[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN111342097A - Preparation method of electrolyte membrane with high conductivity and good mechanical property - Google Patents

Preparation method of electrolyte membrane with high conductivity and good mechanical property Download PDF

Info

Publication number
CN111342097A
CN111342097A CN201811547775.5A CN201811547775A CN111342097A CN 111342097 A CN111342097 A CN 111342097A CN 201811547775 A CN201811547775 A CN 201811547775A CN 111342097 A CN111342097 A CN 111342097A
Authority
CN
China
Prior art keywords
phosphoric acid
preparation
electrolyte membrane
concentration
crystals
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.)
Pending
Application number
CN201811547775.5A
Other languages
Chinese (zh)
Inventor
王素力
闫树华
马文佳
孙公权
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dalian Institute of Chemical Physics of CAS
Original Assignee
Dalian Institute of Chemical Physics of CAS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dalian Institute of Chemical Physics of CAS filed Critical Dalian Institute of Chemical Physics of CAS
Priority to CN201811547775.5A priority Critical patent/CN111342097A/en
Publication of CN111342097A publication Critical patent/CN111342097A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/102Polymeric electrolyte materials characterised by the chemical structure of the main chain of the ion-conducting polymer
    • H01M8/103Polymeric 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]
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1016Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018Polymeric electrolyte materials
    • H01M8/1069Polymeric electrolyte materials characterised by the manufacturing processes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/10Fuel cells with solid electrolytes
    • H01M2008/1095Fuel cells with polymeric electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0065Solid electrolytes
    • H01M2300/0082Organic polymers
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Fuel Cell (AREA)

Abstract

The invention relates to a preparation method of an electrolyte membrane with high conductivity and good mechanical property, which comprises the following steps: (1) taking phosphoric acid with the mass concentration of 40-85%, reducing the temperature, adding seed crystals, standing for 30-600 h, and filtering to obtain phosphoric acid crystals; heating and melting the crystals to obtain high-concentration phosphoric acid doped liquid; (2) putting the polybenzimidazole electrolyte membrane into the high-concentration phosphoric acid doping solution prepared in the step (1) to be completely immersed below the liquid level; taking out after the temperature is between room temperature and 150 ℃ for 2 to 48 hours. According to the invention, by controlling crystallization conditions and by adopting a solution crystallization method, the purity of the commercial phosphoric acid is improved, and the serial high-concentration electrolyte membrane doping liquid is prepared, so that the preparation of the PBI membrane with controllable acid content and high phosphoric acid doping level is realized.

Description

一种高电导率、良好机械性能电解质膜的制备方法A kind of preparation method of electrolyte membrane with high electrical conductivity and good mechanical properties

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m1Cut 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.

m<sub>0</sub>m<sub>0</sub> m<sub>1</sub>m<sub>1</sub> 磷酸掺杂含量Phosphoric acid doping content 483mg483mg 2714mg2714mg 462%462% 480mg480mg 2712mg2712mg 465%465% 475mg475mg 2703mg2703mg 469%469% 482mg482mg 2690mg2690mg 458%458%

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m1Cut 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.

m<sub>0</sub>m<sub>0</sub> m<sub>1</sub>m<sub>1</sub> 磷酸掺杂含量Phosphoric acid doping content 487mg487mg 2211mg2211mg 354%354% 476mg476mg 2190mg2190mg 360%360%

Claims (4)

1.一种高电导率、良好机械性能电解质膜的制备方法,包括以下步骤:1. A preparation method of an electrolyte membrane with high electrical conductivity and good mechanical properties, comprising 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,为获得分布均匀的H3PO4-H2O体系,对所述质量浓度40%-85%的磷酸在40-70℃恒温水浴中搅拌30-60min进行预处理;降低上述磷酸温度至室温~10℃,加入晶种,继续降温至4℃~-20℃,静置30h~60h;过滤,获得磷酸结晶体;加热熔化上述结晶体,获得高浓度磷酸掺杂液;Take phosphoric acid with a mass concentration of 40%-85%, in order to obtain a uniformly distributed H 3 PO 4 -H 2 O system, stir the phosphoric acid with a mass concentration of 40%-85% in a constant temperature water bath at 40-70 ° C for 30-60min Carry out pretreatment; lower the temperature of phosphoric acid to room temperature to 10°C, add seed crystals, continue to cool down to 4°C to -20°C, and let stand for 30h to 60h; filter to obtain phosphoric acid crystals; heat and melt the above crystals to obtain high-concentration phosphoric acid mixed with miscellaneous liquid; (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 将聚苯并咪唑电解质膜放入步骤(1)中制备的高浓度磷酸掺杂液中,使之全部浸于液面以下;室温至150℃持续2-48h后取出即可。Put the polybenzimidazole electrolyte membrane into the high-concentration phosphoric acid doping solution prepared in step (1), so that it is completely immersed below the liquid level; it can be taken out after the room temperature reaches 150° C. for 2-48 hours. 2.按照权利要求1所述的制备方法,其特征在于:磷酸质量浓40%-85%;预处理温度40-70℃,搅拌时长30-60min;首次降温至室温~10℃,终止温度4℃~-20℃;晶种包括磷酸晶体、五氧化二磷、多聚磷酸晶体、尿素、三聚氰胺等中的一种或二种以上;结晶过程中静置时间30h~60h。2. preparation method according to claim 1 is characterized in that: phosphoric acid mass is concentrated 40%-85%; Pretreatment temperature is 40-70 ℃, stirring duration is 30-60min; ℃~-20℃; the seeds include one or more of phosphoric acid crystals, phosphorus pentoxide, polyphosphoric acid crystals, urea, melamine, etc.; the standing time in the crystallization process is 30h~60h. 3.按照权利要求1所述的制备方法,其特征在于:加热溶解过程为60-100℃。3. The preparation method according to claim 1, wherein the heating and dissolving process is 60-100°C. 4.按照权利要求1所述的制备方法,其特征在于:浸渍过程为室温至150℃、2-48h。4. The preparation method according to claim 1, wherein the dipping process is from room temperature to 150°C for 2-48h.
CN201811547775.5A 2018-12-18 2018-12-18 Preparation method of electrolyte membrane with high conductivity and good mechanical property Pending CN111342097A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811547775.5A CN111342097A (en) 2018-12-18 2018-12-18 Preparation method of electrolyte membrane with high conductivity and good mechanical property

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811547775.5A CN111342097A (en) 2018-12-18 2018-12-18 Preparation method of electrolyte membrane with high conductivity and good mechanical property

Publications (1)

Publication Number Publication Date
CN111342097A true CN111342097A (en) 2020-06-26

Family

ID=71186720

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811547775.5A Pending CN111342097A (en) 2018-12-18 2018-12-18 Preparation method of electrolyte membrane with high conductivity and good mechanical property

Country Status (1)

Country Link
CN (1) CN111342097A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Similar Documents

Publication Publication Date Title
CN103570960B (en) A kind of preparation method of the compound proton exchange membrane for high temperature resistant fuel cell
CN103694490A (en) High-temperature polyimide proton exchange membrane and preparation method thereof
CN107556247B (en) Functional cross-linking agent, preparation method and high phosphoric acid-doped cross-linked polybenzimidazole film prepared therefrom
Liu et al. A semi‐liquid electrode toward stable zn powder anode
CN110707294B (en) A three-dimensional fiber frame lithium battery anode co-doped with lithiophilic heteroatoms and metal oxides and its preparation
CN109088098B (en) Preparation method of single-ion polymer electrolyte diaphragm
CN108539235A (en) A kind of polybenzimidazoles proton conductive membrane and preparation method thereof with dual network structure
CN106892459A (en) A kind of preparation method of micro- cube of potassium phosphotungstate
CN111342097A (en) Preparation method of electrolyte membrane with high conductivity and good mechanical property
JP2005133099A (en) Method for producing poly (2,5-benzimidazole), method for producing poly (2,5-benzimidazole), poly (2,5-benzimidazole) polymer electrolyte membrane, poly (2,5-benzimidazole) high Fuel cell comprising molecular electrolyte membrane and poly (2,5-benzimidazole) polymer electrolyte membrane
CN101931070A (en) A method for preparing an organic-inorganic composite proton exchange membrane suitable for vanadium batteries
CN103881123B (en) A kind of PBI/H used for high-temperature fuel cell3PO4The preparation method of doping
CN105742649A (en) High-temperature proton exchange membrane fuel cell membrane electrode and preparation method thereof
JP2015525283A (en) Production method of polyacrylonitrile-methyl methacrylate gel electrolyte membrane, and corresponding electrolyte and production method
CN105826585B (en) A kind of preparation method of high temperature compound proton exchange membrane for fuel cell
KR20150050451A (en) Electrolyte membrane for fuel cell, preparation method thereof and the fuel cell comprising using the same
CN107565114A (en) A kind of binder free anode material of lithium-ion battery and preparation method thereof
CN115700938A (en) Preparation method of metal lithium battery cathode
CN113698644B (en) A kind of cross-linked polybenzimidazole membrane material for high temperature proton exchange membrane and preparation method thereof
CN116706113A (en) Preparation method of a low-cost all-vanadium redox flow battery diaphragm
CN104497328B (en) Method for preparing modified polyvinyl alcohol-based alkaline polymer electrolyte membrane
CN115101790A (en) A kind of composite electrolyte membrane with high electrical conductivity and preparation method thereof
JP4347891B2 (en) Polybenzimidazole-benzamide copolymer and method for producing the same, electrolyte membrane produced from the copolymer, and method for producing the same
CN107768700A (en) A kind of preparation method of perfluorosulfonic acid proton exchange film
CN113991047A (en) Preparation method and application of modified metal zinc cathode

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20200626

RJ01 Rejection of invention patent application after publication