钴-聚吡咯-碳载Pt催化剂的制备及其单电池性能研究

采用脉冲微波辅助化学还原法制备了钴-聚吡咯-碳载Pt催化剂(Pt/Co-PPy-C),并将其作为阴极催化剂,组装单电池。考察了电池运行温度和氢气/空气计量比对单电池性能的影响,并与商业Pt/C催化剂进行了耐久性实验比较。 结果表明,运行温度为70 ℃,氢气与空气的计量比为1.2:2.5时单电池性能最佳。600 mA/cm²恒电流稳定运行150 h耐久性测试中,以Pt/Co-PPy-C为阴极催化剂的单电池平均电压衰退率为0.119 mV/h,是商业Pt/C催化剂的26%。耐久性测试前后,单电池的阴极电荷传递阻抗为7.176和8.767 Ω,均比商业Pt/C催化剂阻抗小;Pt颗粒粒径从2.46 nm增长到3.18 nm,均小于商业Pt/C催化剂的粒径。这表明,以Pt/Co-PPy-C催化剂为阴极催化剂制备的单电池性能优良,在质子交换膜燃料电池中有广泛的应用前景。     

质子交换膜燃料电池Pt/C阴极氧还原动力学模拟

质子交换膜燃料电池的商业化应用迫切要求降低其Pt载量. 本文通过Pt/C氧还原电极的动力学模型计算,研究了Pt/C电极中的氧分布、生成电流以及满足实际应用的最小Pt载量. 结果表明：燃料电池Pt/C电极,阴极产生严重浓差极化的催化层厚度为40mm;功率密度达到1.4 W•cm^-2（2.1 A•cm^-2@0.67 V）的电池性能需要3mm左右的Pt/C阴极催化层,阴极Pt载量为0.122 mg•cm^-2,即可使膜电极的阴极铂用量低于0.087 g•kW^-1.     

聚苯胺修饰Pt/C催化剂对质子交换膜燃料电池动态响应的促进作用

将超级电容器材料聚苯胺引入电极催化剂中以缓冲燃料电池负载的变化.以硫酸为掺杂剂,将化学法合成的聚苯胺(PANI)与Pt/C超声分散混合,制成PANI-Pt/C催化剂.PANI-Pt/C的循环伏安测试和作为质子交换膜燃料电池阴极电催化剂的电池性能测试表明,PANI含量为10%时能够提高Pt/C催化剂对氧的还原动力学速度和燃料电池放电性能.电池在不同电流负载下的电压动态响应和对电池脉冲电流的动态响应以及PANI-Pt/C催化剂多电位电势阶跃计时电流测试显示,聚苯胺在催化剂中具有在瞬间电流负载时缓冲电池电压和电池大电流放电时平稳电压的作用.     

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.     

用于质子交换膜燃料电池抗CO的Pt-CeO2/C催化剂的制备和表征

采用一步沉淀法,制备了纳米级Pt-CeO2/C电催化剂.透射电镜和X射线衍射表征结果表明,制备的催化剂Pt颗粒均匀分散于碳载体表面,其粒径主要分布于1.5～2.5 nm.将Pt-CeO2/C催化剂制备成质子交换膜燃料电池膜电极,经循环伏安和单电池极化曲线测试发现,Pt-CeO2/C催化剂性能与Pt/C催化剂的相当.一氧...     

基于新球型微观结构模型模拟PEMFC催化层

建立了一个新球型催化层微观结构模型, 并基于此模型对质子交换膜燃料电池(PEMFC)性能进行了模拟. 该模型中假设催化层由Pt/C 颗粒和离子聚合物-孔混合相组成. 假设Pt/C 颗粒为球形结构, 其直径符合正态分布, 用不同直径的球来表示随机分散在电极中的Pt/C 颗粒. 计算了催化层内的传递和电化学反应, 研究了质子和氧气及电化学反应速率在电极厚度方向上的分布, 并且通过对比氧气浓度、过电位和电化学反应速率的分布、极化曲线及催化剂利用率等证明了适当的电极厚度与Pt/C颗粒粒径有利于提高电池性能.     

乙烷PBI/H_3PO_4质子传导膜燃料电池性能

研究了以乙烷作为燃料、掺杂了H3PO4的聚苯并咪唑(PBI)材料作为质子传导膜、Pt/C作为电极催化剂构成的燃料电池电化学性能。采用溶液铸造法制备了PBI/H3PO4质子传导膜,考察了在PBI膜中H3PO4的掺杂量与时间的关系及乙烷气体在增湿和不增湿条件下PBI/H3PO4燃料电池的电化学性能;探讨了电池的反应机理及不同操作温度对电池性能的影响。结果表明,PBI膜H3PO4适宜的掺杂时间为8h,电解质中掺杂600mol%H3PO4;乙烷气体增湿后,电池性能变好;操作温度提高,电化学反应速率加快,电池的输出电流与功率密度增加。结构为C2H6,(Pt/C阳极)/PBI/H3PO4膜/(Pt/C阴极),O2的单电池,在200℃和0.1Mpa、乙烷气体的湿度从0增加到0.02kgH2O/kg乙烷时,电池的最大输出电流密度从1.5mA·cm-2增加到34mA·cm-2,最大功率密度从0.33mW·cm-2增加到5.5mW·cm-2。     

Pt纳米催化剂在质子交换膜燃料电池催化层中的尺寸效应研究

以XC-72碳黑为载体, H2[PtCl6]为前驱体, 采用浸渍还原法并结合后续高温处理, 制备出不同尺寸Pt颗粒(3～8 nm)的Pt/C催化剂. 在基于质子交换膜燃料电池(PEMFC)单电池的电化学电解池中, 对实际PEMFC催化层中燃料电池反应的Pt催化剂尺寸效应进行了研究. 结果表明, 在PEMFC催化层环境中, Pt/C纳米催化剂对氢氧化和氧还原反应均有显著的粒度尺寸效应. 随着Pt粒度减小, 氢氧化和氧还原反应的表面积活性均降低.     

直接甲醇燃料电池催化活性层的优化

本文考察了直接甲醇燃料电池 (DMFC)不同催化剂载量的膜电极性能 .对催化剂层中Nafion含量进行优化 ,研究了Nafion含量对电池的阻抗的影响 .实验发现 :DMFC适宜的阳极Pt_Ru/C载量为Pt 4mg/cm2 、Nafion质量百分含量为 2 1.4 % ;高电流密度下 ,阴极Pt/C载量为Pt4mg/cm2 、Nafion质量百分含量为 2 1.4 %时 ,有较好的放电性能 ,继续增加Nafion含量 ,阴极的欧姆极化和浓差极化增大 ,电池性能下降     

乙烷质子传导膜燃料电池的极化与反应机理

制备了以乙烷作为燃料电池膜电极组装(MEA)及构建了单电池系统。研究了Nafion材料作为质子传导膜、Pt/C作为电极催化剂构成的燃料电池在105 ℃和0.4 MPa电化学性能。采用交流阻抗分析法、色谱分析法及根据Faraday定律,考察了电池的电极极化过程,确定了电池的反应产物并探讨了电极的电化学反应机理。研究结果表明,乙烷燃料电池内阻引起的欧姆极化很小,电池阴极的极化主要是欧姆极化过程所控制,阳极极化主要为活化和浓差过程控制,阳极极化比阴极极化显著,乙烷燃料电池的极化主要在阳极侧;在实验操作条件下,阴极反应产物为水,阳极反应的主产物为CO₂且含有少量的CO,电池反应产物不含乙烯。     

多核多氧硫钼酸盐化合物的合成及质子传导性能

质子交换膜燃料电池(PEMFC)因能量转化率高、 污染小、 工作温度低、 启动速度快而被广泛应用. Nafion系列膜成本高、 结构特性模糊, 阻碍了质子传导性能的进一步提高和对传导机理的精确理解. 因此开发具有结构明确、 传导路径清晰的高质子传导率的晶态材料对于燃料电池领域具有重要意义. 本文利用有机配体5-羟基间苯二甲酸作为模板诱导[Mo₂S₂O₂]²⁺阳离子, 自组装成一种多核多氧硫钼酸盐簇[N(CH₃)₄]₂H₂· [(Mo₂S₂O₂)₈(OH)₁₆(C₈O₅H₄)₂]·22H₂O(Mo₁₆). 该化合物清晰明确的结构和结构中存在的密集氢键网络可用于进行质子传导性能的研究. 交流阻抗测试结果表明, Mo₁₆在宽温度范围内具有较高的质子传导性能. 在97%湿度(RH), 85 ℃条件下其质子传导率可达1.9×10^-2 S/cm, 表明该化合物具有作为高效质子导体的良好前景.     

Highly active iridium catalyst for hydrogen production from formic acid

Formic acid(FA) dehydrogenation has attracted a lot of attentions since it is a convenient method for H_2 production. In this work, we designed a self-supporting fuel cell system, in which H_2 from FA is supplied into the fuel cell, and the exhaust heat from the fuel cell supported the FA dehydrogenation. In order to realize the system, we synthesized a highly active and selective homogeneous catalyst Ir Cp*Cl_2 bpym for FA dehydrogenation. The turnover frequency(TOF) of the catalyst for FA dehydrogenation is as high as7150 h~(-1)at 50°C, and is up to 144,000 h~(-1)at 90°C. The catalyst also shows excellent catalytic stability for FA dehydrogenation after several cycles of test. The conversion ratio of FA can achieve 93.2%, and no carbon monoxide is detected in the evolved gas. Therefore, the evolved gas could be applied in the proton exchange membrane fuel cell(PEMFC) directly. This is a potential technology for hydrogen storage and generation. The power density of the PEMFC driven by the evolved gas could approximate to that using pure hydrogen.     

Preparation and characterization of sulfated zirconia (SO4/ZrO2)/Nafion composite membranes for PEMFC operation at high temperature/low humidity

Fine particle superacidic sulfated zirconia (SO₄²⁻/ZrO₂, S-ZrO₂) was synthesized by ameliorated method, and composite membranes with different S-ZrO₂ contents were prepared by a recasting procedure from a suspension of S-ZrO₂ powder and Nafion solution. The physico-chemical properties of the membranes were studied by ion exchange capacity (IEC) and liquid water uptake measurements, scanning electron microscopy (SEM) and X-ray diffraction (XRD) analysis, thermogravimetry–mass spectrometry (TG–MS) and Fourier transform infrared (FT-IR) spectroscopy. The results showed that the IEC of composite membrane increased with the content of S-ZrO₂, S-ZrO₂ was compatible with the Nafion matrix, the incorporation of the S-ZrO₂ could increase the crystallinity and also improve the initial degradation temperature of the composite membrane. The performance of single cell was the best when the S-ZrO₂ content was 15 wt.%, and achieved 1.35 W/cm² at 80 °C and 0.99 W/cm² at 120 °C based on H₂/O₂ and at a pressure of 2 atm, the performance of the single cell with optimized S-ZrO₂ was far more than that of the Nafion at the same condition (e.g. 1.28 W/cm² at 80 °C, 0.75 W/cm² at 120 °C). The 15 wt.% S-ZrO₂/Nafion composite membrane showed lower fuel cell internal resistance than Nafion membranes at high temperature and low relative humidity (RH).     

质子交换膜燃料电池的水平衡

水平衡是制约质子交换膜燃料电池（PEMFC）性能稳定的关键技术之一。本文针对以H2为燃料的PEMFC的水平衡,首先介绍了电池的工作原理及水迁移;通过实验,证明了电池失水、积水对电池性能及寿命的影响,说明了水平衡的重要性;从电池的组成结构及运行参数详细讨论了影响水平衡的主要因素;并对电池水平衡的管理方法作了讨论。     

高性能质子交换膜燃料电池

用全氟碘酸质子交换膜作为质子交换膜燃料电池（ＰＥＭＦＣ）电解质,简化了水和电解质的管理。本文研究了该燃料电池质子交换膜厚度对电池性能影响;性能最佳的Ｎａｆｉｏｎ１１２膜和低铂载量Ｅ－ＴＥＫ电极组装的ＰＥＭＦＣ,在输出功率高达０．９５Ｗ／ｃｍ＾２;同时考察了电池的能量转换效率、Ｅ－ＴＥＫ电极中铂电催化剂利用率和电池的稳定性。     

质子交换膜燃料电池的研究

通过测定电压－电流密度曲线等方法研究质子交换膜燃料电池的电极参数。构造了Ｅｃｅｌｌ＝０．７Ｖ，Ｉ＝０．５５Ａ／ｃｍ＾２并能够稳定运行的燃料电池。改进电池的电极结构，研究了各种操作条件如温度，压力，增湿情况，尾气流量等对电池性能的影响。     

用于二氧化碳电催化还原的电解器研究进展

The electrocatalytic CO₂ reduction reaction (CO₂RR) driven by renewable energy is an efficient approach to achieve the conversion and utilization of CO₂. In this context, CO₂RR has become an emerging research focus in the field of electrocatalysis over the past decade. While a large number of nanostructured catalysts have been developed to accelerate CO₂RR, the tradeoff between activity and selectivity usually renders the overall electrocatalytic performance very poor. Beyond catalyst design, rationally designing electrolyzers is also of substantial importance for improving the CO₂RR performance and achieving its scale-up for practical applications. To a large extent, the electrolyzer configuration determines the local reaction environment near an electrode by affecting the process conditions, thereby resulting in remarkably different electrocatalytic performances. To be techno-economically viable, the performance of CO₂ electrolyzers is expected to be at least comparable to that of the current state-of-the-art proton exchange membrane (PEM) water electrolyzers, with regard to their activity, selectivity, and stability. Researchers have made great progress in the development of CO₂ electrolyzers over the past few years, but they are also facing many issues and challenges. This review aims to provide an in-depth analysis of the research progress and status of current CO₂ electrolyzers including H-cell, flow-cell, and membrane electrode assembly cell (MEA-cell) electrolyzers. Herein, operation at industrial current densities (> 200 mA∙cm⁻²) is set as a basis when these electrolyzers are discussed and compared in terms of the four main figures of merit (current density, Faradic efficiency, energy efficiency and stability) that describe the CO₂RR performance of an electrolyzer. The advantages and drawbacks of each electrolyzer are discussed and highlighted with emphasis on the key achievements reported to date. Compared to conventional H-cell electrolyzers that work well in mechanistic studies, the newly developed electrolyzers using gas diffusion electrodes, both flow-cell and MEA-cell electrolyzers, are able to break the limitation of CO₂ solubility in water and acquire industrial current densities. Although flow-cell electrolyzers have achieved current densities exceeding 1 A∙cm⁻², they suffer from low energy efficiencies because of the significant iR drop and poor stability owing to the use of alkaline electrolytes. These issues can be overcome in the case of zero-gap MEA-cell electrolyzers with ion exchange membranes being as solid electrolytes. The anion exchange membrane (AEM)-based CO₂ electrolyzers are at the center of the current research, as they demonstrate promising activity and selectivity toward specific CO₂RR products and exhibit excellent stability for over thousands of hours in few cases. Meanwhile, the crossover of CO₂ and liquid products from the cathode to the anode through the membrane tends to lower the utilization efficiency of the CO₂ supplied to the AEM electrolyzers. MEA-cell electrolyzers using cation exchange membranes and bipolar membranes have also been explored; however, neither of them have shown satisfactory CO₂RR performance. The development of new polymer electrolyte membranes and ionomers would help address these problems. While issues and challenges still exist, MEA-cell electrolyzers hold the greatest promise for practical applications. As concluding remarks, research strategies and opportunities for the future have been proposed to accelerate the development of CO₂RR technology for practical applications and to deepen the mechanistic understanding behind improved performance. This review provides new insights into rational electrolyzer design and guidelines for researchers in this field.     

Transport and separation of Ag(+) and Zn(2+) by donnan dialysis through a monovalent cation selective membrane

Donnan Dialysis of Ag⁺ and Zn²⁺ was investigated through a cation exchange membrane (CMS Neosepta) when a proton concentration difference was maintained between the two sides of the membrane. Developed for the production of brine from sea water, CMS Neosepta showed a higher permeability to monovalent than to bivalent cations. Several physico-chemical parameters have been determined (electrical resistance, membrane potential, sorption of electrolytes, Zn²⁺ and Ag⁺ diffusion coefficients). The flux of Ag⁺ and the diffusion potential in the membrane increase with HNO₃ concentrations. Ag⁺ and Zn²⁺ can be separated because of the preferential membrane transfer for Ag⁺.     

离子型交联磺化聚酰亚胺质子交换膜的制备及高温燃料电池性能

以2,2′-双(4-磺基苯氧基)联苯二胺、 2-(4-氨基苯基)-5-氨基苯并咪唑和1,4,5,8-萘四甲酸二酐为单体, 通过逐步聚合和溶液成膜法制备了离子型交联磺化聚酰亚胺质子交换膜(SPI PEMs). SPI PEMs具有优异的机械性能和耐水解稳定性, 在高离子交换容量和高湿度下具有和NR212相当的质子传导性能. 电池工作温度为90 ℃时, 高加湿条件下, n(BSPOB)/n(DABI)为5/2的离子型交联SPI PEM(M1)的最大输出功率密度(W_max)为 0.93 W/cm², 高于NR212的0.86 W/cm². 当电池温度提高到110 ℃时, 所有PEMs的电池性能显著下降, M1的W_max为0.54 W/cm², 明显高于共价型交联的SPI PEM. 离子型交联的SPI PEM在110 ℃下300 h的开路电压(OCV)耐久性降低了约10%, 远高于NR212.     

Gas permeation through water-swollen hydrogel membranes

This work deals with water-swollen hydrogel membranes for potential CO₂ separation applications, with an emphasis on elucidating the role of water in the membrane for gas permeation. A series of hydrogel membranes with a wide range of water contents (0.9–10 g water/g polymer) were prepared from poly(vinyl alcohol), chitosan, carboxyl methyl cellulose, alginic acid and poly(vinylamine), and the permeation of CO₂, H₂, He and N₂ through the membranes at different pressures (200–800 kPa) was studied. The gas permeabilities through the dry dense membranes were measured as well to evaluate the resistance of the polymer matrix in the hydrogel membranes. It was shown that the gas permeability in water-swollen membrane is lower than the gas permeability in water, and the selectivity of the water-swollen membranes to a pair of gases is close to the ratios of their permeabilities in water. The permeability of the water-swollen membranes increases with an increase in the swelling degree of the membrane, and the membrane permeability tends to level off when the water content is sufficiently high. A resistance model was proposed to describe gas permeation through the hydrogel membranes, where the immobilized water retained in the polymer matrix was considered to form transport passageways for gas permeation through the membrane. It was shown that the permeability of hydrogel membranes was primarily determined by the water content in the membrane. The model predictions were consistent with the experimental data for various hydrogel membranes with a wide range of water contents (0.4–10 g water/g polymer).