed with phosphotungstic acid and mix evenly. Using the calendering method, heat and knead the adhesive high-pressure polyethylene in a calender until it is completely plasticized, and then add Softener rubber, after uniform mixing, add a small amount of lubricant and the above-mentioned mixed materials, repeatedly knead, pull the film, cover both sides of the film with nylon mesh, and press it with a hydraulic press, and form a film after cooling.

实施例9Example 9

在粒径为7.5nm的二氧化硅粉末中掺入相当于二氧化硅粉末重量45%的硅钨酸,混合均匀。称取100重量份的聚乙烯醇和60重量份掺有磷钨酸的二氧化硅,采用涂浆法,将聚乙烯醇加热溶解于水中,向其中加入含45%磷钨酸的二氧化硅,超声波振荡1分钟,配制成浆液,倾倒在预先铺好玻璃布的钢板上,用玻璃棒推动膜液,覆盖聚酯膜,用压辊挤除残液,压上钢板,加热保温,最后冷却至室温,剥离聚酯膜后即得到所需的复合型质子交换膜。Add silicotungstic acid equivalent to 45% of the weight of the silicon dioxide powder into the silicon dioxide powder with a particle size of 7.5nm, and mix evenly. Weigh 100 parts by weight of polyvinyl alcohol and 60 parts by weight of silicon dioxide mixed with phosphotungstic acid, use the slurry method, heat and dissolve polyvinyl alcohol in water, add silicon dioxide containing 45% phosphotungstic acid, Ultrasonic vibration for 1 minute, prepare a slurry, pour it on a steel plate covered with glass cloth in advance, push the film liquid with a glass rod, cover the polyester film, squeeze out the residual liquid with a pressure roller, press it on the steel plate, heat and keep it warm, and finally cool to After peeling off the polyester membrane at room temperature, the required composite proton exchange membrane can be obtained.

实施例10Example 10

在粒径为7.5nm的硅土粉末中掺入相当于硅土粉末重量45%的磷钨酸,混合均匀。称取100重量份的聚乙烯醇和70重量份掺有磷钨酸的硅土粉末,采用浸胶法,将聚乙烯醇加热溶解于水中,向其中加入含45%磷钨酸的硅土粉末,用超声波振荡30分钟,混合成浆液状,经脱泡后,将其涂刮在维纶网布上,风干后成膜。Add phosphotungstic acid equivalent to 45% of the weight of the silica powder into the silica powder with a particle size of 7.5nm, and mix evenly. Weigh 100 parts by weight of polyvinyl alcohol and 70 parts by weight of silica powder mixed with phosphotungstic acid, heat and dissolve polyvinyl alcohol in water by dipping method, add silica powder containing 45% phosphotungstic acid to it, Vibrate ultrasonically for 30 minutes, mix it into a slurry, after defoaming, apply it on the vinylon mesh, and form a film after air drying.

表1本发明的质子交换膜与Nafion膜的高温甲醇渗透率的比较   温度T(℃)   甲醇浓度(mol/L)   甲醇渗透率(S-1cm2×10-6)   样品1   Nafion117     80     1.0     1.2    4.4     110     1.0     2.0    7.9     130     1.0     2.4    9.1     160     1.0     3.7    13.3 The comparison of the high-temperature methanol permeability of the proton exchange membrane of the present invention and the Nafion membrane of table 1 Temperature T(°C) Methanol concentration (mol/L) Methanol permeability (S -1 cm 2 ×10 -6 ) sample 1 Nafion117 80 1.0 1.2 4.4 110 1.0 2.0 7.9 130 1.0 2.4 9.1 160 1.0 3.7 13.3

Claims (4)

1.一种高温直接甲醇燃料电池用复合型质子交换膜的制备方法,其特征在于其配比和工艺条件如下:1. A method for preparing a composite proton exchange membrane for a high-temperature direct methanol fuel cell, characterized in that its proportioning and process conditions are as follows: (1)在纳米陶瓷粉末中加入相当于纳米陶瓷粉末重量5%~50%的无机多元酸,混合均匀后待用;(1) adding an inorganic polybasic acid equivalent to 5% to 50% of the weight of the nano-ceramic powder in the nano-ceramic powder, and mixing it uniformly for use; (2)取100重量份的聚偏氟乙烯或聚乙烯醇与15~70重量份的掺有无机多元酸的纳米陶瓷粉末,混合均匀备料;(2) Get 100 parts by weight of polyvinylidene fluoride or polyvinyl alcohol and 15 to 70 parts by weight of nano-ceramic powder mixed with inorganic polybasic acid, mix and prepare materials; (3)将聚偏氟乙烯或聚乙烯醇溶解于常规溶剂配制成高分子溶液,并向该高分子溶液中加入掺有无机多元酸的纳米陶瓷粉末,均匀振荡5~30分钟,其中的常规溶剂选自N-甲基吡咯烷酮、丙酮或者水;(3) Dissolve polyvinylidene fluoride or polyvinyl alcohol in a conventional solvent to prepare a polymer solution, and add nano-ceramic powder mixed with an inorganic polybasic acid to the polymer solution, and shake it uniformly for 5 to 30 minutes. The solvent is selected from N-methylpyrrolidone, acetone or water; (4)采用流延热压法,将此混合液平铺在玻璃培养皿表面,在室温~90℃加热10~40分钟,而后室温干燥0.5~20小时;将溶剂干燥后形成的薄膜从培养皿表面撕下,在100~170℃下热压3~20分钟;或者采用涂浆法、压延法或浸胶法工艺制备成膜。(4) Spread the mixed solution on the surface of the glass culture dish by casting hot pressing method, heat at room temperature to 90°C for 10 to 40 minutes, and then dry at room temperature for 0.5 to 20 hours; The surface of the dish is torn off, and hot-pressed at 100-170° C. for 3-20 minutes; or prepared into a film by slurrying, calendering or dipping. 2.根据权利要求1所述的一种高温直接甲醇燃料电池用复合型质子交换膜制备方法,其特征在于:2. a kind of high-temperature direct methanol fuel cell composite proton exchange membrane preparation method according to claim 1, is characterized in that: 无机多元酸是指通式为A3BM12O40·nH2O具有阴离子簇为[BM12O40]n结构(Keggin结构)的化合物,其中A=H,B=Si、P,M=Mo、W;无机多元酸选自硅钨酸、磷钼酸、磷钨酸或硅钼酸等;Inorganic polybasic acid refers to the compound whose general formula is A 3 BM 12 O 4 0·nH 2 O and the anion cluster is [BM 12 O 40 ] n structure (Keggin structure), where A=H, B=Si, P, M =Mo, W; Inorganic polybasic acid is selected from silicotungstic acid, phosphomolybdic acid, phosphotungstic acid or silicomolybdic acid, etc.; 纳米陶瓷粉末选自硅土、锆土或二氧化硅粉末,颗粒粒径≤30nm。The nano-ceramic powder is selected from silica, zirconia or silicon dioxide powder, and the particle size is less than or equal to 30nm. 3.根据权利要求1所述的一种高温直接甲醇燃料电池用复合型质子交换膜制备方法,其特征在于:3. a kind of high temperature direct methanol fuel cell composite proton exchange membrane preparation method according to claim 1, is characterized in that: (1)在粒径5~20nm的二氧化硅粉末中加入相当于二氧化硅粉末重量25~35%的磷钨酸或者加入相当于二氧化硅粉末重量40~50%的硅钨酸,混合均匀后待用;(1) Add phosphotungstic acid equivalent to 25-35% of the weight of silicon dioxide powder or silicotungstic acid equivalent to 40-50% of the weight of silicon dioxide powder to the silicon dioxide powder with a particle size of 5-20nm, and mix Uniform and ready for use; (2)取100重量份的聚偏氟乙烯或聚乙烯醇与30~60重量份的掺有磷钨酸或硅钨酸的二氧化硅粉末混合均匀备料;(2) Get 100 parts by weight of polyvinylidene fluoride or polyvinyl alcohol and 30 to 60 parts by weight of silicon dioxide powder mixed with phosphotungstic acid or silicotungstic acid and mix them evenly to prepare materials; (3)将聚偏氟乙烯或聚乙烯醇溶解于常规溶剂配制成高分子溶液,并向该高分子溶液中加入掺有磷钨酸或硅钨酸的二氧化硅粉末,用超声波均匀振荡30分钟,其中的常规溶剂选自N-甲基吡咯烷酮、丙酮或者水;(3) Dissolve polyvinylidene fluoride or polyvinyl alcohol in a conventional solvent to prepare a polymer solution, and add silicon dioxide powder mixed with phosphotungstic acid or silicotungstic acid to the polymer solution, and oscillate evenly for 30 Minutes, wherein the conventional solvent is selected from N-methylpyrrolidone, acetone or water; (4)混合液平铺在玻璃培养皿表面,在40~80℃加热10~30分钟,而后室温干燥2~15小时;将溶剂干燥后形成的薄膜从培养皿表面撕下,在130℃~170℃热压5~15分钟,或者采用涂浆法、压延法或浸胶法工艺制备成膜。(4) Spread the mixed solution on the surface of the glass petri dish, heat it at 40-80°C for 10-30 minutes, and then dry it at room temperature for 2-15 hours; tear off the film formed after the solvent is dried from the surface of the petri dish, and heat it at 130°C- Hot press at 170°C for 5 to 15 minutes, or prepare a film by slurrying, calendering or dipping. 4.采用权利要求1~3所述的制备方法制得的高温直接甲醇燃料电池用复合型质子交换膜。4. The composite proton exchange membrane for high-temperature direct methanol fuel cells prepared by the preparation method according to claims 1-3.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7115333B2 (en) * 2003-02-07 2006-10-03 Gas Technology Institute High temperature composite proton exchange membranes
US8124294B2 (en) 2006-10-04 2012-02-28 Samsung Sdi Co., Ltd. Polymer electrolyte membrane comprising inorganic nanoparticle bonded with proton-conducting group and solid acid, fuel cell including the same, and method of preparing the polymer electrolyte membrane
CN102714320A (en) * 2010-01-25 2012-10-03 雷蒙特亚特特拉维夫大学有限公司 Electrochemical systems and methods of operating same
CN102847449A (en) * 2012-09-25 2013-01-02 内蒙古科技大学 Preparation method of phosphotungstic acid/polyvinyl alcohol composite proton exchange membrane
CN104347886A (en) * 2014-09-29 2015-02-11 成都新柯力化工科技有限公司 Fuel cell ceramic proton exchange membrane material and use thereof
CN104681834A (en) * 2015-02-05 2015-06-03 成都新柯力化工科技有限公司 Keratin fuel battery proton exchange membrane and preparation method
CN104681833A (en) * 2015-02-05 2015-06-03 成都新柯力化工科技有限公司 Nano ceramic fiber tube fuel battery proton exchange membrane and preparation method
CN110433874A (en) * 2019-09-06 2019-11-12 温州旭扬膜结构工程有限公司 A kind of phosphotungstomolybdic acid-metal organic frame proton exchange membrane and its preparation method
CN113410496A (en) * 2021-06-16 2021-09-17 东北大学秦皇岛分校 All-solid-state trace water-containing low-temperature applicable proton exchange membrane and preparation method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7115333B2 (en) * 2003-02-07 2006-10-03 Gas Technology Institute High temperature composite proton exchange membranes
US8124294B2 (en) 2006-10-04 2012-02-28 Samsung Sdi Co., Ltd. Polymer electrolyte membrane comprising inorganic nanoparticle bonded with proton-conducting group and solid acid, fuel cell including the same, and method of preparing the polymer electrolyte membrane
CN102714320B (en) * 2010-01-25 2015-07-15 雷蒙特亚特特拉维夫大学有限公司 Electrochemical systems and methods of operating same
CN102714320A (en) * 2010-01-25 2012-10-03 雷蒙特亚特特拉维夫大学有限公司 Electrochemical systems and methods of operating same
CN102847449A (en) * 2012-09-25 2013-01-02 内蒙古科技大学 Preparation method of phosphotungstic acid/polyvinyl alcohol composite proton exchange membrane
CN102847449B (en) * 2012-09-25 2014-12-10 内蒙古科技大学 Preparation method of phosphotungstic acid/polyvinyl alcohol composite proton exchange membrane
CN104347886B (en) * 2014-09-29 2017-02-15 成都新柯力化工科技有限公司 Fuel cell ceramic proton exchange membrane material and use thereof
CN104347886A (en) * 2014-09-29 2015-02-11 成都新柯力化工科技有限公司 Fuel cell ceramic proton exchange membrane material and use thereof
CN104681833A (en) * 2015-02-05 2015-06-03 成都新柯力化工科技有限公司 Nano ceramic fiber tube fuel battery proton exchange membrane and preparation method
CN104681834A (en) * 2015-02-05 2015-06-03 成都新柯力化工科技有限公司 Keratin fuel battery proton exchange membrane and preparation method
CN104681833B (en) * 2015-02-05 2017-02-22 成都新柯力化工科技有限公司 Nano ceramic fiber tube fuel battery proton exchange membrane and preparation method
CN110433874A (en) * 2019-09-06 2019-11-12 温州旭扬膜结构工程有限公司 A kind of phosphotungstomolybdic acid-metal organic frame proton exchange membrane and its preparation method
CN113410496A (en) * 2021-06-16 2021-09-17 东北大学秦皇岛分校 All-solid-state trace water-containing low-temperature applicable proton exchange membrane and preparation method thereof
CN113410496B (en) * 2021-06-16 2023-02-14 东北大学秦皇岛分校 All-solid-state trace water-containing low-temperature applicable proton exchange membrane and preparation method thereof

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