乙苯
脱氢
膜反应器
苯乙烯
钯
催化作用
膜
选择性
化学工程
材料科学
化学
无机化学
有机化学
聚合物
共聚物
生物化学
工程类
作者
Ying Shi,Jinyi Han,Yi Ma
标识
DOI:10.1016/s0920-5861(01)00280-2
摘要
The Pd membrane was made by the electroless plating of Pd on the oxidized porous stainless steel (PSS) support with a 0.5 μm grade. The dehydrogenation of ethylbenzene to styrene was carried out in both the Pd membrane reactor and fixed-bed reactor at temperatures from 450 to 625°C and 1.2 atm pressure with a steam/ethylbenzene ratio of 6.8. As the result of the removal of hydrogen, the ethylbenzene conversion in the Pd membrane reactor was about 10% higher than that in the fixed-bed reactor for temperatures above 600°C. More importantly, the styrene selectivity in the Pd membrane reactor was ∼15% higher than that in the fixed-bed reactor.
科研通智能强力驱动
Strongly Powered by AbleSci AI