氢解
化学
催化作用
选择性
介孔二氧化硅
介孔材料
铂金
键裂
铂纳米粒子
纳米颗粒
吸附
多相催化
化学工程
有机化学
工程类
作者
Xun Wu,Akalanka Tennakoon,Ryan Yappert,Michaela Esveld,Magali Ferrandon,Ryan A. Hackler,Anne M. LaPointe,Andreas Heyden,Massimiliano Delferro,Baron Peters,Aaron D. Sadow,Wenyu Huang
摘要
A catalytic architecture, comprising a mesoporous silica shell surrounding platinum nanoparticles (NPs) supported on a solid silica sphere (mSiO 2 /Pt- X /SiO 2; X is the mean NP diameter), catalyzes hydrogenolysis of melt-phase polyethylene (PE) into a narrow C 23 -centered distribution of hydrocarbons in high yield using very low Pt loadings (∼10 –5 g Pt/g PE). During catalysis, a polymer chain enters a pore and contacts a Pt NP where the C–C bond cleavage occurs and then the smaller fragment exits the pore. mSiO 2 /Pt/SiO 2 resists sintering or leaching of Pt and provides high yields of liquids; however, many structural and chemical effects on catalysis are not yet resolved. Here, we report the effects of Pt NP size on activity and selectivity in PE hydrogenolysis. Time-dependent conversion and yields and a lumped kinetics model based on the competitive adsorption of long vs short chains reveal that the activity of catalytic material is highest with the smallest NPs, consistent with a structure-sensitive reaction. Remarkably, the three mSiO 2 /Pt- X /SiO 2 catalysts give equivalent selectivity. We propose that mesoscale pores in the catalytic architecture template the C 23 -centered distribution, whereas the active Pt sites influence the carbon–carbon bond cleavage rate. This conclusion provides a framework for catalyst design by separating the C–C bond cleavage activity at catalytic sites from selectivity for chain lengths of the products influenced by the structure of the catalytic architecture. The increased activity, selectivity, efficiency, and lifetime obtained using this architecture highlight the benefits of localized and confined environments for isolated catalytic particles under condensed-phase reaction conditions.
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