Composite anode for CO tolerance proton exchange membrane fuel cells

Fuel of proton exchange membrane fuel cells (PEMFC) mostly comes from reformate containing CO. which will poison the fuel cell electrocatalyst. The effect of CO on the performance of PEMFC is studied in this paper. Several electrode structures are investigated for CO containing fuel. The experimental results show that thin-film catalyst electrode has higher specific catalyst activity and traditional electrode structure can stand for CO poisoning to some extent. A composite electrode structure is proposed for improving CO tolerance of PEMFCs. With the same catalyst loading. the new composite electrode has improved cell performance than traditional electrode with PtRu/C electrocatalyst for both pure hydrogen and CO/H-2. The EDX test of composite anode is also performed in this paper, the effective catalyst distribution is found in the composite anode. (C) 2002 Elsevier Science B.V. All rights reserved.

Preparation and characterization of multi-walled carbon nanotubes supported PtRu catalysts for proton exchange membrane fuel cells

A series of PtRu nanocomposites supported on H2O2-oxidized multi-walled carbon nanotubes (MWCNTs) were synthesized via two chemical reduction methods - one used aqueous formaldehyde (HCHO method) and the other used ethylene glycol (EG method) as the reducing agents. The effects of the solvents (water and ethylene glycol) and the surface composition of the MWCNTs on the deposition and the dispersion of the metal particles were investigated using N-2 adsorption. TEM. ICP-AES. FTIR and TPD. The wetting heats of the MWCNTs in corresponding solvents were also measured. The characterizations suggest that combination of the surface chemistry of the MWCNTs with the solvents decides the deposition and the dispersion of the metal nanoparticles. These nanocomposites were evaluated as proton exchange membrane fuel cell anode catalyts for oxidation of 50 ppm CO contaminated hydrogen and compared with a commercial PtRu/C catalyst. The data reveal superior performances for the nanocomposites prepared by the EG method to those by the HCHO method and even to that for tile Commercial analogue. Structure performance relationship of the nanocomposites was also studied. (C) 2005 Elsevier Ltd. All rights reserved.

Preparation of supported PtRu/C electrocatalyst for direct methanol fuel cells

In this work, high-surface supported PtRu/C were prepared with Ru(NO)(NO3)(3) and [Pt(H2NCH2CH2NH2)(2)]Cl-2 as the precursors and hydrogen as a reducing agent. XRD and TEM analyses showed that the PtRu/C catalysts with different loadings possessed small and homogeneous metal particles. Even at high metal loading (40 wt.% Pt, 20 wt.% Ru) the mean metal particle size is less than 4 nm. Meanwhile, the calculated Pt crystalline lattice parameter and Pt (220) peak position indicated that the geometric structure of Pt was modified by Ru atoms. Among the prepared catalysts, the lattice parameter of 40-20 wt.% PtRu/C contract most. Cyclic voltammetry (CV), chronoamperometry (CA), CO stripping and single direct methanol fuel cell tests jointly suggested that the 40-20 wt.% PtRu/C catalyst has the highest electrochemical activity for methanol oxidation. (c) 2004 Elsevier Ltd. All rights reserved.

Structure and chemical composition of supported Pt-Sn electrocatalysts for ethanol oxidation

Carbon supported PtSn alloy and PtSnOx particles with nominal Pt:Sn ratios of 3:1 were prepared by a modified polyol method. High resolution transmission electron microscopy (HRTEM) and X-ray microchemical analysis were used to characterize the composition, size, distribution, and morphology of PtSn particles. The particles are predominantly single nanocrystals with diameters in the order of 2.0-3.0 nm. According to the XRD results, the lattice constant of Pt in the PtSn alloy is dilated due to Sn atoms penetrating into the Pt crystalline lattice. While for PtSnOx nanoparticles, the lattice constant of Pt only changed a little. HRTEM micrograph of PtSnOx clearly shows that the change of the spacing of Pt (111) plane is neglectable, meanwhile, SnO2 nanoparticles, characterized with the nominal 0.264 nm spacing of SnO2 (10 1) plane, were found in the vicinity of Pt particles. In contrast, the HRTEM micrograph of PtSn alloy shows that the spacing of Pt (111) plane extends to 0.234 nm from the original 0.226 nm. High resolution energy dispersive X-ray spectroscopy (HR-EDS) analyses show that all investigated particles in the two PtSn catalysts represent uniform Pt/Sn compositions very close to the nominal one. Cyclic voltammograms (CV) in sulfuric acid show that the hydrogen ad/desorption was inhibited on the surface of PtSn alloy compared to that on the surface of the PtSnOx catalyst. PtSnOx catalyst showed higher catalytic activity for ethanol electro-oxidation than PtSn alloy from the results of chronoamperometry (CA) analysis and the performance of direct ethanol fuel cells (DEFCs). It is deduced that the unchanged lattice parameter of Pt in the PtSnOx catalyst is favorable to ethanol adsorption and meanwhile, tin oxide in the vicinity of Pt nanoparticles could offer oxygen species conveniently to remove the CO-like species of ethanolic residues to free Pt active sites. (C) 2005 Elsevier Ltd. All rights reserved.

Enhanced Proton Conduction in Polymer Electrolyte Membranes as Synthesized by Polymerization of Protic Ionic Liquid-Based Microemulsions

Proton-conducting membranes were prepared by polymerization of microemulsions consisting of surfactant-stabilized protic ionic liquid (PIL) nanodomains dispersed in a polymerizable oil, a mixture of styrene and acrylonitrile. The obtained PIL-based polymer composite membranes are transparent and flexible even though the resulting vinyl polymers are immiscible with PIL cores. This type of composite membranes have quite a good thermal stability, chemical stability, tunability, and good mechanical properties. Under nonhumidifying conditions, PIL-based membranes show a conductivity up to the order of 1 x 10(-1) S/cm at 160 degrees C, due to the well-connected PIL nanochannels preserved in the membrane. This type of polymer conducting membranes have potential application in high-temperature polymer electrolyte membrane fuel cells.

The role of CeO2-ZrO2 as support in the ZnO-ZnCr2O4 catalysts for autothermal reforming of methanol

Autothermal reforming of methanol for hydrogen production was investigated over ZnO-ZnCr2O4 supported on a series of metal oxides (Al2O3, CeO2, ZrO2 and CeO2-ZrO2)CeO2-ZrO2 mixed oxides with Ce /Zr molar ratio of 4/1 was found to be the optimal support which showed significant effect on the catalytic activity and selectivity. The ZnO-ZnCr2O4/CeO2-ZrO2 and ZnO-ZnCr2O4 catalysts were characterized by XRD, TEM, H-2-TPR and XPS. The results show that CeO2-ZrO2 mixed oxides have significant effect on the catalytic performance and the supported catalyst shows more uniform temperature distribution in the catalyst bed which was mainly due to its reasonable redox properties.

直接甲醇燃料电池阳极催化剂及甲醇氧化稀土助催化剂剂研究

燃料电池以其高效、环境友好的发电方式，被誉为21世纪的能源技术。其中，直接甲醇燃料电池（DMFC）更以燃料甲醇来源丰富，价格低廉，储存、携带方便而成为近年的研究热点。但是，DMFC在其实用化之前还需要解决一些重要问题，其中的关键之一就是高性能的贵金属催化剂的研究。我们知道，甲醇的电化学活性要低于氢气三个数量级；而且甲醇在R表面进行电化学氧化时，其中间解离吸附产物会造成贵金属催化剂中毒，显著降低了催化剂的活性。因此，要使DMFC具有相当高的电流密度和运行稳定性，就需要对贵金属催化剂制备进行不断的研究和改进。在本文的工作中，主要从Pt/C催化剂的制备方法、新型碳纳米管载体、稀土助催化剂等三个方面进行了研究和探索，取得的具体结果如下：1．Pt／C催化剂制备方法的研究与改进（1）在本组已有的研究结果基础上，对预沉积还原法进行了一些改进，采用原子吸收光谱（AAS）进行表征，发现Pt的利用率得到了明显的提高。采用X射线衍射。（RD）、透射电子显微镜（TEM）和BET表征铂的粒径、晶态结构和催化剂特性，分析表明，经过改进的预沉积还原法制备的催化剂仍然具有良好的分散性、较小的粒径、较低的晶态结构和良好的催化剂特性，电化学测试证明其性能要优于同等的E-TEK催化剂。（2）借鉴冶金学中的相关技术，提出了一种新的Pt/C催化剂制备方法一程序升温焙烧法。该方法的具体步骤增强了金属催化剂粒子和碳载体之间的相互作用力，提高了碳载体的导电性，并且形成了部分有利于催化反应进行的活性晶态结构。得到的R／C催化剂获得了近似E-TEK催化剂的催化活性，在具体方法上仍有改进的潜力。采用了同（1）的催化剂表征方法。2．甲醇电化学氧化稀土助催化剂研究在直接甲醇燃料电池Pt/C催化剂的研究过程中，一个重要的方面就是助催化剂的研究，并且已经得到了较好的结果。本工作选用了稀土元素为研究对象，因为稀土元素属于过渡金属，具有丰富的d电子轨道，易于和金属形成强的类化学键的吸附作用，并且能够和有机小分子形成多种配位化合物。经过初步的工作，发现了有些稀土离子如Sm3+能够在Pt表面吸附并且对甲醇电化学氧化具有较稳定的促进作用，采用循环伏安法，计时电流，交流阻抗等电化学方法进行了表征。根据实验结果，对其反应机理进行了初步的探讨。3．碳纳米管（CNTs）作为贵金属催化剂载体的研究碳纳米管（CNTs）由于其结构上的特殊性（径向尺寸为纳米量级，轴向尺寸为微米量级）而表现出典型的一维量子材料，同时具有较高的机械强度和超常的电学性能，能够为化学反应提供纳米级的反应场所，因此受到了化学界包括电化学研究人员的极大关注。已经在作为贵金属催化剂载体方面进行了一些研究，本工作的主要内容就是针对Pt/CNTs催化剂对碳纳米管的要求，对其预处理方法进行了改进，采用了如（1）中的催化剂表征方法和（2）中的相关电化学方法进行测定，发现碳纳米管作为贵金属催化剂载体时，对它的纯化处理方法的不同明显地影响了其载体性质和催化剂的活性。

直接甲醇燃料电池甲醇替代燃料的研究

论文主要研究了直接甲醇燃料电池（DMFC）中三种甲醇替代燃料，二甲氧基甲烷（DMM）、乙醇和乙二醇及导致阳极催化剂中毒的吸附CO（COad）在光滑R电极及几种新的R基催化剂电极上的电氧化行为。结合对催化剂的X射线光电子能谱（xPS）、X衍射(XRD)、扫描电子显微镜（SEM）和热重分析（TG）表征，初步探讨了几种新催化剂对三种甲醇替代燃料的电催化活性要高于碳载R（PtC）催化剂的原因。另外，还研究了用表面活化处理来提高阳极催化剂对甲醇氧化的电催化活性的方法。本论文得到的主要结果如下：1．在研究DMM在不同条件下，在不同R基催化剂电极上的电化学氧化行为的基础上，发现碳载R和TiO2（Pt-TiO2／C）复合催化剂对DMM氧化的电催化活性要优于Pt/C电极。而Pt-TiO2／C催化剂在吸附Ho3+(Pt-TiO2-Ho3+/C)或Eu3＋（Pt-TiO2-Eu3＋/C）后，对DMM氧化的电催化活性比Pt-TiO2／C电极高。表明TiO2、Eu3+和Ho3+对DMM的氧化都有很好的促进作用，这主要是它们都能为DMM的氧化在电极表面提供更多的含氧物种。由于DMM本身在这些催化剂电极上的氧化性能不好，而且DMM容易在酸性溶液中水解，生成甲醇和甲醛，因此，DMM不是一种好的甲醇替代燃料。2．无论在中性介质中还是在酸性介质中，Eu3＋和Ho3＋对乙醇在R／C电极上的电化学氧化反应都有较好的促进作用，而Eu3＋的促进作用要大于H3+，Eu3＋和H3+在酸性溶液中的促进作用要大于在中性溶液中。无论是中性溶液还是酸性溶液中，吸附CO（COad）在Pt／C催化剂电极上在较正的电位处有一个很大的氧化峰，而在R-Eu3＋／C或R-H3＋／C催化剂电极上在较负电位处有两个小的氧化峰，表明吸附的Eu3＋和Ho3+对cood在R／C催化剂电极上的氧化都有很好的促进作用，主要表现在使Cood的吸附强度降低和吸附量减少。XPs测量表明，当R／C电极表面吸附了Eu3＋或H了十后，使催化剂中Pt和c土的电子云密度变小，因此使Pt对coad的吸附强度减弱。由于Eu3＋或H03＋在电极上吸附不是物理吸附，而是化学吸附，因此，它们与Pt的结合具有相对的稳定性。乙醇电氧化的中间产物，如COad等能强烈地吸附在R上，因此会使R中毒。而Eu3＋或H矿"能降低Coad在R上地吸附强度，因此，Eu3＋或H3+能促进乙醇在Pt／C电极上的电化学氧化反应。Pt-TiO2／C催化剂对乙醇氧化的电催化活性要高于R／C催化剂，表明TiO2对乙醇在R／C电极上的电化学氧化反应也有较好的促进作用。XPS的测量表明，TiO2的加入并不改变Pt的电子状态，因此，TiO2能促进乙醇电氧化反应的主要原因是TIOZ能为乙醇氧化提供含氧物种。实验结果表明，Eu3＋或H3+对乙醇在R-TiO2／C电极上的电化学氧化反应也有一定的促进作用。这是由于Eu3＋或H3+改变了R的电子状态，降低了乙醇电氧化中间产物，COod在Pt上的吸附强度，而TIOZ提供了COod的氧化所必须的含氧物种。3．无论是酸性溶液中还是中性溶液中，乙二醇在R-TiO2／C电极上的氧化活性比在R／C电极上高。这表明TIOZ能促进乙二醇在Pt上的电氧化反应。进一步的实验表明，TIOZ对COad在Pt催化剂电极上氧化的促进作用并不明显。XPS测量表明，这是由于TIOZ并不改变R的电子状态。所以，TiO2对乙二醇在Pt上的电氧化的促进作用只是基于提供乙二醇电氧化所需的含氧物种。无论是酸性溶液中还是中性溶液中，乙二醇在R-WO3／C电极上的氧化活性都比在R／C电极上高。这表明W03能促进乙二醇在R上的电氧化反应。进一步的实验表明，R-WO3／C电极对Coad氧化的电催化活性也要高于R／C电极，XPS测量表明，WO3会降低Pt的电子云密度。所以，WO3对乙二醇在R上的电氧化的促进作用除了提供含氧物种外，还由于它能降低R的电子云密度而降低了乙二醇电氧化中间产物。4．用四氢吠喃和丙酮混合溶液浸泡法对电极进行表面处理后能使Pt／C和Pt-WO3／C电极对乙醇和乙二醇氧化的电催化活性有很大的提高。其原因可能是Pt／C和Pt一w03／C电极在经表面处理后，在电极制备过程中带来的表面活性剂等杂质由于溶解在混合溶液中而被除去，Nafion也可能在用混合溶液浸泡后会发生一定程度的结构变化，因此，使活性中心的位点增加，从而增加了催化剂的电催化活性。另外，经表面处理后，Pt／C和Pt-WO3／C电极的活性中心的结构有一定的变化，使COad的吸附强度降低而容易氧化，降低了COad对催化剂的毒化作用，因而提高了电极对乙醇和乙二醇氧化的电催化活性。

无介体双室微生物燃料电池产电性能初步研究

本文对无介体双室微生物燃料电池的产电性能进行了初步研究，并根据不同运行阶段产电性能的优劣，对其中微生物的差异性进行了比较分析。全文分为两个部分： 第一部分：以乙酸钠为阳极原料构建双室微生物燃料电池（MFC），研究不同阴极受体、外接电阻、乙酸钠浓度和pH等因素对电池产电性能的影响，研究结果表明：在500mL的阴阳极反应体系中，选用乙酸钠作为阳极底物，质量浓度为6.46 g/L， pH 7.0，接入500Ω外电阻，阴极电子受体选择高锰酸钾的情况下，微生物燃料电池产电性能最好，最大电功率密度达到294.72 mW/m2，库伦效率能达到25.87%。在确定最适外接电阻阻值的同时对MFC内阻进行测定，阻值为871.87Ω。 第二部分：微生物燃料电池运行中，比较以厌氧污泥作为接种源的第一阶段和只接入附着有大量微生物电极的第二阶段的产电性能，得出第二阶段产电性能优于第一阶段，最大电功率密度达到353.57mW/m2，比第一阶段提高58.85 mW/m2；库伦效率为39.35%，增幅达52％左右；针对微生物燃料电池运行过程中，底物CH3COONa可能存在其它的代谢途径，本实验进行了第二阶段产电性能与CH3COONa消耗率关系以及阳极液面上方气体成分和含量的研究，发现第二阶段50h前CH3COONa的大量消耗主要用于微生物的生长，在整个运行过程中，阳极液面上方含有CH4和CO2；对气体测定的同时还发现，振荡能增强电功率密度的输出；通过对电极上和污泥中微生物差异性分析得出，δ-变形菌纲、β-变形菌纲和拟杆菌门的菌种更适应微生物燃料电池的运行环境，能在电极上大量富集，提高电池的产电性能，只接入附着有大量微生物的电极能有效降低热袍菌纲的菌种数量，降低了CH3COONa的无为消耗，有效提高了电池的库伦效率。 Electricity production in the mediator-less two-chambered microbial fuel cell(MFC) was researched. Based on the result in the different operation phase in the MFC, the microbial diversity was analysed. The paper involved two parts: Part 1: A two-chambered microbial fuel cell (MFC) was constructed with high-concentration sodium acetate as fuel in the anode. The influence of different electron acceptors in the cathode, external resistance value, pH value and concentration of sodium acetate on electricity generation in MFC was investigated. The result showed that the maximum power density of 294.72 mW/m2 and the coulombic efficiency of 25.87% was achieved at sodium acetate concentration of 6.46 g/L, pH 7.0, external resistance 500Ωin the anode and when using potassium permanganate as electron acceptor in the cathode. While decided the value of resistor, we found that shaking has effect on electricity production in the MFC. Part 2: Comparing the electricity production in different operation phases when using anaerobic sludge as inoculum in the first phase and microbes in the anodic electrode as inoculum in the second phase, the result showed that electricity production in the second phase was more than that in the first phase, the maximum power density of 353.57 mW/m2 and the coulombic efficiency of 39.35% was achieved, 58.85 mW/m2 and 52％ more than that in the first phase, respectively. According to the fact that CH3COONa might be metabolized in other pathway in the running process in the MFC, we determining the relationship between electricity production and CH3COONa consumption, and the gas content in the anode, we found that CH3COONa was mainly used for microbe growth before 50h, and the anode contained CH4 and CO2. At the same time, we found that shaking could improve power density. The analysis on diversity of microbe in the anodic electrode and anaerobic sludge showed that δ-proteobacterium, β-proteobacterium and Bacteroidetes adapted themselves to the running environment of MFC. The anode could enrich them to improve the electricity production while reduced the quantity of Thermotogales, which were obligately anaerobic organotrophs with a fermentative metabolism, to increase the coulombic efficiency effectively.

Effects of treatment in different atmosphere on Pt3Sn/C electrocatalysts for ethanol electro-oxidation

Pt3Sn/C catalyst was prepared by a modified polyol process and treated in air, H-2/Ar, and Ar atmosphere, respectively. XRD analyses indicate that all of these catalysts have face-centered cubic (fcc) crystal structure. Temperature-programmed reduction (TPR) experiments show that more Sn exists in zero-valence in the Ar-treated PtSn catalyst than in the others. Cyclic voltammetry (CV), chronoamperometry (CA) experiments, and the performance tests of direct ethanol fuel cell (DEFC) indicate that the catalytic activity of PtSn/C for ethanol oxidation was affected significantly by the chemical state of Sn in catalyst particles. The as-prepared PtSn/C gives the higher power density, while Ar-treated PtSn/C shows the lower cell performance. It seems that the multivalence Sn rather than the zero-valence Sn in the PtSn catalyst is the favorable form for ethanol oxidation. Energy dispersion X-ray analysis (EDX) of the PtSn/C-as prepared and PtSn/C (after stability test) shows the active species (platinum, tin, and oxygen) composition changed to a different extent. Further attempt to improve the catalyst stability is needed.

Study of sintered stainless steel fiber felt as gas diffusion backing in air-breathing DMFC

Adoption of a sintered stainless steel fiber felt was evaluated as gas diffusion backing in air-breathing direct methanol fuel cell (DMFC). By using a sintered stainless steel fiber felt as an anodic gas diffusion backing, the peak power density of an air-breathing DMFC is 24 mW cm(-2), which is better than that of common carbon paper. A 30-h-life test indicates that the degraded performance of the air-breathing DMFC is primarily due to the water flooding of the cathode. Twelve unit cells with each has 6 cm(2) of active area are connected in series to supply the power to a mobile phone assisted by a constant voltage diode. The maximum power density of 26 mW cm(-2) was achieved in the stack, which is higher than that in single cell. The results show that the sintered stainless steel felt is a promising solution to gas diffusion backing in the air-breathing DMFC, especially in the anodic side because of its high electronical conductivity and hydrophilicity. (C) 2004 Elsevier B.V. All rights reserved.

The mechanism studies of ethanol oxidation on PdO catalysts by TPSR techniques

The paper studies the direct oxidation of ethanol and CO on PdO/Ce0.75Zr0.25O2 and Ce(0.75)Zr(0.2)5O(2) catalysts. Characterization of catalysts is carried out by temperature-programmed desorption (TPD), temperature-programmed surface reaction (TPSR) techniques to correlate with catalytic properties and the effect of supports on PdO. The simple Ce0.75Zr0.25O2 is in less active for ethanol and CO oxidation. After loaded with PdO, the catalytic activity enhances effectively. Combined the ethanol and CO oxidation activity with CO-TPD and ethanol-TPSR profiles, we can find the more intensive of CO2 desorption peaks, the higher it is for the oxidation of CO and ethanol. Conversion versus yield plot shows the acetaldehyde is the primary product, the secondary products are acetic acid, ethyl acetate and ethylene, and the final product is CO2. A simplified reaction scheme (not surface mechanism) is suggested that ethanol is first oxidized to form intermediate of acetaldehyde, then acetic acid, ethyl acetate and ethylene formed going with the formation of acetaldehyde, acetic acid, ethyl acetate; finally these byproducts are further oxidized to produce CO2. PdO/Ce0.75Zr0.25O2 catalyst has much higher catalytic activity not only for the oxidation of ethanol but also for CO oxidation. Thus the CO poison effect on PdO/Ce0.75Zr0.25O2 catalysts can be decreased and they have the feasibility for application in direct alcohol fuel cell (DAFC) with high efficiency.

The experimental research for production of hydrogen from n-octane through partially oxidizing and steam reforming method

The reaction of producing hydrogen for fuel cell which used normal octane as gasoline or diesel oil reactant through catalytic partial oxidizing and steam reforming method has been researched in the fixed-bed reactor. A series of catalysts that mainly used nickel supported on Al2O3 have been studied. It showed that the activity of the catalyst was increased with the content of nickel by using only nickel supported on Al2O3. However, its activity was not obviously increased when the content of nickel was over 5 wt%. The conversion ratio of normal octane and hydrogen selectivity were higher at higher reaction temperature. The single noble catalyst of palladium had better stability compared with that of platinum catalyst although their activity and selectivity were similar during the experimental reaction temperature. The prepared bimetallic catalyst consisted mainly of nickel and little noble metal of palladium supported on Al2O3. It showed that this catalyst had higher activity and selectivity, especially at lower or higher reaction temperatures compared with single nickel or palladium catalyst, and better stability. ((C) 2001 International Association for Hydrogen Energy. Published by Elsevier Science Ltd. All rights reserved.