Preparation of highly active Pt/C cathode electrocatalysts for DMFCs by an improved aqueous impregnation method

An improved aqueous impregnation method was used to prepare 40 wt% Pt/C electrocatalysts. TEM analysis of the samples showed that the Pt particles impregnated for a short time have a very narrow size distribution in the range of 1-4 nm with an average size of 2.6 nm. UV-vis spectroscopy measurements verified that the redox reaction between PtCl62- and formaldehyde took place with a slow rate at ambient temperature via a two-step reaction path, where PtCl42- serves as an intermediate. The use of the short-time-impregnated 40 wt% Pt/C as cathode electrocatalysts in direct methanol fuel cells yields better performance than that of commercial 40 wt% Pt/C electrocatalyst. Experimental evidence provides clues for the fundamental understanding of elementary steps of the redox reactions, which helps in guiding the design and preparation of highly dispersed Pt catalyst for fuel cells.

稀土墩子和稀土氧化物对甲醇在Pt催化剂上电催化氧化性能的影响

直接甲醇燃料电池( DMFC )具有甲醇来源丰富，价格低廉，在常温常压下是液体，易于携带储存；体积小，重量轻，结构简单，容易操作；维修方便，价格低等优点，近年来得到普遍的关注。然而，要达到DMFC的商品化还存在一些问题。其中一个是阳极催化剂的电催化活性低和易被甲醇氧化的中间产物，如CO毒化。对于甲醇阳极电催化剂人们进行了大量的研究，比较有效的都是Pt－过渡金属或金属氧化物复合催化剂，如Pt－Ru、 Pt－Sn、Pt佩Rh、Pt－Pd、Pt佩Re、Pt－Ru－Sn－W、Pt－WO。和Pt－TIO。等。本文研究了电解液中的稀土离子和与Pt形成复合催化剂的稀土氧化物对甲醇电催化氧化反应的促进作用，得到了如下的结果：1．电解液中的稀土Ho, Eu, Gd或Dy离子对甲醇在光滑Pt电极或DMFC中使用的Pt/C电极上的电催化氧化反应有促进作用，主要表现在的起始氧化电位负移和氧化电流增加。而电解液中加入其它种类的稀土离子对甲醇在光滑Pt电极或Pt/C电极上的电催化氧化反应有阻碍作用，如起始氧化电位正移，峰电流降低。Fu、H食Dy或Gd离子对一甲醇在Pt上的电催化氧化反应有促进作用的主要原因可能与这些稀土离子与甲醇生成配合物能力有关。2．不同Pt一稀土氧化物／C催化剂对甲醇电催化氧化反应有不同的影响。当稀土氧化物是Eu, Ho, Dy或Gd的氧化物时，甲醇在Pt一稀土氧化物／C催化剂上甲醇电催化氧化反应的极化性能和稳定性要优于在Pt/C催化剂上，而在其它的Pt-稀土氧化物／C催化剂上，甲醇电催化氧化的极化性能和稳定性要差于Pt/C电极。用不同方法制备的Pt一稀土氧化物／C催化剂对甲醇电催化氧化反应的促进作用取决于催化剂的制备方法。如先在活性碳上还原沉积Pt，再沉积上稀土氧化物所得的Pt－稀土氧化物／C催化剂的促进作用要优于先在稀土氧化物上还原沉积Pt，再一起沉积到活性碳上或先再活性碳上沉积稀土氧化物，再还原沉积上Pt的方法。另外，Pt和稀上氧化物的原子比为2：1时，pt－稀土氧化物／c催化剂对甲醇电催化氧化反应的催化活性最佳。稀土氧化物对pt／C催化剂对甲醇氧化反应的电催化性质的影响与稀土离子相似。但用稀土离子的方法比较简便，因此，相比之下，用稀土离子来促进甲醇在Pt上的电催化氧化反应方法较好。3．用Eu, Gd, Dy, Ho的氧化物制得的Pt-稀土氧化物／C复合催化剂对co的电催化氧化反应的催化活性要高于Pt/C催化剂。相对于的情况，在co在Eu, Gd, Dy,Ho的氧化物的Pt／稀土氧化物／C复合催化剂电极上的循环伏安图中，CO的氧化峰峰电位比在Pt/C电极的有不同程度的负移。吸．初步确定了电极和单体电池制备的较好的工艺参数和工作条件。在发明一种薄电极制备方法，确定最佳的电极催化层配方等的基础上，制得的单体电池，在25℃工作时，输出功率密度峰值达到28 mW/cm~2。

Pt-based anode catalysts for direct ethanol fuel cells

In the present work, several carbon supported PtSn and PtSnRu catalysts were prepared with different atomic ratios and tested in direct ethanol fuel cells (DEFC) operated at lower temperature (T=90 degreesC). XRD and TEM results indicate that all of these catalysts consist of uniform nano-sized particles of narrow distribution and the average particle sizes are always less than 3.0 nm. As the content of Sn increases, the Pt lattice parameter becomes longer. Single direct ethanol fuel cell tests were used to evaluate the performance of carbon supported PtSn catalysts for ethanol electro-oxidation. It was found that the addition of Sn can enhance the activity towards ethanol electro-oxidation. It is also found that a single DEFC of Pt/Sn atomic ratioless than or equal to2, "Pt1Sn1/C, Pt3Sn2/C, and Pt2Sn1/C" shows better performance than those with Pt3Sn1/C and Pt4Sn1/C. But even adopting the least active PtSn catalyst, Pt4Sn1/C, the DEFC also exhibits higher performance than that with the commercial Pt1Ru1/C, which is dominatingly used in PEMFC at present as anode catalyst for both methanol electro-oxidation and CO-tolerance. At 90 degreesC, the DEFC exhibits the best performance when Pt2Sn1/C is adopted as anode catalysts. This distinct difference in DEFC performance between the catalysts examined here is attributed to the so-called bifunctional mechanism and to the electronic interaction between Pt and Sn. It is thought that -OHads, Surface Pt active sites and the ohmic effect of PtSn/C catalyst determines the electro-oxidation activity of PtSn catalysts with different Pt/Sn ratios. (C) 2004 Elsevier B.V. All rights reserved.

Pt based anode catalysts for direct ethanol fuel cells

In the present work several Pt-based anode catalysts supported on carbon XC-72R were prepared with a novel method and characterized by means of XRD, TEM and XPS analysis. It was found that all these catalysts are consisted of uniform nanosized particles with sharp distribution and Pt lattice parameter decreases with the addition of Ru or Pd and increases with the addition of Sn or W. Cyclic voltammetry (CV) measurements and single direct ethanol fuel cell (DEFC) tests jointly showed that the presence of Sn, Ru and W enhances the activity of Pt towards ethanol electro-oxidation in the following order: Pt1Sn1/C > Pt1Ru1/C > Pt1W1/C > Pt1Pd1/C > Pt/C. Moreover, Pt1Ru1/C further modified by W and Mo showed improved ethanol electro-oxidation activity, but its DEFC performance was found to be inferior to that measured for Pt1Sn1/C. Under this respect, several PtSn/C catalysts with different Pt/Sn atomic ratio were also identically prepared and characterized and their direct ethanol fuel cell performances were evaluated. It was found that the single direct ethanol fuel cell having Pt1Sn1/C or Pt3Sn2/C or Pt2Sn1/C as anode catalyst showed better performances than those with Pt3Sn1/C or Pt4Sn1/C. It was also found that the latter two cells exhibited higher performances than the single cell using Pt1Ru1/C, which is exclusively used in PEMFC as anode catalyst for both methanol electro-oxidation and CO-tolerance. This distinct difference in DEFC performance between the catalysts examined here would be attributed to the so-called bifunctional mechanism and to the electronic interaction between Pt and additives. It is thought that an amount of -OHads, an amount of surface Pt active sites and the conductivity effect of PtSn/C catalysts would determine the activity of PtSn/C with different Pt/Sn ratios. At lower temperature values or at low current density regions where the electro-oxidation of ethanol is considered not so fast and its chemisorption is not the rate-determining step, the Pt3Sn2/C seems to be more suitable for the direct ethanol fuel cell. At 75 degreesC, the single ethanol fuel cell with Pt3Sn2/C as anode catalyst showed a comparable performance to that with Pt2Sn1/C, but at higher temperature of 90 degreesC, the latter presented much better performance. It is thought from a practical point of view that Pt2Sn1/C, supplying sufficient -OHads and having adequate active Pt sites and acceptable ohmic effect, could be the appropriate anode catalyst for DEFC. (C) 2003 Elsevier B.V. All rights reserved.

Ethanol electrooxidation on Pt/C catalysts promoted with praseodymium oxide nanorods

The Pt/C electrocatalysts containing Pr6O11 nanorods were successfully prepared. By various electrochemical characterization methods, it was demonstrated that the Pr6O11 nanorods have an obviously promotive role for ethanol electrooxidation catalyzed by Pt/C. However, according to the stripping experiment, the promotive effect of Pr6O11 does not result from the easier electrooxidation of the intermediate adsorbate on Pt-Pr6O11/C than on Pt/C. It was supposed that Pr6O11 could promote a certain step in ethanol oxidation, and that the special morphology of the nanorods could further enhance the activity compared with nanoparticles.

Nanoelectrocatalyst based on high-density Au/Pt hybrid nanoparticles supported on a silica nanosphere

A high-efficiency nanoelectrocatalyst based on high-density Au/Pt hybrid nanoparticles supported on a silica nanosphere (Au-Pt/SiO2) has been prepared by a facile wet chemical method. Scanning electron microscopy, transmission electron microscopy, energy-dispersive X-ray spectroscopy, and X-ray photoelectron spectroscopy are employed to characterize the obtained Au-Pt/SiO2. It was found that each hybrid nanosphere is composed of high-density small Au/Pt hybrid nanoparticles with rough surfaces. These small Au/Pt hybrid nanoparticles interconnect and form a porous nanostructure, which provides highly accessible activity sites, as required for high electrocatalytic activity. We suggest that the particular morphology of the AuPt/SiO2 may be the reason for the high catalytic activity. Thus, this hybrid nanomaterial may find a potential application in fuel cells.

吸附在Pt/C催化剂上Eu~(3+)对CO电氧化的促进作用

引言目前影响质子交换膜燃料电池(PEMFC)迅速发展并商业化的主要问题之一是阳极催化剂抗CO的毒化能力。Pt因其对氢的氧化具有高的催化活性而广泛地用作PEMFC的阳极催化剂,也有人研究将其它金属用于PEMFC阳极催化剂,但催化活性要比Pt低得多[1~4]。而Pt作PEMFC的阳极催化剂一个问题是痕量的CO,如10~100ppm就可以使Pt催化剂中毒[5,6]。现在的PEMFC一般用高压氢作为燃料,有很大的不安全性。人们提出用两种方法来解决这个问题,一是用甲醇、甲烷或汽油现场重整制氢作燃料的方法,但用这种制氢方法制得的氢气中含有大量的CO,即使经过纯化,也会含有ppm级的CO。另一个方法是直接用小分子醇类化合物,如甲醇作燃料,被称为直接醇燃料电池(DAFC)[7~11],但醇类化合物在阳极氧化时会有中间产物,如CO的产生,容易使阳极Pt催化剂中毒。因此,研究抗CO中毒的阳极催化剂已成为PEMFC和DAFC中一个很重要的研究课题。许多文章已报道Pt与其它贵金属或过渡金属的合金催化剂,或Pt与过渡金属氧化物的复合催化剂有一定的抗CO中毒能力。如Pt鄄Ru[12~16]、Pt鄄Bi[17]、Pt鄄Sn[17~19]...

碳载Pt-TiO_2阳极催化剂对甲醇氧化的电催化活性和稳定性

近年来,直接甲醇燃料电池（DMFC）由于使用液体燃料而越来越受到重视,但目前DMFC存在的一个普遍的问题是常用的Pt阳极催化剂易被甲醇氧化的中间产物所毒化.因此,一些研究者研究了能抗甲醇氧化的中间产物毒化的Pt二元合金或Pt和过渡金属氧化物复合催化剂,如Pt-Ru[1]、Pt-Sn[2]、Pt-WOx[3]等.考虑至TiO2在酸性溶液中的稳定性,Hamnett研究组[4]和我们研究组[5]发现pt-TiO2/Ti复合电极对甲醇氧化有很好的电催化活性和抗中毒的能力.本文报道了制备能在DMFC中实际使用的碳载Pt-TiO2催化剂（Pt-TiO2/C）的方法和比较了Pt-TiO2/C和Pt/C电极对甲醇氧化的电催化活性和稳定性.用固相法制备含Pt20％的Pt/C催化剂[6],将制得的pt/C催化剂和Ti（OBu）4按摩尔比1:1的比例悬浮在乙醇中,超声波震荡并加水,使Ti（OBu）4完全水解成TiO2,并均匀沉积到Pt/C催化剂上,洗涤,真空干燥,500℃热处理

Development of electrocatalysts for direct alcohol fuel cells

In the present review, we summarize the recent progress in electrocatalysts for direct alcohol fuel cells, focussing on the research of electrocatalysts for both alcohol oxidation and oxygen reduction, which are crucial in the development of fuel cells. A modified EG (ethylene polyol) method to prepare well-dispersed nano-sized Pt-based electrocatalysts with high loadings is reported. By this method, a more active carbon supported PtRu catalyst for methanol oxidation reaction and a PtSn catalyst for ethanol oxidation reaction have been synthesized successfully. Furthermore, a methanol tolerant Pd-based catalyst for cathode oxygen reduction reaction has been developed. HRTEM and HR-EDS have been employed to characterize the microstructure and micro-components of the above electrocatalysts. Results show that the bimetallic electrocatalysts prepared by the modified EG method display uniform size and homogeneous components at nanometer scale.

异丁烷脱氢制备异丁烯催化剂的研究

Pt-Sn/A1_2O_3负载型双金属催化剂由于其独特的催化性能而被广泛应地用于催化重整工业当中。尽管它对于长链烷烃的脱氢取得较为理想的效果，但用于异丁烷等小分子脱氢却不够理想。Pt-Sn/Al_2O_3负载型双金属催化剂用于异丁烷脱氢，其初活性较高，但对异丁烯的选择性较低，且稳定性较差，易失活。本研究工作就是以Pt-Sn/Al_2O_3负载型双金属催化剂为基础，通过添加碱金属、稀土元素来调变其脱氢性能，一方面提高催化剂的稳定性，另一方面提高对异丁烯的选择性。本文所需要的所有催化剂均是应用传统的共浸法制得。我们首先研究了经碱金属调变的催化剂的脱氢性能。我们发现加入碱金属，尽管催化剂的初活性略有降低，但催化剂对异丁烯的选择性却明显升高，其抗积炭性能也有显著提高。在这三种碱金属当中，K的调变效果最好。我们借助于现代化的测试手段(XRD、XPS、TPR、DTA-TG)对催化剂及其积炭样品进行了表征。结果表明，所有金属组分均以高分散状态存在于载体之上，碱金属钾的加入并没有将离子态的锡还原为金属态。由于K~+是很强的电子施主，它能够减缓活性中心铂的缺电子状态(由于载体效应的存在，铂受载体的拉动效应，它往往以不同程度缺电子状态存在)，从而减缓了活性中心与烃类之间的相互作用，有利于抑制积炭的产生。我们应用DTA-TG研究催化剂的积炭样品发现，碱金属能够抑制了烃类的深度脱氢。碱金属还中和了载体表面的酸性中心，这既抑制了异构化等副反应的发生，提高了对异丁烯的选择性，又抑制了积炭反应的发生。稀土元素对Pt-Sn - K/Al_2O_3催化剂的影响比较复杂。在种稀土元素当中(La、Ce、Pr、Nd、Sm、Eu)，Sm、Ce的调变效果较好，而Eu的调变效果最差。钐的载量不宜太多，以0.30%为宜，太多，一方面有可能将离子态的锡还原成金属态而使催化剂失活，另一方面可能会导致载体晶型有所改变而影响金属组分与载体间的相互作用。TPR结果表明，稀土元素对催化剂的强弱吸附中心的影响是不同的。弱中心上，它作为受电子体，使得铂的缺电子状态加剧，削弱了活性中心与载体之间的相互作用；在强吸附中心上，稀土元素是给电子体，减缓了活性中心铂的缺电子状态，增强了其与载体的相互作用，这两方面共同作用的结果，增强了催化剂的抗积炭能力，提高了催化剂的稳定性。由于铟与锡属于同一周期，且在周期表中处于相临的位置，因此我们考察了铟的不同载量对Pt-In/A1_2O_3催化剂脱氢性能的影响。铟载量跟锡载量相同的情况下，Pt-Sn/Al_2O_3催化剂的活性要比Pt-Sn/Al_2O_3催化剂的活性高，但其对异丁烯的选择性和抗积炭能力却要比Pt-Sn/Al_2O_3催化剂差。另外，随着铟载量的逐渐增加，催化剂的活性逐渐下降，对异丁烯的选择性逐渐升高，异构化逐渐降低。这说明铟在催化剂中起了两方面的作用。首先，它能中和载体表面的酸性中心，再者，对铂活性中心起着一种电子效应。另外我们还考察了碱金属钾对Pt-In/Al_2O_3催化剂的调变作用

三氧杂环己烷的电化学特性

直接氧化一些有机小分子(如甲醇[1~9]和乙醇[10~14]等)的直接氧化燃料电池作为一种对环境友好的能源越来越引起人们的关注.三氧杂环己烷作为一种可再生的能源,可以从地球上存在的大量天然气中得到,来源广泛,价格低廉.三氧杂环己烷反应的基本结构如Scheme 1所示,相对乙醇而言,三氧杂环己烷不存在任何碳碳键,反应更易进行.目前广泛研究的直接氧化燃料电池均采用液体甲醇和S chem e 1 S tru ctu re of tr ioxane乙醇等作燃料,液体燃料的存储运输存在一定的安全隐患,一旦泄漏发生危险,后果非常严重,而三氧杂环己烷作为一种固体,可以有效地避免上述问题的发生,利于安全的储存和运输.Narayanan等[13]研究了三氧杂环己烷在Pt,Pt-Sn和Pt-Ru电极上的电化学行为及其在燃料电池中的应用.本文研究了三氧杂环己烷在不同浓度、不同温度和不同酸度时于光滑铂电极上的电化学行为,初步分析了三氧杂环己烷的反应机理.1实验部分1.1试剂与仪器采用Potentiostat/GalvanostatModel 273A恒电位仪(美国Princeton Applied Research公司),在传统的三...

Surface structure and reaction performances of highly dispersed and supported bimetallic catalysts

Surface structures of Pt-Sn and Pt-Fe bimetallic catalysts have been investigated by means of Mossbauer spectroscopy, Pt-L-III -edge EXAFS and H-2-adsorption. The results showed that the second component, such as Sn or Fe, remained in the oxidative state and dispersed on the gamma-Al2O3 surface after reduction, while Pt was completely reduced to the metallic state and dispersed on either the metal oxide surface or the gamma-Al2O3 surface. By correlating the distribution of Pt species on different surfaces with the reaction and adsorption performances, it is proposed that two kinds of active Pt species existed on the surfaces of both catalysts, named M-1 sites and M-2 sites. M-1 sites are the sites in which Pr directly anchored on the gamma-Al2O3 surface, while M-2 sites are those in which Pt anchored on the metal oxide surface. M-1 sites are favorable for low temperature H-2 adsorption, and responsible for the hydrogenolysis reaction and carbon deposition, while M-2 sites which adsorb more H-2 at higher temperature, are more resistant to the deactivation due to less carbon deposition, and provide major contribution to the dehydrogenation reaction.

Sn-modified Pt/SAPO-11 catalysts for selective hydroisomerization of n-paraffins

The hydroconversion of n-paraffins is a key reaction in hydrodewaxing of lubricating base oil. In this paper, we investigate the performance of Pt/SAPO-11 catalysts for isomerization of n-paraffins by the model compound of n-dodecane. Under this experimental condition, yields of feed isomers as well as cracking products are a function of the total n-dodecane conversion. Primary products are methylundecane while multi-brancheds and cracking products are formed in successive reactions. The result shows that the addition of Sn increases the selectivity for isomerization reaction. The most ideal experimental data for hydroconversion of n-dodecane is that the selectivity of isomerized products gets 90% when conversion of n-dodecane is 90% for the Sn-promoted Pt/SAPO-11 catalyst.