[go: up one dir, main page]

CN116574371A - Conjugated branched anion exchange membrane, preparation method and application - Google Patents

Conjugated branched anion exchange membrane, preparation method and application Download PDF

Info

Publication number
CN116574371A
CN116574371A CN202310496472.XA CN202310496472A CN116574371A CN 116574371 A CN116574371 A CN 116574371A CN 202310496472 A CN202310496472 A CN 202310496472A CN 116574371 A CN116574371 A CN 116574371A
Authority
CN
China
Prior art keywords
exchange membrane
anion exchange
conjugated branched
solution
preparation
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
CN202310496472.XA
Other languages
Chinese (zh)
Inventor
姚进
何庆一
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.)
Ningbo Zhongke Hydrogen Easy Film Technology Co ltd
Original Assignee
Ningbo Zhongke Hydrogen Easy Film Technology Co ltd
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 Ningbo Zhongke Hydrogen Easy Film Technology Co ltd filed Critical Ningbo Zhongke Hydrogen Easy Film Technology Co ltd
Priority to CN202310496472.XA priority Critical patent/CN116574371A/en
Publication of CN116574371A publication Critical patent/CN116574371A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/20Manufacture of shaped structures of ion-exchange resins
    • C08J5/22Films, membranes or diaphragms
    • C08J5/2206Films, membranes or diaphragms based on organic and/or inorganic macromolecular compounds
    • C08J5/2218Synthetic macromolecular compounds
    • C08J5/2256Synthetic macromolecular compounds based on macromolecular compounds obtained by reactions other than those involving carbon-to-carbon bonds, e.g. obtained by polycondensation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • C08G69/265Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids from at least two different diamines or at least two different dicarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/26Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from polyamines and polycarboxylic acids
    • C08G69/28Preparatory processes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • C25B9/19Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
    • C25B9/23Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms comprising ion-exchange membranes in or on which electrode material is embedded
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • C08J2377/06Polyamides derived from polyamines and polycarboxylic acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

The application relates to the technical field of alkaline water electrolytic baths, and particularly discloses a preparation method and application of a conjugated branched anion exchange membrane. The synthesis strategy of the application is simple, convenient and effective, low in preparation cost, excellent in performance, strong in universality, convenient for industrial production and has great application potential.

Description

一种共轭型支化阴离子交换膜、制备方法及应用A kind of conjugated branched anion exchange membrane, preparation method and application

技术领域technical field

本发明属于碱性水电解槽技术领域,特别涉及一种共轭型支化阴离子交换膜、制备方法及应用。The invention belongs to the technical field of alkaline water electrolyzers, and in particular relates to a conjugated branched anion exchange membrane, a preparation method and an application.

背景技术Background technique

发展绿色氢能对于优化当前能源结构和实现人类可持续增长至关重要。与可再生能源相结合的电解水制氢技术将是制备绿色氢能的主要方式,也必将占据未来绝大部分的氢能源制备市场。碱水制氢电解槽制造过程中不使用贵金属资源,成本低,同时还具有工作寿命长的优势,这使得碱水电解制氢成为现阶段电解水制氢市场最主要的技术路线。作为碱性电解水装置中的关键组分——隔膜在电解槽中起到隔绝氢氧、传递离子的作用。理想的隔膜应具有高的气密性、高的电导率以及优异的尺寸稳定性和耐碱性。现阶段市场上的隔膜以比利时Agfa公司开发的Zirfon系列膜与东丽的PPS布为主。但这两种膜本身具有很高面电阻,使得电解水制氢能耗过高,由此造成制氢成本居高不下的问题限制了碱性电解水技术的进一步推广。The development of green hydrogen energy is crucial to optimize the current energy structure and achieve sustainable growth of mankind. The electrolysis of water hydrogen production technology combined with renewable energy will be the main way to produce green hydrogen energy, and it will also occupy most of the hydrogen energy production market in the future. Alkaline water hydrogen production electrolyzer does not use precious metal resources in the manufacturing process, the cost is low, and it also has the advantage of long working life. As a key component in the alkaline electrolyzed water device, the diaphragm plays the role of isolating hydrogen and oxygen and transferring ions in the electrolytic cell. An ideal separator should have high air tightness, high electrical conductivity, and excellent dimensional stability and alkali resistance. The separators on the market at this stage are mainly the Zirfon series membranes developed by Agfa in Belgium and the PPS cloth of Toray. However, these two membranes have high surface resistance, which makes the energy consumption of hydrogen production by electrolysis of water too high, resulting in the high cost of hydrogen production, which limits the further promotion of alkaline electrolysis of water technology.

阴离子交换膜电解槽(AEMWE)是一种新兴的电解水技术。其中,所使用的阴离子交换膜(AEM)是一类含有碱性活性基团、对阴离子具有选择透过性的高分子聚合物膜。致密的均质膜可有效防止两极氢氧的互窜,同时优异的离子传导性能赋予了AEMWE较高的电流密度。例如,基于聚芳基哌啶类AEM构筑的AEMWE在1M KOH溶液、80℃、镍基催化剂条件下,电流密度高达1600mA cm-2(Lee,Y.M.Energy Environ.Sci.,2021,14,6338-6348),显示出了良好的应用前景。经过多年的努力,研究人员已逐渐开发出一系列具有优良综合性能的AEMs,但是目前大部分文献报道的AEMs在聚合单体制备、聚合反应或聚合物后功能化过程中往往需要使用昂贵的过渡金属催化剂或高成本高腐蚀性的超酸催化剂,不可避免地造成阴离子交换膜制备成本的提升,很大程度上限制了AEMWE的进一步推广和应用。因此发展简便有效的合成策略,制备出成本低、具有优良性能的阴离子交换膜材料仍然是目前研究的重点及难点。Anion-exchange membrane electrolyzer (AEMWE) is an emerging water electrolysis technology. Wherein, the used anion exchange membrane (AEM) is a kind of high molecular polymer membrane containing basic active groups and having selective permeability to anions. The dense homogeneous membrane can effectively prevent the cross-channeling of hydrogen and oxygen at the two poles, and the excellent ion conductivity gives AEMWE a higher current density. For example, AEMWE based on polyarylpiperidine-based AEM has a current density of up to 1600mA cm -2 under the conditions of 1M KOH solution, 80°C, and nickel-based catalyst (Lee, YMEnergy Environ.Sci., 2021, 14, 6338-6348 ), showing good application prospects. After years of hard work, researchers have gradually developed a series of AEMs with excellent comprehensive properties, but most of the AEMs reported in the literature often require the use of expensive transitions during the preparation of polymerized monomers, polymerization reactions, or post-polymer functionalization. Metal catalysts or high-cost and highly corrosive superacid catalysts inevitably lead to an increase in the cost of anion exchange membrane preparation, which largely limits the further promotion and application of AEMWE. Therefore, the development of simple and effective synthetic strategies to prepare anion exchange membrane materials with low cost and excellent performance is still the focus and difficulty of current research.

发明内容Contents of the invention

针对现有技术的不足,本发明的目的在于提出了一种共轭型支化阴离子交换膜、制备方法及应用,该类膜构筑的电解槽展现出优异的电解水性能。Aiming at the deficiencies of the prior art, the object of the present invention is to propose a conjugated branched anion exchange membrane, its preparation method and application, and the electrolyzer constructed by this type of membrane exhibits excellent performance in electrolyzing water.

为达到此目的,本发明采用以下技术方案:To achieve this goal, the present invention adopts the following technical solutions:

一种共轭型支化聚合物,结构通式如下:A kind of conjugated branched polymer, general structural formula is as follows:

其中x为支化度(%),x的范围为1-20;R为下述结构中的一种或多种:Wherein x is the degree of branching (%), and the scope of x is 1-20; R is one or more in the following structures:

M结构为下列中的一种或多种:The M structure is one or more of the following:

Q=F、Cl、Br、IQ=F, Cl, Br, I

一种共轭型支化阴离子交换膜的制备方法,其特征在于,包括以下步骤:A kind of preparation method of conjugated branched anion exchange membrane is characterized in that, comprises the following steps:

(1)聚合物制备:惰性气体氛围、-10-20℃下,将催化剂置于有机溶剂a中搅拌10-120min后,滴加聚合单体混合液开始反应。反应24-144h后用碱性溶液淬灭,之后萃取得到聚合物前体。将聚合物前体溶于有机溶剂b中,惰性气氛下加入胺类溶液,20-80℃下反应24-72h,有机溶剂下沉出聚合物,水洗2-8次后真空干燥得到纯粹的聚合物产物。(1) Polymer preparation: in an inert gas atmosphere at -10-20°C, place the catalyst in the organic solvent a and stir for 10-120 minutes, then add the polymerized monomer mixture dropwise to start the reaction. After reacting for 24-144h, it was quenched with an alkaline solution, and then extracted to obtain a polymer precursor. Dissolve the polymer precursor in the organic solvent b, add the amine solution under an inert atmosphere, react at 20-80°C for 24-72 hours, the organic solvent sinks out of the polymer, wash it with water for 2-8 times, and dry it in vacuum to obtain a pure polymer product.

(2)将步骤(1)所得聚合物溶解在有机溶剂b中。经过滤、脱泡后浇筑成膜,得到所述共轭型支化阴离子交换膜。(2) Dissolving the polymer obtained in step (1) in the organic solvent b. After filtering and defoaming, casting to form a membrane, the conjugated branched anion exchange membrane is obtained.

所述惰性气氛为氮气或氩气;The inert atmosphere is nitrogen or argon;

所述催化剂为副族金属及其相应氧化物、卤化物中的一种或多种;进一步优选铜、锌、铜锌合金、镁、锌银合金、三氯化钛、四氯化钛等。The catalyst is one or more of subgroup metals and their corresponding oxides and halides; more preferably copper, zinc, copper-zinc alloy, magnesium, zinc-silver alloy, titanium trichloride, titanium tetrachloride, etc.

所述聚合单体混合液选自二、三官能度酰氯单体的混合物,其中二官能度酰氯单体包括但不限于对苯二甲酰氯、联苯二甲酰氯,三官能度酰氯单体包括但不限于均苯三甲酰氯、1,3,5-三(对甲酰氯基)苯、3,4',5-三酰基氯-1,1-联苯、三(4-甲酰氯苯基)膦。三官能度酰氯单体的加入,显著提升了膜材料的电化学性能。The polymerized monomer mixture is selected from a mixture of difunctional and trifunctional acid chloride monomers, wherein the difunctional acyl chloride monomers include but not limited to terephthaloyl dichloride and biphthaloyl dichloride, and the trifunctional acyl chloride monomers include But not limited to trimesoyl chloride, 1,3,5-tris(p-formyl chloride)benzene, 3,4',5-triacyl chloride-1,1-biphenyl, tris(4-formyl chloride phenyl) phosphine. The addition of the trifunctional acid chloride monomer significantly improved the electrochemical performance of the membrane material.

所述聚合单体混合液占整个体系的摩尔比为0.1-15%;若摩尔比过高,则会导致凝胶,无法得到可溶的聚合物。The molar ratio of the polymerized monomer mixture to the entire system is 0.1-15%; if the molar ratio is too high, it will lead to gelation and cannot obtain a soluble polymer.

步骤(1)所述碱性溶液为氢氧化钾、氢氧化钠、碳酸钠、碳酸钾中的一种或多种水溶液;The alkaline solution described in step (1) is one or more aqueous solutions in potassium hydroxide, sodium hydroxide, sodium carbonate, potassium carbonate;

步骤(1)中所述有机溶剂a为甲醇、乙醇、N,N’-二甲基甲酰胺、二甲基亚砜、乙醚、丙酮、四氢呋喃、乙酸乙酯、二氯甲烷、氯仿、四氯化碳、石油醚中的一种或多种混合。The organic solvent a described in step (1) is methanol, ethanol, N,N'-dimethylformamide, dimethyl sulfoxide, ether, acetone, tetrahydrofuran, ethyl acetate, dichloromethane, chloroform, tetrachloro One or more mixtures of carbon dioxide and petroleum ether.

步骤(1)所述胺类溶液包括但不限于三甲胺水溶液。The amine solution in step (1) includes but not limited to trimethylamine aqueous solution.

步骤(1)、(2)中所述有机溶剂b为N-甲基吡咯烷酮、N,N’-二甲基甲酰胺、N,N’-二甲基乙酰胺、二甲基亚砜中的一种或多种溶剂按任意比的混合。The organic solvent b described in step (1), (2) is N-methylpyrrolidone, N,N'-dimethylformamide, N,N'-dimethylacetamide, dimethyl sulfoxide One or more solvents are mixed in any ratio.

本发明还提出了阴离子交换膜在碱性电解水装置中的应用,包括以下步骤:The present invention also proposes the application of the anion exchange membrane in the alkaline electrolyzed water device, comprising the following steps:

(1)膜电极制备:将共轭型支化阴离子交换膜溶解在极性有机溶剂中得到离聚物溶液;将催化剂Pt/C和IrO2均匀分散在分散剂中配制成催化剂溶液;分别取离聚物溶液与催化剂溶液,混合均匀后,均匀喷涂在共轭型支化阴离子交换膜两侧,制成膜电极;然后在碱性溶液中进行离子交换;(1) Membrane electrode preparation: dissolving the conjugated branched anion exchange membrane in a polar organic solvent to obtain an ionomer solution; uniformly dispersing the catalyst Pt/C and IrO in a dispersant to prepare a catalyst solution; The ionomer solution and the catalyst solution are evenly mixed, and then evenly sprayed on both sides of the conjugated branched anion exchange membrane to form a membrane electrode; then ion exchange is performed in an alkaline solution;

(2)组装电解水装置:将膜电极夹在阴阳极之间来组装电解水装置。(2) Assemble the electrolyzed water device: sandwich the membrane electrode between the anode and cathode to assemble the electrolyzed water device.

极性有机溶剂包括NMP、DMF、DMSO、DMAc等。Polar organic solvents include NMP, DMF, DMSO, DMAc, and the like.

作为优选,阴离子交换膜在碱性电解水装置中的应用,包括如下步骤:Preferably, the application of the anion exchange membrane in the alkaline electrolyzed water device comprises the following steps:

(1)膜电极制备:取上述阴离子交换膜溶解在DMSO中(4wt%)作为离聚物溶液。之后称取一定量的Pt/C和IrO2催化剂(2mg cm-2),加入水和异丙醇溶液作为分散剂配制成催化剂溶液,并通过磁力搅拌和超声破碎使其分散均匀。最后加入离聚物溶液并再次超声处理使其均匀,并将其均匀喷涂在共轭型支化阴离子交换膜两侧,制成膜电极。待溶剂挥发后将其浸于1M KOH溶液中离子交换48h;(1) Membrane electrode preparation: the above-mentioned anion exchange membrane was dissolved in DMSO (4wt%) as an ionomer solution. After that, a certain amount of Pt/C and IrO 2 catalysts (2 mg cm -2 ) were weighed, and water and isopropanol solution were added as dispersants to prepare a catalyst solution, which was uniformly dispersed by magnetic stirring and ultrasonic crushing. Finally, the ionomer solution is added and ultrasonically treated again to make it uniform, and it is evenly sprayed on both sides of the conjugated branched anion exchange membrane to form a membrane electrode. After the solvent evaporates, immerse it in 1M KOH solution for ion exchange for 48 hours;

(2)组装电解水装置:将膜电极夹在阴阳极之间来组装电解水装置;(2) Assemble the electrolyzed water device: sandwich the membrane electrode between the cathode and anode to assemble the electrolyzed water device;

(3)电解水性能测试:电化学测试在浸泡于阳极和阴极的1M KOH溶液中进行,温度保持在80℃。通过测量不同电流密度下的电池电压获得极化曲线。(3) Electrolyzed water performance test: The electrochemical test was carried out in 1M KOH solution soaked in the anode and cathode, and the temperature was kept at 80°C. Polarization curves were obtained by measuring the cell voltage at different current densities.

本发明的有益结果是:Beneficial result of the present invention is:

(1)本发明的共轭型支化聚合物基阴离子交换膜,聚合单体中加入了三官能度的反应物,显著提高了膜的电化学性能,与工业上的碱性电解槽有良好的适配性,还具有良好的尺寸稳定性;本发明制备的聚合物具有良好的溶解性,室温下可以溶解在极性有机溶剂中,如NMP、DMF、DMSO、DMAc等。(1) In the conjugated branched polymer-based anion exchange membrane of the present invention, the reactant of trifunctionality has been added in the polymerized monomer, which significantly improves the electrochemical performance of the membrane, and has a good relationship with the industrial alkaline electrolyzer It also has good dimensional stability; the polymer prepared by the present invention has good solubility and can be dissolved in polar organic solvents at room temperature, such as NMP, DMF, DMSO, DMAc, etc.

(2)本发明具有普适性强的特点,在合理调控二、三官能度反应前体的种类及配比情况下,可实现高性能共轭型支化聚合物的制备。(2) The present invention has the characteristics of strong universality, and can realize the preparation of high-performance conjugated branched polymers under the condition of rationally controlling the types and proportions of difunctional and trifunctional reaction precursors.

(3)本发明降低了阴离子交换膜的制备成本,且合成策略简便有效,更利于产业化推广和使用。(3) The invention reduces the preparation cost of the anion exchange membrane, and the synthesis strategy is simple and effective, which is more conducive to industrial promotion and use.

附图说明Description of drawings

图1搭载实例1-5和对比例1聚合物膜的碱性电解水装置上的极化曲线。Fig. 1 carries the polarization curve on the alkaline electrolyzed water device of example 1-5 and comparative example 1 polymer film.

具体实施方式Detailed ways

结合实例和附图对本发明作进一步描述,实例仅用于对本发明的解释,而本发明并未限定仅能用于此。故参照本发明的要求书,对实例或相关种类共轭型支化聚合物做的简单修改、变化,均属于本发明技术方案的范围。The present invention will be further described in combination with examples and accompanying drawings. The examples are only used to explain the present invention, and the present invention is not limited to be used only for this. Therefore, with reference to the requirements of the present invention, simple modifications and changes made to examples or related types of conjugated branched polymers all belong to the scope of the technical solution of the present invention.

实施例1Example 1

一种共轭型支化阴离子交换膜制备方法,包括以下步骤:A method for preparing a conjugated branched anion exchange membrane, comprising the following steps:

(1)在0℃下将24g的锌铜合金分散在140mL的四氢呋喃中,缓慢滴加15mL四氯化钛,待混合均匀后,加入对苯二甲酰氯(5g)和均苯三甲酰氯(0.3g)反应120h后用10%碳酸钾水溶液淬灭反应,过滤萃取后蒸出溶剂,得到聚合物前体。再将聚合物前体溶于NMP(10wt%)中,氮气氛下加入2M三甲胺的THF溶液,室温下反应72h,用乙酸乙酯沉出聚合物,水洗8次后真空干燥得到共轭型支化阴离子聚合物。(1) Disperse 24g of zinc-copper alloy in 140mL of tetrahydrofuran at 0°C, slowly add 15mL of titanium tetrachloride dropwise, and after mixing evenly, add terephthaloyl chloride (5g) and trimesoyl chloride (0.3 g) After reacting for 120 h, the reaction was quenched with 10% potassium carbonate aqueous solution, filtered and extracted, and the solvent was distilled off to obtain a polymer precursor. Dissolve the polymer precursor in NMP (10wt%), add 2M THF solution of trimethylamine under nitrogen atmosphere, react at room temperature for 72h, precipitate the polymer with ethyl acetate, wash 8 times with water and dry in vacuum to obtain the conjugated Branched anionic polymers.

(2)将烘干聚合物溶于DMAc溶液中(固含量:6%)配成筑膜液,经过滤、脱泡后浇筑在玻璃板上并用刮刀刮平。80℃下烘干6h后,将膜取下,得到厚度约为60μm的共轭型支化阴离子交换膜。(2) Dissolve the oven-dried polymer in DMAc solution (solid content: 6%) to form a membrane-building liquid, which is filtered and defoamed and then poured on a glass plate and scraped off with a scraper. After drying at 80° C. for 6 hours, the membrane was removed to obtain a conjugated branched anion exchange membrane with a thickness of about 60 μm.

实施例2Example 2

一种共轭型支化阴离子交换膜制备方法,包括以下步骤:A method for preparing a conjugated branched anion exchange membrane, comprising the following steps:

(1)在-10℃下将24g的锌分散在120mL的四氢呋喃中,缓慢滴加15mL四氯化钛,待混合均匀后,加入对苯二甲酰氯(5g)和三(4-甲酰氯苯基)膦(0.5g)反应100h后用10%碳酸钾水溶液淬灭反应,过滤萃取后蒸出溶剂,得到聚合物前体。再将聚合物前体溶于NMP(10wt%)中,氮气氛下加入三甲胺,室温下反应72h,用乙酸乙酯沉出聚合物,水洗8次后真空干燥得到共轭型支化阴离子聚合物。(1) Disperse 24g of zinc in 120mL of tetrahydrofuran at -10°C, slowly add 15mL of titanium tetrachloride dropwise, and after mixing evenly, add terephthaloyl chloride (5g) and tris(4-formyl chloride benzene Base) phosphine (0.5 g) was reacted for 100 h, and the reaction was quenched with 10% potassium carbonate aqueous solution, filtered and extracted, and the solvent was distilled off to obtain a polymer precursor. Dissolve the polymer precursor in NMP (10wt%), add trimethylamine under nitrogen atmosphere, react at room temperature for 72 hours, precipitate the polymer with ethyl acetate, wash it with water for 8 times, and dry it in vacuum to obtain a conjugated branched anionic polymer. things.

(2)将烘干聚合物溶于DMAc溶液中(固含量:4%)配成筑膜液,经过滤、脱泡后浇筑在玻璃板上并用刮刀刮平。60℃下烘干6h后,真空80℃干燥3h,将膜取下,得到厚度约为63μm的共轭型支化阴离子交换膜。(2) Dissolve the oven-dried polymer in DMAc solution (solid content: 4%) to form a membrane-building liquid, which is filtered and defoamed, poured on a glass plate, and scraped off with a scraper. After drying at 60° C. for 6 hours, vacuum drying at 80° C. for 3 hours, the membrane was removed to obtain a conjugated branched anion exchange membrane with a thickness of about 63 μm.

实施例3Example 3

一种共轭型支化阴离子交换膜制备方法,包括以下步骤:A method for preparing a conjugated branched anion exchange membrane, comprising the following steps:

(1)在0℃下将18g的镁分散在100mL的四氢呋喃中,缓慢滴加18g三氯化钛,待混合均匀后,加入对苯二甲酰氯(5g)和三(4-甲酰氯苯基)膦(0.3g)反应100h后用10%碳酸钾水溶液淬灭反应,过滤萃取后蒸出溶剂,得到聚合物前体。再将聚合物前体溶于NMP(10wt%)中,氮气氛下加入三甲胺,室温下反应72h,用乙酸乙酯沉出聚合物,水洗8次后真空干燥得到共轭型支化阴离子聚合物。(1) Disperse 18g of magnesium in 100mL of tetrahydrofuran at 0°C, slowly add 18g of titanium trichloride dropwise, and after mixing evenly, add terephthaloyl dichloride (5g) and tris(4-formyl chloride phenyl ) phosphine (0.3 g) was reacted for 100 h and then quenched with 10% potassium carbonate aqueous solution, filtered and extracted, and the solvent was distilled off to obtain a polymer precursor. Dissolve the polymer precursor in NMP (10wt%), add trimethylamine under nitrogen atmosphere, react at room temperature for 72 hours, precipitate the polymer with ethyl acetate, wash it with water for 8 times, and dry it in vacuum to obtain a conjugated branched anionic polymer. thing.

(2)将烘干聚合物溶于DMAc溶液中(固含量:8%)配成筑膜液,经过滤、脱泡后浇筑在玻璃板上并用刮刀刮平。60℃下烘干3h后,真空80℃干燥3h,将膜取下,得到厚度约为67μm的共轭型支化阴离子交换膜。(2) Dissolve the oven-dried polymer in DMAc solution (solid content: 8%) to form a membrane-building liquid, which is filtered and defoamed and then poured on a glass plate and scraped off with a scraper. After drying at 60° C. for 3 hours, vacuum drying at 80° C. for 3 hours, the membrane was removed to obtain a conjugated branched anion exchange membrane with a thickness of about 67 μm.

实施例4Example 4

一种共轭型支化阴离子交换膜制备方法,包括以下步骤:A method for preparing a conjugated branched anion exchange membrane, comprising the following steps:

(1)在20℃下将10g的锌分散在90mL的四氢呋喃中,缓慢滴加18g三氯化钛,待混合均匀后,加入联苯二甲酰氯(8g)和3,4',5-三酰基氯-1,1-联苯(1g)反应100h后用10%碳酸钾水溶液淬灭反应,过滤萃取后蒸出溶剂,得到聚合物前体。再将聚合物前体溶于NMP(10wt%)中,氮气氛下加入三甲胺,室温下反应48h,用乙酸乙酯沉出聚合物,水洗8次后真空干燥得到共轭型支化阴离子聚合物。(1) Disperse 10g of zinc in 90mL of tetrahydrofuran at 20°C, slowly add 18g of titanium trichloride dropwise, after mixing evenly, add biphenyl dicarboxylic acid chloride (8g) and 3,4',5-tri Acyl chloride-1,1-biphenyl (1 g) was reacted for 100 h, and the reaction was quenched with 10% potassium carbonate aqueous solution, filtered and extracted, and the solvent was distilled off to obtain a polymer precursor. Dissolve the polymer precursor in NMP (10wt%), add trimethylamine under nitrogen atmosphere, react at room temperature for 48 hours, precipitate the polymer with ethyl acetate, wash it with water for 8 times, and dry it in vacuum to obtain a conjugated branched anionic polymer. things.

(2)将烘干聚合物溶于DMAc溶液中(固含量:4%)配成筑膜液,经过滤、脱泡后浇筑在玻璃板上并用刮刀刮平。60℃下烘干6h后,真空80℃干燥6h,将膜取下,得到厚度约为58μm的共轭型支化阴离子交换膜。(2) Dissolve the oven-dried polymer in DMAc solution (solid content: 4%) to form a membrane-building liquid, which is filtered and defoamed, poured on a glass plate, and scraped off with a scraper. After drying at 60° C. for 6 hours, vacuum drying at 80° C. for 6 hours, the membrane was removed to obtain a conjugated branched anion exchange membrane with a thickness of about 58 μm.

实施例5Example 5

一种共轭型支化阴离子交换膜制备方法,包括以下步骤:A method for preparing a conjugated branched anion exchange membrane, comprising the following steps:

(1)在0℃下将15g的锌银合金分散在150mL的四氢呋喃中,缓慢滴加15mL四氯化钛,待混合均匀后,加入联苯二甲酰氯(8g)和1,3,5-三(对甲酰氯基)苯(0.8g)反应240h后用10%碳酸钾水溶液淬灭反应,过滤萃取后蒸出溶剂,得到聚合物前体。再将聚合物前体溶于NMP(10wt%)中,氮气氛下加入三甲胺,室温下反应48h,用乙酸乙酯沉出聚合物,水洗8次后真空干燥得到共轭型支化阴离子聚合物。(1) Disperse 15g of zinc-silver alloy in 150mL of tetrahydrofuran at 0°C, slowly add 15mL of titanium tetrachloride dropwise, and after mixing evenly, add biphenyl dicarboxylic acid chloride (8g) and 1,3,5- After reacting tris(p-formyl chloride)benzene (0.8 g) for 240 h, the reaction was quenched with 10% potassium carbonate aqueous solution, filtered and extracted, and the solvent was distilled off to obtain a polymer precursor. Dissolve the polymer precursor in NMP (10wt%), add trimethylamine under nitrogen atmosphere, react at room temperature for 48 hours, precipitate the polymer with ethyl acetate, wash it with water for 8 times, and dry it in vacuum to obtain a conjugated branched anionic polymer. thing.

(2)将烘干聚合物溶于DMAc溶液中(固含量:6%)配成筑膜液,经过滤、脱泡后浇筑在玻璃板上并用刮刀刮平。60℃下烘干6h后,真空80℃干燥6h,将膜取下,得到厚度约为57μm的共轭型支化阴离子交换膜。(2) Dissolve the oven-dried polymer in DMAc solution (solid content: 6%) to form a membrane-building liquid, which is filtered and defoamed and then poured on a glass plate and scraped off with a scraper. After drying at 60° C. for 6 hours, vacuum drying at 80° C. for 6 hours, the membrane was removed to obtain a conjugated branched anion exchange membrane with a thickness of about 57 μm.

对比例1、2为市面采购的FuMA-Tech阴离子交换膜FAA-3-PK-75与FAM。Comparative examples 1 and 2 are commercially purchased FuMA-Tech anion exchange membranes FAA-3-PK-75 and FAM.

实施例6Example 6

对本实施例1-5制备所得共轭型支化阴离子交换膜以及对比例1、2的FuMA-Tech阴离子交换膜FAA-3-PK-75与FAM进行离子交换容量(IEC)、溶胀率、吸水率和离子电导率测试。离子交换容量(IEC)是通过沉淀滴定法,计算出一定质量阴离子聚合物膜中的阴离子含量,从而得到阴离子聚合物膜的IEC。吸水、溶胀是通过将膜浸泡在水中24h后,测试其质量及尺寸与初始状态的差异百分比。离子电导率测量用上海辰华电化学测试系统进行测量,采用两电极交流阻抗法,测量全湿态的阴离子聚合物膜的离子电导率,具体结果见表1。Carry out ion exchange capacity (IEC), swelling rate, water absorption to the obtained conjugated branched anion exchange membrane prepared in the present embodiment 1-5 and the FuMA-Tech anion exchange membrane FAA-3-PK-75 and FAM of comparative examples 1 and 2 rate and ionic conductivity tests. The ion exchange capacity (IEC) is calculated by the precipitation titration method to calculate the anion content in a certain mass of anionic polymer membrane, so as to obtain the IEC of the anionic polymer membrane. Water absorption and swelling are measured by soaking the film in water for 24 hours, and testing the percentage difference between its mass and size and the initial state. The ionic conductivity was measured by Shanghai Chenhua electrochemical testing system, and the ionic conductivity of the fully wet anionic polymer membrane was measured by the two-electrode AC impedance method. The specific results are shown in Table 1.

表1.实施例1-5、对比例1、2的IEC、电导率、吸水率以及溶胀率(均为80℃下测得)Table 1. IEC, conductivity, water absorption and swelling rate of Examples 1-5, Comparative Examples 1 and 2 (all measured at 80°C)

IEC(mmol/g)IEC(mmol/g) 溶胀率(%)Swelling rate (%) 吸水率(%)Water absorption (%) 电导率(mS cm-1)Conductivity (mS cm -1 ) 实施例1Example 1 2.052.05 77 3939 125125 实施例2Example 2 2.082.08 77 4343 130130 实施例3Example 3 2.082.08 88 4242 128128 实施例4Example 4 2.12.1 1111 4545 131131 实施例5Example 5 2.032.03 66 3838 119119 对比例1Comparative example 1 1.241.24 16.716.7 3333 9393 对比例2Comparative example 2 1.371.37 21twenty one 3737 109109

表1说明本发明制得的共轭型支化阴离子交换膜相对于市售品种而言,具有更好的尺寸稳定性和更高的电导率,满足碱性电解水的需求。Table 1 shows that the conjugated branched anion exchange membrane prepared by the present invention has better dimensional stability and higher conductivity than commercially available ones, and meets the needs of alkaline electrolyzed water.

实施例7Example 7

将实施例1-5所得到的共轭型支化阴离子交换膜和对比例1的FuMA-Tech阴离子交换膜FAA-3-PK-75用于碱性电解水槽装置中,具体步骤如下:The obtained conjugated branched anion-exchange membrane of embodiment 1-5 and the FuMA-Tech anion-exchange membrane FAA-3-PK-75 of comparative example 1 are used in alkaline electrolytic water tank device, and concrete steps are as follows:

(1)制备电解水装置的膜电极组件:(1) Prepare the membrane electrode assembly of the electrolyzed water device:

取阴离子交换膜溶解在DMSO中(4wt%)作为离聚物溶液。之后称取一定量的Pt/C和IrO2催化剂(2mg cm-2),加入水和异丙醇溶液作为分散剂配制成催化剂油墨,并通过磁力搅拌和超声破碎使其分散均匀。最后加入离聚物溶液并再次超声处理使其均匀,并将其均匀喷涂在共轭型支化阴离子交换膜两侧,制成膜电极。待溶剂挥发后将其浸于1M KOH溶液中离子交换48h。Take the anion exchange membrane dissolved in DMSO (4wt%) as the ionomer solution. After that, a certain amount of Pt/C and IrO 2 catalysts (2 mg cm -2 ) were weighed, and water and isopropanol solution were added as dispersants to prepare catalyst inks, which were dispersed uniformly by magnetic stirring and ultrasonic crushing. Finally, the ionomer solution is added and ultrasonically treated again to make it uniform, and it is evenly sprayed on both sides of the conjugated branched anion exchange membrane to form a membrane electrode. After the solvent evaporated, it was immersed in 1M KOH solution for ion exchange for 48h.

(2)电解水性能测试:将膜电极夹在阴阳极之间来组装电解水装置。电化学测试在浸泡于阳极和阴极的1M KOH溶液中进行,温度保持在80℃。通过测量不同电流密度下的电池电压获得极化曲线。(2) Electrolyzed water performance test: The electrolyzed water device was assembled by sandwiching the membrane electrode between the cathode and anode. Electrochemical tests were carried out in a 1M KOH solution immersed in the anode and cathode at a temperature of 80°C. Polarization curves were obtained by measuring the cell voltage at different current densities.

附图1是基于实例1-5制备的共轭型支化阴离子交换膜以及对比例1的FuMA-Tech阴离子交换膜FAA-3-PK-75,在碱性电解水装置上的极化曲线。可见,实施例1-5制备的膜组装的电解槽,其电解水性能获得了明显提高,在500mA/cm-2的电压最低为1.53V,明显优于市售水平。Accompanying drawing 1 is the polarization curve of the conjugated branched anion exchange membrane prepared based on Examples 1-5 and the FuMA-Tech anion exchange membrane FAA-3-PK-75 of Comparative Example 1 on an alkaline electrolysis device. It can be seen that the membrane-assembled electrolyzer prepared in Examples 1-5 has significantly improved water electrolysis performance, and the lowest voltage at 500mA/cm -2 is 1.53V, which is obviously better than the commercially available level.

尽管通过上述实例可以部分展示本发明的内容,但本发明并不局限于实例所述单体,即上述实例的描述不是对本发明的限制。本领域技术人员应明了,对本发明的改进、本发明产品原料的等效替换及辅助成分的添加,或直接或间接运用在其他相关技术领域,均应包括在本发明专利保护范围内。Although the content of the present invention can be partially demonstrated through the above examples, the present invention is not limited to the monomers described in the examples, that is, the description of the above examples does not limit the present invention. Those skilled in the art should understand that the improvement of the present invention, the equivalent replacement of the raw materials of the product of the present invention and the addition of auxiliary components, or direct or indirect application in other related technical fields, should be included in the protection scope of the patent of the present invention.

Claims (10)

1.一种共轭型支化阴离子交换膜,其特征在于,阴离子交换膜为共轭型支化聚合物,结构式如下:1. a conjugated branched anion exchange membrane is characterized in that the anion exchange membrane is a conjugated branched polymer, and the structural formula is as follows: 其中x代表支化度%,x的范围为1-20;Wherein x represents the degree of branching%, and the range of x is 1-20; R为下列中的一种或多种:R is one or more of the following: M为下列中的一种或多种:M is one or more of the following: Q=F、Cl、Br、IQ=F, Cl, Br, I 2.一种权利要求1所述的共轭型支化阴离子交换膜的制备方法,其特征在于,包括以下步骤:2. a preparation method of conjugated branched anion exchange membrane according to claim 1, is characterized in that, comprises the following steps: 惰性气氛、-10-20℃下,将催化剂置于有机溶剂a中搅拌10-120min后,滴加聚合单体混合液开始反应;In an inert atmosphere, at -10-20°C, place the catalyst in an organic solvent a and stir for 10-120 minutes, then add the polymerized monomer mixture dropwise to start the reaction; 反应24-144h后用碱性溶液淬灭,之后萃取得到聚合物前体;After reacting for 24-144h, it is quenched with an alkaline solution, and then extracted to obtain a polymer precursor; 将所述聚合物前体溶于有机溶剂b中,惰性气氛下加入胺类溶液,20-80℃下反应24-72h,有机溶剂下沉出聚合物,水洗2-8次后真空干燥得到聚合物;Dissolve the polymer precursor in an organic solvent b, add an amine solution under an inert atmosphere, react at 20-80°C for 24-72 hours, sink the polymer in the organic solvent, wash it with water for 2-8 times, and dry it in vacuum to obtain a polymer thing; 将所述聚合物溶解在有机溶剂b中,经过滤、脱泡后浇筑成膜,得到所述共轭型支化阴离子交换膜。The polymer is dissolved in the organic solvent b, filtered, defoamed, and cast to form a membrane to obtain the conjugated branched anion exchange membrane. 3.根据权利要求2所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述惰性气氛为氮气或氩气。3. The preparation method of conjugated branched anion exchange membrane according to claim 2, characterized in that, the inert atmosphere is nitrogen or argon. 4.根据权利要求2所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述催化剂为副族金属及其相应氧化物、卤化物中的一种或多种。4. The method for preparing a conjugated branched anion exchange membrane according to claim 2, wherein the catalyst is one or more of subgroup metals and their corresponding oxides and halides. 5.根据权利要求2所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述有机溶剂a为甲醇、乙醇、N,N’-二甲基甲酰胺、二甲基亚砜、乙醚、丙酮、四氢呋喃、乙酸乙酯、二氯甲烷、氯仿、四氯化碳、石油醚中的一种或多种混合;所述有机溶剂b为N-甲基吡咯烷酮、N,N’-二甲基甲酰胺、N,N’-二甲基乙酰胺、二甲基亚砜中的一种或多种溶剂按任意比的混合。5. the preparation method of conjugated branched anion exchange membrane according to claim 2 is characterized in that, described organic solvent a is methanol, ethanol, N,N'-dimethylformamide, dimethylmethylene One or more mixtures of sulfone, ether, acetone, tetrahydrofuran, ethyl acetate, methylene chloride, chloroform, carbon tetrachloride, and petroleum ether; the organic solvent b is N-methylpyrrolidone, N,N' One or more solvents in dimethylformamide, N,N'-dimethylacetamide, and dimethyl sulfoxide are mixed in any ratio. 6.根据权利要求2所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述聚合单体混合液为二、三官能度酰氯单体的混合液,所述聚合单体混合液占整个体系的摩尔比为0.1-15%。6. the preparation method of conjugated branched anion exchange membrane according to claim 2, is characterized in that, described polymerized monomer mixed solution is the mixed solution of two, trifunctional acid chloride monomer, and described polymerized monomer The molar ratio of the mixed liquid to the whole system is 0.1-15%. 7.根据权利要求6所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述二官能度酰氯单体选自对苯二甲酰氯、联苯二甲酰氯;三官能度酰氯单体选自均苯三甲酰氯、1,3,5-三(对甲酰氯基)苯、3,4',5-三酰基氯-1,1-联苯、三(4-甲酰氯苯基)膦。7. the preparation method of conjugated branched anion exchange membrane according to claim 6 is characterized in that, described difunctionality acid chloride monomer is selected from terephthaloyl dichloride, biphenyl dicarboxylic acid chloride; Trifunctionality Acyl chloride monomers are selected from trimesoyl chloride, 1,3,5-tri(p-formyl chloride)benzene, 3,4',5-triacyl chloride-1,1-biphenyl, tris(4-formyl chloride)benzene base) phosphine. 8.根据权利要求2所述的共轭型支化阴离子交换膜的制备方法,其特征在于,所述碱性溶液为氢氧化钾、氢氧化钠、碳酸钠、碳酸钾中的一种或多种水溶液;所述胺类溶液为三甲胺水溶液。8. the preparation method of conjugated branched anion exchange membrane according to claim 2 is characterized in that, described alkaline solution is one or more in potassium hydroxide, sodium hydroxide, sodium carbonate, potassium carbonate An aqueous solution; the amine solution is trimethylamine aqueous solution. 9.一种共轭型支化阴离子交换膜的应用,其特征在于,所述共轭型支化阴离子交换膜为权利要求1的共轭型支化阴离子交换膜,或者权利要求2-8中任一项所述的制备方法制备得到的共轭型支化阴离子交换膜,所述共轭型支化阴离子交换膜用于碱性电解水制氢。9. An application of a conjugated branched anion exchange membrane, characterized in that, the conjugated branched anion exchange membrane is the conjugated branched anion exchange membrane of claim 1, or in claims 2-8 The conjugated branched anion exchange membrane prepared by any one of the preparation methods, the conjugated branched anion exchange membrane is used for hydrogen production by alkaline electrolysis of water. 10.据权利要求9所述的阴离子交换膜的应用,其特征在于,所述共轭型支化阴离子交换膜在碱性电解水制氢的应用,包括以下步骤:10. The application of the anion-exchange membrane according to claim 9, characterized in that the application of the conjugated branched anion-exchange membrane in the production of hydrogen from alkaline electrolyzed water comprises the following steps: (1)膜电极制备:将共轭型支化阴离子交换膜溶解在极性有机溶剂中得到离聚物溶液;将催化剂Pt/C和IrO2均匀分散在分散剂中配制成催化剂溶液;分别取离聚物溶液与催化剂溶液,混合均匀后,均匀喷涂在共轭型支化阴离子交换膜两侧,制成膜电极;然后在碱性溶液中进行离子交换;(1) Membrane electrode preparation: dissolving the conjugated branched anion exchange membrane in a polar organic solvent to obtain an ionomer solution; uniformly dispersing the catalyst Pt/C and IrO in a dispersant to prepare a catalyst solution; The ionomer solution and the catalyst solution are evenly mixed, and then evenly sprayed on both sides of the conjugated branched anion exchange membrane to form a membrane electrode; then ion exchange is performed in an alkaline solution; (2)组装电解水装置:将膜电极夹在阴阳极之间来组装电解水装置。(2) Assemble the electrolyzed water device: sandwich the membrane electrode between the anode and cathode to assemble the electrolyzed water device.
CN202310496472.XA 2023-05-04 2023-05-04 Conjugated branched anion exchange membrane, preparation method and application Pending CN116574371A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202310496472.XA CN116574371A (en) 2023-05-04 2023-05-04 Conjugated branched anion exchange membrane, preparation method and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202310496472.XA CN116574371A (en) 2023-05-04 2023-05-04 Conjugated branched anion exchange membrane, preparation method and application

Publications (1)

Publication Number Publication Date
CN116574371A true CN116574371A (en) 2023-08-11

Family

ID=87542470

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202310496472.XA Pending CN116574371A (en) 2023-05-04 2023-05-04 Conjugated branched anion exchange membrane, preparation method and application

Country Status (1)

Country Link
CN (1) CN116574371A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5254261A (en) * 1991-08-12 1993-10-19 Hydranautics Interfacially synthesized reverse osmosis membranes and processes for preparing the same
CN105646924A (en) * 2016-03-29 2016-06-08 郑州大学 Monovalent anion selective ion exchange membrane and preparation method thereof
CN111729694A (en) * 2020-07-01 2020-10-02 中国科学技术大学先进技术研究院 Preparation method of anion exchange membrane and anion exchange membrane
CN112844046A (en) * 2021-01-19 2021-05-28 恩泰环保科技(常州)有限公司 Positively charged nanofiltration membrane and preparation method thereof
CN114853985A (en) * 2022-06-06 2022-08-05 中国科学技术大学 Self-crosslinking anion exchange membrane without ether conjugated aromatic main chain and preparation method thereof
US20220306677A1 (en) * 2019-06-04 2022-09-29 Yale University Compositions and methods for making hybrid polypeptides

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5254261A (en) * 1991-08-12 1993-10-19 Hydranautics Interfacially synthesized reverse osmosis membranes and processes for preparing the same
CN105646924A (en) * 2016-03-29 2016-06-08 郑州大学 Monovalent anion selective ion exchange membrane and preparation method thereof
US20220306677A1 (en) * 2019-06-04 2022-09-29 Yale University Compositions and methods for making hybrid polypeptides
CN111729694A (en) * 2020-07-01 2020-10-02 中国科学技术大学先进技术研究院 Preparation method of anion exchange membrane and anion exchange membrane
CN112844046A (en) * 2021-01-19 2021-05-28 恩泰环保科技(常州)有限公司 Positively charged nanofiltration membrane and preparation method thereof
CN114853985A (en) * 2022-06-06 2022-08-05 中国科学技术大学 Self-crosslinking anion exchange membrane without ether conjugated aromatic main chain and preparation method thereof

Similar Documents

Publication Publication Date Title
US9975995B2 (en) Ion conducting polymer comprising partially branched block copolymer and use thereof
JP5384335B2 (en) Ion conductive membrane
EP2490279A1 (en) Aromatic polymer ion exchange membrane and its complex membrane and its application for acidic electrolyte flow energy storage battery
CN102299351B (en) Polybenzimidazole polymer ion exchange membrane and its preparation and application
CN118119649A (en) Proton exchange membrane for electrochemical reactions
CN116535619A (en) Preparation method and application of high molecular weight arylene isatin polymer and ionic solvent film
CN115895014A (en) High-hydrophilicity inorganic doped composite porous polymer diaphragm, preparation method and application
CN118580470A (en) A cationic polymer based on halogenated meta-terphenyl group and its preparation method and application
EP3252035A1 (en) Compound comprising aromatic ring, and polyelectrolyte membrane using same
JP2005183311A (en) Polyelectrolyte for direct methanol type fuel cell electrode, varnish composition, and direct methanol type fuel cell
KR20240168454A (en) Anion exchange polymers and membranes for electrolysis
TW201031676A (en) Polymeric laminates, processes for producing the same, and use thereof
CN116574371A (en) Conjugated branched anion exchange membrane, preparation method and application
US7981567B2 (en) Polymer having oxocarbon group, and use thereof
CN103724648A (en) Strong alkaline polyarylether ionomer anion-exchange membrane as well as preparation and application thereof
CN115093559B (en) Self-polymerization microporous ionomer, and preparation method and application thereof
CN118988016A (en) Gel polybenzimidazole ion solvent membrane with double-crosslinked cation network structure, preparation method thereof and application of gel polybenzimidazole ion solvent membrane in hydrogen production by alkaline water electrolysis
KR20250042180A (en) Anion exchange polymers and membranes for electrolysis
CN117362722A (en) A proton exchange membrane, its preparation method and a membrane electrode for electrolyzing water to produce hydrogen
CN115536885A (en) Preparation method of submicron phase separation anion exchange membrane
JP5233065B2 (en) Polymer having ionic group, polymer electrolyte material, polymer electrolyte component, membrane electrode composite, and polymer electrolyte fuel cell
KR102629899B1 (en) Compound, polymer comprising monomer derived from same, polymer separation membrane using same, membrane electrode assembly, fuel cell and redox flow cell using same
JP4292856B2 (en) Polymer electrolyte, polymer electrolyte membrane and fuel cell using them
JP5581593B2 (en) Polyarylene-based copolymer, proton conducting membrane and solid polymer electrolyte fuel cell
KR102892174B1 (en) Polymer electrolyte membrane and preparation method thereof

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