苯酚
苯
钯
催化作用
化学
氧气
产量(工程)
氢
多孔性
无机化学
化学工程
有机化学
材料科学
冶金
工程类
作者
Shu‐ichi Niwa,Muthusamy Eswaramoorthy,Jalajakumari Nair,Anuj Raj,Naotsugu Itoh,Hiroshi Shoji,Takemi Namba,Fujio Mizukami
出处
期刊:Science
[American Association for the Advancement of Science]
日期:2002-01-04
卷期号:295 (5552): 105-107
被引量:524
标识
DOI:10.1126/science.1066527
摘要
Existing phenol production processes tend to be energy-consuming and produce unwanted by-products. We report an efficient process using a shell-and-tube reactor, in which a gaseous mixture of benzene and oxygen is fed into a porous alumina tube coated with a palladium thin layer and hydrogen is fed into the shell. Hydrogen dissociated on the palladium layer surface permeates onto the back and reacts with oxygen to give active oxygen species, which attack benzene to produce phenol. This one-step process attained phenol formation selectivities of 80 to 97% at benzene conversions of 2 to 16% below 250 degrees C (phenol yield: 1.5 kilograms per kilogram of catalyst per hour at 150 degrees C).
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