CN111342097A - Preparation method of electrolyte membrane with high conductivity and good mechanical property - Google Patents
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- 239000012528 membrane Substances 0.000 title claims abstract description 45
- 239000003792 electrolyte Substances 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 132
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 66
- 239000004693 Polybenzimidazole Substances 0.000 claims abstract description 15
- 229920002480 polybenzimidazole Polymers 0.000 claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 239000013078 crystal Substances 0.000 claims abstract description 10
- 238000002425 crystallisation Methods 0.000 claims abstract description 8
- 230000008025 crystallization Effects 0.000 claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims description 6
- 238000007598 dipping method Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 claims 2
- 229920000877 Melamine resin Polymers 0.000 claims 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims 1
- 239000004202 carbamide Substances 0.000 claims 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 claims 1
- 229920000137 polyphosphoric acid Polymers 0.000 claims 1
- 239000002253 acid Substances 0.000 abstract description 4
- 238000001914 filtration Methods 0.000 abstract description 3
- 238000002844 melting Methods 0.000 abstract 1
- 230000008018 melting Effects 0.000 abstract 1
- 239000000446 fuel Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 2
- 238000009864 tensile test Methods 0.000 description 2
- 125000006615 aromatic heterocyclic group Chemical group 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000005518 polymer electrolyte Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012546 transfer Methods 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
- H01M8/102—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
- H01M8/103—Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer having nitrogen, e.g. sulfonated polybenzimidazoles [S-PBI], polybenzimidazoles with phosphoric acid, sulfonated polyamides [S-PA] or sulfonated polyphosphazenes [S-PPh]
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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
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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
- H01M2008/1095—Fuel cells with polymeric electrolytes
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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
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0082—Organic polymers
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- 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
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Abstract
Description
技术领域technical field
本发明涉及一种具有高电导率、良好机械性能磷酸掺杂聚合物电解质膜的制备。The invention relates to the preparation of a phosphoric acid-doped polymer electrolyte membrane with high electrical conductivity and good mechanical properties.
背景技术Background technique
工作温度在120-200℃的质子交换膜燃料电池与工作温度在80-90℃的质子交换膜燃料电池相比,具有更高的CO耐受能力、简化的水热管理系统等技术上的优势,因此开发高温PEMFC成为近年来最为活跃的研究领域之一。作为高温质子交换膜燃料电池核心材料的质子交换膜(PEM)需要满足在高温低湿度条件下具有较高的质子传递能力、良好的热稳定性和机械性能等要求。Compared with the proton exchange membrane fuel cell with a working temperature of 80-90°C, the proton exchange membrane fuel cell with an operating temperature of 120-200°C has technical advantages such as higher CO tolerance and simplified hydrothermal management system. Therefore, the development of high-temperature PEMFC has become one of the most active research fields in recent years. As the core material of high temperature proton exchange membrane fuel cell, proton exchange membrane (PEM) needs to meet the requirements of high proton transfer capacity, good thermal stability and mechanical properties under high temperature and low humidity conditions.
聚苯并咪唑(PBI)是一类芳香杂环高分子聚合物,具有突出的热稳定性和成膜性能,膜材料力学性能优良,同时聚合物中的碱性苯并咪唑基团对酸的亲和力,可使酸掺杂在聚合物骨架中。磷酸掺杂PBI膜的质子电导率取决于膜中的磷酸含量,即膜的磷酸掺杂水平越高,膜的电导率也越高。然而目前市场在售的磷酸最高浓度在85%左右,无法实现高磷酸掺杂水平电解质膜的制备,从而限制了磷酸掺杂膜电导率的提升。Polybenzimidazole (PBI) is a class of aromatic heterocyclic polymers with outstanding thermal stability and film-forming properties. Affinity allows acid to be doped into the polymer backbone. The proton conductivity of phosphoric acid-doped PBI membranes depends on the phosphoric acid content in the membrane, that is, the higher the phosphoric acid doping level of the membrane, the higher the membrane conductivity. However, the highest concentration of phosphoric acid currently on the market is about 85%, which cannot achieve the preparation of electrolyte membranes with high phosphoric acid doping levels, thus limiting the improvement of the conductivity of phosphoric acid doped membranes.
针对上述问题,本发明的目的在于利用磷酸结晶特性,在磷酸的冷却结晶过程中,通过控制磷酸结晶条件,获得系列高浓度磷酸,从而制得高浓度电解质膜掺杂溶液,制备酸含量可控、高磷酸掺杂水平电解质膜,提高电解质膜的电导率。In view of the above problems, the purpose of the present invention is to utilize the crystallization characteristics of phosphoric acid, in the process of cooling and crystallization of phosphoric acid, by controlling the crystallization conditions of phosphoric acid, a series of high-concentration phosphoric acid can be obtained, thereby preparing a high-concentration electrolyte membrane doping solution, and preparing a controllable acid content , High phosphoric acid doping level electrolyte membrane, improve the conductivity of the electrolyte membrane.
发明内容SUMMARY OF THE INVENTION
通过控制结晶条件,通过溶液结晶法将市售磷酸纯度提高,制备系列高浓度电解质膜掺杂液,进而实现酸含量可控、高磷酸掺杂水平PBI膜的制备。By controlling the crystallization conditions and improving the purity of commercially available phosphoric acid by solution crystallization, a series of high-concentration electrolyte membrane doping solutions are prepared, thereby realizing the preparation of PBI membranes with controllable acid content and high phosphoric acid doping level.
一种高电导率、良好机械性能电解质膜的制备包括以下步骤:The preparation of an electrolyte membrane with high electrical conductivity and good mechanical properties comprises the following steps:
(1)高浓度磷酸掺杂液的制备(1) Preparation of high concentration phosphoric acid doping solution
取质量浓度40-85%的磷酸,将其在-20℃~4℃静置24h~120h,使磷酸部分或全部结晶。取出上述磷酸,将上清液滤除,加热溶解固体部分,获得高浓度磷酸掺杂液。Take phosphoric acid with a mass concentration of 40-85%, and let it stand at -20°C to 4°C for 24h to 120h to crystallize part or all of the phosphoric acid. The phosphoric acid was taken out, the supernatant was filtered off, and the solid portion was dissolved by heating to obtain a high-concentration phosphoric acid-doped solution.
(2)高磷酸掺杂水平电解质膜的制备(2) Preparation of high phosphoric acid doping level electrolyte membrane
将PBI膜干燥后放入步骤(1)中制备的高浓度磷酸掺杂液中,轻轻晃动使之全部浸于液面以下,室温至150℃持续2-72小时。After drying, put the PBI film into the high-concentration phosphoric acid doping solution prepared in step (1), shake it gently to make it all immersed below the liquid level, and continue from room temperature to 150° C. for 2-72 hours.
通过磷酸掺杂前后膜质量的变化,可以计算出PBI电解质膜的磷酸掺杂含量。The phosphoric acid doping content of the PBI electrolyte membrane can be calculated by the change of the membrane quality before and after phosphoric acid doping.
磷酸掺杂含量的计算公式为:磷酸掺杂含量%=100*(m浸渍后-m浸渍前)/m浸渍前其中m浸渍后为磷酸掺杂后膜质量,m浸渍前为磷酸掺杂前干膜质量。The calculation formula of phosphoric acid doping content is: phosphoric acid doping content%=100*(m after dipping-m before dipping )/m before dipping, where m after dipping is the film quality after phosphoric acid doping, m before dipping is before phosphoric acid doping dry film quality.
本发明所述高电导率、良好机械性能电解质膜的制备具有如下优点:The preparation of the electrolyte membrane with high electrical conductivity and good mechanical properties of the present invention has the following advantages:
(1)工艺简单,易于操作、调控;(1) The process is simple, easy to operate and control;
(2)制备得到的电解质膜磷酸掺杂水平高,含水量低;(2) The prepared electrolyte membrane has high phosphoric acid doping level and low water content;
(3)制备得到的磷酸掺杂电解质膜具有较高的电导率。(3) The prepared phosphoric acid doped electrolyte membrane has high electrical conductivity.
附图说明Description of drawings
图1为所制备的高磷酸掺杂水平电解质膜的电导率随温度变化曲线。Fig. 1 is a curve of the electrical conductivity of the prepared electrolyte membrane with high phosphoric acid doping level as a function of temperature.
图2为所制备的高磷酸掺杂水平电解质膜在拉伸测试时应力随应变的变化曲线。Figure 2 shows the stress versus strain curve of the prepared electrolyte membrane with high phosphoric acid doping level in the tensile test.
具体实施方式Detailed ways
实施例1Example 1
取800g质量浓度85%磷酸,60℃恒温水浴中边加热边搅拌40min;温度降至室温后,加入磷酸晶体5g,于室温降温至-8℃,静置48h。将上述磷酸取出后,立即过滤去除上清液,将固体部分置于80℃烘箱加热12h。对获得的高浓度磷酸掺杂液进行搅拌。Take 800 g of phosphoric acid with a mass concentration of 85%, heat it in a constant temperature water bath at 60 °C and stir for 40 min; after the temperature drops to room temperature, add 5 g of phosphoric acid crystals, cool down to -8 °C at room temperature, and let stand for 48 h. After the phosphoric acid was taken out, the supernatant was removed by filtration immediately, and the solid part was heated in an oven at 80°C for 12 h. The obtained high-concentration phosphoric acid-doped liquid is stirred.
裁取大小为10cm*10cm的PBI膜4张,120℃烘箱中干燥4h,称重记为m0。将该PBI膜放入上述高浓度磷酸掺杂液中,轻轻晃动使之全部浸于液面以下。80℃烘箱中加热10h,得到高磷酸掺杂水平电解质膜。将上述电解质膜以滤纸擦除表面磷酸后称重记为m1。Cut out 4 PBI films with a size of 10cm*10cm, dry them in an oven at 120°C for 4 hours, and record the weight as m 0 . The PBI film was placed in the above-mentioned high-concentration phosphoric acid doping solution, and was gently shaken so that it was completely immersed below the liquid surface. Heating in an oven at 80 °C for 10 h yields an electrolyte membrane with a high phosphoric acid doping level. The above-mentioned electrolyte membrane was weighed and recorded as m 1 after the surface phosphoric acid was wiped off with filter paper.
下表1为上述4张膜处理前后的质量、磷酸掺杂含量数值。Table 1 below shows the quality and phosphoric acid doping content of the four films before and after treatment.
从表1可以看出此类膜具有较高的磷酸掺杂水平及一致性。It can be seen from Table 1 that such films have higher phosphoric acid doping levels and consistency.
图1为实施例1所制备的高磷酸掺杂水平电解质膜的电导率随温度变化曲线。在图1中,横坐标为温度(℃),纵坐标为电导率(mS cm-1);由图1可知,此类膜在160℃的电导率>200mS cm-1,能够满足燃料电池对电解质膜电导率的要求。FIG. 1 is a curve of the electrical conductivity of the electrolyte membrane with high phosphoric acid doping level prepared in Example 1 as a function of temperature. In Figure 1, the abscissa is the temperature (°C), and the ordinate is the conductivity (mS cm -1 ). It can be seen from Figure 1 that the conductivity of this type of membrane at 160°C is >200 mS cm -1 , which can meet the requirements of fuel cells. Electrolyte membrane conductivity requirements.
采用TA公司的Q800对高磷酸掺杂水平电解质膜的机械强度进行测试。利用拉伸模式,拉伸速率为100%。图2为上述制备的膜在拉伸测试时应力随应变的变化曲线。其中纵坐标为应力(MPa),横坐标为应变(%)。制备的膜的抗拉强度室温下大于7MPa,其断裂伸长率大于120%,表明这类膜具有良好的机械性能,能够满足在燃料电池中应用的需求。The mechanical strength of the electrolyte membrane with high phosphoric acid doping level was tested by Q800 of TA company. Using stretch mode, the stretch rate is 100%. FIG. 2 is the stress-strain curve of the films prepared above in the tensile test. The ordinate is stress (MPa), and the abscissa is strain (%). The tensile strength of the prepared membrane is greater than 7MPa at room temperature, and its elongation at break is greater than 120%, indicating that this type of membrane has good mechanical properties and can meet the needs of application in fuel cells.
实施例2Example 2
取800g质量浓度85%磷酸,70℃恒温水浴中边加热边搅拌30min;Take 800 g of phosphoric acid with a mass concentration of 85%, heat it in a constant temperature water bath at 70 °C and stir for 30 min;
温度降至15℃后,加入磷酸晶体5g,继续冷却至-18℃,静置30h。将上述磷酸取出后,立即过滤去除上清液,将固体部分置于80℃烘箱加热12h。对获得的高浓度磷酸掺杂液进行搅拌。After the temperature dropped to 15°C, 5 g of phosphoric acid crystals were added, and the solution was continued to cool to -18°C and allowed to stand for 30 hours. After the phosphoric acid was taken out, the supernatant was removed by filtration immediately, and the solid part was heated in an oven at 80°C for 12 h. The obtained high-concentration phosphoric acid-doped liquid is stirred.
裁取大小为10cm*10cm的PBI膜2张,150℃烘箱中干燥2h。将该PBI膜放入上述高浓度磷酸掺杂液中,轻轻晃动使之全部浸于液面以下。70℃烘箱中加热10h,得到高磷酸掺杂水平电解质膜,磷酸掺杂含量分别为500%、506%。Cut out 2 PBI films with a size of 10cm*10cm, and dry them in an oven at 150°C for 2h. The PBI film was placed in the above-mentioned high-concentration phosphoric acid doping solution, and was gently shaken so that it was completely immersed below the liquid surface. Heating in an oven at 70°C for 10 h yields an electrolyte membrane with a high phosphoric acid doping level, and the phosphoric acid doping content is 500% and 506%, respectively.
实施例3(对比例)Example 3 (comparative example)
裁取大小为10cm*10cm的PBI膜2张,120℃烘箱中干燥4h,称重记为m0。将该PBI膜放入质量浓度85%的磷酸中,轻轻晃动使之全部浸于液面以下。80℃烘箱中加热10h,得到磷酸掺杂电解质膜。将上述电解质膜以滤纸擦除表面磷酸后称重记为m1。Cut out 2 PBI films with a size of 10cm*10cm, dry them in an oven at 120°C for 4 hours, and record the weight as m 0 . The PBI membrane was put into phosphoric acid having a mass concentration of 85%, and was gently shaken so that it was completely immersed below the liquid surface. Heating in an oven at 80 °C for 10 h yields a phosphoric acid doped electrolyte membrane. The above-mentioned electrolyte membrane was weighed and recorded as m 1 after the surface phosphoric acid was wiped off with filter paper.
下表2为上述2张膜处理前后的质量、磷酸掺杂含量数值。Table 2 below shows the mass and phosphoric acid doping content of the two films before and after treatment.
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CN111682248A (en) * | 2020-06-29 | 2020-09-18 | 香港科技大学 | A PBI membrane activation treatment method with high proton conductivity and ion selectivity |
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US4655789A (en) * | 1985-05-08 | 1987-04-07 | Freeport Research And Engineering Company | Phosphoric acid crystallization process |
JP2007001834A (en) * | 2005-06-27 | 2007-01-11 | Shimonoseki Mitsui Chemicals Inc | Method of producing high purity purified phosphoric acid |
CN103881123A (en) * | 2012-12-21 | 2014-06-25 | 中国科学院大连化学物理研究所 | A preparation method of PBI/H3PO4 doped film for high temperature fuel cell |
CN104030261A (en) * | 2013-12-30 | 2014-09-10 | 广西明利化工有限公司 | A production method of high-purity electronic grade phosphoric acid |
CN108178137A (en) * | 2016-12-08 | 2018-06-19 | 中国科学院大连化学物理研究所 | The preparation of a kind of high-purity phosphoric acid and phosphoric acid/PBI composite membranes and film and application |
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US4655789A (en) * | 1985-05-08 | 1987-04-07 | Freeport Research And Engineering Company | Phosphoric acid crystallization process |
JP2007001834A (en) * | 2005-06-27 | 2007-01-11 | Shimonoseki Mitsui Chemicals Inc | Method of producing high purity purified phosphoric acid |
CN103881123A (en) * | 2012-12-21 | 2014-06-25 | 中国科学院大连化学物理研究所 | A preparation method of PBI/H3PO4 doped film for high temperature fuel cell |
CN104030261A (en) * | 2013-12-30 | 2014-09-10 | 广西明利化工有限公司 | A production method of high-purity electronic grade phosphoric acid |
CN108178137A (en) * | 2016-12-08 | 2018-06-19 | 中国科学院大连化学物理研究所 | The preparation of a kind of high-purity phosphoric acid and phosphoric acid/PBI composite membranes and film and application |
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CN111682248A (en) * | 2020-06-29 | 2020-09-18 | 香港科技大学 | A PBI membrane activation treatment method with high proton conductivity and ion selectivity |
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