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负载于结构化和非结构化碳上的钯:钯颗粒尺寸及活性氢性质的考量

Palladium supported on structured and nonstructured carbon: a consideration of Pd particle size and the nature of reactive hydrogen.

作者信息

Amorim Claudia, Keane Mark A

机构信息

Department of Chemical and Materials Engineering, University of Kentucky, Lexington, USA.

出版信息

J Colloid Interface Sci. 2008 Jun 1;322(1):196-208. doi: 10.1016/j.jcis.2008.02.021. Epub 2008 Feb 19.

Abstract

This study sets out a comprehensive characterization of bulk Pd and Pd (ca. 8% w/w) supported on activated carbon (AC), graphite and graphitic nanofibers (GNF). Catalyst activation has been examined by temperature programmed reduction (TPR) analysis and the activated catalysts analyzed in terms of BET area, TEM, H2 chemisorption/TPD, and XRD measurements. While H2 chemisorption and TEM delivered the same sequence of increasing (surface area weighted) average Pd particle sizes, a significant difference (by up to a factor of 3) in the values obtained from both techniques has been recorded and is attributed to an unwarranted (but widely adopted) assumption of an exclusive H2/Pd adsorption stoichiometry=1/2. It is demonstrated that TEM analysis provides a valid mean particle size once it is established that the associated standard deviation is small and insensitive to additional particle counting. XRD line broadening yielded an essentially equivalent Pd size (20-25 nm) for each supported catalyst. The nature of the hydrogen associated with the supported catalysts has been probed and is shown to comprise of chemisorbed (on Pd), spillover (on the carbon support), and hydride (associated with Pd) species. Physical mixtures of bulk Pd + support (AC, graphite, and GNF) were also considered in order to assess hydrogen spillover by H2 TPD analysis. Generation of spillover hydrogen at room temperature is established where temperatures in excess of 740 K are required for effective desorption from the supported Pd catalysts, i.e., 280 K higher than that required for the desorption of chemisorbed hydrogen. Pd hydride formation (at room temperature) is shown to be reversible with decomposition occurring at ca. 380 K. Taking the hydrodechlorination of chlorobenzene as a test reaction, the capability of Pd hydride to promote a hydrogen scission of C-Cl in the absence of an external supply of H2 is demonstrated with a consequent consumption of the hydride. This catalytic response was entirely recoverable once the Pd hydride was replenished during a subsequent reactivation step.

摘要

本研究全面表征了负载在活性炭(AC)、石墨和石墨纳米纤维(GNF)上的块状钯及钯(约8% w/w)。通过程序升温还原(TPR)分析研究了催化剂的活化过程,并对活化后的催化剂进行了比表面积(BET)、透射电子显微镜(TEM)、氢气化学吸附/程序升温脱附(H₂化学吸附/TPD)和X射线衍射(XRD)测量分析。虽然氢气化学吸附和TEM得出了相同的(按表面积加权的)平均钯粒径增加顺序,但两种技术所得值存在显著差异(相差高达3倍),这归因于对氢气/钯吸附化学计量比仅为1/2这一不合理(但被广泛采用)的假设。结果表明,一旦确定相关标准偏差较小且对额外的颗粒计数不敏感,TEM分析就能提供有效的平均粒径。XRD线宽化得出每种负载型催化剂的钯粒径基本相当(20 - 25 nm)。对负载型催化剂相关的氢的性质进行了探究,结果表明其包含化学吸附(在钯上)、溢流(在碳载体上)和氢化物(与钯相关)物种。还考虑了块状钯与载体(AC、石墨和GNF)的物理混合物,以便通过H₂ TPD分析评估氢溢流。已确定在室温下会产生溢流氢,而从负载型钯催化剂上有效脱附则需要超过740 K的温度,即比化学吸附氢脱附所需温度高280 K。已表明氢化钯的形成(在室温下)是可逆的,在约380 K时会发生分解。以氯苯的加氢脱氯作为测试反应,证明了在没有外部氢气供应的情况下,氢化钯能够促进碳 - 氯键的氢裂解,从而消耗氢化物。一旦在后续的再活化步骤中补充氢化钯,这种催化响应就完全可以恢复。

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