加氢脱氧
化学
催化作用
液相
相(物质)
材料科学
有机化学
化学工程
纳米颗粒
纳米技术
热力学
选择性
物理
工程类
作者
Rajamanickam Maheswari,John Meynard M. Tengco,Anand Ramanathan,John R. Regalbuto,Bala Subramaniam
出处
期刊:Acs Symposium Series
日期:2020-01-01
卷期号:: 213-238
标识
DOI:10.1021/bk-2020-1359.ch007
摘要
The liquid phase hydrodeoxygenation (HDO) of guaiacol in aqueous medium was studied at 110 °C and relatively low hydrogen partial pressure (12.4 bar) over Pd/HY zeolite to explore the effects of Pd loading and catalyst acidity. Pd/HY catalysts with two different Pd loadings (0.075 and 2.5 wt %) were prepared using commercial HY zeolite supports with different SiO2/Al2O3 ratios (5.1, 12, and 30) via the strong electrostatic adsorption (SEA) method. On both catalysts, the primary products were aromatics (AR) (phenol and anisole) that progressively undergo ring hydrogenation at longer reaction times to yield nonaromatic (non-AR) products (cyclohexanone, cyclohexanol, and 1-methyl-1,2-cyclohexanediol). Increased acidity enhances the yields of the primary AR products. The near lack of AR products on Pd/KIT-6 catalysts indicates that both Pd and acidity are essential to form the AR intermediates. HDO experiments using model AR compounds reveal that substrates with adjacent oxygen (phenol and anisole) are more susceptible to ring hydrogenation compared to those wherein the oxygen atom is nonadjacent to the AR ring (i.e., benzyl alcohol). The HDO of benzyl alcohol over both Pd/Y30 and Pd/KIT catalysts yields predominantly toluene with turnover frequencies (TOFs) (36–885 s-1) increasing with Pd particle size in the range of 2–20 nm.
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