Promising SiC support for Pd catalyst in selective hydrogenation of acetylene to ethylene

乙炔 催化作用 乙烯 X射线光电子能谱 材料科学 解吸 选择性 化学吸附 热脱附光谱法 热重分析 吸附 无机化学 化学工程 催化剂载体 化学 物理化学 有机化学 工程类
作者
Zhanglong Guo,Yuefeng Liu,Yan Liu,Wei Chu,Yan Liu,Wei Chu
出处
期刊:Applied Surface Science [Elsevier BV]
卷期号:442: 736-741 被引量:42
标识
DOI:10.1016/j.apsusc.2018.02.145
摘要

In this study, SiC supported Pd nanoparticles were found to be an efficient catalyst in acetylene selective hydrogenation reaction. The ethylene selectivity can be about 20% higher than that on Pd/TiO2 catalyst at the same acetylene conversion at 90%. Moreover, Pd/SiC catalyst showed a stable catalytic life at 65 °C with 80% ethylene selectivity. With the detailed characterization using temperature-programmed reduction (H2-TPR), powder X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), N2 adsorption/desorption analysis, CO-chemisorption and thermo-gravimetric analysis (TGA), it was found that SiC owns a lower surface area (22.9 m2/g) and a broad distribution of meso-/macro-porosity (from 5 to 65 nm), which enhanced the mass transfer during the chemical process at high reaction rate and decreased the residence time of ethylene on catalyst surface. Importantly, SiC support has the high thermal conductivity, which favored the rapid temperature homogenization through the catalyst bed and inhabited the over-hydrogenation of acetylene. The surface electronic density of Pd on Pd/SiC catalyst was higher than that on Pd/TiO2, which could promote desorption of ethylene from surface of the catalyst. TGA results confirmed a much less coke deposition on Pd/SiC catalyst.
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