Sol-gel法在燃料电池用质子交换膜制备中的应用

主要综述了溶胶-凝胶(sol-gel)法在制备质子交换膜中的应用。将Sol-gel法应用到质子交换膜的制备中,提供了一种制膜和优化膜的行之有效的途径。本文着重从利用sol-gel法制备有机/无机杂化型、磷酸/二氧化硅型以及全氟磺酸膜的改进型质子交换膜等方面加以介绍。     

ZrO2纳米粒子原位杂化PVDF膜的制备及其抗污染性能

针对传统聚合物膜抗污染性差的问题,本文从杂化膜结构设计出发,提出将ZrO2纳米粒子的原位制备和聚偏氟乙烯(PVDF)相转化成膜过程有机结合的制膜新方法.该方法将阴离子交换树脂引入到N,N-二甲基甲酰胺(DMF)中,以氧氯化锆为原料,利用阴离子交换树脂提供的―OH与无机盐的阴离子进行交换,得到ZrO2纳米粒子均匀分散的N,N-二甲基甲酰胺溶胶体系.随后将PVDF聚合物溶解到所得的N,N-二甲基甲酰胺溶胶体系中,获得均一、透明的铸膜液.利用X射线光电子能谱(XPS)和透射电子显微镜(TEM)对杂化膜中锆的存在状态和分散性能进行了表征.结果表明,ZrO2纳米粒子均匀分散在PVDF基体中,并且形成的纳米粒子的粒径约为10-20 nm.通过粘度、分相速度和膜形态的测定,研究了成膜机理.结果表明,ZrO2纳米粒子的引入加速了铸膜液成膜过程的分相速度.杂化膜的亲水性能通过接触角测定仪进行了评价.并选择以牛血清蛋白为代表模拟污染物,考察了杂化超滤膜的抗污染性能.结果表明,原位形成的ZrO2纳米粒子显著提高了膜的亲水性,减少了膜对蛋白质的吸附.这种将ZrO2纳米粒子的原位制备和PVDF相转化成膜过程有机结合的制膜新方法在有机-无机杂化膜的制备领域具有显著意义.     

燃料电池聚合物电解质膜的研究进展

本文根据聚合物电解质膜燃料电池操作温度、使用的电解质和燃料的不同,将其分为高温质子交换膜燃料电池、低温质子换膜燃料电池、直接甲醇燃料电池和阴离子交换膜燃料电池,综述了它们所用电解质膜的最新进展.第一部分简要介绍了这4种燃料电池的优点和不足.第二部分首先介绍了Nafion膜的结构模型,并对平行柱状纳米水通道模型在介观尺度上进行了修正;接着分别对应用于不同燃料电池的改性膜的改性思路作了分析;最后讨论了用于不同燃料电池的新型质子交换膜的研究,同时列举了性能突出的改性膜和新型质子交换膜.第三部分介绍了阴离子交换膜的研究现状.第四部分对未来聚合物电解质膜的研究作了展望.     

多羧基酞菁铜、乙酰基二茂铁改性CMC/CS双极膜的制备及表征

柔性链高分子聚乙二醇(PEG)分别与阳离子交换膜层羧甲基纤维素钠(CMC)、阴离子交换膜层壳聚糖(CS)共混以增强界面的相容性和膜的机械性能.以金属有机高分子多羧基酞菁铜(CuPc)改性CMC、乙酰基二茂铁改性CS,采用流延法制备了CuPc-mCMC/mCS双极膜.双极膜溶胀性和热重分析结果表明膜改性后稳定性能得到提高.膜交流阻抗、I-V工作曲线的测定结果表明该双极膜阻抗及工作电压均较小.双极膜经改性具有较高的离子渗透性能。     

有机-无机复合质子交换膜的制备与界面特性

有机-无机复合质子交换膜的开发是燃料电池用质子交换膜的一个重要研究方向,本文综述了有机-无机复合质子交换膜的制备方法,分析了两相之间的界面特性,并对这种复合膜的研究前景进行了展望.     

1,4-双(二苯基膦)丁烷交联的季膦化聚芳醚酮阴离子交换膜

以1,4-双(二苯基膦)丁烷为交联剂,以具有四甲基联苯结构的聚芳醚酮为基体材料,分别制备了刚性三苯基膦和柔性三丁基膦修饰的阴离子交联膜材料.交联剂在交联结构形成的过程中转变成季膦盐,在提高膜材料机械稳定性的同时保持离子交换功能基团的含量.研究了2种阴离子交换膜的尺寸稳定性、电导率、机械性能及耐碱稳定性等.研究结果表明,当交联度为20%时,三苯基膦与三丁基膦修饰的阴离子交换膜的拉伸强度分别由未交联时的27和18 MPa提高到45和30 MPa;交联的膜材料在60℃的3 mol/L KOH溶液中浸泡120 h后,三苯基膦修饰的阴离子交换膜的电导率保留率为81%,三丁基膦修饰的阴离子交换膜的电导率保留率为69%,膜的耐碱稳定性均较未交联时有明显提高.交联度相同时,三苯基膦修饰的阴离子交换膜表现出更高的拉伸强度和更好的耐碱稳定性.     

聚合物燃料电池离子交换膜新进展

聚合物离子交换膜是聚合物电解质燃料电池的关键部件之一,根据聚合物携带反离子种类,可分为质子交换膜燃料电池（PEMFC）和碱性阴离子交换膜燃料电池（APEFC）。本文着重阐述近年来研究热点：高温低湿质子交换膜（HTPEM）和聚合物碱性阴离子交换膜（APE）的研究进展,指出燃料电池中聚合物离子交换膜（HTPEM和APE）面...     

燃料电池用质子交换膜的研究进展

质子交换膜是燃料电池的重要组成部分。本文介绍了全氟磺酸膜的优缺点,对其进行改进的方法以及新型质子交换膜的发展情况,重点讨论了各类质子交换膜的制备、结构、性质以及它们在质子交换膜燃料电池(PEMFC)或直接甲醇燃料电池(DMFC)的应用,最后提出质子交换膜的发展趋势。     

基于阳离子交换基团的阴离子交换膜研究进展

近年来,阴离子交换膜燃料电池的发展受到了广泛关注。 开发具有碱稳定性能优异、电导率高的阴离子交换膜材料成为了研究的热点。 阴离子交换膜(AEM)主要由聚合物骨架和阳离子基团组成,除了聚合物骨架结构,离子交换基团是影响膜碱稳定性和电导率的重要因素,因此,设计离子基团是提高膜性能的重要手段之一。 本文综述了近年来功能基团分别为季铵、胍基、咪唑鎓盐、季鏻、金属配合物、N-螺环季铵盐、哌啶和吡咯等阳离子交换基团的AEM的研究进展,其中包括不同种类阳离子交换基团的AEM的结构,碱稳定性能和OH^-电导率,同时对于含有阳离子交换基团的AEM的结构设计进行了分析和展望。     

辣根过氧化物酶自组装多层膜结构形貌与活性的研究

用分子沉积自组装作制备了阳离子化和阴离子化的辣根过氧化物酶自组装膜；并用原子力显微镜（AFM）研究了不同离子化辣根过氧化物酶单层及多层自组装膜的形貌结构与自组装膜的活性变化关系。结果表明：阴离子化的辣根过氧化物酶自组装膜的表面形貌比较粗糙，均方根粗糙度（RMS）及酶分子粒径较大，且组装膜的活性比较大。     

Polymers with Tethered Anionic and Cationic Groups as Membranes for Fuel Cells

Ionic clustering, water binding, and ion conductivity were studied in polymers functionalized with sulfonic acid and quaternary ammonium hydroxide groups. Small-angle x-ray scattering showed that no clustering occurred in the quaternary ammonium containing anion exchange membranes, while evidence of ionic clusters was present in both sulfonated poly(phenylene) and in Nafion, a poly(perfluorosulfonic acid). Interestingly, the water self-diffusion coefficients of the anion exchange membranes were generally greater than those observed for the sulfonated poly- (phenylene)s, and moreover, the water self diffusion coefficients in anion exchange membranes were not a strong function of diffusion time. The water binding behavior lead to increased normalized conductivity in anion exchange membranes as compared to proton exchange membranes at the highest ion exchange capacities.     

Preparation and properties of anion exchange membranes having pyridinium or pyridinium derivatives as anion exchange groups

Anion exchange membranes with pyridinum groups and various pyridinium derivative groups were prepared from a copolymer membrane composed of chloromethylstyrene and divinylbenzene, and pyridine and pyridine derivatives. The anion exchange membranes obtained showed excellent electrochemical properties in electrodialysis. The transport numbers of sulfate ions, bromide ions, nitrate ions, and fluoride ions relative to chloride ions were evaluated in connection with the species of a substituent and the position of the substituent in the pyridinium groups. In general, when a hydrophilic substituent (methanol groups) existed at the 2-position of the pyridinium groups, nitrate ions and bromide ions, which are less hydrated, permeated through the membranes with difficulty, and sulfate ions permeated selectively through the membranes. On the other hand, when hydrophobic groups, for example, ethyl groups, existed at the 2-position of the pyridinium groups, bromide ions and nitrate ionspermeated selectively through the membranes and fluoride ions had difficulty permeating through the membranes. The carbon number of the alkyl chain of 4-alkyl pyridinium groups also affected permeation of nitrate ions and bromide ions due to the change in hydrophilicity of the membranes. Though the hydration of the anions and the species of the substituent at the 2-position of the pyridinium groups were related to selective permeation of the anion through the membranes, permeation of sulfate ions was not as sensitive to the hydrophilicity of the membranes. © 1998 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 36: 49–58, 1998     

Preparation and characterization of Type II anion exchange membranes from poly(2,6-dimethyl-1,4-phenylene oxide) (PPO)

To separate hydrophilic anions from hydrophobic ones, Type II PPO-based anion exchange membranes were developed. Different from Type I (with both trimethylbenzylammonium and triethylbenzylammonium groups), Type II has an excellent hydrophobicity modifier as fixed groups: dimethyethanolammonium groups, which were introduced into PPO (poly(2,6-dimethyl-1,4-phenylene oxide)) by following benzyl bromination of PPO and subsequent quaternary amination with a dimethylethanolamine (DMEA) aqueous solution. The membrane's intrinsic properties are dependent on DMEA concentration and amination temperature. The optimum conditions for membrane preparation are as follows: amination temperature 70 °C, time 30–48 h, and DMEA concentration 1:3–1:5 (v/v, DMEA to water). The obtained Type II anion exchange membranes had an IEC of 1.5 mmol/g dry membrane, water content of 30%, and membrane area resistance of 30 Ω cm². The introduced dimethyethanolammonium groups can block hydrated anions from the access to membranes but let hydrophobic anions transport; hence, an effective separation between hydrophilic and hydrophobic anions can be achieved during electro-membrane operation.     

Generation of light-induced electrical potential from ion exchange membranes containing 4,4′-bipyridine moiety. II. Effect of species of anion exchange membranes on photovoltage

Various anion exchange membranes containing the 4,4′-bipyridine moiety as anion exchange groups were prepared from membranous copolymers of chloromethylstyrene and divinylbenzene and membranes of chloromethylated polysulfone and 4,4′-bipyridine. After evaluating the electrochemical properties of the obtained anion exchange membranes, the effect of membrane species on the generation of a photovoltage was examined by irradiation using a xenon lamp. The membranes swelled with ethylene glycol were clamped between two ITO electrodes and sealed by adhesive. The generated photovoltage and photocurrent from about a 120 μm thick membrane were about 80 mV and 400 nA, respectively, in a 200K Ω load resistance, though dependent of membrane species. The voltage decreased with increasing crosslinking by the divinylbenzene in the copolymer membranes. The effect of counter ion species on the voltage was examined and a chloride ion form of membrane showed the highest photovoltage. The membranes with different thicknesses, which were prepared from polysulfone derivatives, were evaluated and the voltage decreased with decreasing thickness. Even a porous membrane from polysulfone derivatives showed a photovoltage though a porous membrane in which a methyl viologen ethylene glycol solution had been impregnated did not have a stable voltage. Also, the anion exchange membrane containing the benzyl trimethylammonium moiety, which is the conventional anion exchange groups, did not show a high and stable photovoltage upon photoirradiation. © 1996 John Wiley & Sons, Inc.     

Preparation of alkaline anion exchange membranes based on functional poly(ether-imide) polymers for potential fuel cell applications

A novel poly(ether-imide)-based alkaline anion exchange membrane with no free base has been prepared and characterized for its ionic conductivity in water, which is a critical metric of its applicability in a liquid-fed direct methanol fuel cell. The poly(ether-imide)-based membranes were prepared by chloromethylation, quaternization and alkalization of commercial poly(ether-imide) and the derivatives were characterized by NMR. The chemical and thermal stabilities were investigated by measuring changes of ionic conductivities when the membranes were placed in various alkaline concentrations and temperatures for 24 h. The membranes were stable at all concentrations of KOH at room temperature, but not at elevated temperatures. The membranes were stable in 1.0 M KOH solution up to 80 °C without losing membrane integrity. The measured conductivity of the formed membrane ranged from 2.28 to 3.51 × 10⁻³ S/cm at room temperature. This preliminary study indicates that functionalized poly(ether-imide) has suitable conductivity suggesting that it can be used as an alkaline anion exchange membrane in fuel cell applications.     

碱性直接甲醇燃料电池含氟阴离子交换膜的制备及性能研究

以甲基丙烯酸二甲基氨基乙酯和甲基丙烯酸三氟乙酯为单体,经过自由基聚合反应、成膜和碱化3个步骤制备氢氧型的DMAEMA/TFMA聚合物阴离子交换膜,系统表征该聚合物膜的结构和性能.结果表明:室温下其电导率可达10-2 S.cm-1;该膜的甲醇渗透系数低于10-7 cm2.s-1;以该膜组装的单电池在室温下的最大功率密度为43.2 mW/cm2,在燃料电池中有良好的应用前景.     

Synthesis of ionic polybenzimidazoles with broad ion exchange capacity range for anion exchange membrane fuel cell application

In this study, new anion exchange membranes (AEM) based on crosslinked polybenzimidazole (m-PBI) with quaternary ammonium groups, crosslinkable allyl groups, and hydrophobic ethyl groups as side chains are synthesized and characterized. The AEMs are crosslinked by thermal thiol-ene reaction using a dithiol crosslinker. The ion exchange capacity (IEC) values and crosslinking density were controlled by the number of quaternary ammonium groups and allyl groups, respectively. The introduction of ethyl groups improved the solubility of ionic PBIs even at very low IEC values by eliminating the hydrogen bonding interaction of imidazole rings. This method allows ionic PBIs with broad IEC values, from 0.75 to 2.55 mmol/g, to be prepared. The broad IEC values were achieved by independently controlling the numbers of quaternary ammonium groups, allyl groups, and hydrophobic ethyl groups during preparation. The crosslinked ionic PBIs revealed hydroxide conductivity from 16 to 86 mS/cm at 80°C. The wet membranes also showed excellent mechanical strength with tensile strength of 12.2 to 20.1 MPa and Young's Modulus of 0.67 to 1.45 GPa. The hydroxide conductivity of a crosslinked membrane (0.40Q0.60Et1.00Pr, IEC = 0.95 mmol/g) decreased only 7.9% after the membranes was immersed in a 1.0 M sodium hydroxide solution at 80°C for 720 h. A single fuel cell based on this membrane showed a maximum peak power density of 136 mW/cm² with a current density of 377 mA /cm² at 60°C.     

Synthesis of guanidinium‐based anion exchange membranes and their stability assessment

Alkaline fuel cells potentially offer improved conversion efficiency and the prospect of using non‐noble metal catalysts; however, low conductivity and fast degradation of anion exchange membranes (AEMs) prevent their widespread application. In this work, a series of novel composite AEMs were synthesized by incorporating guanidinium‐based polymers into a porous polytetrafluoroethylene (PTFE) film. The guanidinium‐based polymers were polymerized using a condensation process between a guanidinium salt and two different diamines so that the guanidinium cations were tethered to the polymer backbone to enhance both conductivity and durability. In addition, polymer crosslinking was conducted to further reinforce the mechanical strength of the membranes and interlock the guanidinium moieties to the porous PTFE. It was found that the ionic conductivity of the synthesized membrane reached up to approximately 80 mS cm^?1 at 20°C in deionized water. These membranes also exhibited superior stability compared to commercial quaternary ammonium AEMs after being exposed in 5 M KOH solution at 55°C for 50 h. Copyright © 2013 John Wiley & Sons, Ltd.     

Binding Aedes aegypti densonucleosis virus to ion exchange membranes

Experimental and numerical results for binding Aedes aegypti densonucleosis virus (AeDNV) using anion and cation exchange membranes are presented. AeDNV particles are adsorbed by anion and cation exchange membranes providing the virus particles and membranes are oppositely charged. Q membranes which are strongly basic anion exchangers were the most effective. Dynamic and static capacities for Q membranes were found to be similar. A numerical model is proposed which assumes a log normal pore size distribution. By estimating the required parameters from static binding experiments, the model may be used to calculate the breakthrough curve for virus adsorption.