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Solid electrolytes as active catalyst supports: Electrochemical modification of catalytic activity and selectivity.

机译:固体电解质作为活性催化剂的载体:催化活性和选择性的电化学修饰。

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With a conventional promoter it is possible to tune the degree of promotion by adjusting its concentration or changing it chemically. For scientific investigations of promoter/poison effects, as well as for industrial operations that depend on them, it would be highly effective and efficient if one could have a continually variable promoter which could be dosed or removed just by "turning a knob". The long sought goal of controlled promotion of catalyst surfaces appears now to be possible using non-Faradaic electrochemical modification of catalytic activity (NEMCA).; Two different systems were studied during the course of this research: methanol oxidation on Pt/YSZ cells and benzene hydrogenation on {dollar}rm Pt/betasp{lcub}primeprime{rcub}(Na)Alsb2Osb3.{dollar} The systems, in terms of NEMCA, exemplified the two extremes of behavior in electrochemical promotion: while one system could be understood in terms of promotional effects and rate enhancements due to {dollar}rm Osp{lcub}2-{rcub}{dollar} pumping to the catalyst; the other, benzene hydrogenation, exemplified a case of strong electrocatalytically-induced poisoning due to sodium doping on the catalyst surface. Both behaviors, although opposite, represented a clear example of the fact that NEMCA is not restricted to a specific reaction or to a specific electrolyte and provided some more general understanding for this phenomena. Additionally, in each system, a spectroscopic probe was used to identify and, in some cases, quantify the NEMCA-induced spillover species.; It was found that the catalytic activity and selectivity of Pt for the oxidation of methanol to formaldehyde and {dollar}rm COsb2{dollar} can be altered significantly and reversibly by depositing a Pt catalyst film on an yttria-stabilized-zirconia (YSZ) disc and by applying current or potential between the catalyst film and a Ag film deposited on the other side of the {dollar}rm Osp{lcub}2-{rcub}{dollar}-conducting YSZ disc. Both the catalyst film and the Ag counter and reference electrodes are exposed to the reacting {dollar}rm CHsb3OH{dollar}-{dollar}rm Osb2{dollar} mixture. The observed increase in the rate of {dollar}rm Hsb2CO{dollar} production was typically a factor of 100 higher than the rate of {dollar}rm Osp{lcub}2-{rcub}{dollar} supply to the catalyst with a concomitant two-fold increase in selectivity.; The catalytic hydrogenation of benzene to cyclohexane was studied in a Pt-single-pellet electrocatalytic reactor configuration. By interfacing the catalyst with {dollar}betasp{lcub}primeprime{rcub}{dollar}-{dollar}rm (Na)Alsb2Osb3,{dollar} a {dollar}rm Nasp+{dollar} conductor, and by supplying or removing sodium ions to or from the catalyst surface by applying potential to the cell, the catalytic activity of Pt can be strongly and reversibly modified.; It was found that by setting the catalyst potential more positive than its open-circuit emf (i.e., potentiostatic stripping of sodium from the Pt surface) caused a beneficial effect in activity, increasing the rate to two times the open-circuit value. Application of more negative potentials (i.e., potentiostatically-controlled sodium dosage onto the Pt surface) caused a negative effect on the rate, reducing it to almost zero for coverages of sodium of around 0.02, as calculated by integration of the potentiostatically induced ionic-current. The results suggested an electrophobic behavior for this reaction, with sodium acting as a poison for this system, and with the chemisorptive properties of Pt altered ("knob-tuned") by application of an external bias. The average poison-index experimentally calculated for this system was {dollar}-{dollar}130, thus suggesting poison effects of an electronic nature. This new result is the first one, at least with {dollar}betasp{lcub}primeprime{rcub}{dollar}-{dollar}rm (Na)Alsb2Osb3,{dollar} showing the feasibility of NEMCA in hydrogenation reactions. (Abstract shortened by UMI.)
机译:使用常规的启动子,可以通过调节其浓度或化学​​改变其浓度来调节其促进程度。对于科学研究人员对启动子/毒物的影响,以及对依赖它们的工业操作的研究,如果人们能够拥有一个连续可变的启动子,而只需通过“转动旋钮”就可以对其进行剂量分配或去除,那将是非常有效的。使用非法拉第电化学改性的催化活性(NEMCA),现在看来,长期追求的控制催化剂表面促进的目标是可能的。在研究过程中,研究了两种不同的系统:Pt / YSZ细胞的甲醇氧化和{rm} Pt / betasp {lcub} primeprime {rcub}(Na)Alsb2Osb3 {dollar}的苯加氢。 NEMCA的研究举例说明了电化学促进行为的两个极端情况:一方面,由于将{dol} rm Osp {lcub} 2- {rcub} {dollar}泵送到催化剂,在促进效果和速率提高方面可以理解一个系统;另一种是苯加氢,举例说明了由于钠掺杂在催化剂表面而引起的强电催化中毒的情况。两种行为虽然相反,但却清楚地表明了NEMCA不仅限于特定的反应或特定的电解质,而且为这种现象提供了更一般的理解。另外,在每个系统中,使用光谱探针来识别和量化NEMCA诱导的溢出物种。已经发现,通过将Pt催化剂膜沉积在氧化钇稳定的氧化锆(YSZ)盘上,可以显着且可逆地改变Pt对甲醇氧化为甲醛和{rm} COsb2 {dollar}的催化活性和选择性。并且通过在催化剂膜和沉积在传导导电的Ysz圆盘的另一面的Ag膜之间施加电流或电势。催化剂膜以及Ag对电极和参比电极均暴露于反应的{rms CHsb3OH {dollar}-{rmal} Osb2 {dollar}混合物中。观察到的{shr} rm Hsb2CO {dollar}生成速率的增加通常比向催化剂供应的{rmsrm Osp {lcub} 2- {rcub} {dollar}的生成速率高100倍。选择性增加两倍。在Pt单颗粒电催化反应器配置中研究了苯催化加氢成环己烷的过程。通过将催化剂与{dolph} betasp {lcub} primeprime {rcub} {dollar}-{dollar} rm(Na)Alsb2Osb3与{dollar} rm Nasp + {dollar}导体连接,并通过提供或除去钠离子通过向电池施加电势到催化剂表面或从催化剂表面起,Pt的催化活性可以被强烈和可逆地改变。发现通过将催化剂电势设置成比其开路电动势更正(即,从Pt表面的钠的恒电位汽提)对活性产生有益作用,将速率增加到开路值的两倍。施加更多的负电势(即,将恒电位控制的钠剂量施加到Pt表面)会对速率产生负面影响,对于约0.02的钠离子覆盖率,将其降低至几乎为零,这是通过将恒电位诱导的离子电流积分而得出的。结果表明该反应具有疏水性,其中钠用作该系统的毒物,并且通过施加外部偏压改变了Pt的化学吸附性能(“旋钮调谐”)。通过实验计算出的该系统的平均毒物指数为{dolal}-{dollar} 130,因此表明具有电子性质的毒物效应。该新结果是第一个结果,至少与{dolph} betasp {lcub} primeprime {rcub} {dollar}-{dollar} rm(Na)Alsb2Osb3,{dollar}相似,这表明NEMCA在加氢反应中的可行性。 (摘要由UMI缩短。)

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